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6 y. 42A11SE8064 6 3.4458 HOYLE 010 PROGRESS REPORT 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE Timmins, Ont. September, 1984 TOWNSHIPS A. Philipp Geologist \

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Page 1: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

6 y.

42A11SE8064 63.4458 HOYLE010

PROGRESS REPORT

1984 PROGRAM

BELL CREEK PROJECT

PROJECT 045

MURPHY S HOYLE Timmins, Ont. September, 1984

TOWNSHIPS A. Philipp Geologist

\

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42A11Sea864 63.4458 HOYLE 010C

TABLE O F CONTENTS

Page

SUMMARY i . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . l

CONCLUSIONS ......................................... 2

RECOMMENDATIONS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3

INTRODUCTION . . . . . . . . . . . . . . . . . .-. . . . . . . . . . . . . . . . . . . . . . 5

PROPERTY ............,................. . . . . . . . . . . . . . . 6

ACCESS . ............................................. 7

PREVIOUS WORK . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 7

RESULTS OF 1984 PROGRAM . . . . . . . . . . . . . . . . . . . . ......... 9

A. FIELD WORK - DIAMOND DRILLING

1. Drilling on Marl hi 11-Broulan Option..... 10

2. Drilling on Rose Option . . . . . . . . . . ...... 13

3. Drilling on Wetmore Option ............. 15

4. Drilling on Staked Claims (04 Group).... 16

5. Drilling on Allerston Optioned Claims... 17

B. OFFICE INTERPRETATIONS

North ft Bell Creek Zones - Surface X DrillGeology PI an .... 18

North Zone - Drill Hole Deviation Plan...... 18

C. SUPPLEMENTARY REPORT

Stripping and trenchingMarlhill-Broulan Property (complete with 2 maps) Attached to this report.

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TABLE OF CONTENTS

Page

LIST OF FIGURES

FIGURE l

FIGURE 2

FIGURE 3

FIGURE 4

FIGURE 5

FIGURE 6

PROPERTY MAP . . . . . . . . . . . . . . . . . . . . . . . . After P6

DDH LOCATION MAP FOR MARLHILL-BROULAN201, 202, 203, 211 and 212 .......... After P12

DDH LOCATION MAP FOR ROSE - 207, 208and 209 . . . . . . . . . . . . . . . . . . . . . . . . -. . . . . After P14

DDH LOCATION MAP FOR WETMORE - 213 .. After P15

DDH LOCATION MAP FOR 04 GROUP - 204,205 and 206 . . . .'. . . . . . . . . . . . . . . . . . . . . After P16

DDH LOCATION MAP FOR ALLERSTON - 210. After P17

LIST OF APPENDICES

APPENDIX A

APPENDIX B

APPENDIX C

LIST OF ACTIVE CLAIMS - PROJECT 045.. After P18

DRILL LOGS: DDH'S-201, 202, 203, 204,205, 206, 207, 208,209, 210, '211 , 212, and 213 ......... . After P18

DRILL SECTIONS: DDH'S- 201, 202, 203,

204, 205, 206, 207,

208, 209, 210, 211,

212, and 213.......After P18

MAP lMAP 2

MAP 3

MAP 4

LIST OF MAPS

LOCATION MAP - TIMMINS AREA ..........Back Pocket

PLANS OF MARLHILL ZONES - E&W SHEETS..Back Pocket

DRILL HOLE DEVIATION PLAN - NORTHZONE 1:500 ...........................Back PocketSURFACE AND DRILL HOLE GEOLOGY PLANCOLOURED - 1:1000 ....................Back Pocket

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SUMMARY

Canamax, as the operator of the 50/50 Bell Creek Joint Venture with Dupont of Canada initially, and now with

"Canadian South African Management", who most recently

replaced DuPont as the J.V. partner, have in 1984 continued to explore the Bell Creek properties located northeast of Timmins.

The gold oriented exploration program in the project area consisted.of .diamond drilling only. This work was executed during the winter months, was exploratory in

nature and involved various optioned properties in Hoyle and Murphy Twps. There, dri11-targets already existed from

earlier geophysical surveys, or drilling was again continuing on known auriferous vein zones as in the case of Marlhill. A total of 2,451.0 nfetres of drilling was performed in 13' drill holes.

No drilling was done in 1984 on the North - or Bell Creek auriferous zones which have recently been made acce ssible from highway 101 by the construction of a gravelled motor road. Also currently underway are constructions of ancillary facilities at the Bell Creek mine site for a shaft- sinking and underground development program aimed at the future exploitation of the above named gold deposits.

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CONCLUSIONS

A 250 metre long segment of Marlhill's MI vein lying between holes 212 and section 150W is fairly straight and probably mineable. The latest drilling shows that the vein can also be continuous to a depth of 200 metres but more drilling is needed to verify dimensions and average grade, the latter is probably in excess of 4 gms Au. A potential - but early tonnage reserve of at least 200,000 tonnes can be calculated using the following dimensions:

250m x 150m x 2.0 x 2.7 sp.g.

The presence of a second vein zone nearby, the BRI vein, has been known to exist for a long time but was difficult to follow in old drill holes. Additional future drilling on this vein should follow-up on the success of our most recent drill holes in tracing this zone.

Drilling on the Rose and Wetmore Options culminated with the abandonment of these properties. Although these claims may still hold some merit for more exploration, none could be recommended at this time.

The completion of our drilling on the 04 group brought these claims to 'Lease' as well as the information that the northern limits of the volcanics lie on Stringer ground and no further north.

The results of the Allerston drill hole show that weak alteration zones containing some gold do exist west of the dike and in line of strike of those east of the dike.

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RECOMMENDATIONS

Surface exploration is recommended for the Broulan-

Marlhill properties, the bulk of it is in the form of diamond dri11 i ng.

DRILLING

Broulan S^ Lot

Drill one hole of about 150 metres in length north

of the North Zone and north of 81-45 with the objective to explore the ground between this hole and the graphitic marker. Known to date are several parallel auriferous zones

in the hangingwalls of the North Zone and this planned hole,

which is on the same block of ground as all zones would seem to stand a good chance of finding others in the footwalls.

Marlhill - Broulan NH Lots

Several holes are recommended from 150 - 200m each

to test the MI vein at depth in the large unexplored gap laying between the hole 211 intercept and section Line SOW.

This drilling will simultaneously search for the NW extension

of the BRI vein.

Another hole should be drilled due west from a location 30 metres north of the base line on BR ground. After cutting the MI vein zone, this hole will explore for

a possible third vein lying west of the MI vein and which may strike northerly as well. The existence of such a zone

is suspected from a so far unexplained vein intercept in hole 80-18 assaying 8.0 gms Au over 6.7 metres and which cannot be 'correlated with the MI vein. {DDH 80-18 following

the strike of a vein?)

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IP SURVEY

Marlhill S?s Lot

Perform a carefully conducted IP survey with a twotarget approach:

1) Search for subtle IP anomalies coupled with resistivity-highs extending south-easterly from the MI-BRI veins.

2) Run a survey using different dipole separations on lines which cross the possible strike extensions of our. two North Zone horizons to the east of Bell Creek.

The re-cutting and chaining of older Rosario picket lines at 125m intervals for a total of 5 km of survey lines would have to precede the IP survey if we consider surveying the entire ^ lot.

STRIPPING

A re-evaluation of areas suitable for bulldozing or backhoeing in the 4 corner areas of the Marlhill-Broulan \ l ots may selectively reveal additional areas for stripping. If such work were contemplated, it would necessitate the prior clearing and burning of trees, a job preferring the fall or late winter months.

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INTRODUCTION

The 1984 drilling was the latest exploration work in a now 5 year old search for gold deposits throughout the project's property holdings. This work was initiated by Rosario, which became Canamax, in equal partnership with DuPont till 1984, when Canadian South African Management acquired Dupont's share.

The past exploration efforts led to the discovery of three separate gold deposits for which one of these, namely the North Zone's 'A' Horizon, production is planned once it's economic potential .can be verified underground together with a then prevail ing strong price for gold. The occurrence of a second nearby deposit in the form of the. dual Bell Creek Zone, can later be further evaluated by concurrent underground exploration as well. No diamond drilling was performed this year on the above named two deposi ts .

This report deals with some additional drilling oh a third deposit known as the Marlhill vein (s) and on other exploratory drilling on optioned and staked ground as des cribed below in detail.

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PROPERTY

The Bell Creek project comprises .109 parcels (40 acre claim equivalents) in the form of patented lots, staked and optioned claims in Hoyle and Murphy Townships.

The aggregate property area now actively being held totals 4360 acres or 1765 hectares.

The main block of ground is contiguous and extends from Lot 8 in Hoyle Twp. westerly to Lot 4 in Murphy Twp. In north-south direction the property extends from Con II north to include the south ^ o f Con IV in Hoyle Twp., while in Murphy Twp. it extends north from the Tisdale-Murphy boundary to the south h o f Con IV, as well. In addition there is one isolated group of 4 claims in Lot 5 of Con II in Murphy Twp.

The Bell 04 group of staked claims in Hoyle and Murphy Twps. have now earned sufficient assessment credits, therefore, an application for.'Lease' was filed.

During the year 8 staked claims in Murphy Twp., - known as the -10 group, were allowed to lapse as they were assessed unfavorable from geophysical data and from the fact that they lie west of the Burrows-Benedict Fault which implies displacement of our Bell Creek stratigraphy. Two other patented and optioned properties were also dropped as a consequence of the herein described drill program, namely the Rose h L ot in Murphy Twp. and the 10 patented Wetmore claims are not included in the above total".. A list of all active claims and options is appended.

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MURPHY TWP.

N

Road to B*ll Crt*k MlntSIU

TISDALE TWP.

aWHITNEY

TWP.

Bell Creek J.V,

Rose a Wetmore Options Dropped

Fig. l

CANAMAX RESOURCES INC.

—— Property Map ——

Q 1000 2000F—i—H-—i—rmttr*t

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ACCESS

Canamax has recently constructed a gravelled motor road to the Bell Creek Shaft site on the Broulan Option. The rest of the Bell Creek properties are best accessible from here by muskeg bombadiers over the various trails or winter roads.

The distance from Timmins to the property travelling east on highway 101 and later on the gravelled road via the former Reef Mine, is about 25 km.

PREVIOUS WORK

The heavily overburdened area was prospected for gold many years ago when an auriferous quartz vein was found in Lot 9 of Con II in Hoyle Twp. This occurrence was later staked and drilled by Broulan Reef Mines which in the pro cess patented their claims. In the late 1970's Rosario Resources acquired this property along with various other patented h l ots or staked claims. These properties still represent the core of the actual Bell Creek holdings.

Following the acquisition of this ground and the layout of grids, Rosario then embarked on a program of overburden drilling and ground geophysics initially alone and later in joint venture with DuPont of Canada. The then ongoing exploration work as mapping, trenching and diamond drilling was continued with Amax (Canamax) coming to the scene in 1982 replacing Rosario as the J.V. partner and operator o'f the program.

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During the course of the past activities, the Marlhill MI vein system was found followed by the Bell Creek dual auriferous zones and the North Zone's orebody, known as the 'A' Horizony all located in Hoyle Twp.

Also prior to 1984, other exploratory diamond drilling was performed on the Allerston, Stringer, Dommel , Fisher, Prentice, *Thomson, *0ntario Paper, *Joanis, Chartrand, Rose and Wetmore options, the last six properties are now no longer part of our active holdings. Since the inception of Rosario's diamond drilling phase in 1978, a total of 31,664 metres of drilling was done over the entire- project area and was shared by all joint venture partners. * = p roperties never included in project 045, but incl. in total drilled metreage.

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RESULTS OF THE 1984 PROGRAM

A. F i e 1 d Work - Diamond Drilling

Some of this year's drilling was done on veins in Marlhill's northern ^ lot where a multiple vein system may develop into a third gold deposit.

Other drilling also reported here in detail was exploratory in nature and was intended to further evaluate some of our optioned properties like the Rose and Wetmore options where some of our drilling was already done in 1983. As the overall results were disappointing, these two properties were recently dropped.

With the simultaneous objective of fulfilling assessment work on our 04 group of staked claims, located along the northern fringe of our property - holdings, a cross-section was drilled to explore a segment of this area. Drilling revealed the existence of extensive sedimentary formations in this totally overburdened area.

Finally, one drill hole was put down along the common Allerston-Broulan Reef boundary with the objective to check across the postulated strike extension of the Bell Creek stratigraphy west of the diabase dike. A weak aurife rous zone encountered here may need follow-up work at a future date.

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l - Drilling on Marl hi 11-Broulan Option

Two drill holes for a total of 471.0 metres were drilled in the winter of 1984 on Marlhill's northwest h lot. These 2 holes, numbered 201 and 202, were drilled below MI vein intercepts of 1983 drilling. Holes 201 and 202 established the downward continuity of this vein to a vertical depth of 150 metres and 200 metres, respectively. The return of erratic gold assays from this vein indicate the sporadic nature of free gold occurring mostly in quartz rather than with more consistent sulphide associations.

f

Three more holes, aggregating 447m i numbered 203, 211 and 212, were drilled during the winter from the adjoining Broulan Reef northern^ lot in westerly direction so as to intercept the east dipping MI vein at greater depth. As can be seen on the drill plan, the curving MI vein strikes northerly at this point. The MI vein was cut, however, all vein intercepts are already on Broulan Reef ground. The vein intercept in hole 203 assaying 6.47 gms Au over 2.4 metres appears to correspond to the Broulan Reef #1 vein (BRI), which outcrops south of the 212 collar. Thus, hole 203 was probably stopped short of reaching the MI vein as this vein retreats northwesterly from here on. At the same time and as to compound the difficulty in reaching this vein, DDH 203 deflected significantly to the north. If the MI vein indeed lies ahead of the end of this hole, it's location would be vertically below the Marl hi 11-Broulan Reef boundary. As to the above mentioned BRI vein, if it continues in northwesterly direction then it is projected to enter Marlhill ground about 160m north of the surveyed Marl hi 11-Broulan four corner post.

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What follows are some brief comments on drill holes 201 , 202, 203, 211 and 212.

DDH 045-01-201

This hole was drilled due south at -75 on Line 150W. The MI vein was cut at a vertical depth of 150 metres which is 100m below the intercept in hole 167. Sulphide mineralization and gold contents are low, similar to hole 167 above. The vein zone appears spread-out along this

drill section but it's true width will be less than indicated, This hole was not surveyed with a directional drill hole compass but is assumed to have deflected to the west similar as other surveyed holes have done in this area.

Drilling on this 150 W section appears to have delimited the vein's westerly extent for the time being.

DDH 045-01-202

This hole on section 90 W was drilled due south also, but at -70 0 . The MI vein was cut at a vertical depth of 200m, or 140m below the hole 169 intercept. The direction al Tropari survey indicates that the vein intercept was to the west of section which brings the assays obtained in line

with those from holes 166 and 168.

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DDH 045-01-203

This hole was collared on Broulan ground and drilled due west at -75 0 . It's objective was to cut the two northwest striking and east dipping vein zones known as the BRI and MI veins, at greater depth. As already mentioned above, only one vein intercept was achieved assaying 6.47 gms over 2.4 metres and which seems to correlate with the BRI vein. Thus the MI vein was apparent ly not reached as the drill hole and MI vein zone turn away in opposing directions.

DDH 045-01-211

The hole's collar was 35 metres south of 203, drilling was also due west at -75 0 and has accomplished it's objective to cut the east dipping BRI and MI vein zones. Both zones are spread-out and so are their values. From earlier drilling here the MI vein is known to be 'broken-up 1 along this section, which suffered maximum deformation. The vertical depth of the vein intercepts was 50 metres for the BRI vein and 90 metres for the MI vein.

DDH 045-01-212

The direction of drilling was again parallel with hole 211 at the same dip. As above, the drill targets were the two veins of which the BRI vein crops out near the hole's collar and which was subsequently cut near surface, assaying 7.98 gms. Au over 2.2 metres. The MI vein was also relati vely well .mineralized and showing some VG. The geological width of the zone was 5.2 metres and this can be substan tiated with averaged assays of 2.86 gms over this width or 4.19 gms over 2.0 metres. This intercept was 75 metres vertically below surface.

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PROGRESS REPORT

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Seal*: 112500

8*pt. 1984

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2. Drilling on Rose Option - Murphy Twp.

Three drill holes numbered 207, 208 and 209 were drilled during the winter for a total of 579.0 metres-.

The purpose for this drilling was to evaluate previously untested IP anomalies and a minor auriferous zone found in last year's drilling.

As a result of this work a broad geological cross- section was obtained across most of this heavily over burdened ^ lot. Rocks encountered were all of mafic volcanic origin. Their strike is roughly E-W and they dip steeply to the south. The talcose komatiitic basalt and fragmental units from hole 199 re-appeared again in this year's hole 207, showing the continuity of these units in E-W direction. Lacking other work along strike it is difficult to say whether they actually are the western extensions of the Pipestone Fault stratigraphy.

The weak auriferous zone in last year's hole 199 does not seem to have continuity, at least not in westerly direction and where tested with hole 207. A more interesting and broader alteration zone found in hole 208 correlates with an IP anomaly but unfortunately does not contain any mineralization of economic interest. It was, therefore, recommended not to excercise another year's option when it was due in July.

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Below follows a brief summary of 1984 drill holes:

DDH 045-01-207

This hole was collared some 58 metres west of hole 199 and drilled north at -50 0 . Rock types encountered are talcose komatiitic basalts and fragmentals as in 199 but without it's small gold occurrence.

DDH 045-01-208

This hole was collared south of hole 199 and drilled north towards it, nearly accomplishingan 'overlap 1 with the south dipping volcanics. A shear zone near the top of hole and a pyrite-minerali zed, strongly calcitic alte ration zone from 135.0 - 143.5 metres will account for the IP anomalies. This zone contains locally abundant tour maline but no anomalous gold values.

DDH 045-01-209

Exploratory drilling to the north of 199 encounter ed mafic fragmental volcanic rocks but no alteration zones of any kind.

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i i PROGRESS REPORT F i 9- 3 c rn i a . i.^nnn

Sept. 1964

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3. Drilling on Wetmo re Option - Hoyle Twp.

A total of 162.0 metres were drilled in one driM hole numbered 213. The purpose for this drilling was to evaluate certain - hitherto untested horizons prior to up coming option payments in August. In the light of the disappointing results obtained, this option was likewise not renewed.

Drilling concentrated on geophysical targets pre viously located. These consisted of magnetic and EM anomalies which are locally flanked by responses from an induced polarization survey. The area is heavily over burdened. The strike direction of the underlying rocks was determined from the EM survey. Drill hole 213 showed that a sequence of sedimentary rocks dip northerly. This reve lation implies the possible existence of a previously un recognized syncline, marked by the presence of these rocks in correlative direction with a regional AEM anomaly.

Summary of DDH 045-01-213

This hole was drilled due north at -50 on Line 500E, collar location was 225N.

It's target was a HEM anomaly with flanking,IP and some subtle magnetic correlations. The hole stayed in sediments all the way as alternating argillite with grey wacke beds whi eh, signi f icantly, dip steeply to the north.

The argillite contains some graphite and pyrite. Nothing was seen to explain the weak mag feature. Check samples sent for assay did not reach the gold anomalous threshold values of 0.5 PPM.

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Tit lint,

PRENTICE

PROJECT - 048— BELL CREEK

PROGRESS R EPORT

WETMORE

I1984 Diamond Drill Hoi*

1983 Diamond Drill Hoi* ii

HontLot

HOYLE TWP.

WETMORE

BdMlint

800m aOBffl

UJ

•00m

WETMORE

600m

WETMORE

tSCHUMACHER

WETMORE

WETMORE

SCALE 1:5000WHITNEY TWR LOT f Fig. S* pt. 1984

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- 16 -

4. Drilling on Staked Claims 04-Group, Hoyle Twp.

With the performance of three drill holes numbering 204, 205 and 206 for a total of 606.0 metres of drilling', we completed all assessment work required to bring all claims in this group to 200 days, while exploring this previously undrilled area for mineralized zones.

The 3 holes were put down north of the Stringer Option and along the old Rosario Line 36E. The holes were planned to roughly cross-section the area in N-S fashion while checking a local weak HEM conductor at the same time. Thus, drilling covered portions of claims P525276, 525303 and 525306.

All holes encountered a folded sequence of massive greywackes with argillites striking E-W and showing local variations in their dips as being either north or south dipping. The width of these sediments as defined by the drilling amounts to 1700 metres when measuring from Rosario Hole 80-4 located in the north k o f the Stringer Option, which already was in sediments.

Nothing of any economic interest was seen in the drilling. All check samples sent for assays returned NIL values in gold, even from some quartz veins or from minor graphitic or pyritized sections.

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®

N

3.3

Hoyle Township

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P525306

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P525303

u W IOJl

li

. ZOI.Om

-04-204

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P 525305

si

P525304

04 - Group C AN AM AX RES.

BELL CREEK J.V. - O45

Progress Report

* 1984 Diomond Drill Hole

Township ' Claim No. ' Line No. 'D.D.H.No. : Bearing i Dtp iLength of D.D.H 'Date !

Hoyle P 525306 L36E, 2850N045 - 04 - 204 True North -500

201.0m

Sept '84 Scale- 1:5000

Fig. 5

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Hoyle . Township

04 - Group

CANAMAX RES.

BELL CREEK J.V. - O45

lProgress Report

1984 Diamond Drill Hole

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il

P525304

i

Township iClaim No. 'Line No. '

HoyleP 525306, P525303

L36E , 285OND.D.H.No.BearingDipLength of D.D.H

045 - 04 - 205I80 0-45 0

204.0 m

Dote Se p*'-? 84 l:50pQl

Page 26: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

P52527I P525272

N

P525273

P525275

J2~3l

045-O4-2O6

P525276

SOI.Om . .

P 525277

f231

04 - Group

CANAMAX RES.

BELL CREEK J.V. - O45

Township iClaim No. 'Line No. '

Hoyt*P525276L36E, I900N

Progress Report

l 1984 Diamond Drill Hole

D. D. H. No. 'Bearing 'Dip -Length of D.D.H i

045-04- 2061800-45*

201.0mDate Sept' 84 Seal* l: 5000

Page 27: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

5. Drilling on Allerston Optioned Claims - Hoyle Twp.

Drilling on these optioned claims which already have 'Leased Status 1 amounted to 186.0 metres in l drill hole.

The Allerston Hole was numbered 210 and was drilled north at -50 0 along it's common boundary with Broulan. The hole's objective was to explore across the projected strike extension of the Bell Creek stratigraphy in westerly direct ion from the diabase dike.

Hole 210 encountered a weak alteration zone assaying 1.95 gms Au over 1.2 metres in tuffaceous basalt near it's contact with leucoxene basalt. This occurrence is near other anomalous gold intercepts in hole 81-17 which are all roughly on strike with other auriferous alteration zones in similar rock east of the dike. Although weak in character, these occurrences nevertheless point out the direction for future exploration.

Page 28: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

14i

P5I5780

t

P5I5779

O

:l

5900 N

5800 N

57OO N

5600 N

55OO N

5400 N

R*ftft M

5200 N

l( ( {

l

J 14

J 0' MB

^ tf)

P! 15781

r Jo -S' j

K) 140

1

.. _ L -.--OIS8

11

(eoc

P 5 15782

- -

li UJ (ft

3 o 5 20 K)

bctK

1

)

bC

cM

j

l i) 1

O

eio t.

j t) 4) 4d i}

i ui u

\ 8 8) K) K)

L4 1699

i~ ~ i — -~-^.-- j t

j l i1 1

120 ^

|j l

1

L' 4698 i

X I

1

1

-r---.~7 ~ -81.17 |

1

\

j

1li tl

|J UJ 0 uD 0 o 5 -0 gnmo

LOT IIAllerston

HOYLE TOWNSHIP

l i

LOT 10

BELL CREEK - J.V. Project 045

PROGRESS REPORT

1984 Diamond Drill Hoi*

1988 Diamond Drill Hoi*

Fig. OS*pt 1 84 Sealtt i: SOOO

Page 29: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 18 -

B. Off i c e Interpretation

North l B ell Creek Zones -

A "Surface S Drill Hole Geology Plan" was pre pared at a scale of 1:1000.(In Back Pocket).

The plan shows outcrop-geology near the 290 metre surface level and an up-dip projection of drill hole geology or mineralized zones to the 250 metre level, which is approx. 10 metres below the bedrock-overburden inter face.

Interpreting a coloured print of this map suggests an easterly plunge and a structural deformation of the volcanic/sediment assemblage along the course of Bell Creek.

North Zone -

A 'Drill Hole Deviation Plan 1 at a scale of 1:500 is included in the back pocket.

The plan shows that drill holes on the North Zone will consistently deviate to the west amounting to a relative displacement of - 15 metres from the horizontal, depending on the depth of the intercepts.

Submitted by:

Timmins, Ontario Al September, 1984 Geologist

Page 30: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

APPENDIX A

LIST OF ACTIVE CLAIMS

Page 31: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

PROJECT: 4045 - BELL CREEK JOINT VENTURE

(Claims held as of September 30, 1984)

045-01

Township

045-03

Murphy

045-04

Murphy S Hoyle

Hh Lot 11 \\h Lot 1C Sh Lot i Sh Lot K W-2 Lot i Sh Lot l tih Lot 1] N^ Lot l? N*s Lot 1C

P. 515775 P. 515776 P. 515777 P, 515778 P. 515779 P. 515780 P. 515781P. 515782

P. 515785P. 515786P. 515787P. 515788P. 515789P. 515790P. 515791P. 515792P. 515793P. 515794

P. 516562P. 516563P. 516564P. 516565P. 516572P. 516573P. 516574P. 516575P. 525270P. 525271

L, Con. 1 ), Con. 2 ), Con. 2 ), Con. 2 ), Con. 2 ', Con. 1 i, Con. 2 ?, Con. 2 ), Con. 1

AT 1 rrH1 n 1 1 ci a

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.

P.P.

P. 15504 Fisher P. 13435 Marl hi 11 NW P. 13436 Marl hi 11 SE L. 168 Broulan SW L. 100253 Broulan NE P. 1487 Geiger P. 10568 Stringer P. 9083 Dommel P. 460 Prentice

;on

516309516310516311516312516313516314516315516316516152516153

525272525273525274525275525276525277525303525304525305525306

P. 516154P. 516155P. 516156P. 516157P. 516158P. 516159P. 636457

P. 540402P. 540403P. 540404P. 540405P. 546519P. 546522P. 546523P. 546524P. 546525P. 546526

P.546527 P.546528

Appendix A

Page 32: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 11

045-05

Hoyle P.508687 P.508688 Allerston

045-07

Murphy P.641546 P.641579 P.641580 P.641585

Totals: 73 - 40 acre claims

9 - 160 acre parcels109 - 40 acre claim equivalents

(4360 acres or 1765 hectares)

Page 33: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAAAAX

APPENDIX B

DRILL LOGS

Page 34: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD kNo. ...04.5.-01-201...—.......-

HOI. so. 045-01-201 ste. J....,.,. ......p,op.n,.Marihi..l.l...CBel.l...Cr.,.,.0,v,)

uc.1 J" LI 50 W. .C300...N L ........... ..........

Con Uxr.lion .....HOy.l 6 ..Camp .. S i.te...... ......

untih 213.0m combed —fe.bruary. 4, 1984...... p, Collar -75" , ^ _hanni 180 Comptaej February 7, 1984D,. -75 0 ' " """ "" Dniimico St. Lambert ElcllTe" Dt '"11 M*; T™oicuv. To test Marlhili Ml.. ... CmSlK . .^Q....... ........................................ ....JL..............40.,.Om........80^...........76^ .

...vein...a.t....gr.eater...depth. . c.iin( u(./ LO.I in HOI. ..Plastic ni.pes.... ......" ...............80. m......... 78 ..............73 ......4 below hole 8J-167 down to bedrock, " 120m 71" 65"

. ... . . ..... . .......,... ,, ....,............................................ ......"...........,,..]S6m.......68...0 .........6.1 0 .

Keuurki ..MI . Ve.) n.. Zone.. was...cut...a t . 145. m .vert 1cal..,depth....f.rora...surfa.ce.. but.. flea.r.J..t!..s wes tern............. _ ,,., ,..................................................................................extremity Sulphide mineral i ration in rather weak but abundant tourmaline does occur.

Wfiro

From

0.00

28.0

34.0

123.0

141.0

154.85

162.6

203.0

210.0 -

To

28.0

34.0

123.0

141.0

154.85

162.6

203.0

210.0

213.0

213.0

DESCRIPTION

CASING - OVERBURDEN

GREEN WEATHERED BASALT

ALTERED VARIOLITIC BASALT (FLOW TOP BRECCIA)

CARBONATED BASALT

CARBONATED FRAGMENTAL 8ASACT

CARBONATED i MINERALIZED MI VEIN ZONE

GREY CARBONATED BASALT

CARBONATED BASALT - NARROW QUARTZ VEINS

CARBONATED BASALT - AS ABOVE

END OF HOLE

SampleNo

UMOOl100002100003W0004U50005100006100007iooooa1000091000 10W001 1100012

100013

i00014.0001 5

88.4151.8152.3153.8154.8155.8156.8157.8159.4160.4161.4162.6

202.9

207.9208.9

89.7152.8153.8154.8155.8156.8157.8159.4160.4161.4162.6163.75

^03.9

208.9209.9

LengthMctrci

1.31.0

1.0

1.01.01.01.01.61.01.01.21.15

1.0

1.01.0

1

AUPPM

50

0702

NIL020000010

5?1501010221488002

NIL

00

3804

AUPPM

4.59

2.47

1.23

2ndPH! P

4.53

Appendix \i

Page 35: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Halt N o. 0.15-0.1-201..

Shtcl No............2...............Metrti

From To

0.00

28.0

34.0 '

123.0

S.

28.0

34.0

123.0

141.0

DESCRIPTION

CASING - OVERBURDEN

GREEN WEATHERED BASALT

Fine-grained basalt, weakly chloritic and calcitic. Rock is schistose andleached. Low core angles range from 0-10 to the core axis.

ALTERED VARIOLITIC BASALT (FLOW TOP BRECCIA)

Fine-grained, greenish-grey, weakly carbonated basalt 1s fairly massive andappears to be variolitic in nature and pillowed as well. Rock is stillweakly chloritic but calcite alteration increases with depth. Occasionalbarren carbonate veins (calcite) with little quartz. Local large fragment isbleached and saussuratized. Basalt contains dark-grey alteration zones overnarrow sections which appear to be composed of minor graphite, chlorite.calcite or some local Po. Lower contact is arbitrary.

38.7 m 1 cm wide calcitic band with 15* combined Po 4 Cpy at 100 tothe core axis.

88.4 - 89.7 m Calcitic alteration zone, minor quartz. Section contains 4tcombined Py, Po 4 Aspy. Foliation is about 30 to the coreaxis. (True width of zone is much less than indicated).

102.4 -102.9 m Narrow band of semi-massive Po, little Py 4 Cpy in calciticmatrix, at low angle to the core axis.

CARBONATED BASALT

Fine-grained green calcitic carbonated rock. Basalt appear to be pillowed andmore massive than In unit above, fragments and varioles appear to be mostlyabsent or else they are more obscured here because of the higher degree ofalteration.

Sample No.

WOOOl

From To

88.4 89.7

Lenelh Metres

1.3

AU PPM

5.07

AU PPM

4.59

2nd PULP

4.53

*

t*

Page 36: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORD Hol.No.045.-01.r2Ql.. Shwt No..........3................

MtlrrsFrom To

1

141.0

154.85

f .

154.85

162.6

DESCRIPTION

CARBONATED FRAGMENTAL BASALT

Fine-grained, dark-grey fragmental rock. Calcitic alteration throughout 1.Large scattered cubes of pyrite below 151.6 m. Minor local quartz sweats orcrosscutting veinlets or whips of calcite. Lower sharp but irregular contactapprox. at 30 to the core axis.

CARBONATED AND MINERALIZED MI VEIN ZONE

Stmplc No.

W0002 IVQ0003

As in hole 167 above, zone consists of a number of silicified sections or jJSSnne irregular quartz veins. A lower - and upper silicified section is divided by C™''-? barren rock. '-Individual quartz veins appear mostly crosscutting the core and r™ 0™, mineralization is the form of pyrite and Aspy or rather weak disseminations. CnSJnnfl Good tourmaline occurs locally with minor talc-like hydromuscovite. No SHnnno visible gold is seen. Carbonate alteration is both calcite and lesser luOvvin dolomite, pervasively. Vein orientation is in part parallel to schistosity, r?™'!,

i.e. at low angles to the core axis, knn012

154.85 - 155.7 m Silicified rock, abundant brown tourmaline, 3-4* Py, veryminor Aspy.

155.7 - 159.5 m Carbonated but little mineralized rock, few scattered cubesof Py, minor quartz stringers or sweats in bottom 80 cm.

159.5 - 162.6 m Section is silicified in an irregular manner. Calcite-ankerite alteration. Tourmaline and minor Aspy occurlocally associated with quartz as well as Py, showingstronger near the bottom.

From

151.8 152.8153.8 154.8 155.8 156.8 157.8 159.4 160.4 161.4 162.6

.

To

152.8 153.8154.8 155.8 156.8 157.8 159.4 160.4 161.4 162.6 163.7!

Until) Mrlrn

1.0 1.01.0 1.0 1.0 1.0 1.6 1.0 1.0 1.2 1.15

AU PPM.

0.02NIL0.52 2.15 0.01 0.01 0.02 0.21 0.48 1.80 0.02

AU PPM

2.47

1.23

2ndPULP

7

t

Page 37: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORD Hole No. (M5.-Q1.-2QL.... Sheet No. ........4.......................

Metre*From

162.6

203.0

210.0

To

203.0

210.0

213.0

213.0

DESCRIPTION

GREY CARBONATED BASALT

Fine-grained, grey and massive rock is well carbonated - calcitic alteration.Colour is grey to tan, occasional fragments. Irregular foliation is at low angle to the core axis, i.e. from 10 - 30 to the core axis. Local quartzsweats and minor cubic Py.

CARBONATED BASALT - NARROW QUARTZ VEINS

Fine-grained grey calcitic carbonated rock as above. Occasional outlines ofaltered fragments. Some widely spaced quartz veins locally mineralized withtourmaline and pyrite - additional barren quartz sweats. Quartz veins occuras follows:

203.10 - 203.40 m Quartz vein with some black tourmaline and green muscovite.No sulphides.

207.9 - 210.0 m Silicified rock, quartz sweats and 40 cm wide irregularquartz veins, seams of tourmaline and minor Py.

CARBONATED BASALT AS ABOVE

Grey calcitic carbonated rock as above.

END OF HOLE

Sample No.

00013

10001400015

From

202.9

207.9208.9

To

203.9

208.9209.9

length Metres

1.0

1.01.0

AU PPM

NIL

0.380.04

AUPPM

2nd Pill P t

fc

Page 38: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD oic NO. 045-01-202

Hole No, 0 Property M Township H

Location L

Logged By . Cone Locjti

*5- 01- 202, shed,,,!,,,.,,.,,, a.rlhi.1 L..(BeU...Creek...OVl ayle,,,,,,,,,,,.,,,,,,,,,,,,,,,,.90W...(30Q...N).............,.....................^••••p^lllpp-——— -- •-••••-

M, Hoyle .camp Sue

Remarks TropaH tests indicate Ml well silicified with a bur be brily about H of indicc

Mcltc-i

From

0.00

27.5

60.0

106.5

192.0

209.55

212.7

232.0

To

27.5

60.0

106.5

192.0

209.55

212.7

232.0

258.0

258.0

u th 258.0mt*.",,, T 86;B, , ... ...^o....... ——— ™ .....

Object ...IO...test..Mar1h.:(ll.jL.,,...,....ye.in..zone .at .greater....

depth and below Hole....8.3-169.,,..........,,,....,,.....,.,.....,......

vein zone was intersected 30m widaht As'py S tourmaline showings,ted width.

D E S C R 1 P T 1

CASING - OVERBURDEN

LIGHT-GREEN FLOW TOP BRECCIA

WEAKLY GRAPHITIC ASH 8, TUFF

ALTERED FLOW TOP BRECCIA

GREY CARBONATED BASALT

CARBONATED AND MINERALIZED MI VEIN ZONE

GREY CARBONATED BASALT

MASSIVE GREENISH-GREY BASALT

END OF HOLE

Comm.^ ...February 7, 1984 oomold February 9, 1984Driiiin, co. , St .....Lambert ....... . ...,.Core Size ' .J.Q.,.....,, ,,.,,,,,,,,,,,,,,.

Casing Left/ Los, in Hole .P..l.aS 1 1.C ,.P.l .p6Sdown to bedrock.

est of section. Vein Zone is "but"'true"width"of zone 'should--

Dip: Collar ,..,-7.0,,,...,,,,,.,-..,,,,,,,,,,,.Dig

Eich Tesl Deplh Wlf Tru

Tropari 60m -72" Az. 18511li '

20m -69" A 180m,, -68? A240m -61" A

?, J 96 z. 219 z."228

0 NSample

No.

WOO 16 (\00017

A00018 W001 9 A00020 A00021 W0022 A00023 A00024

From

138.5 139.5

206.0 207.0 208.0 209.4 211.3 212.7 213.6!

To

139.5140.5

207.0 208.0 209.4 211.3 212.7 213,6? 214. 6C

Length Metres

1.0 1.0

1.0 1.0 1.4 1.9 1.4 0.95 0.95

' ' : :O O O O :

—————— SOBS —————

Loon i o rv Sketch North

1Claim No.

Scale:

AU PPM

0. 0.

0. 0. 0. 3. 7. 0. 0.

2315

03 01 03 54 20 30 02

AU PPM,

0.33*

6.72

Page 39: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORD Hole No. .....M5-Q.1.-ZQ2..,.ShetlNo..................2...................

MetresFrom | To

0.00

27.5

60.0

27.5

60.0

106.5

DESCRIPTION

CASING - OVERBURDEN

LIGHT-GREEN FLOW TOP BRECCIA

Fine-grained, light greenish-grey altered basalt. Abundant coarse bleachedfragments, some minor small varioles. Low core angles of foliation range from 0 - 20 to the core axis. Chlori te-calcite alteration, some leachedvugs.

55.0 - 60.0 m Fracture zone. Fractured and broken core, light oxidation onfracture planes. Core angles near 25 to the core axis.

WEAKLY GRAPHITIC ASH S TUFF

Fine-grained, dark-grey, weakly graphitic ash-rock. Pervasive graphite-calcite-muscovite alteration, sulphides next to nil. Foliation is at lowangles to the core axis. Rock is leached and broken in the upper *s of section;with some leached quartz sweats - veins and some mica. Rock becomes morecompetent and massive in the lower h i few crosscutting calcitic gash veins.Lower contact is arbitrary as alteration obscures a seemingly gradationalcontact at low core angles.

63.0 m - schistosity angles at 250 to the core axis.

80.0 m - same as above

106.2 - 106.5 m - semi-massive fine-grained Po with minor Cpy across 2 cms.Band runs down core axis at 15 .

Simple No.

From To Length Mtlres

Tt

Page 40: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD i. NO. ..045-01-2!

Sheet No...., ........3...Metres

From

106.5

192.0

209.5!

To

192.0

209.55

212.7

DESCRIPTION

ALTERED FLOW TOP BRECCIA

Fine-grained, greyish-green, weakly carbonated basalt. Abundant fragmentsthroughout, they are set in a chloritic matrix. Calcitic alteration.Occasional minor quartz-carbonate sweat or stringers, no sulphides exceptwhere noted below. Flow is fairly massive, local foliations are at lowangles to the core axis as hole continues subparallel down the schistosityplanes. Bottom contact is only an alteration contact as carbonate alterationincreases at that point.

138.75 - 141.5 m - Weakly silicified section with Q .5% Py. Very minor Po.Few 2 - 3 cm wide quartz-calcite bands and minor quartzsweats. Quartz-carbonate banding from 30 - 40 to thecore axis.

GREY CARBONATED BASALT

Fine-grained, carbonated basalt - flow top breccia as above. Calciticalteration throughout, becoming more intense down hole. Local Py occurrencesbelow 207 m. Lower irregular contact with HI vein zone approx. at 30 to thecore axis.

CARBONATED i, M INERALIZED MI VEIN ZONE

Vein zone consists of foliated quartz-tourmaline rich rock in a calcitic -carbonated host. Arsenopyrite occurs abundantly throughout as very finegrains, pyrite with Po is from 2 -31 but is higher locally.209.55 - 211.30 m -Main silicified J foliated section containing a continuous iquartz-vein section Of about 80 cm in it's lower part. ' *Silicified tourmaline-rich rock occurs on top of section. 'Abundant fine-grained Aspy occurs in 1 cm wide bands 'locally parallel or subparallel to the core axis. Py - Po *content is from 4 - 53! Py is mostly cubic and appears to 'predominate. Fractures in the quartz contains talc-like

hydromuscovite, sulphides, tourmaline and little bluish-grey ankerite. One freak grain of sphalerite occurs inthe quartz-vein.

Simple No,

0001600017

100018100019100020100021(00022100023100024

From

138.5139.5

206.0207.0208.0209.4211.3212.7213.65

To

139.5110.5

207.0208.0

Length Metro

1.01.0

1.01.0

209.4 1.4211.3212.7213.6214.6

1.91.4

i 0.95) 0.95

AU PPM

0.23,0.15'

0.030.010.033.547.200.300.02

AU PPM

0.33"

6.72

Page 41: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD .NO. ...0.4.5-Q.b202,...

MthrrsFrom

212.7

232.0

f.

To

232.0

258.0

258.0

DESCRIPTION

CONTINUED

211.30 - 212.10 a - L ittle silicified basalt. \ -2t combined Py, Po and somefine Aspy.

212.10 - 212.70 o - Silicified section, 3-42! Py, Po 4 Aspy. Some regular core angles near the bottom are at 40 to the core axis.

GREY CARBONATED BASALT

Fine-grainecf, grey, calcitic basalt is probably pillowed, local foliationline at 225.7 m may contain some coarse cubes of Py with minor tourmaline asisolated minor occurrences. Local narrow calcitic bands with minor quartz Spyrite.

MASSIVE GREENISH-GREY BASALT

Rock is med f -JIB- g rained, increasingly massive and fresh downhole. Pillowedbasalt --appears to grade into an altered leucoxene basalt where leucoxeneappears to rave altered to pale-white sphene.

END OF HOLE

Sample No. From To Length

Metres 1 1

f* •'

Page 42: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD HoleNo.Q45-Dlr.203...-

BrouTan Re To.ruhip Hoyle............. UC..UK L6.0.E...-..125

e?lBe{i:CryV

iczzzzzzzcore uoc.no,, ...Hoy].e ..Camp .SI le...........

ter, ,h 144 0"!Be.'.( 2.7.0* ............. .........—— ........ ___ .....

Hole 81.-42.............................. ......

commenced ..February ...9 .-.l 984 ............ compieiej ..February ..].3*..J984.........

Core Si/e .. BQ . ......

Kenurk. ..MI. Vein.. Zp.ne...vya.s..,io.tercepted...whe.re.i,t .s tarts .....tiir.ni .ns..nflr.thwes.tedy .1. ..lt.'.s...diR,.i.s...near..............-55 easterly tPCatlpn of int-prrpnt l*; lOOm YprtirMTlv frfim c-lirfarp - nn Rrnnlan RppfProoertv.

Metro

From

0.0

12.50

26.30

102.50

103.30

116.40

-

To

12.50

26.30

102.50

108.3

116.40

144.0

144.0

Dip: C

Etch T

Trop

ollar ....7Z5.0 .......................... ...........

en Dcpih *JS True

ar.1..........21m........ -720- Az ...,2.800 C 0.Aci.d....Test..42m............T68^u ....... . . 0

..Tr.op8r.i.,,,T21m.,,,,....760?.,Az......e960 CO

...............,. — ..,.....................................................

Location Sketch Nonh

1

DESCRIPTION

CASING - OVERBURDEN

MASSIVE ALTERED BASALT

GREY CARBONATED BASALT

CARBONATED AND MINERALIZED HI VEIN ZONE - VG

DARK-GREY CARBONATED FOOTWALL

GREY CARBONATED ROCK

END OF HOLE

No.

A00025A00026A00027A00028A00029A00030A00031A00032A00033

101.5102.5103.5104.5105.9107.3108.3109.3110.3

102.5103.5104.5105.9107.3108.3109.3110.3111.3

Melrci

1.01.01.01.41.4-:1.01.01.01.0

AUPPM

NILNIL0.0.1.

14.0.0.0.

09030395971502

AUPPM

12.07

2ncT PULP

14.67

2nd PULP

Page 43: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hoi,NO. .04.5-01-203...

Metre*From 1 To

0.0

12.50

26.30

12.50

26.30

102.50

J.

DESCRIPTION j S'™r'*

CASING - OVERBURDEN

MASSIVE ALTERED BASALT

Hole is being drilled at 2700 which is roughly parallel with bedding.

Rock is medium-grained and green in top h o f section, changing to fine-grained greyish-green, weakly carbonated basalt in the bottom 15. Fractures are chloritic, a coarse quartz sweat with cubic pyrite occurs near the bottom.

GREY CARBONATED BASALT

Grey, fine-grained basalt, likely being our pillowed flow top breccia. Calcitt carbonate alteration Increases downhole showing some isolated barren quartz- carbonate stringers or sweats with a little Py in their walls. Fragments are easier discernable with depth and there rock is usually bleached to a lighter grey. Carbonatedbasal t becomes rather massive and is of medium-grain in bottom 15 m.

33.8 - 34.8 schistose broken core

- 39.4 oxidized fracture at 450 to the core axis.

- 42.4 as above, oxidation next to 3 cm wide quartz-carbonate vein with some pyrite, at 45 to the core axis.

- 43.8 as above - no quartz.

- 50.3 9 cm wide oxidized quartz vein at 500 to the core axis. No sulphides.

From To Lentlh 1 AU Mam 1 PPM

Page 44: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hole No. ...P.45-01-20.3.

Shtcl No,..............?................Melrn

Krom

102.50

108.30

116.40

s .

To

108.3

116.10

144.0

144.0

DESCRIPTION

CARBONATED AND MINERALIZED MI VEIN ZONE - VG

The indicated broad width of this zone is due to silicified hangingwall rockwhich is included here. The main mineralized and gold-bearing zone is pro bably around 1.5 m in width.

Calcite-carbonate alteration changes to ankerite (dolomite) in the quartzvein and immediately below it.

102.50 - 107.3 silicified wallrock. Numerous foliated quartz stringers-sweats or narrow veins. 1-23! coarse Py-cubes or littlefine Py t, Po. Minor Aspy in bottom ^ ra.

107.3 - 108.3 VG - Main MI quartz vein. Grey to milky-white quartzshowing 11 specks of free occurring gold along a vein'length of 30 cm. Vein is flecked with fine muscovite mica.ankerite or brown tourmaline. Py is about 2S, Po is 0.5J!and only very minor Aspy in the vein itself. Some Aspyoccurs at the foliated bottom contact together with one finespeck of gold.

DARK-GREY CARBONATED FOOTWALL

Highly altered, dark-grey carbonated rock. Pervasive graphite (?) dolomite-calcite-hydromuscovite alteration. A 0.5 m long foliated section right belowvein shows foliation running parallel to the core axis. Minor carbonatedstringers and quartz, add coarse cube of Py.

GREY CARBONATED ROCK

Fine-grained carbonated rock as above. Calcitic constituents increase. Colouragain becomes darker grey near the end with an apparent increase of quartz-carbonate sweats and stringers - now less calcite. Very minor local specksof Py. Schistosity is from 30 - 40 to the core axis.

END OF HOLE

Simple No.

A00025A00026MD0027A00028A00029A00030A00031A00032A00033

Front

101.5102.5103.5104 5105.9107.3108.3109.3110.3

To

102.5103.5104.5105.9107.3108.3109.3110.3111.3

Ltn(!h Melrn

1.01.01.01.41.41.0\.o1.01.0

AUPPM

NILNIL0.090.031.0314.950.970.150.02

AU PPM

12.07

2nd PULP

14.6:

r t

Page 45: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD He* No. -.045-0.4:104..—........-

Hole No 0 Property 1.

45T 04-204 e'1 Creek 3.V.Hovle

Loc.,,on ...,L36E,-,.2850N,,,,,,

Lowed By ... A, ..Phi Vi PP ................ .. .........coreL,xntor,,M.N.R...r Storage........

L.n,,h ..?01.Q,m............................... ..T CA0k.ri., ...360.........................

Kf . ..-50,.......................,.......^......... ....ob^ii.e ..To....tes.t,.Geo.lo.oy.,Si...Weftk.

HEM..anomaly.. .while. ,..........

work.. .... ........... .............. ......—...

commenced ..Eebruary.,,14 ....1983..........Complied -February, 16:,-. 1983..........

Remark Hoi e 84 -. 2.04 eacoun.tered...a...nQrth-(H ppi ng, sedimentary ..sequence ,Qf.,greywack.es ..and .........,...........-.4.rgl.],l,1..tes,.,...No..Qt)y.tous.. ' " ' ""' ' ' '

Metro

From 1 To

0.00

15.10

40.90

78.50

100.00

118.6

119.25

162.0

178.8

15.10

40.90

78.50

100.00

118.6

119.25

162.0

178.8

201.0

201.0

reasons T.or...t;ne...w.eaK....HLM...ano(naiy ,,were,.seen ...in ...tne.se .rocks. ,,..,...,.,.

Dip ColUr -50 -. .

Etch Ten Depth Rdg. True

.J1,...,". ,.,,,, .,.,40m,..,.,,,,,,,,-,...,.,,,.42"

.-.".,,,!',,,..,..,,,,90ni.,,,,.,,.,....... _ .......37;:

.J.',...,"...,,.,,.,.1.4.1m.,,,... __ ,,,......,,.,,30^l...,'.'...,.,,,,200m.....,,,,,,..,,..,,..,.....25c

— ...., — .....,,.,..,.,,. — ,,,.,, — ,,,,, — ,.,,.,.

DESCRIPTION

CASING - OVERBURDEN

ARGILLITE AND GREYWACKE

MASSIVE GREYWACKE

ALTERED GREYWACKE AND MINOR ARGILLITE

ALTERED GREYWACKE AND BEDDED ARGILLITE

QUARTZ VEIN

GREYWACKE AND ARGILLITE INTERBEDS - AS ABOVE

MASSIVE GREYWACKE

GREYWACKE AND ARGILLITE

END OF HOLE

SampleNo.

MJ0034A00035A00036

A00037

A00038

94.795.796.7

118.3

157.5

95.796.797.7

119.4

159.0

LengthMelrci

1.01.01.0

1.1

1.5

Location Sketch

At.

k,3V

M* i*W*

,,,^f*** p

\SUiiS

1

}fin'-*

North

1cw.n..iLS53gL.-Scale: 1 1 15, 000

PPM

NILNILNIL

NIL

NIL

T

t

Page 46: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD HOI. NO. 045-04-204...

ShKl No. ..........Z............ ..Mtlrn

From 1 To

0.00

15.10

40.90

78.50

15.10

40.90

78.50

100.00

*

DESCRIPTION

CASING - OVERBURDEN

ARGILLITE AND GREYWACKE

Intermittent argillite and greywacke interbeds showing Individual contactsfrom 20 - 32 to the core axis, i.e. hole is going down-dip. Argillite bedsare composed of very fine-grained silt-like materials, moderately bedded;colour ranges from grey to darker grey, the latter may be due to minorpervasive graphite.Greywackes are composed of fine, medium and locally coarse-grained polymicticrocks showing local inclusions of argillite. Colour is greenish-grey. Indi vidual argillite-greywacke contacts are usually sharp and well defined butlocally they are ragged or flame-like into the greywacke*. Leached quartz- .carbonate bands, minor local Po. Bottom contact at 20 to the core axis.

- 16.5 Ragged argillite-greywacke contact, graded bedding in grey wacke indicate tops are up-hole i. e, south.

MASSIVE GREYWACKE

Grey, fine to locally medium-grained rock has the appearance of alteredleucoxene basalt. Detrital coarser material are grains of quartz, feldsparsand lensy inclusions composed of a light grey, fine-grained material. Rockcontains some minor disseminations of Py S Po, The only other features arenarrow barren quartz-carbonate bands which cross-cut rock near 60 to thecore axis and some small angular inclusions of a finer grained rock in bottom3 metres.

ALTERED GREYWACKE AND MINOR ARGILLITE

Rock is schistose and calcitic to 84 m with minor dark-grey, massive beds ofargillite. This is followed by altered fine-grained greywacke which may bederived from fine volcanic tuffs or ash, rock is more massive than on top ofsection. Some pervasive alteration and discolouration is due to intermittentcross-cutting quartz veins or stringers showing minor Py or Po in the walls.Section shows only minor bedded materials.- 82.0 Schistosity over printing bedding at 700 to the core axis.

94.7 - 97.7 Widely spaced barren quartz stringers and veins, minor Pyin the walls.

Sample No.

W0034H00035 A00036

From

94.795.7 96.7

To

95.796.7 97.7

Lertfih Melm

1.01.0 1.0

AU PPM

NILNIL NIL

1

Page 47: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD tioie NO. 045-04-204...

Shed No...........,3 ............Mttrtf

From

100.00

118.6

119.25

J.

162.0

To

118.6

119.25

162,0

178.8

DESCRIPTION

ALTERED GREYWACKE AND BEDDED ARGILLITE

Altered, dark-grey, fine-grained greywacke with numerous fine-grained argillite interbed*, locally showing ragged contacts. Greywacke contains fragmental inclusions of argillite locally. Minor local quartz stringers and very minor sulphides in the walls.

- 103.5 Narrow well bedded argillite at 300 to the core axis.

- U5.5 Argillaceous greywacke at 400 to the core axis.

QUARTZ VEIN

Grey.massive quartz vein occurs in foliated, chloritic argillite. Inclusions are chlorite and minor Po with very minor Cpy. Upper irregular contact is at 20 and lower is at 65 to the core axis.

GREYWACKE AND ARGILLITE INTERBEOS - AS ABOVE

Fine-grained, grey, massive greywacke, predominating over intermittent finer grained bedded argillite. As above, narrow barren and sericitized guartz veins are seen widely spaced and cross-cutting the greywackes at 60 to the core axis which then would be parallel to schistosity and making their emplace ments a contemporaneous event. Individual greywacke-argillite contacts are from 30 - 40 to the core axis, greywacke near top of section shows numerous inclusions or minor lenses of argillite similar to section near the bottom.

157.6 - 157.95 Grey quartz vein with some minor Py l sericitic near broken contacts. Some quartz sweats in foliated and sericitized rock near 159.0m.

MASSIVE GREYWACKE

Greenish-grey massive rock, detrital grains of quartz and feldspars or very minor lenses of a finer grained pale-green rock. Greywacke becomes dense near the bottom and grades into argillite.

Simple No

A00037

W0038

From

118.3

157.5

To

119.4

159.0

Untiti Metres

1.0

1.5

MM

NIL

NIL

T fc

Page 48: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hole No. ..0.45-Q4- 204..

ShKl No............J...............MrtrnFrom To

578.8 201.0

201.0

j .

DESCRIPTION

GREYWACKE AND ARGILLITE

Interbeds of argillite or numerous Inclusions of argillite in the more massivegreywacke sections down to 196m after which rock is again predominantly massivfgreywacke. Somewhat irregular argil 11 te-greywacke contacts are near 35 to thfcore axis.

- 200.9 Grading In greywacke shows coarser grains downhole, I.e.,tops are south!

END OF HOLE

Sample No. From To l.tnjlh

Mcimr fc

Page 49: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

JCANAMAX RESOURCES INC.

DIAMOND DRILL RECORD HO*NO. .045-04-205.

HokNo. C Property ^To vi. ni hi p H

45-04,205. Sheet ...J.,,,,,..,ell Creek J.v.oy I.e.,.., 36E - 285ON,,. . ............

LoueJ By A.., PHI 1 1 PP . ,, ...,..,,,, ,.,,.,

Core lontion , ...MNR, -. StOFftge ..-... _ .

Rem.rk* Hote 84-205, as In hole

Be.nn, ...ISQ*.......,,..,,....................,

oijectire -To test geology .while,.... perform.} ng.,assessment.,.

con,™^ .....February. J 6. ...1.984......completed .February. ..18, J.984...... Dniiin, co. ..,,S,t..,..lamber.t,,..,,,,....,.CoreSue ,,..B.Q,...,. ,. ,.,,,,,, ,,,..,,.,.,..

,2.04.,d.r.i Lied north, ...encountered .a. steeply, to ..the north, to.,,,..,....,....,.,,.ve.rt.ic^l.ly....d.ipp.ing...sedimenta.ry..seqijence.,0f,greywacke,wittv,a rg 11.1.1 tes.,.....,Nothing,of..., _ .

economic interest was seen.Metro

From

0.00

15.40

24.4

28.5

67.3

92.0

103.4

117.0

138.7

174.3

200.5

203.1

To 1

15.40

24.4

28.5

67.3

92.0

103.4

117.0

138.7

174.3

260.5

203.1

204.0

204.0

D,C,CO,U, . -450Etch Ttii Depth Rdg. True

" " 45 m 41 0" " 89 m 35" " 130 m 30i

...,'L, L.,. ..19Q. m 25"

CASING - OVERBURDEN

MASSIVE GREYWACKE

ARGILLITE-GREYWACKE INTERBEOS - FAULT

MASSIVE GREYWACKE

GREYWACKE AND ARGILLITE

GREYWACKE - MINOR ARGILLITE

GREYWACKE AND ARGILLITE

GREYWACKE - MINOR ARGILLITE

GREYWACKE iARGILLITE

GREYWACKE - MINOR ARGILLITE

SILICIFIED GRAPHITIC ARGILLITE AND GREYWACKE

ALTERED GREYWACKE AND ARGILLITE

END OF HOLE

SimpleNo.

W0039\00040\00041\00042\00043

26.3199.5200.5201.5203.1

27.3200.5201.5203.1204.0

lenjthMelrei

1.01.01.01.60.9

Location Sketch

V

"

11*1*

r'jj\'**

^AUPPM

NILNILNILNILNIL

~/ - V

1

Li

Nonh

1cu N P525306'P525303'"""

Scilc - 1:15,000

AUPPM

NIL

Page 50: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hole No. .045-04-205

ShMl No.............2..............Mtl r**

from

0.00

15.40

24.4

28.5

To

15.40

24.4

28.5

67.3

DESCRIPTION

CASING - OVERBURDEN

MASSIVE GREYWACKE

Fine grained, grey greywacke, massive throughout, very minor inclusions of argillite and then mainly in the bottom Jj. ,

ARGILLITE-GREYWACKE INTERBEDS - FAULT

Fine grained, dark-grey argillite with some narrow greywacke interbeds which dip north. Overprint of schistosity is visible in the softer argillite but no reliable grading features are seen in this section. A silicified and brecciated fault occurs just above the 27 m mark.

24.8 Narrow greywacke interbeds with sharp contacts st 600 to the core axis. Schistosity of foliation - overprint in argillite is from 20 - 30 to the core axis.

26.5 - 27.4 Silicified and sericitized fault zone, brecciation and graphitic beds occur in both walls of actual fault plane occurring at 26.85 m and which is seen crossing core axis at 25 , some weak slickensiding on fault plane is at 45 to the core axis. Greywacke interbeds below this section dip at 55 to the core axis.

28.0 2 cm wide quartz vein at 200 to the core axis. Minor Po i Py in walls.

MASSIVE GREYWACKE

Greenish-grey, fine to locally medium grained rock, some minor, finer grained, argillaceous material which is poorly bedded.

SimpleNo,

A00039

From

26.3

To

27.3

Length Mtlrrt

1.0

AUPPM

NIL

Page 51: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD HOI.NO. ..MM1.-2.P.5...

ShMl No,......,-....?................

MetresFrom

67.3

92.0

-r103.4

To

92.0

103.4

117.0

DESCRIPTION

CONTINUED

-34.5 Argillaceous greywacke at 350 to the core axis.

- 47.0 Quartz vein 20 cm wide, minor inclusions of graphite, chlorite and greenish mica (sericite or muscovite), contacts at 25 4 35 to the core axis respective to upper or lower contacts.

- 53.5 Rock as above, at 400 to the core axis.

- 60.0 Medium grained greywacke at 550 to the core axis.

GREYWACKE AND ARGILLITE

Alternating greywacke and argillite beds, greywacke component is about 70* of total. Minor disseminations of Py or Po on odd slips.

- 68.8 Grading in greywacke shows coarser material downhole. I.e., tops are north, bedding is at 60 to the core axis.

- 76.6 Core angles are 600 to the core axis (Bedding).

- 80,0 Core angles-bedding- from 60 - 650 to the core axis.

81.6 - 82.4 Minor quartz-calci te alteration in fractured greywacke.

GREYWACKE-MINOR ARGILLITE

Greenish-grey, massive greywacke, minor Inclusions or narrow beds of darker grey and finer grained argillite.

GREYWACKE AND ARGILLITE

Alternating greywacke-argillite beds, as above. Greywacke again about 70X of total. Numerous local inclusions of argillite 1n greywacke or vice-versa. Frequent flame contacts into coarse greywacke.

SimpleNo. Fiom To Length

Metres T

t

Page 52: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hoi. No. ..04.5-04-205,

Sheet No. .........A................MetresFrom

117.0

138.7

174.3

20015

To

138.7

174.3

200.5

203.1

DESCRIPTION

GREYWACKE - MINOR ARGILLITE

Fine to medium grained. greenish-grey greywacke, S% for the rest. Gradedcoarser material towards dowhole as in section near 131.3m, i.e., tops facenorth.

GREYWACKE OR ARGILLITE

Alternating greywacke-argillite beds, greywacke about 605! of total. Numerousinclusions of argillite in greywacke, minor irregular quartz-calcite stringers.No sulphides. Local light foliations in argillite.- 140.7 10 cm wide quartz vein, some mica in tight cracks. No sulphides.Upper contact at 30 , lower at 40 to the core axis.- 145.7 Regular sharp bedding at 650 to the core axis.- 152.8 Regular sharp bedding at 600 to the core axis.

GREYWACKE - MINOR ARGILLITE

Alteration as pervasive calcite and greenish mica increases with minor quartz-carbonate stringers. Greywacke is now finer grained and somewhat darker.Narrow bedded argillaceous material comprise about Wi of total but shows anincrease below 189.6 m.

- 192.65 Sharp greywacke - argillite contacts at 650 to the core axis.- 200.20 As above.

SILICIFIED GRAPHITIC ARGILLITE AND GREYWACKEDark-grey and weakly graphitic sections starts with a 10 cm wide barren quartzvein which occurs isolated in altered greywacke.

Sirrtpte No.

A00040A00041ft00042400043

From

199.5200.5201.5203.1

To

200.5201.5203.1204.0

Length Metre?

1.01.01.60.9

pffl

NILNILNILNIL

AU .PPM

NIL

Page 53: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORDHOI.NO. ...0.45-04-205,...Shttl No.......—,-5 .................

MtlmFrom | To

203.1

f..

204.0

204.0

DESCRIPTION

CONTINUED

201.50 - 203.1 Rock becomes stronger graphitic and shows a number of Irregular

quartz-carbonate veins in finer grained argillite. This

section contains about Mi sulphides as fine Po 4 Py plus

occasional grains of sphalerite galena and very minor Cpy.

- 202.8 Orientation of parallel quartz stringers from 450 - 650 to the

core axis. Numerous crenulated quartz seams 1n graphitic rock.

ALTERED GREYWACKE AND ARGILLITE

Top 4 of section contain 1 - 21 of Po 4 Py as very fine disseminations or at

one location: massive in hairline seams. Rock is altered and weakly graphitic.

Bottom ^ becomes fresher greywacke with minor argillite and minor quartz 'L

stringers which show some fine Po in hangingwall.

END OF HOLE

Simple No.

From To Unjlh 1 AU MtllM l PPM — r —

t

Page 54: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD

Hole No. 0.45-04; 206. Stol ,J^...

fo*fuhip ' toy le,., . .

LogjeJ B, ...A.,,PM 1 1 .PP.., ,,,.,,,, . ,,,,.,,core Location , MNR StQr.ase,,.....,.,,,...,.

Remarks ,,

Unrh .. 201 6Q..m........... ______

K * - 450Obuctive To test geology while

performing assessmentwork

Commerced Jet) ™? ry 20 , 1 984 Compitrf February 22, 1984Dniiin,co. ..S.t.,...Lamp,e.rl.....................CoreS,,e ...BO.......... ....,.......................Caiirn Lefl'Lottin Mute NOnfi

Southerly dipping sequences of sedimentary greywackes and argillites were found.Nothing of economic interest was seen

Melrn

From

0.00

29.0

52.5

78.0

128.0

156.30

167.50

176.5

197.75

To

29.0

52.5

78.0

128.0

156,30

167.50

176.5

197.75

201.0

201.0

Di Collar ~^" __ . ____ . - Location Sketch Nonh

Eich Ten Depth Rdt True" " 42m 40JJ" " 81m 35" " 152m 270" 'r 186m 230

,,..,,,,,,, — ,. — ,,,. —— ,,..,,,,,,,,,,,,,,

DESCRIPTION

CASING - OVERBURDEN

GREYWACKE AND

GREYWACKE

ARGILLITE

GREYWACKE - LITTLE ARGILLITE

GREYWACKE AND ARGILLITE

GREYWACKE - MINOR ARGILLITE

GREYWACKE AND ARGILLITE

SILICIFIED GREYWACKE - 20* ARGILLITE

SERICITIZED GREYWACKE - VERY MINOR ARGILLITE

END OF HOLE

-

Sample No

A00044A00045A00046A00047A00048A00049A00050

A00051A00052A00053A00054A00055

Ffom

70.8

71.873.574.575.576.563.2

84.085.086.087.088.0

To

71.873.574.575.576.577.5

164.2

185.0186.0187.0180.0189.0

Lcn|th Metres

1.01.71.01,01.01.01.0

1.01.01.01.01.0

M. L*mm*v

^r.s5,)ft ^

N

AU P PH

NILNILNILNILNILNIL:NIL

NILNILNILNILNIL

AUPPM

NIL

M,l -jtr7-

EJZ —

1ci, So P-525276

scat L:15,000

Page 55: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hoi.No. .045-04-206..

Sheet No..............?.................Metres

From

0.00

29.0

52.5

78.0

128. e*

To

29.0

52.5

78.0

128.0

156.30

DESCRIPTION

CASING - OVERBURDEN

GREYWACKE AND ARGILLITE

Alternating beds of grey greywacke and darker grey argillite both being ofapproximate equal amounts. Hole appears to be going downdip of bedding butfrom graded bedding, tops appear to point south. Core is broken in top 5.5mof section and leaching produced cavities along thin quartz-carbonate bands.- 41.4 Bedding at 350 to the core axis, graded greywacke shows coarsematerial up-hole, i.e., tops face south.- 45.6 Same as above.

GREYWACKE

Fine to medium grained, light greenish-grey rocJe which is genera'\}y massiveor locally poorly bedded. Minor argillite inter-beds. Leached and Irregularquartz-carbonate stringers, some are seen crosscutting bedding. Foliationand bedding is nearly parallel in this area.71.9 - 76.5 Silicified greywacke. Irregular quartz-carbonate stringers orveins, some finely disseminated cubic Py locally to 0 .51. Veins

Simple No

A00044A00045A00046show greenish-white muscovite or sericite micas. W00047GREYWACKE - LITTLE ARGILLITE

Section is composed of about 803! greywacke in to? of section with even lesseramounts of argillite lower down. Some narrow quartz veins or stringers.green mica alteration in adjacent walls, some occasional cubic Py.- 113.7 Minor bedded argillite at 350 to We core axis.

GREYWACKE AND ARGILLITE

Alternating beds of greywacke and argillite, as above. Very minor quartz-carbonate stringers or seams, no sulphides.

H00048W0049

From

70.871.873.574.575.576.5

To

71.873.574.575.576.577.5

Melrn

1.01.71.01.01.01.0

AU PPM

NILNILNILNILNILNIL

i '

t

Page 56: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hole No. ..0.45:04-206.,

Shwl No.............3..............MetresFrom

156. 3C

167.5

176.5

v*

To

167.50

176.5

197.75

DESCRIPTION

CONTINUED

- 133.6 Graded bedding at 520 to the core axis, tops to the south.- 139.4 As above, bedding at 450 to the core axis.- 144.4 Bedding at 350 to the core axis.- 148.7 Graded bedding at 400 to the core axis, tops face south. '

GREYWACKE - MINOR ARGILLITE

Grey, fine grained greywacke, locally massive or with minor bedded argillaceous material. Odd tight fracture showing fine cubic Py.- 163.6 30 cm long Irregular quartz vein, minor Py-Po-Cpy and chlorite in tight fractures, core angles in lower walls are 40 to the core axis.

GREYWACKE AND ARGILLITE

Well bedded argillaceous greywacke with narrow argillite beds, at 450 to the core axis.

SILICIFIED GREYWACKE - 20* ARGILLITE

Widely spaced quartz-carbonate stringers and veins showing affinities for the greywackes which are consequentely sericitized. Locally abundant green micas. Most veins appear to crosscut bedding, some minor cubic pyrite is associated. Widest vein is 30 cm and it occurs at 188.0m.

- 188.8 Bedding in argillaceous greywacke at 550 to the core axis.- 192.0 Bedding at 450 to the core axis.- 196.2 Bedding at 400 to the core axis.

S's7"i F"™

A00050

A00051 AOOQ52 A0005: A0005' A0005E

163.2

184.0 185.0 186.0 187.0 188.1

To

164.2

185.0 186.0 187.0 188.1 189.0

l.enjlhMelm

1.0

1.0 1.0 1.0 1.10.9

. AU PPM

ML

NILNIL NIL NIL NIL

NIL

Page 57: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hoi.NO. 045-04-206.

Sheet No.............i...............Metre*

f tom

197.75

J

To

201.0

201.0

DESCRIPTION

SERICITIZED GREYWACKE - VERY MINOR ARGILLITEGrey altered greywacke, fine to medium grained. Local cubes of Py. Thinsiliceous beds, a few thin quartz-stringers crosscut bedding.

- 200.5 Minor thin argillite beds at 500 to the core axis.END OF HOLE

SimpleNo, From To Length

Metre*-

Page 58: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD HOICNO. 0.4.5-0.1-207...™.........

Hole No. 04

Projxity B e

Locution 4-

Logjed By ' Core 1 oil, K

5-01-207 5tml 111 Creek J.V. Roserphy3m W J ..3....t....50N....................

I.. Philipp n. Hoyle.Camp..S..ite.. ...........

SiliceousRemittl ,. . ...... ....... . .....are on s.trMeirn

From

0.00

37.5

61.0

77.80

90.0

w-

To

37.5

61.0

77.80

90.0

126.0

126.0

carbonate-talc[ke..wi.th...the..a

u ,ft 126.0mBc.nn, 360^

ovcm, IlZJpIt'eiOincrffiocelZ. ,.. ...* long . s.tr i k.e a . _ .........Par' rP.V auriferous^"zone found in hole - ————— -•—83:799"'" --••-••••--••••••l —————————————————————

c~™c- February 23,. 1984CAnofetoc February 24, 1984

-.-..-. ......... _veins occur in a E-W striking komatiitic r-isalt unit and which

urlferpus zone found in hole 199 . Only .ir" -ne r po was seen,

Dip: C

Etch T

oiu, -50"D eit Depth Rag. MXi

50m 44" " 123m 41

33

DESCRIPTION-

CASING - OVERBURDEN

MAFIC FRAGMENTAL TUFF

MASSIVE ALTERED BASALT

FINE GRAINED BEDDED TUFF

ALTERED KOMATIITIC BASALT (TALC-CHLORITE ALTERATION)

END OF HOLE

Sample No

A00056 A00057 A00058 A00059 A00060 A00061 A00062 A00063 A00064

fiom

97.5 99.0

100.0 101.0 102.0 103.0 104.0 105.0 106.0

To

99.0 100.0 101.0 102.0 103.0 104.0 105.0 106.0 107.0

Length Mctrei

1.5 1.01.0 1.0 1.0 1.0 1.0 1.0 1.0

Location Sketch North T

1CU.m No ......... _ .... .....

Sole:

ALT PPM

NIL NIL NIL NIL NIL NIL NIL NIL NIL

AU PPM

NIL

Page 59: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CAXAMAZ RESOURCES INC.DIAMOND DRILL RECORD HOU NO. .M5-0.1..-2.Q7...

ShMlNo.............2

From

0.00

37.5

61.0

77.80

90.0

S.

To

37.5

61.0

77.80

90.0

126.0

DESCBlrTIOX

CASING - OVERBURDEN

MAFIC F3AGMENTAL TUFF

Green, coarsely fragmental tuff, ccerser rarer-fit -:-.c7'.ud2 block-sized clasts of a lighter green basaltic rock in t:? of tVs secir'so. "lasts then become smaller sized and bedded near the Sot ton saving ~ps of 65 to the core axis. Rock is well altered to pervasive cilcite-rrrtor-fca ilts-atlon, quartz-carbonate sweats are coimion and there is seme local irinor "y. Ccr-e is broken and badly leached in intermittent: sections dcwn to 52 TO. (Schistose, sericitized and leached rock).

MASSIVE ALTERED BASALT

Greenish-grey, fine grained basalt, altered and swri*!jr calcitic throughout. Wisps of quartz-carbonite material a '.d sore very ir1 -c r rubic Py. Basalt grades into fragmental rock below.

FINE GRAINED BEDDED TUFF

Green to dark-green rock, few fragrents rear the -^?, locally bedded at 650 to the core axis. Miner quartz-cartcnate sweats. Alteration increases to a mixture of talc-chlori -,s n ear the tetter.

ALTERED KOMATIITIC BASALT (TALC-CHLCSITI AV-T'ATICfi;

Soft, fine grained, dark-green, massive rccr. by- 'jcsd *nth numerous calcitic bands, stringers and sweats, alon.j nith sane quJ-zz ire Ught-green talc. Pervasive talc - chlorite alterat::n is st.-anger -i tre jpper and lower parts of this section.

l

-

Page 60: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX EHSOURCES INC.DIAMOND DRILL RECORD HOI. NO. .0.4.5-0.1-2.07,..

Shut No..........3.............

MelrnFrom ' To

*

126.0

DESCRIPTION

CONTINUED

90.0 - 106.0 Strong talc-chlorlte alteration, irregulir. 30 an l ong calcitic, quartz-talc vein at 99.6 m containing grjfis of pyrrhotite. This vein occurs on strike (dip) with auriferous vein in hole199 which is 58 m to the east. Another -*2fn - 20 cm wide -occurs at 105.6 m but is barren of sulph'icS.

106.0 - 118.1 Massive komatiitic basalt, minor polysufcjring with calcitlc-carbonate fillings. This harder section ;^sies on both sidesInto talc-chlorlte rock.

118.1 - 126.0 Increase of talc-chlorite-calcite contents, is 1n top ofsection. Also as above, rock is soft but cairoetent.

END OF HOLE

Stmplf No.

A00056 A00057 A00058A00059A0006CA00061A00062A00063A00064

From

97.5 99.0

100.0101.0102.0103.0104.0105.0106.0

TO

99.0 100.0 101.0102.0103.0104.0105.0106.0107.0

Length Mnrts

1.5 1.0 1.01.01.01.01.01.01.0

AUPPM

NILNIL NILNILNILNILNILNILNIL

W*

NIL

Page 61: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hoi. No. D45.-01.r208,.

Hole No. 04.5-01-208 , Sheel , .1 ,,,,,,,,,,,.

Property Bel ],,CteBk .,iL V ,. .Rose ,,,,,, Township Murphy,,,,,,.,.,,,,. ... ........... Locnion ...,L375W.Jt90N .

A. Phi H ODCOM: Loca.ion HoyJ e....-'. Camp...Si t.e............

Un tK 1 56H360

Di ' " 500objective fo check an IP anomaly

ari'd g'eolo 6h pre viously unexploredground.

commenced February 27, 1984r0 i, .d Marc h' t, 1984Drilling co. ,St,... .Lambert ..............................Core Size .19,...,....,. ....,.....................................Casing Left/ Lost in Hole ......QPfl.?...........,...............

Remarki A shear zone near the top of hole and a pyrite-mineral ized alteration zone from 135.0 -143.50 metres will account for the IP anomalies

Metres

From

0.0

39.0

45.0

51.0

60.8

75.0

102.0

118.3

122.9

135.0

143.50f.

To

39.0

45.0

51.0

60.8

75.0

102.0

118.3

122.9

135.0

143.50

156.0

156.0

D E S C R 1 P T 1

CASING - OVERBURDEN

.en"

Etch Tesl Depth Rdg if oV

" " 40m -47"11 " 87m -4; u" " 153m -354'

RUSTY WEATHERING TUFFACEOUS BASALT (QUARTZ VEINS)

GREEN ALTERED BASALT

CARBONATED TUFFACEOUS BASALT

GREEN MASSIVE BASALT

OXIDIZED SHEAR ZONE (SOME LOST CORE)

WEAKLY CARBONATED BASALT

ALTERED AND WEAKLY GRAPHITIC BASALT

ALTERED TUFFACEOUS BASALT

MINERALIZED ALTERATION ZONE

WEAKLY CARBONATED BASALT

END OF HOLE

SampleNo.

A00219

A00220A00221A00222A00223

A00224A00225

A00226A00227A00228

A00229A00230A00231A00232

A00065A00066W0067(\00068W0069(\00070A0007 1W0072

41.5

53.054.055.056.1

87.088.0

99.0100.0101.0

120.0121.0122.0123.0

129.0130.0131.0132.0133.0134.0135.0136.0

42.5

54.055.056.157.0

88.089.0

100.0101.0102.0

121.0122.0123.0124.0

130.0131.0132.0133.0134.0135.0136.0137.0

LengthMetres

1.0

1.01.01.10.9

1.01.0

1.01.01.0

1.01.01.01.0

1.01.01.01.01.01.01.01.0

Location Sketch North

I

1

—— — — — —— — — t —— '

AUPPM

0

0

01

01NIL00

0201

NILNIL

NILNIL0

0.

01

01NIL0 08NIL

NIL0.04NILNILNILNILNILNIL

AUPPM

0.02

0.14

NIL

Page 62: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORDHole NO. 045-01-208..SheelNo..........J-.A..........

Metre*From To

DESCRIPTIONSample

No.

A00073(\00074A00075A00076A00077A00078A00079JA00080W00081JA00082

.

A00083A00084A00085A00086A00087

From

132.0138.013'i.O139.9141.0142.0143.0144.1145.0146.0147.0148.0149.0150.0151.0

To

13C.O139.0139.9141.0142.0143.0144.1145.0146.0147.0148.0149.0150.0151.0152.0

Length Metres

1.01.00.91.11.01.01.10.91.01.01.01.01.01.01.0

AU PPM

0.010.020.02NILNILNILNIL0.05NILNILNILNILNIL0.010.01

AU PPM

0.02

NIL

Page 63: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND 'DRILL RECORD Hole No. 045-0.1-206.Sheet No............2...............

MetresFrom

0.0

39.0

45.0

51.0

To

39.0

45.0

51.0

60.8

DESCRIPTION

CASING - OVERBURDEN

RUSTY WEATHERING TUFFACEOUS BASALT (QUARTZ VEINS)

Brown, fine grained, oxidized rock, locally sheared at 650 to the core axis.Rock is soft and badly broken, some core was ground. A 30 cm wide quartz veinat 42 m shows abundant tourmaline or rutile, sericite on breaks, but nosulphides.

GREEN ALTERED BASALT

Fine grained, green, basaltic volcanic rock is altered and broken, it's truenature can not be ascertained. Rock appears to be fragmental.

CARBONATED TUFFACEOUS BASALT.

Sample No.

H00219

A00220A00221

Fine grained, grey and oxidized volcanic rock, some quartz-carbonate sweats or (\00222 veins with pyrite. Calcitic carbonate alteration but centre portion is \00223dolomitic as well. Rock is locally bedded, some altered fragments are alsodiscernible.

53.0 - 54.0 Oxidized, somewhat bedded, carbonated rock at 600 to the coreaxis. Section contains a 10 cm wide quartz vein with a traceof either tourmaline or rutile. A narrow quartz-carbonatesweat with some Py at the bottom.

55.0 - 56.05 Grey carbonate rock containing quartz stringers and a 40 cmalteration zone near the end, showing 25S Py as aggregates,trace of tourmaline. Zone is highly calcitic but carbonatealteration across this section is both dolomitic and calcitic.

From

41.5

53.054.055.0 56.1

To

42.5

54.055.056.1 57.0

I.tn(lh Metrct

1.0

1.01.01.10.9

AU PPM

0.01

0.01NIL0.02 0.01

AU PPM

rt

0.02

Page 64: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORDHoi. NO. 045-01 -208..ShttlNo,,.......3...............

Metres

From

60.8

75.0

102.0

To

75.0

102.0

118.3

DESCRIPTION

GREEN MASSIVE BASALT

Fine grained, green and locally strongly chloritic basalt. Rock shows some

local fragments and becomes carbonated again near the bottom with the

development of some minor Py,

OXIDIZED SHEAR ZONE (SOME LOST CORE)

Fine grained, sheared and carbonated volcanic rock evidently of basaltic origin

Oxidized rock is highly calcitic throughout, strong development of muscovite

mica and narrow barren quartz veins below 99 m. Rock is broken mostly

throughout and some core has been ground in the micaceous sections and as

marked below.

83,0 - '90.0 Brokenand locally micaceous rock, about 2.7m of core was

ground. At 88.5m drillers report a one foot long 'seam 1 .

Section is void of sulphides or quartz veins.

92.3 Shearing at 600 to the core axis.

92.3 - 96.5 As above, brown, oxidized and somewhat foliated rock, calcitic

carbonates and abundant muscovite mica. About 0.5m of core

was ground in broken sections. No sulphides or quartz veins.

99.0 - 102.0 Barren white quartz veins in oxidized carbonated rock.

WEAKLY CARBONATED BASALT

Fine grained, greenish-grey basalt, weakly schistose and carbonated throughout.

Rock is intermittently variolitic down to 117, Om, small varioles have blurred

outlines and are of a light green colour. In addition, rock shows some

occasional large clasts of same light green colour. Orientation of varioles

Or clasts show alignment with schistosity at 60 to the core axis, Pervasive

alteration minerals include calcite, dolomite, chlorite and light green mica,

the latter accounts for the bleaching of varioles and clasts. 2X coarse and

fine Py near bottom associated with carbonate stringers.

SimpleNo.

A00224A00225

A00226A00227H00228

From

87.088.0

99.0100.0101.0

To

88.089.0

100.0101.0102.0

Ltntth Mtlrts

1.01.0

1.01.01.0

AU PPM

NILNIL

NILNIL0.01

AUPPM

T

t ,,

Page 65: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORDHoi. No. 045-0.1-208.Sheet No...............4.............

MetresFrom

118.3

122.9

135.0

*

To

122.9

135.0

143.50

DESCRIPTION

CONTINUED

103.5 Oxidized fracture causes rock to be stained for a 30 cm long section.

ALTERED AND WEAKLY GRAPHITIC BASALT

Fine grained, greenish-grey to dark-grey rocks shows weak but pervasivegraphite and calcite contents. Basalt may be tuffaceous as there are someminor bedded sections dipping at 65 to the core axis. Widely spaced quartz- carbonate stringers or sweats give cause to some coarse aggregates of pyrite Bottom contacts with greenish-grey altered basalt is sharp at 45 to the coreaxis and there is 0.52S fine pyrite associated with quartz-carbonate stringers.

121.1 - 121.3 Quartz-carbonate stringers, some coarse Py.

ALTERED TUFFACEOUS BASALT

Fine grained rock is greyish-green and weakly carbonated (calcitic alterationwith light green muscovite mica). Alteration increases in the lower Jj,minor bedded and stretched clasts begin to appear. There is the odd narrowquartz-carbonate band with some coarse pyrite.

MINERALIZED ALTERATION ZONE

Altered fine grained rock appears to be a tuffaceous basalt. Weak butpervasive graphite alteration gives this rock a grey to locally darker grey colour. Section contains from 5 - IDS Py as fine or coarse cubes. Somefine cubic Py forms streaks of massive Py in association with patches ofmassive brown tourmaline or with white dull quartz veins, containing abundantgrey calcite which is locally coarsely crystalline. (No Aspy or differentsulphides).

Sample No.

A00229A00230 A00231A00232

A00065A00066A00067A00068 A00069A00070 A00071A00072 A00073A00074(\00075A00076A00077A00078(\00079(\00080W0081W0082H00083

From

120.0121.0122.0123.0

129.0130.0131.0132.0 133.0134.0 135.0136.0 137.0138.0139.0139.9141.0142.0143.0144.1145.0146.0147.0

To

121.0122.0 123.0124.0

130.0131.0132.0133.0 134.0135.0 136.0137.0 138.0139.0139.9141.0142.0143.0144.1145.0146.0147.0148.0

Length Metres

1.01.0 1.01.0

1.01.01.01.0 1.01.0 1.01.0 1.01.00.9I.!1.01.01.10.91.01.01.0

AU PPM

O.D1NIL 0.08NIL

NIL0.04NILNIL NILNIL NILNIL 0.010.020.02NILNILNILNIL0.05NILNILNIL

AUPPM

0.14

NIL

0.02

NIL

t

Page 66: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hole No, ...045

Sheet No..rQl, 208,

MetresFrom

143.50

To

156.0

156.0

DESCRIPTION

WEAKLY CARBONATED BASALT

Fine grained, grey and weakly carbonated basalt. Some minor incipient leucoxe ne can be seen locally. Minor quartz-calcite stringers, odd coarse Py orminor fragments.

END OF HOLE

Sample No.

\00084 \00085\00086 \00087

From

148.0 149.0150.0 151.0

To

149.0 150.0151.0 152.0

Length Mflrn

1.01.01.0 1.0

AU PPM

NIL NIL0.01 0.01

1t

Page 67: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD HokNo 045:01-209..

HokNo 045-01 -209 s hCT , 1 ",7pe,,, Sell Creek J.vrfRoserTo*nthip ' Locat.u* L

urphym———--

LoUedB,B. SlairjA.P.)...core uoit.oa . Hpy.l.e...-. ..Camp..!!. t.e.........

jumirki ...Th.e...cor.e.,d.1.d...np.t...pr.oduc,e

u h 2 97A"

t"" :.-5o0::7:.::;:;::::::Objective ...J0 tes.t Jin , '.-.P..'.. ...........,

anomaly while" ob tain i tig a geologicalcross section of the ——————— noic pt-opoi'ty — — —— J —————————————————————

Commenced March 2, 1984completed March 6, 1984D.iii!*, Co S t',... Camber t. .Co.................

.... __ ................. _ ....................

..a., satisfactory.. .e.xplana.tipn...fQr -.the....l,P..,...anQmaly..............................................

Metre!

From

0.0

27.50

279.04

To

27.50

279.04

297.0

297.0

•f-

Dip: Collar ... :.5Q"..NOrth

Etch Ten Depth Rdf. Tru

Add 42m 4j84m 4 1

130m' 4;

eo0'o

195m ' ' ~~'~ • •-—•36"

fropari 239m 3520 360

DESCRIPTION

OVERBURDEN

MAFIC FRAGMENTAL VOLCANIC

ALTERED MAFIC FRAGMENTAL VOLCANIC

END OF HOLE

SampleNo

A00088A00089A00090A00091A00092A00093A00094A00095A00096A00097A00098A00099AOOIOOftOOlOlW0102A00103(V00104\00105\00106\00107

279.0280.0281.0282.0283.0284.0235.0286.0237.0288.0289.0290.0291.0292.0293.0294.0295.0296.0102.0191.75

280.0281.0282.0283.0284.0285.0286.0287.0288.0289,0290.0291.0292.0293.0294.0295,0296,0297.0103.0192.5

LenithMetre*

1.0

1.01.01.01.01.01.01.01.01.01.01.01.01.01.01.01.01.01.01.0

-

Location Sketch North

T

AUPPM

NILNILNIL0.01NILNIL0.02NILNILNILNILNILNILNILNILNILNILNILNILNIL

AOPPM

0.02

0.02

Page 68: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX H2SOURCES INC.DIAMOND DRILL RECORD Hoi.No.P45rO.l-Z.oa.,

Shetl No..,...-.?...,,.,.....,MeHnfiom i To

0.00

27.50

*

27.50

279.04

DESCRIPTION

OVERBURDEN

MAFIC FRAGMENTAL VOLCANIC

Moderately hard, green-grey fragmental unit ts locally luea-JHy carbonated by the influx of small calcite and quartz-carbonate velrs. Carbonate and chlorite have developed preferencially along fractures ard fragment rims. - Fracturing of rock 1s locally prominent and approaches t?-* degree of brecciation. This appears to be due to a late state tectonic event.The core from 27.50 to 76.30 is strongly affected by weathering because It 1s highly fractured so close to the bedrock surface. The consolidation of the rock increases with depth as 76.30 metres is approached.The fragments are lithologically the same as the fine g ra f nad matrix.102.40 - 102.67 Quartz Vein. Milkycoarse grained vein *?th 20!C carbonate and concentrations of chlorite (5 - 715-110.08 - 110.17 Quartz Vein. Dark grey vein cuts thro'jjrs the volcanic rock incorporating a lot of small green volcanic fragments causing an irregular contact within tre jnit.

- 122.0 Lineations at 600

143.83 - 144.22 Quartz-Carbonate Vein. Smokey *hite qus~tz with abundant carbonate having a fragmental texture. :itches of chlorite fill fractures within this vein.

192.10 - 192.30 Quartz Carbonate Vein. Coarse grained ir Iky quartz vein has 5* calcite and 103S dolomite.

From 164.0 there is an Increase in quartz-carbonate veinfrc with the small zones being dark grey quartz carbonate veins having a hlz.- "seal density. There is a slight increase in density of small quartz veils. The fragmental texture of the volcanics still has a flow-breccia type a;c*2rance to it.

Simple No.

WO 106

H00107

From

102.0

191.75

To

103.0

192.75

Unfth Mtlrn

1.0

1.0

AU j PPM

NIL

NIL

Page 69: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hoi. No. ...045-01-201

Shed No.............A...............MtunFrom 1 To

279.04

j.

297.0

DESCRIPTION

CONTINUED

222.2 Orientation of fragments are at 650 to the core axis.242.16 - 242.42 Quartz Vein. Milky white quartz vein with minor dolomite and chlorite. Cpy dominates over pyrrhotite with a total sulphide

content of 3 - 5*.

251.06 - 251.19 Quartz-Carbonate Vein. Smokey grey quartz and calcite vein has a fragmental texture of coarse large sub-angular fragmentsrinmed-'by chlorite. Sulphides are fine grained pyrrhotite(3-4*) and small pyrite blebs (2X) which are predominantlyalong shear planes.

273.67 - 273.74 Quartz Carbonate Vein. Milky white coarse grained calcite(50 - 603!) and clear quartz. No visible sulphides.

ALTERED MAFIC FRAGMENTAL VOLCANIC

Dark grey to dark green-grey, fine grained fragmental volcanic with bleached zones of carbonate alteration. Clasts are sub-angular and are up to 2-3cmin size. Finely disseminated sulphide (1-2*) occur as Py and Po throughout,Upper contact is sharp and at 300 to the core axis. Weakly graphitic bands are perpendicular to the core axis and form black bands.This unit is crosscut by numerous quartz-carbonate veins ranging from mm to

Simple No.

W0088 \00089W0090 W0091W0092 \00093W0094 H00095 U0096W0097cm scale. feaA00099Lineations at 285.50 at 300 . ' POOJOOftooioiQuartz-carbonate veining is more prominent then in the previous unit, with quartz being dominant.H00102 W0103 W0104UJ0105

From

279.0280.0281.0 282.0283.0 284.0285.0 286.0 287.0288.0289.0290.0291.0292.0293.0 294.0 295.0296.0

To

280.0 281.0282.0 283.0284.0 285.0286.0 287.0 288.0289.0290.0291.0292.0293.0294.0 295.0 296.0297.0

l.enflh Mclro

1.0 1.01.0 1.01.0 1.01.0 1.0 1.01.01.01.01.01.01.0 1.0 1.01.0

AU PPM

NIL NILNIL 0.01NIL NIL0.02NIL

.NILNILNILNILNILNILNIL NIL NILNIL

0.01

0.02

Page 70: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD Hole NO. 04.5r.01.-209..

Sheel No............4................Metre*

From

J

To

297.0

DESCRIPTION

CONTINUED

NOTE: Alteration in this moderately fractured unit is caused by chlorite, minor local pervasive graphite, few minor quartz-carbonate stringers (calcite) with very minor local sulphides as described above. Unit is not pervasively carbonated but the calcite content increases in the weakly graphitic sections below 290.5 m.

Core angles given aboye do not reflect bedding angles, some rare reliable beddi.ng angles can be found locally in connection with small clasts, which are oriented from 60 - 70 to the core axis.

END OF HOLE

Simple No. From To Length

Mttrn

rt

Page 71: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

AMAX M INERALS EXPLORATION(A Oiviiioo of A mex of Canada Limited)

DIAMOND DRILL RECORD HOI.NO. 0.4.5-02-.21.Q..Hole No 0' Property OC To*ntnipH( Locution 5'

togged By . Core Locitio

u.Renurkl "P

we

5-02^210. SK* ..I.. ......™ l.l.,Creek..J..V...(Allerstoryle . . . . . . ...,...20N..5292

A7.JPhi"ii"p n,.,Hoyle-

E

p.............................. Camp Site

mineraUzed carbonatedakl.y graphitic rpck at,

Foouge/ MetresFrom

0.00

44.00

50.3

79.3

85.2

147.65

S

To

44.0

50.3

79.3

85.2

147.65

186.0

186.0

Length ...18.6 .0(11,....,.. _ ,...—..,.. __ ....) Boring ,North...O. ...,....,...,.,.......,,.....,,.,cnu

objective Jo , exp 1 Q r e... for.... a, poss i - ,.b.l e, wes tern, extension,,, ..of ...the, Se 1.1. Creek.. Zone , .onto.. Allerstoa ground....

Commenced ..JMe,.r.Ch...7.....1904 ......,..........completed .Warch,,9,,J984,.,,,.,,,..,..

Cor, 5,/e ..BO ................,. ,,,,.....,..,,...,,,,

plastic, pi pes. above..Horizons were located. A narrow alteration zone is related to

34 metres.

D E S C R 1 P T 1

cnO

Az DfEtch Ten Depth Xfcl* J! K.Tropari 54m 353000 -48:::;;::,:.:.:::i)4m--- --;

161m 352V-46

.....,.-32

s0 0- 0

O N

CASING - OVERBURDEN -'

MEDIUM GRAINED BASALT

ALTERED LEUCOXENE BASALT

WEAKLY GRAPHITIC TUFFACEOUS BASALT - NARROW ALTERATION ZONES

ALTERED TUFFACEOUS BASALT

GREEN KOMATIITIC BASALT

END OF HOLE

Simple No

W0191A00192 A00193

A00194

From

82.4 93.4 84.6

158.0

To

83.4 84.6 85.6

159.0

Length

1.0 1.21.0

1.0

Location Sketch North

AU PP

1Claim No. ............. ,., ....

Scale:

M

NIL 1.47 0.02

0.15

PPM

2.26

2ndPHI P

2.13

2ndPill P

1.92

Page 72: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD HOI, NO. ..015-02-2.) Q...

ShMI No...........JLMetre*

0.00

44.00

50.3

79.3

85.2

^

T*

44.0

50.3

79.3

85.2

147.65

OESCRIPTIO-N

CASING - OVERBURDEN

MEDIUM GRAINED BASALT

Pale greenish-grey basalt or andesite. Rock is massive and medium grained.Leaching produced numerous pits and there 1s some broken core in near surface sections. Lower contact with finer grained unit is fairly sharp at 60 to thecore axis.

ALTERED LEUCOXENE BASALT

Rock 1s greenish-grey and fairly massive. Fine altered leucoxene or spheneis locally visible. Numerous thin crosscutting quartz-calcf te veins andstringers, some occasional minor Po. Rock has a fair chlorite content.WEAKLV GRAPHITIC TUFFACEOUS BASALT - NARROW ALTERATION ZONES

Rock 1s fine grained and locally poorly bedded in upper weakly graphiticsection, at 63 to the core axis. Pervasive high calcite content.83.3 - 84.6 Alteration zone, grey cherty quartz-carbonate (calcite) veins,1-2* Py - locally. Section contains some muscovite mica and atrace of either tourmaline or rutile.

ALTERED TUFFACEOUS BASALT

Grey to greenish-grey rock. Alternating massive basalt sections with weaklygraphitic fragmental sections, to 114 metres.

Calcite-chlorlte alteration. Local occurrances of Po S minor Cpy. Widelyspaced barren quartz-carbonate veins and sweats. Massive Po seams with minorCpy at bottom of unit may be the actual contact with unit below.98.0 - bedded fragmental section at 600 to the core axis.105.5 - beds as above, from 55 - 600 to the core axis.

Simple PJo

A00191A00192A00193

From

82.483.484.6

To

83.484.685.6

Length Mtlret

1,01.21.0

AUPPM

NIL!.470.02

AU PPM

2.26

2nd PULP

2.13

2ndPULP

1.92

Page 73: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORD .HOI,NO. .045:02-210.Sheet No................J...........

MclrtsFrom

147.65

S.

To

186.0

186.0

DESCRIPTION

GREEN KOMATIITIC BASALT

Green to dark-green, altered fine grained rock 1s Inherently massive but thereare numerous veins, stringers and patches of calcite alteration with a littlequartz. Rock is fairly soft but competent. Minor local fragmentation due topolysuturlng. Below 158ni this strongly chloritic rock is also weakly talcoseand besides containing some local fragments there is a downhole increase ofbrown to orange-brown biotite or hydrobiotite.

The lithologic bottom section of this hole should nearly overlap with the unitin the top section of hole 83-200, which was collared to the north of 210but not exactly on the same section.

END OF HOLE

Simple No

00194

From

158.0

To

159. C

length Metre*

1.0

AU PPM

0,15

ffo

Page 74: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

AMAX MINERALS EXPLORATION(A Di*t* io d of Area* of Canada Limited)

DIAMOND DRILL RECORDHokNo 045-01-211 shctl 1property Bel L Creek ...J .y. .. BR Pate

Location L60E .,.90H.-.....,.....—..................

The MI Vein Zone occur "*" ' 'wide"area7"""TneTr iridi

U..IK 1 5000mntjt^H . 270" (West!ita~nn, ..,,. :75o,.v...,.....Y................. .

objective ^0 test east dipping'nose' bf MI veinbelow old holes 81-39and 81-41

c d March 10, 1984Combed ,....^rCh,,12.,.l?84,,..,,.....

Dr,iitn. Co s t - LambertCor, Si,. ...JO................... ,................ ....

c.iin, Left/ Lost in Hok ...One. ..leng.th, of.,...J.Q,, casing,,,,,,.,,,,,,.

. as widely spaced 'broken-up' quartz veins scattered over a/idual sulphide contents are rather low. the 8RI vein zone was

ciit as we'll and was found to be well mineralized.Footage/ Metret

From

0.0

4.0

19.3

44.0

52.5

88.7

107.0

119.0

133.0

To

4.0

19.3

44.0

52.5

88.7

107.0

119.0

133.0

150.0

. 150.0

. _

Etch Teit Depth ftd|. True

Trppari.,,,,,60m ,,,.,,, -70" ,281 *00Tropar.i,,,,,l,12m,,,,,.,,-73n,,286"ooT.r.opa r i,,,,, 1 ,50m ,,,,,,, .-650 ..... 298000

.......... — . — ..........,,,.,........,,....... — ,...,...-. — —,,,......,

DESCRIPTION

CASING - OVERBURDEN

ALTERED LEUCOXENE BASALT

CARBONATED BASALTIC FLOW TOP BRECCIA

CARBONATED AND MINERALIZED BROULAN REEF VEIN (BRI Vein)

CARBONATED BASALTIC FLOW TOP BRECCIA

CARBONATED MI HORIZON

CARBONATED MASSIVE BASALT

GREEN PILLOW BASALT

CARBONATED BASALT

END OF HOLE

Sample No

WO 108\00109\00110\ooinV001124001134001144001 1 54001164001 1 7400118

400119

400120400121400122

4001234001 24400125400126400127400128400129

From

43.044.045.046.047.048.049.050.051.052.553.5

64.0

68.569.570.5

87.588.589.590.591.593.094.0

To

44.045.046.047.048.049.050.051.052.553.554.5

65.5

69.570.571.5

88.589.590.591.593.094.095.0

Un,,h

1.01.01.01.01.01.01.01.01.51.01.0

1.5

1.01.01.0

1.01.01.01.01.51.01.0

tocttion Sketch North

1- .

W*

0.191.740. 31.082.340.260.28

.392.150.060.04

0.02

NIL0.040.02

NIL0.570.140.040,014.870.12

AU PPM

2.26

2.19

4.05

2nd PULP

4.53

Page 75: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORDHOI. No. ..045-01:211Shed No.............'' ".............

Metre*From To

,v

DESCRIPTION

*

SimpleNo.

W0130H00131(\00132&00133A00134W0135W50136A00137W0138A00139W0140A00141W014Z

From

95.096.097.098.099.0

100.0101.0102.0103.0104.0105.0106.0107.0

To

96.097.098.099.0

100.0101.0102.0103.0104.0105.0106.0107.0108.0

Length Metre*

1.01.01.01.01.01.01.01.01.01.01.01.01.0

ft.

NILNILNIL0.100.430.500.040.610.070.010.071.590.02

&UPPM

2.00

pSr? ft

Page 76: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD

HOI. NO..,9.45-01-?.1LShttlNo................?...........

MelrrtFiom

0.0

4.0

19.3

44.0

J,

To

4.0

19.3

44.0

52.5

DESCRIPTION

(HOLE WAS DRILLED DUE WEST)

CASING - OVERBURDEN

ALTERED LEUCOXENE BASALT

Greenish-grey massive basalt, chlorlte-calcite alteration. Minor quartz -carbonate stringers with a little pyrite. Bottom contact 1s sharp at 30 tothe core axis.

CARBONATED BASALTIC FLOW TOP BRECCIA

Grey, altered fragmental rock becoming progressively stronger carbonateddownhole showing some sporadic cubes of pyrite and minor quartz-carbonatebands or sweats. Calcitic carbonate alteration. Minor tight oxidizedfractures near bottom.

CARBONATED AND MINERALIZED BROULAN REEF VEIN (BRI VEIN)

This 1s the old Broulan Reef vein which is being intersected for the firsttime by Canamax drilling. Vein material is spread-out over a wide areawhich 1s due to the fact that the drill hole is not cutting the vein atright angles.

This mineralized vein zone is a grey carbonated and fragmental unit, Inter mittently silicified, pervasive hydromuscovite mica occurs throughout,carbonate alteration is now dolomitic. Entire section contains 2-33S pyriteand local appreciable very fine Aspy. Pyrite occurs in aggregate - or cubicform, subhedral Py in snowflake crystal clumps. Fractured sections arestrongly oxidized, some vein material was ground near 48 m.

44.0 - 44.7 Silicified section, fine Aspy and some tourmaline near the top.

44.7 - 46.2 Grey carbonated rock, minor quartz-carbonate sweats, 0 - 5Xfine snowflake pyrite.

46.2 - 46.9 Strongly oxidized section with 30 cm wide quartz vein, carbonat ed minerals in the vein are oxidized.

Simple No.

A00108A00109A00110WillA00112 A00113

From

43.044,045.046.047.0 48.0

To

44.045.046.047.048.0 49.0

Length Mtlrei

1.01.01.01.01.0 1.0

AU PPM

0.191.740.131.082.34 0.26

2.26

Page 77: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORD Sheel No.

045-01-211""""""3"""""""-— -. . ,. ......................................^

MetresFrom 1 To

52.5

88.7

**"

88.7

107.0

DESCRIPTION

CONTINUED

Simple No

A00114A00115

46.9 - 48.4 Carbonate rock with some Aspy near top hosting a grey quartz-ftOOl 16carbonate vein below 47.5 m. Section from 47.7 - 48.1 mconsists of loose pieces of quartz and wallrock materialwhich could have come out of a cave.

48.4 - 50.0 Well carbonated rock. IX Py, some fine subhedral Py insnowflake form.

50.0 - 52.5 Main mineralized section, quartz-carbonate veins and sili cified rock. Fairly abundant Aspy down to 51.8 m, coarseraggregates of Py from 2 - 3i. Minor local tourmaline.

CARBONATED BASALTIC FLOW TOP BRECCIA

Fine grained, grey carbonated fragmental rock. Some local narrow quartz-carbonate stringers or sweats giving rise to some disseminated fine Py andvery minor Aspy. Pervasive dolomite carbonated alteration and fine greenish-white hydromuscovite. Schistosity angles at 83.5m are 25 to the core axis.

CARBONATED MI HORIZON

The actual MI vein appears to occur at the top of section but the entiresection will be sampled as there are some sporadic quartz veins with minorPy at different locations, therefore, any Au mineralized branch-veins may getpinpointed by assays. The dolomitic carbonate alteration with pervasive micadevelopment extends nearly to the bottom of this section where it is replacedby calcitic alteration. This in Itself usually marks the end of any mineral ization.

88.7 - 89.3 Strongly foliated quartz-ankerite vein, abundant mica, seamsof massive brown tourmaline or rutile (?) 1 - 2 H, Py andminor Aspy.

89.3 - 106.0 Carbonated flow top breccia, few sporadic quartz-carbonatebands or sweats, minor coarse aggregates of Py at random locations or fine subhedral Py in snowflake clumps.

W01 1 7won 8

won 9WOl 20toOl 21100122

to0123to0124100125toOl 26toOl 27100128toOl 29100130to01311001321001 33to0134toOl 35to0136100137100138toO 139 100140

From

49.050.051.052.553.5

64.0

68.569.570.5

87.588,589.590.591.593.094.095.096.097.098.099.0

100.0101.0102.0103.0104.0 105.0

To

50.051.052.553.554.5

65.5

69.570.571.5

88.589.590.591.593.094.095.096.097.098.099.0

100.0101.0102.0103.0104.0105.0 106.0

Untlh Metres

1.01.01.51.01.0

1.5

1.01.01.0

1.01.01.01.01.51.01.01.01.01.01.01.01.01.01.01.01.0 1.0

AUPPM

0.281,392.150.060.04

0.02

NIL0.040.02

NIL0.570.140.040.014.870.12NILNILNIL0.100.430.500.040.610.070.01 0.07

AU PPM

2.19

4.05

2ndPULP

4.53

Page 78: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORD s™,', NO.'MtliH

From ] To

107.0

119.0

133.0

119.0

133.0

150.0

150.0

DESCRIPTION

CONTINUED

106.0 - 106.3 Quartz-carbonate vein, 3X sulphides as fine Aspy and coarseaggregates of pyrite.

CARBONATED MASSIVE BASALT

Grey, fine grained to medium grained basalt, weakly schistose, decreasingintensity of carbonated alteration downhole, bottom area of carbonatedalteration seems to co-1ncide with change of rock type, from altered leuco xene basalt to a finer grained green pillow basalt.

GREEEN PILLOW BASALT

Green, fine grained basalt, rock is chloritic and weakly fragmental. Oddcoarse Py-aggregates in chloritic pillow selvages. Rock again becomescarbonated near the bottom of section.

CARBONATED BASALT

Carbonated fragmental basalt near the top becoming darker grey and possiblytuffaceous from 140 m to 144 m. This section shows a light pervasivegraphite - and strong calcite content. Some crosscutltng quartz-carbonatebands and minor Py. Below 144 m rock is lighter grey but still carbonated.Calcitic carbonate alteration.

END OF HOLE

Sirnplt No.

A00141A00142

From

106.0107.0

To

107.0108.0

Ltnjlh Mrtres

1.01.0

AUPPM

1.590.02

-AUPPM

2.00

45-01-211•••-4—————

j

Page 79: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

EXPLORATION^ctfiada Limited)

DIAMOND D?-HL RECORD MS-PI-?!2..

Hok No l Ptopcny .f

Towmhip ^

Location .L

45-01-212 1ell. Creek J. Y., ...... oyle..... .,............ _ ....................60E, 60K ......,.........................

coKLoJiioa Hoyle - camp site

i.,..,. 153A01Z-, "276* {West)—-- —DIB "75Objects — To t es t..the ...nprth-

striking and eastdipping MI Vein Zoneon 6R gYound.

cr-n ' ~ \ -* ~ ~- "^ "i ength of^ ess - Tir

- -This hole found a well mineralized MI vein zone showing sore 'tfS imd ibtxcam ispy -

Remark. .... .... ,. .- ... .. ...... ......,........^. -. - ^"' ••••r^-- nn1 -- ^•t -^~-l 'Sf ---?-lt^ t^*-^ .^* f!""^ **^-a 1 *— 9-^ uoll.. much improved, o ver.Jio] e..

FooiifCi Meiret

From

0.00

3.00

9.0

11.2

57.0

76.8

82.0

87.7

102.0

To

3.0

9.0

11.2

57.0

76.8

82.0

87.7

102.0

153.0

153.0"^

Dip: ColUr ...'J.'. ___ . ___ ....

Etch Ten Depth Rdf.

Troparl 42m -71...,,,,..............V53( ......,.,.....74o......

True281 000'

' 300000' 305000'

J........... ......... . (w.ll.l..no.t . t?e...used) ...,. .......

DESCRIPTIOX

CASING - OVERBURDEN

CARBONATED BASALT

BROULAN REEF VEIN ZONE (BR-!) - MINERALIZED

GREY CARBONATED PILLOW BASALT (Some fragments*

CARBONATED BASALTIC FLOW TOP BRECCIA

CARBONATED AND MINERALIZED MI VEIN ZONE - VG

WELL ALTERED FOOTWALL BASALT

CARBONATED FLOW TOP BRECCIA

CARBONATED BASALT

END OF HOLE

Sample

A00143!A00144A00145 A00146A00147 A0014EA00149 A001 5CA00151 A00152A00153 A00154

A001 5E

AGO l SeA0015/ A001 5EA0015! A0016CA00161Aooie;A0016:A0016'A0016!A0016EA0016/A0016f

3.04,05.0 6.07.0 7.99.0

10.011.2 12.013.2 14.2

64.9

70.371.8 72.873.8 74.875.876.878.079.080.081.082.083.0

4.0 5.06.0 7.07.9 9.0

10.0 11.212.2 13.214.2 15.2

65.9

71.872.8 73.874.8 75.876.878.079.080.081.082.083.084.0

1.01.01.01.00.9 1.11.0 1.21.0 1.01,0 1.0

1.0

1.51.0 1.01.0 1.01.01.21.01.01.01.01.01.0

Location Sketch North

1

Scale:

AUPPM

0,01NILNIL NILNIL NIL1

120 0

09 3403 03

0.49 0.06

0.40

0.090 00 0032007.0.0.

360212 061470262295540201

AUPPM

13.92

3.00

7.68

2ndPULP

14.3;

7.23

T

Page 80: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

iHlC2S INC.RECORD

Hoi. NO. .04.5-01-212...Shett No.........J :.A__......

Mtlin

'

DtscatirTso 1*-

'

'

,.•'

TrUJ0169\00170V00171\00172\00173

\00174\00175\00176\00177\00178

W0179\00180W0181W0182W0183M) 184l\00185A00186^00187100188100189

WO 190

84.085.086.087.088.0

94.596.097.098.099.0

111.7112.7113.7114.7115.7117.0118.0119.0120.0121.0122.1

131.6

85.086.087.088.089.0

96.097.098.099.000.0

12.713.714.715.717.018.019.0

120.0121.0122.1123.0

132.6

VI el r e*

1.01.01.01.01.0

1.51.01.01.01.0

1.01.01.01.01.31.01.01.01.01.10.9

1.0

PPM

0.160.030.33NILNIL

0.020.070.030.07NIL

0.040.03NILNIL1.84NILNILNIL0.010.09NIL

0.19

PPM

0.06

1.41

lt

Page 81: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD HOI.NO. ...Q4.5-ON21.L

Shetl No.............2._...;.,.M* (r rt

From

0.0

3.0

9.0

11.2

To

3.0

9.0

11.2

57.0

DESCRIPTION

CASING - OVERBURDEN

CARBONATED BASALT

Grey, fine to medium grained massive basalt. Some oxidized sections relatedto leached carbonate minerals and fractures. Harrow tj-jartz-carbonate veinsor sweats showing some coarse Py in aggregate-form.7.9 - Alteration is becoming more intense showing good developments ofhydromuscovite mica, shicstosity planes are almost parallel to the

Simplt No

100143AQ0144core axis. ' W00145M0146(MINERALIZED) 8ROULAN REEF VEIN ZONE (BR-1) W00147JW0148Grey schistose zone, oxidized In 0.6m long upper secf'rm as zone intercept (A00149was still relatively close to surface. Calcite-dolom:^3 carbonate alteration, JA00150pervasive greenish-white mica, quartz-tourmaline vein iid about 83! sulphides A00151as Py and fine Aspy, mostly throughout. Upper vein cc-^tact Is in broken core, W00152lower contact is as a gradually diminishing quartz conant. JAOQ153

9.0 - 9.8 Oxidized section, narrow quartz vein near top 1s broken and someOf it was ground. Foliation is subparaTIal to core axis. 2J!Py occurs as aggregates or as fine cryswl clumps in 'snowflake 1form.

9.8 - 11.2 Best mineralized section, top 70 cm long silicified sectionshows abundant brown tourmaline at tr.e beginning,. 8 - 9X Py and fine Aspy throughout. Schistosity angles are 30 to the coreaxis.

GREV CARBONATED PILLOW BASALT (SOME FRAGMENTS)Rock is fine to medium grained. Carbonate alteration i~ccnes calcitic.Occasional quartz-carbonate sweats showing spotty pyrira. Some fragments arelocally discernible.

WO 154

From

3.04.05.06.07.07,99.0

10.011.212.213.214.2

To

4.05.06.07.07.99.0

10.011.212.213.214.215.2

I.tnich Metres

1.01.01.01.00.91.11.01.21.01.01.01.0

Au "PPM

0.01NILNIL*NILNILNIL1.09

12.340.030.030.490.06

•AU"PPM

13.9!

2nd PULP

14.33

i ———— f t

Page 82: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CJLKAMAZ H -SOTTRCES INC.DIAMOND DRILL RECORD Hole NO. .045-0.1-2.1.2...

Sheet No................3.............Metre!

From 1 To

57.0

76.8

76.8

82.0

v'

DES-CRIFTIO*

CONTINUED

18.6 5 on wide quartz-carbonate vein iriih 1=1 r-j slfrnfti -im dip of schistosity at 30 to the core axis.CARBONATED BASALTIC FLOW TOP BRECCIA

Grey, fine grained carbonated basalt, alteratfcm iooreiSBS arc; so does thenumber of quartz-carbonate sweats and stringers oiln CTJS itsaaT coarse aggre gates of Py. Some quartz-carbonate- tourmaline fs'^s t^cstr ieTx 71.9m.Carbonate alteration is a mixture of calcite and cfaloitl^a- Clists are of agreenish-tan colour as they are strongly altered ra hj-ir-sraiscc-i-i te mica.61.7 dip - angles of schistosity including quans-s^r^mpers i. iO0 to thecore axis.

65.0 - 66.0 Strongly altered and foliated serrfsn. riiii^tr -carbonate(dolomite) stringers and n*sats- 2.51 ?y s verall.70.3 - 76.8 Increase in the number of q-jartr-caricra-t^ vaf.-s and stringers,strong local hydromuscovite nict s'^anifDn i.-d j? to 2X Pyover narrow intervals. This secrricra f re T Kies a 30 cm widequartz-carbonate-tourralire veirr s. 72 n trc 5 veil altered10 cm wide zone containing lOi ?-jr i.ii 31! *3. 5- ?*-Jm.

CARBONATED AND MINERAL IZEO MI VEI.'I ZONE - VGThis intercept found the zone to be well e^erec. s*ix-'-?' z ric-er upper0.5m wide quartz vein section with VS and 3 l ower s;T-c1f* *2 sscVen withrelatively abundant Aspy.76.8 - 77.4 VG-quartz-ankerite vein, seams c- io.-mai '-ne. s^ sulphides asfine Aspy in bluish-grey cjoonaiK rrcc •'-^jner^s and somesubordinate Py. About 10 fine S;*KCS :r '."3 c-cc:-' 3-0 cm belowtine top in smokey quartz near saams :f -^linre'-.Te ir/d greenish-white hydromuscovite itica.

Simple No.

A00155

A00156A00157A00158A00159A00160A00161

W0162A00163A00164A00165WO 166W0167WO 168W0169\00170\00171\OOI72W0173

From

64.9

70.371.872.873.874.875.8

76.878.079.080.081.082.083.084.085.086.087.088.0

To

65.9

71.872.873.874.875.876.8

78.079.080.081.082.083.084.085.086.087.088.089.0

Length Metres

1.0

1.51.01.01.01.01.0

1.21.01.01.01.01.01.01.01.01.01.0.1.0

AUPPM

0.40

0.090.360.020.120.060.14

3.702.260.220.957.540.020.010.160.030.33NILNIL

AU PPM

3.00

7.68

2ndPUIP

7.23

*

Page 83: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD H.l. No. .04.5-01.-.?.!.?.

Sheet No........4.....................Metret

From

82.0

87.7

102.0:

To

87.7

102.0

153.0

DESCRIPTION

CONTINUED

77.4 - 79.0 Well altered section, quartz-carbonate-mica veins. Sectionends with a 30 cm wide foliated quartz-ankerite vein containingabundant yellowish-green mica and some brown tourmaline.Overall Py is from 2 - 3*, minor local Aspy.79.0 - 82.0 Well carbonated and altered rock. Pervasive quartz-ankerite-mica contents. About 8* very fine Aspy and S-4% Py. Sectiongrades into unmlneralized carbonated rock.WELL ALTERED FOOTWALL BASALT

Grey carbonated and locally silicified basaltic flow top breccia, as abovepervasive dolomitic carbonate alteration and yellowish-green mica especiallyin altered fragments. Isolated occurrances of Py.

CARBONATED FLOW TOP BRECCIA

Grey to greenish-grey carbonated fragmental basalt, as above. Pervasivedolomitic carbonate alteration, mica and thinquartz-carbonate stringerslocally with some pyrite. Lower boundary with calcitic carbonated basaltis perceiveable through a subtle change of colour.

96.35 - 96.85 Alteration zone with quartz-sweats at 450 to the core axis.5-6? disseminated Py, some oriented in streaks, some fineAspy.

98.4 - 98.9 Quartz-carbonate alteration zone. St f ine Py and Aspy.CARBONATED BASALT

Grey, fine grained carbonated basalt Is more massive than unit above but somefragments are still present in the upper part. Carbonate alteration 1s nowpredominantly calcitic. Sections of rock are locally cut by quartz-calclteveins with the usual Py associations and also some local fine Aspy. Alteredleucoxene is conspicuous below 133m. Sporadic occurrances of quartz-carbonate material are present right to the end of hole.

Sample No.

A00174WO) 75H001 76W0177H00178

W0179WO 180W0181W0182H00183W0184W0185WO 186

From

94.596.097.098.099.0

111.7112.7113.7114.7115.7117.0118.0119.0

To

96.097.098.099.0

100.0

112.7113.7114.7115.7117.0118.0119.0120.0

Length Metret

1.51.01.01.01.0

1.01.01.01.01.31.01.01.0

AU PPfL

0.020.070.030.07NIL

0.040.03NILNIL1.84NILNILNIL

AUPPM

0.06

0.41

Page 84: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CAXAMAX H2SOURCES INC.

DIAMOND DRILL RECORD 045-01-21?Shwt No. ___ 5

MclrnFrom i To

153.0

f.

DESCRIPTION

CONTINUED

111.9 - 122.1 VG-intermittent quartz-carocr-a-is [calc'is) veins and alteration zones containing rone pyr-:-^ j.r.d local Aspy. A 15 cm wide cherty quartz-circo-ate vein * -. 1 16.8 m . Contains 1 speck of VS. pyrite i-*vj sesus :f very fine Aspy. Fair hydromuscovite aica is pressnt.

132.1 - 132.5 Quartz-carbonate alta ri 3 ere Tore, ninor 9y, t race of tourmaline and Aspy.

END OF HOLE

Simple No.

W0187 UJ0188 \00189

\00190

From

120.0 121.0 122.0

131.6

TO 1 V;"1"1i Mttrn

121.0 122.0123.0

132.6

1.0 1.01.0

1.0

AUPPM

0.01 0.09NIL

0.19

AUPPM

;:

ii| lili

1

t.

t

j1j

i

I

j

Page 85: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD note NO. .045.-01.r2l3..

Hole So. 045*01,213.. Sheet ....1............. ...Piopcny 6TooruhipH L(xinon Li

5l.l-Creek...J..V..(Wetflior.e).. 3vle^j t *. ....-...........—M™.....-.................... }OOE,...225N.................................. .

A. PhilippCoic Loijnon ... -.. .. ........... .^................... ...... .. ...

Bc*rini 360 North

Objcctwe To test HEM anomalywith flanking IPanomaly

Rcii,4.n intermittent narrow graphitic argillite beds will account

Commenced ........March . .1 4 ,.J 984. ... .....

OriiiiniCo St. Lambert Co. . ....Core Siie ........BQ...,...,,.,............,,,......,.......,.

for the HEM anomaly. Mainconductive .section... i s... from 58.8.- 70- Om. . . . ....... ..... . .... ........ . ........... ........... .... ...

Mciie.

fun,

0.0

43.?

117.0

To

43.2

117.0

162.0

162.0

j.

en" ^f Dip. ColLi ..".T;*........................................................ Location Skttch Noun

Etch Tot D

Tropari" 1

epth

55m OOiii'"""

152m

Kd|. Tru

-48^ 356^0C -40"""""358^0C

-43 360 OC

e)' )' )'

Acid test, at J 00. m..,. ,,...,. ,...,,,. ,....Cuii

\

i No . . ... ... .

Si. J 1C

CASINGS - OVERBURDEN

GRAPHITIC ARGILLITES AND GREYWACKES

GREYWACKE AND

END OF HOLE

MINOR ARGILLITE

SjniplcNo.

i\00208

A00209A002IO JA00211A00212

A002I3^00214A002I5i\002 ! 6A002 1 7A00218

68.8

87.908.9 89.9

101 .7

111.0112.0113.0114.01 15.0116.0

70.0

88.989.9 90.9

103.6

112.0113.0114.0115.0116.0117.0

LengthMcnei

1.2

1.01.0 1.01.9

1.01.01.01.01.01.0

AUPPM

0.07

NILNIL 0.09NIL

0.030.140.100.140.190.09

AUPPM

0.15

.

Page 86: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.DIAMOND DRILL RECORD

Hoi,NO. ,P45-0)-213.Shed No...... .....2 .

Metre*From To

0.0

43.2

.

43.2

117.0

f..

DESCRIPTION

CASINGS - OVERBURDEN

GRAPHITIC ARGILLITES AND GREYWACKES

Numerous alternating beds of dark grey, thinly bedded argillite with greywacke.Argillite beds predominates in the upper part. Bedding angles face north, i.e.drill hole is going down-dip. Rock is broken mostly throughout. Leachingproduced numerous pits. Occasional cross fractures show cubes of pyrite alongfracture planes. Sections containing quartz stringers or veins were check-sampled, their locations are recorded below. Locally, greywacke graded into asofter foliated mudstone showing numerous crumpled quartz-carbonate bedswhich often contain minor Py and locally some specks of sphalerite. Bedded andweakly graphitic argillite become subordinate to greywacke or mudstone,downhole.

61.0 - 63.0 Greywacke-argillite interbeds from 30 - 400 to the core axis.66.0 - Interbeds as above, at 35 to the core axis.

68.8 - 70.0 Main conductive section as being a foliated graphitic mudstonewith greywacke fragments and seams of pyrite.

78.0 - 88.0 Local foliated section, rock appears to be an argillaceous mud.Bedding in less deformed section at 87.0 m dips at 30 to thecore axis.

68.0 - 90.6 Numerous leached calcitic quartz veins or stringers crosscuttingbedding. Widest vein is about 2 cm. These veins may containsome fine Py and odd coarse speck of sphalerite.

101.7-103.6 Quartz-calcite veins in a calcitic mud or greywacke. Minor Py.Bottom vein contact is sharp at 55 to the core axis, againstgraph) tic a rg i l li te.

107,5-117.0 Softer, crumpled calcitic greywacke or mudstone, as above. Thinfoliated fine Py and occasional speck of sphalerite. Rock isvery broken near top of section.

SimpleNo.

W0208

\00209i\002!0\00211

W02I2

\00213\00214\00215\00216\002 1 7\00218

From

68.8

87.988.989.9

101.7

111.0112.0113.01M.O115.0116.0

To

70.0

88.989.990,9

103.6

112.0113.0114.0115.0116.0117.0

l.enjih Milrt*

1.2

1.01.01.0

1.9

1.01.01.01.01.01.0

AU PPM

0.07

NILNIL0.09

NIL

0.030.1 '10.100.140.190.09

AU PPM'

0.15

t

t

^p

Page 87: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC.

DIAMOND DRILL RECORDHUU NO. 045-01 : 213Sheet No. ..............L..........

Mrirck

Fi o m To

117.0 162.0

162.0

v'

DESCRIPTION

GREYWACKE AND MINOR ARGILLITE

Fine grained, greenish-grey greywacke becoming massive and harder locally.

Minor narrow crenulated beds of weakly graphitic argillite. Greywacke will

grade to crumpled calcitic mud sections as above, showing fine pyrite and

occasional specks of chocolate-brown sphalerite in crenulated quartz-carbonate

beds or stringers. There is much broken core,

126.5 - 129.0 Some interbedded crenulated argillite beds from 40 - 500 to the

core axis. These beds are granitic and contain minor Py.

130.0 - Fair sphalerite as specks and seams in harder greywacke.

134.0 - 145.0 Grey calcitic greywacke or mudstone. Numerous crumpled quartz-

carbonate beds, as above. Minor local fine pyrite or sphaleri

te, like at 139.3m. Much broken core.

153.1 - Coarse specks of sphalerite along quartz-carbonate stringers

in harder and more massive greywacke.

160.0 - 162.0 Narrow weakly graphitic argillite beds from 40 - 450 to the

core axis. Section is silicified showing crosscutting quartz-

carbonate veins, some thin veins are conformable with bedding.

Minor Py.

END OF HOLE

SimpleNo.

Krum To l.tii(ihMcllei

. — - — . —— —

tfc

w^

Page 88: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAH

APPENDIX C

DRILL SECTIONS

Page 89: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

SUMMARY OF BELL CREEK UNDERGROUND EXPLORATION PROGRAM

To Accompany 198fr OMEP Submission

INTRODUCTION

The objective of the Bell Creek underground exploration

is the in situ examination of the 'A 1 horizon of the North

Zone on four levels. Current plans call for drifting on the

drill*-indicated economic portions of the deposit on the 60,

120, 180 and 240 metre levels, and raising between the

levels. A sampling regime consisting of a combination of

face, back and muck samples will be used to compare grade, and

thereby determine the economic viability of the deposits.

WORK COMPLETED

In May 1984 a contract was awarded to Patrick Harrison

and Company to erect a mining plant, sink the shaft to 260

metres, cut stations on four levels and carry out certain

specified lateral work. The contractor commenced work in

3une. Copies of Progress Reports from R. MacPhail P. Eng. are

attached along with a graphic presentation of the actual

versus the proposed work schedule. Photographs showing

changes at the site between November 1983 and November 1984,

as well as the surface plant are attached.

Page 90: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

r-2-

COMMENTS

The Bell Creek underground program is proceeding on

budget but is somewhat behind schedule. An irregular bedrock

profile in the area of the service building resulted in more

rock work than was anticipated. This coupled with a late

start and a delay in delivery of the prefabricated building

resulted in a two month set back in the planned work

schedule. Barring unforseen delays it may be possible to make

up some of the delay during the sinking and crosscutting

sequence now in progress.

Toronto, Ontario /C/P

March 11, 1985 R.A. Knutson

Page 91: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

SHAFT SINKING, MINE DEVELOPMENTAND

CONSTRUCTION OF ANCILLARY FACILITIES

WORK SCHEDULEPREPARED FOR: CANAT'iAX RESOURCES INC.

- BELL CREEK PROJECT CONTRACT No. 3045-84-01

ACTIVITIES

MOBILIZATIONSiTE" •ptR.u; PPv^RTiONj

SURFACE INSTALLATION S SHAFT COLLAR

SHAFT SINKING

STATION S BROW POCKET EXCAVATION C/W

/9

,|t

SK

ALL MECHANICAL INSTALLATIONS;- J

- 60 IrvEL 1- 120 LEVEL S- 180 LEVEL

240 STN. EXCAV. X MECH. INSTALLATION

CHANGEOVER

LEVEL DEVELOPMENT SIMULTANEOUSLY ONALL 4 LEVELS

DRIVE OREPASS RAISESSURFACE VENT RAISE COLLAR EXCAVATIONRAISEBORE VENT RAISE

INSTALL ESCAPEWAY IN VENT RAISE

MECHANICAL INSTAL.OF ALL VENT. EQUIP.

ELECTRIC INSTALLATIONS

DEMOBILIZATION

fcSS

Ei 14

22?*

tM fsv x^

1

li

W

'i/sTc D

~5c.pl"- . OeTf- ilb

^

J5 K 17 t a 2D 21 2

*y

1

Woo. , !D(?c. ,23

B

K. Z Z W a a z a

I

D

l

ffANl. FX 9 s. B

ea

ww vw

B

a*

re.

OS

•ON

Ba

T

B

s E K a

•B*

n

5- f

•H

1

K r

•a

s

i

s

•a

t

c c c

64^

"f- a tt

\

1

P \ o. rv r-\ e. d i ^

A otucx l VlH

PREPARED BY: PATRICK HARRISON 8 CORPAKY LIMITEDDATE : TAY UlTH, 198*1

Page 92: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past
Page 93: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

1*1

,ir

in nCy^^l

Bell Creek-Section L ooking East

Page 94: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

•IP

Page 95: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

f^CANAMAXc^RESOURCES INC.SUITE 1100 - 181 UNIVERSITY AVE., TORONTO, CANADA MSH 3M7

TO:

JAM

C ' ' '

1 1 (* ST sot)

Fred Johnston S

FROM: Ross MacPhail

SUBJECT: Progress Report for Bell Creek Project

Date: December 31 , 1984

During the month of December development of the Bell Creek Project, Company Limited, was as follows:

MEMORANDUM

DATE:

... f- r...

. H W S

1984 the work on the by Patrick Harrison and

MINE HOIST: The brake paths were precision ground and the new..... wooden brake shoes were arced to fit. The hoisting ropes can be installed as soon as the L... Lilleys are calibrated and after the mine inspector and hoist consultant have the brake deceleration :c readings to their satisfaction, hopefully by January 3rd.

. T:M ........., V A.'.'C ......__

ELECTRIC POWER: The electrical sub-contractor and his crewhave spent all of the month of December installing the hoist and hoist signal electrics. Throughout most of this time they worked on two shifts, 5^ days per week. Patrick Harrison and Company Ltd. have installed their two Sullair, screw-type, compressors and augmented the 600 volt power supply by installing a 500 K.V.A. dry transformer in the shop area. Even since it was energized, our used 1000 K.V.A., 2400 to 600 volt, transformer has emitted a loud vibration hum and .we may have to have the supplier replace this unit.

The electric cables for the yard lighting, the parking lot, the ventilation raise and the industrial water pump have been buried on surface, but none of these facilities have been completed.

SERVICE BUILDING AND ACCESS TUNNEL_______________ The shower and toilet facilities are complete and the hoistroom and the permanent office are finished. The contractor has erected a temporary wall to separate the miners' clothes dry from the shop area and enclosed an office space for his clerk and engineering technician

Page 96: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 2 -

All of the propane heaters and one of the three electric floor heaters are operational. Most of the permanent lighting panel is connected, and when the light fixtures are delivered and installed, the service building construction will be finished.

In the access tunnel the lights, doors and heater are installed and all of the electric lines and the various pipe lines have been run and connected. A second pair of cable portholes had to be put in the wall when we learned that there was only one cable attachment hole in each hoist drum.

HEADFRAME: Except for the east side of the headframe tower, all of the painted steel cladding is in place. The roof and all four walls are cladded on the upper portion of the penthouse. Until the shaft bottom has been sunk another 80 to 100 feet, the east wall of the tower will remain open to allow for the blasting percussion. The ore slide above the bin and the shaft sinking dump doors, complete with pistons and controls, have been installed.

After the hoisting ropes are installed the bucket and sinking crosshead will be installed in the north hoisting compartment which will permit the attachment of the guides and chairs in this com partment. The sinking clam will have to remain in the south hoisting compartment until the shaft has been deepened enough for several timber sets to be installed.

ORE 6 WASTE BINS: The ore chutes have been installed in the bottom of the ore bin, the entry to the south side of the load out has been partition off and temporary wooden doors have been installed on the north side. Lights, heaters, and the permanent rollup door on the north entry are pending. The availability of welders and mechanics has delayed the building of the bin house on top of the the reinforced concrete ore and waste bins. This bit of construction should not interfere with the sinking operation. In the meantime the waste rock will be dumped through the bin and chute directly onto the truck.

C.C. Robert E. Johnson

Page 97: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

r^CAIMAAAAX^.'RESOURCES INC.SUITE 1100 - 181 UNIVERSITY AVE., TORONTO, CANADA MSH 3M7

/TO: Fred Johnston

FROM: Ross MacPhail

SUBJECT: Progress Report I Bell Creek Project,

Date: November 30, 1984

MEMORANDUMDATE:

C.-- ' v V

. L N

During the month of November 1984 the work on the development of the Bell Creek Project, by Patrick Harrison and Company Limited, was as follows:

Mine Hoist: The auxiliary air compressor for the hoist is connected to th,e hoist braking system, and all of the safety valves are in place and connected to their air lines. The main 600 volt electric power lines to the motor and the various auxiliary power lines are being installed. When the hoist can be turned the brake paths will be precision ground and the new brake shoes arced to fit.

Electric Power: All of the electric power in use at the site is being furnished by the main sub-station. The power lines to the parking area, the yard lighting and the water supply pumps are being run and buried. Until recently the electric power on the site has been distributed through surface lines from the contractor's Diesel generator.

The new hoist panels and resistance grids have been installed in the hoist-room and are being connected to the 600 volt power supply.

Service Building and Access Tunnel: Except for the glass for the windows and man doors, the outside of the building is complete. Inside, the divider wall between the hoist-room and the shop is half built and the walls for the office and bathroom have been framed. The propane unit heaters are in place, and most of the gas lines have been run. In the access tunnel, the concrete floor has been laid, the potable water line and the propane gas line have been laid between the stairway and the mine shaft. There are no permanent lights in the access tunnel or in the service building, in fact none of the lighting wires have been installed.

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Air Compressors: The contractor has brought two rotary screw type air compressors to the site, and because of their size and the sound they generate, he has chosen to install them in a temporary building against the outside north wall of the service building.

Headframe: The main structure has been completed, aligned and the bolts tongued. The sheave wheels have been aligned and bolted down, the manway completed, and the lightning rod and the flagpole, with an aircraft warning light, are installed above the roof. The cladding of the headframe tower has commenced with the west side being covered from the roof of the collar house up to the lower sheave deck. Until the deck house roof is installed and the shaft deepened, the east side of the tower will remain open, but the north and south sides will be cladded to the penthouse roof. The collar house requires the hanging of the doors, the lights and the metal flashing around the eaves.

Ore S Haste Bins: The reinforced concrete walls are finished to height and after the ore and waste chutes and the skip dump slide are in place the deck house will be built to enclose the top of the bins. Until there are more definite plans for the road and the mill conveyorway, the loadout from the ore and waste bins will operate through a north door only and the south door opening will be partitioned.

Shaft Sinking Equipment: The blasting set is in place in the shaft collar and four tugger hoists have been installed around the collar. One to raise and lower the mucking clam, two to handle the moving of the blasting set and the fourth for general servic ing. The electric drive motors are wired and the hoisting ropes installed on all of these tugger hoists.

The cross heads and sinking buckets have been delivered to the site and the dump doors and sinking clam are to be delivered in a few days.

Miscellaneous: Lake Shore Inc. are doing an analysis of the steel head frame for the siemic and wind load conditions of this area. We require this for certification and as installed in the St. Louis, Missouri area the headframe was .designed for use^as.jjT,

structure^ and because the shaft was used for hoistingthe crossbracing extended right to the ground on all

four sides of the tower. For our use, we have to be able to move supplies and equipment on and off the cage and, therefore, we have to eliminate the crossbraces on one side of the tower, on the deck house side. Lake Shore will determine whether some reinforcing steel pieces are required for the certification in the Timmins area.

C.C. Bob Johnson

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. o'.'. S ....... ...

Mine Hoist:

Patrick Harrison has a mechanical foreman assembling the hoist, putting all the brakes and clutch linkages etc. together. When everything is in place and properly adjusted the final grouting of the motor base and the brake posts will be made. The delay in the delivery of the pre- engineered service building interfered with this hoist assembly work.

Service Building and Access Tunnel:

Angle-iron brackets were attached to the north side of the access tunnel and the 8 inch compressed air line was installed on the lower shaft of the brackets. An upper shaft will hold the electric wires for the headframe and the underground. With the laying of the concrete floor and the lighting, the access tunnel will be completed.

The frame for the service building has been erected, the large overhead doors were installed and the wall cladding commenced. Over the two bays, which house the hoist and the electrical switch gear, the roof lining was put into place to provide shelter from the weather and to permit working on these components.

Headframe:

A steel frame, 44 feet high was erected on the north side of the headframe tower to extend the shaft manway up past the collar house. When enclosed, this section will house the stairs up to the bin deck. From the elevation of the bin deck the headframe manway will extend up in the west side of the tower. At the end of the month one landing and two stairs had been installed for the headframe manway. As soon as the manway landings are completed the installation of the girts and the cladding will start.

V e^CAN AM AXdQk&RESOURCES INC. M EMORANDUMSUITE 1100 - 181 UNIVERSITY AVE., TORONTO, CANADA MSH 3M7

DATE:

TO. Fred Johnston . -^i^;, r, /^^FROM: Ross MacPhail ,-—^"—--— "" . ' ." ^ " ''"' rf-"

l ^^ -- -- (Jt- SUBJECT: Progress Report/Bell Creek Project ^.^ ^.'

Date: October 31, 1984 ' C [i'/' - t^-.'7 -j.. ....'^TtiV'*

During the month of October 1984 the work on the development.-; - 3of the Bell Creek Project, by Patrick Harrison and Company Limited, .... r:-.; ,.........was as follows: . .,.\.-. - ..........

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At times the work on the upper portions of the headframe has to be stopped to allow the ore and waste bin construction to proceed on the ground below.

Electric Power:

The main sub-station is complete with the fence erected and the connection to the mine site end of the pole line made. All of the secondary switches and distribution panels are in place in the service building and their connection to the primary sub-station is in progress. The energizing of this sytem should be possible by mid month.

Potable Water Supply:

Potable water is being supplied to Harrison resident trailer at the site, but the pipe line to the headframe and the service building has not been completed.

Industrial Water Supply:

A two inch pipe line in an insulated box has been laid from the creek pump house to the shaft area. This line is heat taped also and will be extended across the road to the shaft manway.

The pump and pump line for the reclaimed water has not been constructed yet. This will require another small pump house and an insulated pipe box.

Ore and Wate r Bins:

The ore and waste bins are being constructed of reinforced concrete. To date the foundation walls and the floor for the bins has been completed. A form, 10 feet high, has been built and ready for the concrete to be poured, with this pour the bottom third of the concrete bin walls will be ready for the forming and pouring of the next two lifts.

Telephone:

The permanent telephone line has been brought to the mine site and from a junction box temporary lines have been extended to the con tractors' two office trailers and to the superintendant's resident trailer.

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r^CANAAAAX.'RESOURCES ING.

SUITE 1100 - 161 UNIVERSITY A VE., TORONTO, CANADA M5H 3M7

TO. Fred Johnston

FROM: Ross MacPhail

.' * V i

OCT 22 iS54

c:

MEMORANDUM

DATE: September 31, 1984

The main bearings for the hoist were set and grouted, and the main shaft and drums assembly were loaded on a truck and made ready for installation on the foundation. All of the other hoist components have been moved to the mine site. The delivery of the new electrical control panel is still pending, and the valves and switches, that comprise the new braking safety controls, are on order.

............L. l* T ______

......—... HWS .

SUBJECT: Progress Report, Bell Creek Project .....-..-.™........ *r...... M a M............. W -4

During the month of September 1984 the work on the development - .- ' *of the Bell Creek Project, by Patrick Harrison and Company Limited, was - -.- 1-*as follows: ............. ...

Shaft Collar: ...,...... OH-.V

Early in the month, the concrete was poured in the forms for ............e**~the walls for the shaft collar and the eastern terminal of the access ..............AW.tunnel. The steel beam and posts to support the main deck floor, at the ........................shaft compartments, were installed and also the extension posts to support ...-..-•ap..the west legs of the headframe tower were put in place. This permittedthe pouring of the collar house concrete floor. - c Tc

............. TIM

...........VANC

Hoist and Hoist Foundation: .......................

Service Building and Access Tunnel:

The backfilling and compacting of the granual fill was completed, the installation of the reinforcing grid wire and it's connection to the electrical bus bars was made, which permitted the concrete pour to form the finished floor slab. The electrical bus bars will carry off-peak power to heat the service building.

Except for the finish soil topping, the access tunnel is com pletely buried in granular compacted fill, and the installation of the concrete floor will complete the access tunnel.

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Headframe:

With all of the main frame of the headframe standing, it would appear that the headframe erection was almost finished, in reality it is about half done. Most of the connections are only partially bolted and after the remaining crossbraces are added the structure must be aligned and all of the bolts torqued. Additional pieces must be added for the guides, the skip dumps, the manway to the top, and the girts for the cladding on the outisde of the tower.

Our hoist and skip arrangement is different from that used in Missouri and the sheave deck had to be refabricated. This was accomplished by rearranging the steel components from the original two sheave wheel decks. Some new steel had to be fabricated to complete our hoisting compartment configuration.

Sewage Disposal System:

The concrete septic tanks were set in place all of the piping for the inlet and discharge was completed, inspected, approved and buried.

Settling Ponds:

The two settling ponds were completely built, the overflow wells built and the 6 inch inlet and discharge pipes installed. The return water pumping system remains to be constructed.

Industrial Water Supply:

In order to get the 20 ft length of 4 ft diameter culvert pipe in the proper position, a second excavation was made which permitted the top of the culvert pipe to be lowered to the road top elevation. A precast concrete collar was installed, completing the suction well for the industrial water. Work began on the building of a l x l foot pipe box to house the 2 inch industrial water supply line.

Potable Water Supply:

The 12000 gallon potable water tank was anchored to the bedrock and buried immediately north of the pumphouse at diamond drill hole MH 81-6, The 25 gal. per min. suction pump will supply water to the large storage tank, and a domestic type pressure pump will distribute the potable water to the mine site buildings.

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Ma i n sub-station:

The tower and the primary 3750 K.V.A. transformer was transported to the mine site and installed on it's foundation. A ground grid with a resistance of 5.0 ohms was installed to the northeast of the sub-station and when the surrounding fence is built and the incoming and outgoing electric cables attached the sub-station will be ready to be energized.

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CANAAAAXRESOURCES INC.

SUITE 1100 - 181 UNIVERSITY AVE., TORONTO. CANADA MSH 3M7

MEMORANDUM

DATE: September 14, 1984

C.C. Robert E. Johnson•TO: Mr. Fred Johnston

FROM: Ross MacPhail

SUBJECT: Progress Report, Bell Creek Project

During the month of August, 1984 the work on the development of the Bell Creek Project, by Patrick Harrison and Company Ltd. covered the following subjects:

Shaft collarHoist foundationService building and access tunnelHeadframe foundationSewage leaching bedSettling pondsIndustrial water supply

In conjunction with the above construction Canamax addressed the following equipment and service items:

Main sub-stationHoist refurbishingHoist electrics and ultra sonic tests

. ....... 6AB

C T 3.....™....- Tl M .

.......... VAN C

Shaft collar: By the end of the month the forming for the shaftcollar and access tunnel walls was completed and when poured will complete the shaft collar except for the ceiling of the access tunnel at the shaft compartments. This ceiling area requires a steel support set and will be poured as part of the deck house floor.

Hoist foundation: The forming, reinforcing and pouring of the concretehoist foundation was completed and after the initial curing period the bearings for the hoist main shaft will be set and grouted in place.

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Headframe piers: After pouring a block of concrete in the form of a 5 ft cube for a rough footing, the pyramidal piers for the head- frame back legs were formed, reinforced and poured. The four legs of the headframe tower rest on the concrete shaft collar.

Service building and access tunnel: The sectional steel culvert pipe that forms the access tunnel was bolted together and when it is alligned and all the bolts torqued the back filling with granular fill can begin. All of the back fill will be compacted in about one foot lifts and in the northeast corner about 12 feet of fill will be required.

At the west end of the access tunnel the steel pipe is attachedto a rectangular concrete box which will house the stairs leadingup to the shop floor. At the east end the access tunnel pipeattaches to an extended north wing of the shaft collar.

Sewage leaching bed: The granular fill for this leaching bed has been trucked to the site and an area about 100 ft square has been built to a depth of about 5 ft. This area is required to permit the laying of the 500 ft of pipe for the sewage disposal system. The concrete septic tank has been delivered to the site, but the pipe laying and tank installation has not been started.

Settling ponds: The granular fill to build the first half of the wall for these two settling ponds has been brought to the site and laid in place.

Industrial water supply: Some of the large pieces of rock from the road levelling was deposited on the west side of the main culvert at the creek and a 4 ft culvert pipe with screened inlet holes was stood on end to form a suction wall for the industrial water pump.

Main sub-station: The footings, piers and the top slab for thisfoundation were poured and the fill compacted around it.

Hoist refurbishing: A great deal of time was taken with the machineshop work on the main shaft and the clutch hubs and other refurbi shing work had to be delayed until the final measurements of the main shaft were available; such as the finish machining of the drum bushings and the main bearings. All of machine shop work is now completed and most of the final assembly has been made.

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Hoist Electrics: The new electrical controls are ready and as soon asdrawings for the mine inspection approval are received we will have the electrical controls delivered. We commissioned Walter Dow S Company to provide us with approved drawings for our sub station installation and now they are to draw up the hoist control schematics.-'A! Higgins of Can-Test brought his test equipment from Sudbury to ultra sonically test the pins and rods of the hoist brakes and to magnetically inspect the brake paths and other components of the hoist that were not tested in Red Deer Alberta before we purchased it. Even though the brake and clutch pins are all new, ultra sonic testing is necessary before the hoist can be commissioned and thereafter every twelve months.

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^CANAAAAXi^RESOURCES INC.;

1100 - 181 UNIVERSITY AVE., TORONTO, CANADA M5H 3M7

MJG 27 l-:

C A ^ •'~ MEMORANDUMV

DATE: August 21, 1984 s '

TO Fred J. Johnston

FROM: Ross MacPhail

SUBJECT: Progress Report, Bell Creek Project

Date: July 31, 1984

During the month of July, 1984, the work on the development of the Bell Creek Project, by Patrick Harrison and Co. Ltd., covered the following subjects:

Road on the siteShaft collarHeadframe piersService building and access tunnel

l/'

In conjunction with the above construction Canamax addressed the following equipment and service items:

Hydro electric power Telephone line Main sub-station Mine hoist

Road on the site: The drilling and blasting to lower the western extension of the road was completed and grading of the finished extension started. The excavation of the rock was required to prevent the run off water from accumulating at the shop doors.

Shaft collar: Except for the blasting of a few pops all of the rock work above the 285 metre elevation was completed during the month of June. In the month of July the 7.8 x 3.6 metre excavation was taken down 4.8 metres and an additional 6.83 x 2.80 metre excavation was taken down 2.44 metres. The present shaft bottom is at an elevation of 277 metres and the airtrack holes extend down to the 267 metre elevation. In the larger top portion of the excavation the walls were drilled for #8 re-bar dowels and this portion of the shaft collar was formed and poured with reinforced concrete.

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Headframe piers: The bedrock was uncovered, washed and dowel!ed pre paratory to pouring rough footings for the back leg piers. The headframe columns will rest on the concrete shaft collar.

Service building and access tunnel: In preparation for this structuresome rock excavation was needed for the west end of the access tunnel and a shaving off of about 0.3 metres in the southwest area. Most of the broken rock from here and from the road excavation will serve as fill to support the floor slab for this building.

An greement has been made with the contractor for an extension of 3 x 12.2 metres to the north side of this building to house the main secondary electrics. The access tunnel which extends from the west end of the service building and below the floor slab will have reinforced concrete walls and floor at each end and the main, or center section, will be a corrigated steel culvert. To more or less level the area where the hoist foundation will be constructed, a form was built, the bedrock was washed and dowel!ed and about 37 cubic metres of concrete were poured.

Hydro electric power: The local power commission has completed theirrehabilitation of their power line and made the connect ion to own line.

Telephone: Canamax has prepaid the construction costs for the permanent telephone line to be built from Florence St. in the east region of the city and construction will commence as soon as the material arrives.

The main sub-station: The dismantling of the Langmuir sub-station has beencompleted and the components will be set up at our mine site when the concrete base is ready. Patrick Harrison's crew has taken on the work of building the sub-station foundation.

Hoist: The main shaft and clutch hubs will be shipped from the Toronto machine shop as soon as the new keys are pressed into the keyways. All of the other mechanical components are ready for the new installation. Dominion Electric has been contracted to supply us with an up to date refurbished electrical control system which will include a new consul and dynamic braking.

C.C. Robert E. Johnson

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42A11SE8ZI64 63.4458 HOYLE 020

An Investigation of

THE RECOVERY OF GOLD

from samples

submitted by

AMAX INCORPORATED

Progress Report No. 2

Project No. LR. 2686

NOTE:

This report refers to the samples as received,

The practice of this Company in issuing reports of this nature is to require the recipient not to publish the report or any part thereof without the written consent of Lakefield Research.

LAKEFIELD RESEARCHA DIVISION OF FALCONBRIDGE LIMITED

April 17, 1985

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42A1ISE0064 63.4458 HOYLE

I N u t A oeoc

ABSTRACT

INTRODUCTION

SUMMARY

1. Head Analyses ................................

2. Gravity Concentration and Magnetic Separation

3. Direct Cyanidation Testwork3.1. Effect of Fineness of Grind ............3.2. Effect of Cyanide Concentration ........3.3. Effect of Retention Time3.4. Effect of Preaeration3.5. Effect of Pulp Density3.6. Effect of Creek Water

4. Intensive Cyanidation ........................

5. Zinc Precipitation Testwork

6. Cyanide Destruction Testwork6.1. Alkaline Chlorination6.2. 502/Aeration

7. Settling and Filtration Testwork7.1. Settling Tests7.2. Filtration Tests

8. Bond Work Indices

9. Effluent Simulation

SAMPLE PREPARATION

DETAILS OF TESTS ......... ....... ..... ...................,

Page No.

1

2

3-22

3

4

5-116789

1011

12

13

13 - 151415

16 - 171617

18

19 - 22

23

24 - 154

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ABSTRACT

Testwork was conducted on two composites prepared from Bell Creek

project samples to investigate the recovery of gold. The amount of free gold

in each sample averaged 60 7o. Gold extractions of 96 7. to 98 "l, were achieved

by amalgamation and cyanidation.

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INTRODUCTION

This report contains the results of testwork conducted on Bell Creek

project samples as requested by Mr. B. Ball, Amax Incorporated. The program

involved gravity concentration, cyanidation and zinc precipitation tests to

investigate the recovery of gold, as well as effluent treatment, settling and

filtration testwork and Bond Work Index determinations.

The results were discussed frequently in telephone conversations with

Mr. Ball.

LAKEFIELD RESEARCH

D.M. Wyslouzil, P. Eng.

Manager

IV Jackman

Project Engineer

Experimental Work by: C. Caza

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Gold Assays, g/t Au Head 1 Head 2

3.27,3.10 3.81,3.90 2.39,4.40 12.7,8.25 21.0,22.8 18.4,20.8 3.84,4.58 3.46,4.19 5.18,4.28 3.88,4.05 7.33,5.91 17.2,20.9 4.40,5.63 5.36,3.93

Average g/t Au

3.52 6.94 20.8 4.02 4.35 12.9 4.83

NUMMARY

1. Head Analyses

The two head samples riffled out of each of the seven original samples

were assayed for gold in duplicate with the following results:

Sample No.

A00201 A00202 A00203 A00204 A00205 A00206 A00207

Composite A, a combination of the seven samples, and Composite B, prepared

from specific samples as described under SAMPLE PREPARATION, were analysed for the

elements shown below:

Element______________Composite A___________Compsoite B

Gold, g/t Au 5.85,7.06,9.47,11.8 6.23,6.66,10.1,10.6average 8.53 8.40

Silver, g/t Ag 1.3 1.3Sulphur, 7. S 1.88 1.65Iron, 7. Fe 7.01 6.66Arsenic, 7. As ^.02 -:0.02

The average calculated gold head assays from testwork were:

Composite A: 9.36 g/t Au

Composite B: 6.34 g/t Au

Several samples of both composites were amalgamated prior to cyanidation

tests to remove the salting effect of free gold. The amount of gold recovered by

amalgamation from Composite A ranged from 56-72 7. and from Composite B ranged

from 48-72 7..

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ary - Continued

2. Gravity Concentration and Magnetic Separation

The recovery of gold by gravimetric methods was investigated. A sample

of each composite was ground to 53 7. minus 200 mesh and fed over a laboratory

Wilfley table. The table concentrate was cleaned on a Mozley mineral separator.

The Mozley table concentrate was further upgraded by removing the magnetics in a

Frantz magnetic separator. The results are summarized in Table No. 1.

Table No. l

Gravity Concentration

Test

No.

190

167

Comp.

A

B

Product

Non-MagneticsGravity CI. Cone.Gravity Ro. Cone.Gravity Tail.

Head (Calc.)

Non-MagneticsGravity CI. Cone.Gravity Ro. Cone.Gravity Tail.

Head (Calc.)

Weight

7.

0.71.35.5

94.5

100.0

0.41.14.195.9

100.0

Assays, g/t

Au

54132388.62.48

7.20

54425582.11.43

4.72

7. Distribution

Au

49.657.168.532.5

-

41.559.570.929.1

-

A mineralogical examination was performed on the magnetic and non-magnetic

fractions of the cleaned gravity concentrate from test No. 190 (Composite A).

Essentially all the gold in the non-magnetic product was free whereas over 90 *l, of

the gold in the magnetics was present as middlings. The size of the free gold varied

from 3 to 70 urn. The results of a grain count on particles in the non-magnetics

showed that 84 7, of the particles were non-opaques, 11 7, were pyrite and 5 7, were

arsenopyrite or marcasite. Over 80 7, of the sulphides'were liberated. These results

suggest that it should be possible to produce a higher grade gold concentrate by

gravimetric methods. Cleaning of the gravity concentrate in the laboratory was

limited by the size of the sample.

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Summary - Continued

3. Direct Cyanidation Testwork

The effect of the following parameters on the recovery of gold from

Composites A or B were investigated: fineness of grind, cyanide concentration,

retention time, preaeration, pulp density and creek water. All tests were conducted

in bottles on rolls. In tests 108-119, the variation in the residue assays indicated

the presence of free gold. These residues were amalgamated and reassayed in

triplicate to determine a residue assay not affected by the presence of free gold.

It is the average of these assays which is included in the tabulated results. The

feed to tests 121-128 was tabled prior to leaching, and the table concentrate was

amalgamated. The amalgamation and table tailings were combined for cyanidation

tests. In all subsequent tests, the ore was amalgamated and the amalgamation tail was

used as feed to the leach tests.

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SuWmcnary - Continued

3.1.Effect of Fineness of Grind

The fineness of grind was varied from 53 7, to 87 7c minus 200 mesh to

examine its effect on gold extraction from Composite A. The sample was aerated

for 6 hours prior to leaching. The cyanide and lime concentrations were maintained

at 0.5 g/L NaCN and 0.5 g/L Ca(OH)2 respectively. The results are summarized in

Table No. 2.

Table No. 2

Effect of Fineness of Grind

Test No.

144140126121131

145141127122132

7.-200 Mesh

5359697787

5359697787

Time Hours

1616161616

2424242424

Reag. Cc NaCN

0.420.300.060.080.06

0.480.390.060.240.21

ns. .kg/t CaO

0.630.620.680.811.33

0.660.670.801.140.87

7, Au Ree 'y Hg * Cyn.

91.293.696.896.997.9

92.495.897.796.698.0

Residue g/t Au

0.980.670.400.220.19

0.920.440.240.300.19

Head g/t Au

10.710.511.57.919.26

10.710.511.57.919.26

At the coarser grinds, 53 ml, and 59 7, minus 200 mesh, there was an

increase in the residue assays resulting in reduced gold extraction.

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. Effect of Cyanide Concentration

Tests were conducted on Composite A in which the cyanide concentration was

reduced from 0.5 g/L NaCN. Again, the samples were amalgamated and the tailing was

preaerated for 6 hours prior to the cyanide leach. The results are presented in

Table No. 3.

Table No. 3

Effect of Cyanide Concentration

Test No.

121152155

122153156

NaCN g/L

0.50.40.2

0.50.40.2

2-200 Mesh

777474

777474

Time Hours

161616

242424

Reag. Co NaCN

0.080.080.02

0.240.200.04

is. ,kg7t CaO

0.811.011.15

1.140.961.16

1, Au Rec( Cyn. Only

93.172.976.6

92.477.78.07

Dvery Hg+Cyn.

96.988.291.2

96.690.392.7

Residue g/t Au

0.221.650.86

0.301.110.80

Head (Gale.) g/t Au

7.9112.710.3

7.9112.710.3

Reducing the cyanide concentrate below 0.5 g/L NaCN led to higher residue

assays and a lower extraction of gold. The results from earlier testwork showed that

the difference in fineness of grind in the range shown above did not affect the

cyanidation results and therefore could not account for the increase in the residue

assays.

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nary - Continued

3.3. Effect of Retention Time

The effect of increasing the retention from 12 to 36 hours on the recovery

of gold from Composite A was investigated. In tests 108 to 116, the samples were

preaerated for six hours before the cyanide leach. The cyanidation residues were

later amalgamated. The residue assays given in Table No. 4 are those obtained after

amalgamation. The recoveries and calculated heads are based on these assays. In

tests 121 to 145, the ore sample was amalgamated before leaching. The reagent

concentrations in all tests were 0.5 g/L NaCN and 0.5 g/L Ca(OH)z.

Table No. 4 - Effect of Retention Time

Test No.

108126109127110

111121112122113

114131115132116

139140141

143144145

Time Hours

1616242436

1616242436

1616242436

121624

121624

7. -200 Mesh

6969696969

7777777777

8787878787

595959

535353

Reag. CoNaCN

0.120.060.120.060.33

0.120.080.180.240.27

0.120.060.360.210.39

0.240.300.39

0.360.420.48

ns. .kg/t CaO

1.200.681.350.801.50

1.220.811.441.141.54

1.211.331.360.871.55

0.630.620.67

0.550.630.66

7o Au Re c o Cyn. only

86.6

90.4

93.1

92.4

92.7

92.9

76.377.084.7

77.672.275.8

very Hg+Cyn.

93.296.897.297.796.7

95.996.996.996.698.6

96.497.994.998.098.5

93.493.695.8

92.991.992.4

Residue g/t Au

0.430.400.190.240.25

0.270.220.280.300.18

0.280.190.460.190.15

0.670.670.44

0.610.980.92

Head g/t Au

7.1411.57.7311.58.12

6.587.919.067.9113.4

7.849.269.009.2610.1

10.410.610.6

10.010.911.2

Due to the variation in results from tests conducted under similar conditions

and the variation in the calculated head assays, it is not possible to draw strict

conclusions on the effect of retention time.

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^BKricnary - Continued

3.4. Effect of Preaeration

The effect of preaeration on reagent consumption and gold recovery was

examined. The preaeration time was varied from Q to 24 hours. The cyanide

concentration was maintained at 0.5 g/L NaCN throughout the 24 hour leach period

and the lime concentration at 0.5 g/L Ca(OH)2 during prearation and leaching.

The results are summarized in Table No. 5.

Table No. 5 - Effect of Preaeration

Test No.

124122

128127

132133

119112118117

Preaer . Hours

06

06

612

06

1224

7,- 200 Mesh

7777

6969

8787

77777777

Reag. Cons NaCN

0.330.24

0.250.06

0.210.15

0.480.180.090.08

..kg/t CaO

0.861.14

0.740.80

0.871.29

1.441.441.561.86

7o Recovery Au

97.596.6

97.297.7

98.098.3

96.196.994.698.7

Residue g /t Au

0.270.30

0.290.24

0.190.16

0.200.280.350.19

Head g/t Au

8.138.37

11.311.4

9.279.32

5.099.066.4714.8

Preaeration had no significant effect on the extraction of gold after

24 hours, however, the addition of a 6 hour preaeration stage did reduce the

consumption of cyanide. Extending the preaeration time from 6 to 12 hours further

reduced the cyanide consumption in the tests conducted. Because of the range of

consumption figures seen in other testwork, further tests would be required to

quantify the effect of extending the preaeration stage beyond 6 hours. The fineness

of the material entering the preaeration stage will also have an effect on the lime

required and the absolute cyanide consumption. An additional benefit from the

preaeration may be the reduced iron concentration in the cyanidation circuit.

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3.5. Effect of Pulp Density

The effect of pulp density on the cyanidation recovery of gold from

Composite B was briefly examined. A sample was ground to 84 7. minus 200 mesh and

amalgamated to remove the free gold. Cyanidation tests were conducted on the

amalgamation tailing at various pulp densities. In each test, the sample was

preaerated for 6 hours then leached in a 0.5 g/L NaCN solution for 24 hours.

Table No. 6 contains the results.

Table No. 6

Effect of Pulp Density

TestNo.

164165166

7.Solids

304050

Reag. Cons . ,kg7tNaCN

0.240.270.21

CaO

1.771.030.97

7. Au RecoveryCyn . + Hg

97.698.197.7

Residueg /t Au

0.140.180.14

Headg/t Au

6.558.086.04

Pulp density had no effect on the extraction of gold in the range

investigated.

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SumrnsSummary - Continued

3.6. Effect of Creek Water

Parallel cyanidation tests were conducted on Composite B using tap water

and the creek water sample provided. The test charges were ground to 77 7o minus

200 mesh and amalgamated. Each amalgamation tailing was split into two parts to

run the parallel leach tests. Each sample was preaerated for 6 hours followed by a

24 hour leach maintaining 0.5 g/L NaCN. The results are given in Table No. 7.

Table No. 7

Effect of Creek Water

Test No.

180 181

183 184

Source of Water

Tap* Creek**

Tap Creek

Reag. Cor NaCN

0.10 0.14

0.16 0.10

s-.kg/t CaO

0.82 0.85

1.04 0.89

7c Au Recovery Cyn. -H Hg

97.9 97.5

96.5 97.4

Residue g/t Au

0.15 0.16

0.22 0.18

Head g/t Au

6.53 6.53

6.89 6.89

* Lakefield tap water** Bell Creek water

Using creek water in place of tap water did not affect the cyanidation

results of Composite B under these test conditions.

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Semiticnary - Continued

4. Intensive Cyanidation

Tests were conducted on Composites A and B to investigate the recovery of

gold from a gravity concentrate by intensive cyanidation. The effect of regrinding

the concentrate prior to leaching was briefly examined. The gravity concentrate

was agitated in a covered plastic jar using an Agitair cell. Oxygen was circulated

to the sample throughout the leach period. At the beginning of the leach, 30 g/L

NaCN was added raising the pH above 11. The results are summarized in Table No. 8.

Table No. 8 - Intensive Cyanidation Results

Test No.

186

188

189

Comp .

B

B

A

Regrind Min.

0

10

10

Time Hours

24

24

6

CN Cons kg/t NaCN

121

116

121

7. Au Ri Cyn.

69.2

98.8

97.9

scovery O'all

36.5

80.0

57.0

Residue g /t Au

15.1

0.97

1.87

Head, Cone.

49.1

82.0

90.1

g/ 1 Au O'all

3.25

5.81

5.81

Gold recoveries in the cyanidation stage of 98 7, were achieved from both

composites. Regrinding of the concentrate was essential.

The degree of regrinding required to obtain a high recovery was not

determined. The results from test No. 189 suggest that a retention time less than

24 hours may be sufficient. Further testwork is required to optimize this process.

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Smmary - Continued

5. Zinc Precipitation Testwork

The precipitation of gold from a pregnant solution using zinc dust was

briefly investigated. The cyanide concentration of the pregnant solution was adjusted

to 0.5 g/L NaCN. The solution was deaerated with nitrogen. Lead nitrate and zinc

dust were added and the solution was agitated with the nitrogen gas. It was then

filtered while maintaining an oxygen-free environment. The results varied. The

best results were achieved in Test No. 149. With a zinc dust addition 100 times

the theoretical requirements, the gold in solution was reduced from 2.34 mg/L Au to

0.012 mg/L which represents 99.5 7. precipitation. In other tests, the precipitation

was less efficient, possibly due to inadequate contact with the zinc dust.

6. Cyanide Destruction Testwork

Cyanide destruction tests were conducted on zinc precipitation barren

solutions from Composite A using the alkaline chlorination and SOa/aeration methods.

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nary - Continued

6.1. Alkaline Chlorination

Two alkaline chlorination tests were performed on a sample of zinc

precipitation barren solution. Chlorine was added slowly as a 5 7, NaOCl solution

while maintaining the pH above 11 with lime. When the emf had stabilized, it was

assumed that the reaction was complete. Sodium arsenate was added to fix any

residual chlorine. The results are presented below.

Table No.9 - Alkaline Chlorination Results

Test No.

136

137

C1:CN Ratio

10:1

7:1

Solution

Feed Barren

Feed Barren

Anal y CNT

197 2.9

197 9.3

ses , rCNS

303 0. 5

303 0. 5

ng/L Fe

0.57 0.54

0.57 0.51

By increasing the Cl/CN ratio from 7 to 10, the total cyanide level in

the effluent was reduced from 9 to 3 mg/L CN . The iron in the barren solution could

account for 1.5 mg/L CN as a ferrocyanide complex. It would not be possible to

reduce the cyanide below this level using this method despite increases in the

chlorine addition as the ferrocyanide complexes are not destroyed by alkaline chlorina

tion.

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- Continued

6.2. S0 2 /Aeration

The destruction of cyanide using the S02 /aeration method was also examined.

Tests were conducted in a baffled vessel with agitation provided by a mechanical

mixer. An 802/air mixture was metered into the solution. The pH was maintained at

8.5-9 using an automatic titrator to control the flow of a lime slurry. Copper

was added as a dilute copper sulphate solution.

In the initial tests, 50 mg/L Cu was added and the SOa/CN ratio was

varied from 3.2 to 4.5 g/g, with a retention time of 30 minutes. Under these

conditions, the cyanide level in the barren solution was not reduced below 43 mg/L CN,

Subsequently, sufficient copper was added to complex the free cyanide (assuming

Na 2 Cu(CN) 3 ) before- 'the S02 addition. In test No. 150, sufficient SOz was added to

provide a 4:1 SOa/CN ratio over 30 minutes. The total cyanide in solution was

reduced from 238 mg/L to 2.8 mg/L CN . Extending the retention time to 60 minutes

resulted in a barren solution analysing 2.3 mg/L CN . In a continuous test, test No.

158, twice the amount of copper required to complex the free cyanide was added. The

SOj/CN ratio was maintained at 6. The barren solution analysed 107 mg/L CNT and

68 mg/L Cu. A sample of barren solution was retreated for 30 minutes with a 4/1

SC-2/CN addition and no further copper addition. The retreated barren solution

analysed 0.25 mg/L CN and 1.8 mg/L Cu. The results indicate that it is possible to

reduce the cyanide content to acceptable levels using S02 /aeration method but further

testwork would be required to optimize the conditions.

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Semiticnary - Continued

7. Settling and Filtration Testwork

Settling and filtration tests were conducted on Composite B using samples

of creek water. The feed was ground to 77 'L minus 200 mesh and amalgamated before

further treatment.

7.1. Settling Tests

Tests were performed to investigate the effect of pulp density and lime

addition on the settling characteristics of the amalgamation tailing. A single

test was conducted on a sample of pulp after a 24 hour cyanidation. The results

are summarized in Table No. 10.

Table No. 10 - Settling Test Results

Test No.

169170171172

174

Feed

amal tail.amal tail.amal tail.amal tail.

cyn Pulp

Ca(OH) 2 g/L

0.210.220.420.43

PH

10.810.811.511.5

11.7

7. Soli Initial

15201520

30

ds Final

62.561.157.459.6

63.9

Feed Cc Rate*

1.000.660.960.96

0.42

me . Zone Area**

0.210.210.220.15

0.18

Compres Rate*

0.250.160.260.17

0.13

s ion Zone Area**

0.200.330.230.25

0.28

* metres/hour** square metres/tonne of dry solids/24 hours

The supernatant was very cloudy in tests 169 to 172 particularly with

the lower lime addition.

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nary - Continued

7.2. Filtration Tests

The filtration characteristics of Composite B after cyanidation in creek

water were investigated. In test No. 175, the cyanidation was carried out at 30 7.

solids and the pulp was thickened to 50 7, solids for the filtration tests. The

cyanidation was conducted at 50 7o solids in test No. 178. Standard "pick-up" tests

were conducted producing a cake thickness of approximately 15 mm.

Table No. 11

Filtration Test Results

Test No.

175

178

Time Form

30303030

30303030

, Seco Dry

306090120

306090

120

ids Cycle

90135180225

90135180225

Filter Ca 7. Moisture

20181715

20181615

ke Rate*

865670355337

932611475363

Filtrate Rate**

887778413406

921735504441

The filtration rates were high and the filtrate clarity was very

good .

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- Continued

8. Bond Work Indices

The Bond Work Index of Composite A was determined in a standard Bond ball mill

closed circuit grindability test.

The results are summarized below:

Bond Work Index: 10.8

Test screen size, pm 147

Net undersize produced perrevolution, g 2.05

Product Keo, P 109.6

Feed K8o , Mm 1873

Using this known value, the Bond Work Index of the earlier samples was

estimated by comparing the size distribution of similar grinds.

Sample BWI

MG-B 8.7

LG-A 8.8

LG-B 8.8

AG-B 9.0

HG-A 10.3

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- Continued

9. Effluent Simulation

Tests were conducted on Composite A and Sample AG-B to simulate the barren

bleed and tailing. A l kg sample of each was ground to 77 "l, minus 200 mesh and

amalgamated. The amalgamation tailing was preaerated for 6 hours then leached in

a 0.5 g/L NaCN solution for 24 hours, filtered and washed three times with water.

The pregnant and wash solutions were combined and the gold precipitated with zinc

dust. This gold barren solution was used to wash and repulp a second cyanided

pulp. The repulp was followed by a fresh water wash. The procedure was used to

simulate a 2-stage drum filtration circuit. The solutions were combined and treated

by zinc precipitation to produce a sample of barren solution. The procedure is

outlined in Figure No. 1. More detailed flowsheets are included in the Details

of Tests section, tests 159-162.

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aBroricnary - Continued

9. Effluent Simulation - Cont'd

Figure No. l - Effluent Simulation Flowsheet

Ore (Tests 159,161)

i

Hg

Barren Sol'n

Water

Ore (Tests 160,162)

Tail

MFinal Barren

Solution

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- Continued

9. Effluent Simulation - Cont'd

The gold and cyanide levels were followed throughout. The results are

tabulated below.

Table No. 12 - Effluent Simulation Results

Test No.

159

160

161

162

Sample

Comp . A

Comp . A

AG-B

AG-B

Product

AmalgamPreg 'n+WashZn Barren Sol'nResidueAmalgamPreg'n Sol'nWash 1FiltrateWash 2Final Barren Sol 'rTailing

AmalgamPreg'n+WashZn Barren Sol 'nResidueAmalgamPreg'n Sol 'nWash 1FiltrateWash 2Final Barren Sol'nTailing

Assays, mg, r Au

A. 621.030.0470.3210.170.800.670.140.080.0340.25

3.650.820.500.252.370.790.790.500.480.0490.18

ng/L.g/t CNT

125125

141125117103

240230

253252231195

7. Distribution Au

61.034.71.64.3

84.211.11.41.10.20.92.0

59.636.322.14.150.028.74.410.32.83.43.8

The analyses of the wash solution in test No. 162 was limited by the

low efficiency in the zinc precipitation stage of test No. 161. The reason for

the reduced efficiency was not determined.

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- Continued

9. Effluent Simulation - Cont'd

Samples of the final tailing and barren solution were sent to "The

Environmental Applications Group Limited" as requested by Mr. Ball for environmental

testing. Limited analyses were performed on the final barren solutions at

Lakefield Research.

Table No. 13

Barren Solution Analyses

Element

Gold (Au)Silver (Ag)Zinc (Zn)Copper (Cu)Lead (Pb)Nickel (Ni)Thiocyanate (CNS)

Analyses Composite A

0.034^.0512.04.45*:0.32.16448

, mg /L Sample AG-B

0.049^.0542.010.00.50.8060.7

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SAMPLE PREPARATION

On April 2, 1984, five core and two reject samples were received at

Lakefield Research and given our Reference No. 8424478. Each of the core samples

was crushed to minus 6 mesh. Two separate head samples were riffled out of each of

the seven samples. The remainder of the samples were combined to produce Composite A,

Approximately 10 kg of minus 6 mesh material was cut out for Bond Work Index

determination. The remaining ore was further crushed to minus 10 mesh. Two head

samples were riffled out and test charges were prepared.

Composite B was prepared by combining the following samples:

LG-A

LG- B

LG-A+BHG-A

MG- B

Comp . A

2 kg1 kg1 kg2 kg5 kg5 kg

Two head samples were removed and l kg charges were prepared for

testwork.

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DETAILS OF TESTS

Test No.

108-119120

121-124125

126-129130

131-133 135-137

138 139-141

142 143-145

147149150151

152-153154

155-156157158

159-160 161-162

163 164-166

167168

169-172173174175176177178179

180-181182

183-184185186187188189190

Composite Procedure

A A A A A A A A A A A A A A A A A A A A A A

AG-B B B B B B B B B B B B B B B B B B B B B A A

CyanidationGravity Sep'n+Amal.CyanidationGravity Sep'n+Amal.CyanidationAmalgamationCyanidationCN DestructionAmalgamationCyanidationAmalgamationCyanidationCN DestructionZinc PrecipitationCN DestructionAmalgamationCyanidationAmalgamationCyanidationZinc PrecipitationCN DestructionEffluent SimulationEffluent SimulationAmalgamationCyanidationGravity SeparationAmalgamationSettling TestsCyanidationSettling TestFiltration TestAmalgamationCyanidationFiltration TestAmalgamationCyanidationAmalgamationCyanidationGravity SeparationIntensive CyanidationGravity SeparationIntensive CyanidationGravity Sep'n+Cyn.Gravity SeparationBond Work Index

Page No.

24 - 3839

40 - 4344

45 - 4950

51 - 53 54 - 58

59 60 - 63

6465 - 68 69 - 71

72 73 - 74

75 76 - 78

79 80 - 81

8283 - 84 85 - 92 93 - 97

9899 - 103

104 - 106107

108 - 119 120 - 122 123 - 125 126 - 127

128129 - 131 132 - 133

134 135 - 138

139 140-142

143144145146

147 - 148 149 - 150 151 - 154

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-su

No. 108

Purpose:

Procedure;

Feed:

Solution Volume:

To investigate the gold recovery with a coarse grind and a 16 hour retention time from Composite A.

The sample was pulped with water in a 2 litre bottle and preaerated for 6 hours with lime. NaCN and lime were added and the cyanidation was carried out on rolls in one 16 hour stage. The pulp was filtered and the residue washed three times with water.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.50 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball at 657o solids for 8 minutes.

Time ,

Hours

Preaeration:0-22 - 4.5

4.5 - 6Cyanidation:0-16

Total

Added, Grams

Act NaCN

- -

0.35

0.35

ual Ca(OH) 2

0.500.160.08

0.03

0.77

Equiv NaCN

---

0.33

0.33

alent CaO

0.380.120.06

0.02

0.58

Residual

Gr* NaCN

---

0.29

0.29

uns CaO

0.130.190.23

0.18

0.18

Consumed

Grt NaCN

-.-

0.04

0.04

uns CaO

0.250.060.02

0.07

0.40

pH

From

11.711.811.8

11.9

To

11.011.811.8

11.8

Reagent Consumption (kg/tonne of cyanide feed) NaCN: 0.12CaO: 1.20

Metallurgical Results

Product

16 h Preg. 4- Wash Soln 16 h Cy Residue*

Head (calculated)

Amount

1510 mL 333.2 g

333.2 g

Assay, mg/L.g/t Au

1.47 1.72

8.37

7, Distri Au

79.7 20.4

100.0

bution Au**

93.3 6.7

100.0

* The residue was later amalgamated to remove any free gold not leached during cyanidation . After amalgamation, the residue was assayed in triplicate. Residue: 0.48, 0.40, 0.42 g/t Au

** Based on average residue assay after amalgamation

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- 25 --

Test No. 108 - Continued

Screen Analysis

16 h Cyanide Residue

Mesh Size(Tyler)

* 28354865

100150200270400

- 400

Total

7. RetainedIndividual

1.70.61.02.75.69.511.311.011.045.7

100.0

Cumulative

1.72.33.36.011.621.032.343.354.3100.0

-

7o PassingCumulative

98.397.796.794.088.479.068.756.745.7-

-

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- 26 -

st No. 109

Purpose:

Procedure:

To investigate the gold recovery with a coarse grind and a 24 hour retention time from Composite A.

The sample was pulped with water in a 2 litre bottle and preaerated for 6 hours with lime. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

Feed :

Solution Volume:

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind :

Reagent Balance:

l kg sample ground in the lab ball mill at 657. solids for 8 minutes.

Time ,

Hours

Preaeration:0-33-6

Cyanidation:0 - 16.5

16.5 - 24

Total

Added, Grams

Act NaCN

--

0.350.03

0.38

ual Ca(OH) 2

0.500.16

0.080.12

0.86

Equiva NaCN

--

0.330.03

0.36

ilent CaO

0.380.12

0.060.09

0.65

Residual

Gre NaCN

--

0.300.32

0.32

tms CaO

0.130.19

0.160.20

0.20

Consumed

Gr*NaCN

--

0.080.01

0.04

uns CaO

0.250.06

0.090.05

0.45

PH

From

11.711.5

11.711.9

To

11.011.5

11.712.0

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.12CaO: 1.35

Metallurgical Results

Product

24 h Preg. + Wash Soln 24 h Cy Residue

Head (calculated)

Amount

1030 mL 333.3 g

333.3 g

Assay .mg/L, g/t Au

2.43 0.30*

7.80

7. Distri Au

96.2 3.8

100.0

but ion Au**

97.2 2.8

100.0

* After it was amalgamated, the residue assayed 0.19 g/t Au (average of 0.22, 0.16, 0.19 g/t Au)

** Based on average residue assay after amalgamation.

Page 138: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 27

list No. 110

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the recovery of gold from Composite A, with a 36 hour retention time and a coarse grind.

The sample was pulped with water in a 2 litre bottle and pre-aerated for 6 hours with lime. NaCN and lime were added and the cyanidation was carried out on rolls in one 36 hour stage. The pulp was filtered and the residue washed three times with water.

333 grams minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill at 657. solids for 8 minutes.

Time,

Hours

Pre-aeration:0-22 - 4.5

A. 5 - 6Cyanidation:

0 - 16.516.5 - 36

Total

Added, Grams

Act NaCN

---

0.350.01

0.36

ual Ca(OH) 2

0.500.160.07

0.000.12

0.85

EquiVc NaCN

---

0.330.01

0.34

alent CaO

0.380.120.05

0.000.09

0.64

Residual

Grf NaCN

---

0.320.23

0.23

uns CaO

0.130.200.25

0.160.14

0.14

Consumed

Grs NaCN

.--

0.010.10

0.11

uns CaO

0.250.050.00

0.090.11

0.50

pH

From

11.511.811.8

11.711.8

To

11.011.811.6

11.912.0

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.33CaO: 1.50

Metallurgical Results

Product

36 h Preg.-f- Wash Soln 36 h Cyanide Residue*

Head (calculated)

Amount

1940 mL 332.6 g

332.6 g

Assay, mg/L, g/t Au

1.35 0.57

8.45

7. Distri Au

93.2 6.8

100.0

bution Au**

96.7 3.2

100.0

* After it was amalgamated, the residue assayed 0.25 g/t Au (average of 0.26, 0.25 and 0.24 g/t Au)

Based on residue assay after amalgamation

Page 139: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 28 -

rst NO. ill

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery from Composite A with a 16 hour retention time and a finer grind.

As for Test No. 108.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill for 10 minutes at 657. solids.

Time,

Hours

Preaeration:0-22 - 4.5

A. 5 - 6Cyanidation:

0-16

Total

Added, Grams

Act NaCN

---

0.35

0.35

ual Ca(OK) 2

0.500.200.07

0.03

0.80

Equiva NaCN

---

0.33

0.33

ilent CaO

0.380.150.05

0.02

0.60

Residual

Gr f NaCN

---

0.29

0.29

ims CaO

0.100.200.23

0.19

0.19

Consumed

Gr* NaCN

--

0.04

0.04

uns CaO

0.280.050.02

0.06

0.41

PH

From

11.611.811.8

11.8

To

11.211.811.8

11.8

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.12CaO: 1.22

Metallurgical Results

Product

16 h Preg.+Wash Soln 16 h Cy Residue*

Head (calculated)

Amount

1510 mL 334.8 g

334.8 g

Assay,mg7L,g7t Au

1.40 0.60

6.90

7. Distri Au

91.3 8.7

100.0

bution Au**

95.9 4.1

100.0

* After it was amalgamated, the residue assayed 0.27 g/t Au (average of 0.32, 0.27 and 0.22 g/t Au)

** Based on residue assay after amalgamation

Page 140: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 29 -

Test No. Ill - Continued

Screen Analysis

16 h Cyanide Residue

Mesh Size(Tyler)

* 28354865100150200270400

- 400

Total

7, RetainedIndividual

0.50.20.31.13.47.3

10.412.912.351.6

100.0

Cumulative

0.50.71.02.15.512.823.236.148.4100.0

-

7. PassingCumulative

99.599.399.097.994.587.276.863.951.6-

-

Page 141: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 30 -

test No. 112

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery from Composite A with a finer grind and a 24 hour retention time

As for Test No. 109.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill for 10 minutes at 657. solids.

Time,

Hours

Preaeration:0-33-6

Cyanidation:0 - 16.5

16.5 - 24

Total

Added, Grams

.-- Act NaCN

--

0.350.03

0.38

ual Ca(OH) 2

0.500.20

0.070.15

0.92

Equivi NaCN

--

0.330.03

0.36

ilent CaO

0.380.15

0.050.11

0.69

Residual

Gr B NaCN

--

0.300.30

0.30

tms CaO

0.100.20

0.140.21

0.21

Consumed

Gr i NaCN

--

0.030.03

0.06

ims CaO

0.280.05

0.110.04

0.48

PH

From

11.611.2

11.711.9

To

11.211.5

11.712.0

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.18CaO: 1.44

Metallurgical Results

Product

24 h Preg.+Wash Soln 24 h Cy Residue*

Head (calculated)

Amount

1250 mL 333.0 g

333.0 g

Assay, mg/L, g/t Au

2.34 1.79

10.60

7. Distrj Au

83.0 17.0

100.0

L bution Au**

96.9 3.1

100.0

* After it was amalgamated, the residue assayed 0.28 g/t Au (average of 0.25, 0.35, 0.24 g/t Au)

** Based on residue assay after amalgamation

Page 142: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 31 -

Fst No. 113

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery from Composite A with a finer grind and a 36 h retention time.

As for Test No. 110.

333 grams minus 10 mesh Composite A.

666 mL Pulp Density: 337- solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill at 657o solids for 10 minutes.

Time,

Hours

Preaeration:0-22 - 4.5

4.5 - 6Cyanidation:

0 - 16.516.5 - 36

Total

Added, Grams

Act NaCN

---

0.350.05

0.40

ual Ca(OH) 2

0.500.180.07

0.000.11

0.86

Equivi NaCN

---

0.330.05

0.38

alent CaO

0.380.140.05

0.000.08

0.65

Residual

Gr i NaCN

-.-

0.280.29

0.29

ims CaO

0.110.200.25

0.170.14

0.14

Consumed

Gra NaCN

.

.-

0.050.04

0.09

ins CaO

0.270.050.00

0.080.11

0.51

PH

From

11.511.311.8

11.711.9

To

11.211.711.6

11.912.0

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.27CaO: 1.54

Metallurgical Results

Product

36 h Preg.-fWash Soln 36 h Cy Residue*

Head (calculated)

Amount

1930 mL 332.1 g

332.1 g

Assay, mg/L, g/t Au

2.27 0.26

13.46

7. Distri Au

98.0 2.0

100.0

bution Au**

98.6 1.4

100.0

* After it was amalgamated, the residue assayed 0.18 g/t Au (average of 0.22, 0.17, 0.16 g/t Au)

** Based on residue assay after amalgamation

Page 143: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 32 -

ist No. 114

Purpose:

Procedure:

Feed :

Solution Volume:

To investigate the gold recovery from Composite A, with a finer grind and a 16 hour retention time.

As for Test No. 108.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill for 12 minutes at 657. solids.

Time,

Hours

Preaeration:0-22 - 4.5

4.5 - 6Cyanidation:

0-16

Total

Added, Grams

Act NaCN

---

0.35

0.35

ual Ca(OH) 2

0.500.170.08

0.04

0.79

Equivf NaCN

---

0.33

0.33

dent CaO

0.380.130.06

0.03

0.60

Residual

Gr i NaCN

---

0.29

0.29

mis CaO

0.120.190.22

0.20

0.20

Consumed

Gr*NaCN

---

0.04

0.04

mie CaO

0.260.060.03

0.05

0.40

PH

From

11.511.411.8

11.8

To

11.311.811.8

11.9

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.12CaO: 1.21

Metallurgical Results

Product

16 h Preg.+Wash Soln 16 h Cy Residue*

Head (calculated)

Amount

1470 mL 330.6 g

330.6 g

Assay, mg/L, g/t Au

1.70 0.34

7.89

7. Distri Au

-95.8 4.2

100.0

bution Au**

96.4 3.6

100.0

* After amalgamation, the residue assayed 0.28 g/t Au (average of 0.23, 0.20, 0.41 g/t Au)

** Based on residue assay after amalgamation.

Page 144: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 33 -

"st No. 114 - Continued

Screen Analysis

16 h Cyanide Residue

Mesh Size(Tyler)

+ 28354865100150200270400400

Total

7o RetainedIndividual

0.1.0.10.20.83.78.2

12.313.161.5

100.0" '

Cumulative

0.1-0.20.41.24.9

13.125.438.5100.0

-

7. PassingCumulative

99.9v

99.899.698.895.186.974.661.5-

-

Page 145: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

'st No. 115

Purpose :

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery from Composite A with a finer grind and a 24 hour retention time.

As for Test No. 109.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill at 657. solids for 12 minutes.

Time,

Hours

Preaeration0-33-6

Cyanidation0 - 16.5

16.5 - 24

Total

Added, Grams

Act NaCN

--

0.350.06

0.41

ual Ca(OH) 2

0.500.20

0.080.07

0.85

Equivi NaCN

- .-

0.330.06

0.39

ilent CaO

0.380.15

0.060.05

0.64

Residual

Gr a NaCN

--

0.270.27

0.27

ims CaO

0.100.19

0.200.19

0.19

Consumed

Gra NaCN

--

0.060.06

0.12

ims CaO

0.280.06

0.050.06

0.45

PH

From

11.511.4

11.711.8

To

11.211.5

11.712.0

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.36CaO: 1.36

Metallurgical Results

Product

24 h Preg.+Wash Soln 24 h Cyanide Residue*

Head (calculated)

Amount

1330 mL 331.7 g

331.7 g

Assay, mg/L, g/t Au

2.13 1.84

10.37

7. Distri Au

82.3 17.7

100.0

bution Au**

94.9 5.1

100.0

* After it was amalgamated, the residue assayed 0.46 g/t (average of 0.43, 0.33, 0.63 g/t Au)

** Based on residue assay after amalgamation.

Page 146: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 35 -

fs t No. 116

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery from Composite A with a finer grind and a 36 hour retention time.

As for Test No. 110.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill at 657o solids for 12 minutes.

Time,

Hours Preaeration:

0-22 - A. 5

4.5 - 6Cyanidation:

0 - 16.516.5 - 36

Total

Added, Grams

Act NaCN

.,--

0.350.05

0.40

ual Ca(OH) 2

0.500.170.11

0.000.15

0.93

Equivc NaCN

--

0.330.05

0.38

dent CaO

0.380.130.08

0.000.11

0.70

Residual

Gr* NaCN

^--

0.280.25

0.25

irns CaO

0.120.170.25

0.140.18

0.18

Consumed

Gr t NaCN

--

0.050.08

0.13

ims CaO

0.260.080.00

0.110.07

0.52

PH

From

11.411.711.9

11.711.9

To

11.311.911.6

11.712.0

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.39CaO: 1.55

Metallurgical Results

Product

36 h Preg.+Wash Soln 36 h Cy Residue*

Head (calculated)

Amount

1865 mL 335.2 g

335.2 g

Assay, mg/L.g/t Au

1.79 0.17

10.14

7, Distri Au

98.2 1.8

100.0

bution Au**

98.5 1.5

100.0

* After it was amalgamated, the residue assayed 0.15 g/t Au (average of 0.19, 0.13 and 0.13 g/t Au)

** Based on residue assay after amalgamation.

Page 147: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 36 -

"st No. 117

Purpose:

Procedure;

Feed:

Solution Volume:

To investigate the gold recovery from Composite A with a 24 hour preaeration and a 24 h retention time.

The sample was pulped with water in a 2 litre bottle and preaerated for 24 hours at 0.5 g/L lime. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill for 10 minutes at 657. solids.

Time,

Hours

Preaeration:0-22-44-20

20 - 24Cyanidation:0-22-20

20 - 24

Total

Added, Grams

Act NaCN

--.-

0.350.000.00

0.35

ual Ca(OH) 2

0.500.170.090.13

0.050.000.06

1.03

Equiv. NaCN

----

0.330.000.00

0.33

ilent CaO

0.380.130.070.10

0.060.000.06

0.80

Residual

Gr eNaCN

-..-

0.330.330.30

0.30

ims CaO

0.120.180.150.19

0.250.190.18

0.18

Consumed

GreNaCN

.

.

v

-

0.000.000.03

0.03

tins CaO

0.260.070.100.06

0.000.060.07

0.62

PH

From

11.711.611.511.5

12.011.811.6

To

11.311.711.411.8

11.811.411.5

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.08CaO: 1.86

Metallurgical Results

Product

24 h Preg.+Wash Soln 24 h Cy Residue*

Head (calculated)

Amount

1910 mL 333.8 g

333.8 g

Assay, mg/Ljg/t Au

2.56 2.16

16.8

7. Distri Au

87.0 13.0

100.0

bution Au**

98.7 1.3

100.0

* After it was amalgamated, the residue assayed 0.19 g/t Au

** Based on residue assay after amalgamation.

Page 148: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 37 -

k No. 118

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery from Composite A, with a 12 hour preaeration and a 24 hour retention time.

The sample was pulped with water in a 2 litre bottle and preaerated for 12 hours with lime. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill at 657e solids for 10 minutes.

Time,

Hours

Preaeration:0-22-44-99-12

Cyanidation:0 - 17.5

17.5 - 24

Total

Added, Grams

Act NaCN

--.-

0.350.03

0.38

ual Ca(OH) 2

0.330.320.160.09

0.000.12

1.02

Equiv NaCN

--.-

0.330.03

0.36

alent CaO

0.250.240.120.07

0.000.09

0.77

Residual

Grc NaCN

----

0.300.33

0.33

ims CaO

0.010.130.180.25

0.160.25

0.25

Consumed

Gr* NaCN

-..-

0.030.00

0.03

ims CaO

0.240.120.070.00

0.090.00

0.52

PH

From

11.211.611.711.7

11.911.6

To

10.511.611.611.8

11.411.7

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.09CaO: 1.56

Metallurgical Results

Product

24 h Preg.+Wash Soln 24 h Cy Residue*

Head (calculated)

Amount

1820 mL 333.1 g

333.1 g

Assay, mg/L.g/t Au

1.12 1.37

7.51

7. Distri Au

81.6 18.4

100.0

bution Au**

94.6 5.4

100.0

* After it was amalgamated, the residue assayed 0.35 g/t Au (average of 0.39, 0.30, 0.36 g/t Au)

** Based on residue assay after amalgamation.

Page 149: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 38 -

Test No. 119

Purpose:

Procedure:

Feed :

Solution Volume;

To investigate the gold recovery from Composite A with no preaeration and 24 h cyanidation.

The sample was pulped with water in a 2 litre bottle. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g minus 10 mesh Composite A.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill at 657. solids for 10 minutes.

Time,

Hours

0-22-44-20

20 - 24

Total

Added, Grams

Act NaCN

0.350.000.050.00

0.40

.ual Ca(OH) 2

0.330.130.090.14

0.86

Equiv* NaCN

0.330.000.050.00

0.38

ilent CaO

0.250.100.070.11

0.66

Residual

GrfNaCN

0.300.280.300.22

0.22

ims CaO

0.150.180.140.18

0.18

Consumed

Gr* NaCN

0.030.020.030.08

0.16

ims CaO

0.230.070.110.07

0.48

pH

From

11.812.011.711.8

To

11.711.811.511.9

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.48CaO: 1.44

Metallurgical Results

Product

24 h Preg.+Wash Soln 24 h Cy Residue*

Head (calculated)

Amount

1225 mL 333.3 g

333.3 g

Assay, mg/L, g/t Au

1.33 0.26

5.16

7. Distril Au

94.8 5.2

100.0

aution Au**

96.1 3.9

100.0

* After it was amalgamated, the residue assayed 0.20 g/t Au (average of 0.18, 0.18 and 0.25 g/t Au)

** Based on residue assay after amalgamation.

Page 150: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 39 -

jst No. 120

Purpose:

Procedure;

Feed :

Grind:

To recover the free gold in a table concentrate to beamalgamated.

The sample was pulped with water and fed over a Deistertable in open circuit.The table concentrate was placed into a l litre bottle.Mercury and sodium hydroxide were added and the bottle wasplaced on the rolls for 2 hours. Elutriation was then usedto recover the mercury.The amalgamation and table tailings were combined forcyanidation.

l kg sample Composite A.

l kg sample ground in the lab ball mill for 10 minutes at 657. solids.

Amalgamation Conditions:Mercury - 10 grams/100 grams of sample NaOH - 0.5 grams/100 grams of sample.

Metallurgical Results

Product

Amalgam Amal. Tailing

Head (calculated)

Weight7.

100.0

100.0

Assays, mg, g/t Au

4.387 3.52

7.91

7. Distribution Au

55.5 44.5

100.0

Page 151: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 121

Purpose:

Procedure:

Feed :

Solution Volume:

- 1*0 -

To investigate the gold recovery with a six hour pre- aeration and 16 hour cyanidation time.

The sample was pulped with water in a 2 litre bottle and preaerated for 6 hours with 0.5 g/L lime. NaCN and lime were added and the cyanidation was carried out on rolls in one 16 hour stage. The pulp was filtered and the residue washed three times with water.

250 g combined table and amalgam tailing from Test No. 120.

500 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-6

Cyanidation:0-16

Total

Added, Grams

Act NaCN

-- .

0.26

0.26

ual Ca(OH) 2

0.250.16

0.05

0.46

Equivi NaCN

--

0.25

0.25

ilent CaO

0.190.12

0.04

0.35

Residual

Gr*NaCN

.-

0.23

0.23

ims CaO

0.070.15

0.15'

0.15

Consumed

Gr a NaCN

--

0.02

0.02

ims CaO

0.120.04

0.04

0.20

PH

From

11.611.4

11.6

To

11.211.2

11.6

Reagent Consumption (kg/t of cyanide feed)

Metallurgical Results

NaCN: 0.08 CaO: 0.81

Product

1. 16 h Preg. Soln 2. Wash Solution 3. 16 h Cy Residue

Head (calculated)

Amount

440 mL 1140 mL 245.9 g

245.9 g

Assay Au

1.34 0.12 0.22*

3.17

s.mg/L.f Fe

0.19

-

s/tCu

2.78

-

7. Distribution Au

75.6 17.5 6.9

100.0

* average of 0.22, 0.22, 0.19 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 1580 mL 0.46 - - 93.1

Total Au recovery by amalgamation and cyanidation: 96.97.

Page 152: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

-la

No. 122

Purpose:

Procedure:

Feed :

To investigate the gold recovery with a six hour pre- aeration and a 24 hour retention time.

The sample was pulped with water in a 2 litre bottle. Pre-aeration was carried out for 6 hours at 0.5 g/L Ca(OH)z. NaCN and lime were then added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

250 g combined table and amalgam tailings.

Solution Volume: 500 mL Pulp Density: 337. solids

Solution Composition: 0.50 g/L NaCN0.50 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration0-22-6

Cyanidation:0-22-24

Total

Added, Grams

Act NaCN

--

0.260,00

0.26

ual Ca(OH) 2

0.250.17

0.060.03

0.51

Equiv. NaCN

--

0.250.00

0.25

ilent CaO

0.190.13

0.050.02

0.39

Residual

Gr a NaCN

--

0.250.19

0.19

ims CaO .

0.060.14

0.170.11

0.11

Consumed

Gra NaCN

--

0.000.06

0.06

ims CaO

0.130.05

0.020.08

0.28

pH

From

11.611.7

11.511.6

To

11.411.4

11.411.6

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.24CaO: 1.14

Metallurgical Results

Product

1. 24 h Preg. Soln 2. 24 h Wash Soln 3. 24 h Cy Residue

Head (calculated)

Amount

445 mL 1100 mL 245.3 g

245.3 g

Assays Au

1.68 0.14 0.30*

3.98

, mg/L Fe

0.13

-

g/tCu

3.19

-

7. Distribution Au

76.6 15.8 7.6

100.0

* average of 0.25, 0.32, 0.31 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 1545 mL 0.58 - - 92.4

Total Au recovery by amalgamation and cyanidation: 96,67.

Page 153: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 123

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery from Composite A without pre-aeration and a 16 hour retention time.

The sample was pulped with water in a 2 litre bottle. NaCN and lime were added and the cyanidation was carried out on rolls in one 16 hour stage. The pulp was filtered and the residue washed three times with water.

250 g combined table and amalgam tails from Test No. 121.

500 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

0-16

Total

Added, Grams

Act NaCN

0.26

0.26

ual Ca(OH) 2

0.25

0.25

Equivj NaCN

0.25

0.25

alent CaO

0.19

0.19

Residual

Grc NaCN

0.20

0.20

ims CaO

0.06

0.06

Consumed

Gra NaCN

0.05

0.05

uns CaO

0.13

0.13

pH

From

11.6

To

11.5

Reagent Consumption (kf/t of cyanide feed) NaCN: 0.21CaO: 0.54

Metallurgical Results

Product

1. 16 h Preg. Cy Soln 2. 16 h Wash Soln 3. 16 h Cy Residue

Head (calculated)

Amount

430 mL 965 mL 240.9 g

240.9 g

Assays Au

1.29 0.15 0.54*

3.45

s, mg/L Fe

2.06

-

g/t Cu

3.26

-

7. Distribution Au

66.9 17.5 15.7

100.0

* average of 0.36, 0.98, 0.27 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 1395 mL 0.49 - - 84.3

Total Au recovery by amal. * Cyn: 93.0 7.

Page 154: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 124

Purpose:

Procedure:

Feed :

Solution Volume:

To investigate the gold recovery from Composite A with a 24 hour retention time and without pre-aeration.

The sample was pulped with water in a 2 litre bottle. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

250 g combined table and amalgam tails from Test No. 120.

500 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,Hours

0-22-17

17-24

Total

Added, Grams

Act NaCN

0.260.000.07

0.33

ual Ca(OH) 2

0.250.140.09

0.48

Equiv NaCN

0.250.000.07

0.32

alent CaO

0.190.110.07

0.37

Residual

Gr,NaCN

0.250.180.24

0.24

ims CaO

0.080.120.16

0.16

Consumed

Gr i NaCN

0.000.070.01

0.08

ims CaO

0.110.070.03

0.21

PH

From

11.611.611.8

To

11.411.211.8

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.33CaO: 0.86

Metallurgical Results

Product

1. 24 h Preg. Cy Soln 2. 24 h Wash Soln3. 24 h Cy Residue

Head (calculated)

Amount

460 mL 1050 mL243.3 g

243.3 g

Assay Au

1.55 0.120.29*

3.74

s.mg/L, Fe

0.12

-

-

B/t Cu

3.43

-

-

7. Distribution Au

78.4 13.87.8

100.0

* average of 0.27, 0.41, 0.20 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 1510 mL 0.56 - - 92.2

Total Au recovery by amal. * cyn: 97.5 7.

Page 155: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- hk -

st No. 125

Purpose:

Procedure:

Feed:

Grind:

To recover the free gold in a table concentrate to be amalgamated.

As for Test No. 120.

l kg sample Composite A.

l kg sample ground in the lab ball mill for 8 minutes at 657. solids.

Amalgamation Conditions:

Mercury - 10 grams/100 grams of sample NaOH: - 0.5 grams/100 grams of sample

Metallurgical Results

Products

Amalgam Amalgam Tailing

Head (calculated)

Amount

1000 g

1000 g

Assays, mg, g/t Au

8.757 2.70

11.5

7. Distribution Au

76.4 23.6

100.0

Page 156: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 126

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery of a combined table and amalgam tailing with a six hour pre-aeration and 16 hours cyanidation retention time.

The sample was pulped with water in a 2 litre bottle. Pre-aeration was carried out for 6 hours with 0.5 g/L Ca(OH)2. NaCN and lime were added and the cyanidation was carried out on rolls in one 16 hour stages. The pulp was filtered and the residue washed three times with water.

333 g combined amalgam and table tailing from Test No. 125.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.50 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-6

Cyanidation:0-16

Total

Added, Grams

Ad NaCN

--

0.35

0.35

ual Ca(OH) 2

0.330.18

0.08

0.59

Equiv NaCN

--

0.33

0.33

alent CaO

0.250.14

0.06

0.45

Residual

Gr.NaCN

--

0.31

0.31

ims CaO

0.110.19

0.23

0.23

Consumed

Gra NaCN

--

0.02

0.02

ms CaO

0.140.06

0.02

0.22

PH

From

11.611.6

11.7

To

11.311.2

11.7

Reagent Consumption (kg/tonne of cyanide feed) NaCN: 0.06CaO: 0.68

Metallurgical Results

Product

16 h Preg. * Wash 16 h Cy Residue

Head (calculated)

Amount

1990 mL 322.5 g

322.5 g

Assays, mg/L.g/t Au

0.42 0.40*

2.99

7. Distribution Au

86.613.4

100.0

* average of 0.32, 0.51, 0.36 g/t Au

Total Au recovery by amal. * Cyn: 96.4 7.

Page 157: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 127

Purpose:

Procedure:

Feed:

To investigate the gold recovery of a combined table and amalgam tailing with a six hour preaeration.

The sample was pulped with water in a 2 litre bottle. Preaeration was carried out for 6 hours at 0.5 g/L Ca(OH)2. NaCN was then added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g combined table + amalgam tailing from Test No. 125.

Solution Volume: 666 mL

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Pulp Density: 337. solids

Reagent Balance:

Time,

Hours

Preaeration:0-33-6

Cyanidation:0-22-24

Total

Added, Grams

Act NaCN

--

0.350.00

0.35

ual Ca(OH) 2

0.330.18

0.070.04

0.62

Equivc NaCN

--

0.330.00

0.33

ilent CaO

0.250.14

0.050.03

0.47

Residual

Gr i NaCN

--

0.330.31

0.31

ims CaO

0.110.20

0.220.21

0.21

Consumed

Gre NaCN

--

0.000.02

0.02

ims CaO

0.140.05

0.030.04

0.26

PH

From

11.611.4

11.811.8

To

11.111.3

11.511.7

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.06CaO: 0.80

Metallurgical Results

Product

24 h Preg. + Wash Soln 24 h Cy Residue

Head (calculated)

Amount

1940 mL 324.6 g

324.6 g

Assays, mg/L.g/t Au

0.38 0.24*

2.51

7. Distribution Au

90.4 9.6

100.0

* Average of 0.25, 0.30, 0.17 g/t Au

Total Au recy by amal. ^ Cyn: 97.77.

Page 158: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 128

Purpose:

Procedure:

Feed:

To investigate the gold recovery from a combined table and amalgam tailing with just a 24 hour retention time.

The sample was pulped with water in a 2 litre bottle. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g combined table * amalgam tails from Test No. 125.

Solution Volume: 666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance:

l kg sample ground in the lab ball mill at 657. solids for 8 minutes.

Time,

Hours

0-33-88-24

Total

Added, Grams

Act NaCN

0.350.000.03

0.38

ual Ca(OH) 2

0.330.170.08

0.58

Equivi NaCN

0.330.000.03

0.36

ilent CaO

0.250.130.06

0.44

Residual

Gr s NaCN

0.330.300.28

0.28

tins CaO

0.120.190.20

0.20

Consumed

GriNaCN

0.000.030.05

0.08

ims CaO

0.130.060.05

0.24

PH

From

11.711.611.7

To

11.311.511.7

Reagent Consumption (kg/t of cyanide feed)

Metallurgical Results

NaCN: 0.25 CaO: 0.74

Product

24 h Preg. * Wash Soln 24 h Cy Residue

Head (calculated)

Amount

1760 mL 324.4 g

324.4 g

Assays, mg/Ljg/t Au

0.43 0.29*

2.62

7. Distribution Au

88.3 11.7

100.0

* average bf 0.32, 0.24, 0.30 g/t Au

Total Au recy by amal. * Cyn: 97.2 7.

Page 159: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

kst No. 129

Purpose:

Procedure:

Feed :

Solution Volume:

To produce a pregnant cyanide solution for Zn pptation and CN destruction tests.

The sample was pulped with water in a 4 litre bottle. Preaeration was carried out for 6 hours maintaining 0.5 g/L Ca(OH)a. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

3 x 1000 g Composite A, -10 mesh

3 x 2000 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Grind:

Reagent Balance: Test 129-A

3 x l kg sample ground in the lab ball mill at 657. solids for 10 minutes/kg.

Time,

Hours

Preaeration:0-22-44-6

Cyanidation:0-17

17-24

Total

Added, Grams

Act NaCN

---

1.050.42

1.47

ual Ca(OH) 2

1.000.710.39

0.300.68

3.08

Equivc NaCN

---

1.000.40

1.40

ilent CaO

0.760.540.30

0.230.52

2.35

Residual

Grt NaCN

---

0.600.95

0.95

an s CaO

0.220.460.53

0.240.58

0.58

Consumed

GraNaCN

---

0.400.05

0.45

ms CaO

0.540.300.23

0.520.18

1.77

PH

From

11.611.711.7

11.812.0

To

11.611.711.7

11.612.0

Reagent Balance: Test 129-B

Preaeration :0-22-44-6

Cyanidation:0-1717-24

Total

.i.-

1.050.42

1.47

1.000.710.42

0.370.71

3.21

-.-

1.000.40

1.40

0.760.540.32

0.280.54

2.44

--

-

0.600.85

0.85

0.220.440.48

0.220.55

0:55

---

0.400.75

0.55

0.540.320.28

0.540.21

1.89

11.611.711.7

11.812.0

11.611.711.7

11.612.0

Page 160: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

tst No. 129 - Continued

Reagent Balance: Test 129-C

Time,

Hours

Preaeration0 - 22-44-6

Cyanidation:0-17

17-24

Total

Added, Grams

Act NaCN

—.--

1.050.42

1.47

ual Ca(OH) 2

1.000.710.39

0.340.68

3.12

Equivj NaCN

---

1.000.40

1.40

ilent CaO

0.760.540.30

0.260.52

2.38

Residual

Gr t NaCN

-.-

0.600.84

0.84

ims CaO

0.220.460.50

0.240.61

0.61

Consumed

Gr* NaCN

.--

0.400.16

0.56

uns CaO

0.540.300.26

0.520.15

1.77

PH

From

11.6'11.711.7

11.812.0

To

11.611.711.7

11.712.0

Reagent Consumption (kg/t of cyanide feed, A-C)

Metallurgical Results

NaCN: 0.52 CaO: 1.81

Product

24 h Preg. Cy Soln 24 h Wash Soln 24 h Cy Residue

Head (calculated)

Amount

4900 mL 6210 mL 3017.0 g

3017.0 g

Assays, mg/L, g/t

Au

2.42 0.44 5.44

9.28

Ag

0.35

-

Cu

3.97

-

Fe

0.60

-

Zn

0.28

-

7. Distribution

Au

42.4 9.7

47.9

100.0

Page 161: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 50 -

1st No. 130

Purpose:

Procedure:

Sample:

Grind:

Mercury:

NaOH:

To recover the free gold from Composite A prior to cyanidation.

The sample was ground, then transferred into a 4 litre bottle. Mercury and sodium hydroxide were added and the bottle was placed on the rolls for 2 hours. The sample was then placed into a separatory funnel and the mercury was recovered by elutriation. The mercury was assayed for' gold and the amalgam tail, was used as feed for cyanidation tests.

l kg minus 10 mesh Composite A.

l kg sample ground in the lab ball mill for 12 minutes at 657. solids.

10 grams/100 grams of sample.

2.0 grams

Metallurgical Results

Product

Amalgam Amalgam Tailing

Head (calculated)

Amount

1000 g

1000 g

Assays, mg, g/t Au

6.595 2.66

9.25

7. Distribution Au

71.3 28.7

100.0

Page 162: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 51 -

t No. 131

Purpose:

Procedure;

Feed :

Solution Volume:

To investigate the gold recovery from an amalgam tailing with a 6 hour preaeration.

The sample was pulped with water in a 2 litre bottle. Preaeration was carried out for 6 hours with 0.5 g/L Ca(OH) 2 . NaCN and lime were then added and the cyanidation was carried out on rolls in one 16 hour stage. The pulp was filtered and the residue washed three times with water.

333 g Composite A amalgam tailing from test 130.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-6

Cyanidation:0-16

Total

Added, Grams

Act NaCN

--

0.35

0.35

ual Ca(OH) 2

0.330.22

0.07

0.62

Equiv. NaCN

--

0.33

0.33

ilent CaO

0.250.17

0.05

0.47

Residual

Gr i NaCN

--

0.31

0.31

ims CaO

0.080.20

0.03

0.03

Consumed

Gra NaCN

.-

0.02

0.02

ms CaO

0.170.05

0.22

0.44

PH

From

11.611.9

12.0

To

11.611.7

11.6

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.06CaO: 1.33

Metallurgical Results

Product

16 h Preg.-fWash Soln 16 h Cy Residue

Head (calculated)

Amount

1620 mL 330.6 g

330.6 g

Assay, mg/L.g/t Au

0.49 0.19*

2.59

7. Distribution Au

92.7 7.3

100.0

* average of 0.23, 0.16, 0.19 g/t Au

Total Au recovery by amal. * Cyn = 97.97o

Page 163: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 52 -

st No. 132

Purpose:

Procedure;

Feed :

Solution Volume:

To investigate the gold recovery from an amalgam tail, with a 6 hour preaeration and a 24 hour cyanidation time.

The sample was pulped with water in a 2 litre bottle. Pre aeration was carried out for 6 hours with 0.5 g/L Ca(OH)2. NaCN and lime were then added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g Composite A Amalgam Tail, from Test 130.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-6

Cyanidation:0-19

19 - 24

Total

Added, Grams

Ad NaCN

.-

0.350.03

0.38

tual Ca(OH) 2

0.330.21

0.080.09

0.71

Equivi NaCN

--

0.330.03

0.36

alent CaO

0.250.16

0.060.07

0.54

Residual

Gr i NaCN

--

0.300.29

0.29

ims CaO

0.090.19

0.180.25

0.25

Consumed

GriNaCN

.-

0.030.04

0.07

am s CaO

0.160.06

0.070.00

0.29

PH

From

11.611.9

12.012.0

To

11.611.7

11.611.4

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.21CaO: 0.87

Metallurgical Results

Product

24 h Preg.+Wash Soln 24 h Cy Residue

Head (calculated)

Amount

1790 mL 331.6 g

331.6 g

Assays, mg/L^/t Au

0.46 0.19*

2.67

7. Distribution Au

92.9 7.1

100.0

* average of 0.15, 0.21, 0.20 g/t Au

Total Au recovery by amal. -t- Cyn. ^ 98.0 'L

Page 164: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 53 -

;t No. 1 33

Purpose:

Procedure:

Feed:

Solution Volume:

To investigate the gold recovery from an amalgam tailing with a 12 h preaeration and a 24 hour cyanidation.

The sample was pulped with water in a 2 litre bottle. Preaeration was carried out for 12 hours with 0.5 g/L Ca(OH)z. NaCN and lime were then added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g Composite A Amalgam Tail, from Test 130.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-44-88-12

Cyanidation:0-16

16 - 24

Total

Added, Grams

Act NaCN

-w--

0.350.00

0.35

ual Ca(OH) 2

0.330.200.240.05

0.000.08

0.90

Equiv NaCN

----

0.330.00

0.33

alent CaO

0.250.150.180.04

0.000.06

0.68

Residual

Gn NaCN

~.--

0.330.28

0.28

ims CaO

0.100.070.210.25

0.190.25

0.25

Consumed

GrtNaCN

-.--

0.000.05

0.05

uns CaO

0.150.180.040.00

0.060.00

0.43

PH

From

11.611.612.011.9

12.012.0

To

11.511.611.711.9

11.612.0

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.15CaO: 1.29

Metallurgical Results

Product

24 h Preg.+Wash Soln 24 h Cy Residue

Head (calculated)

Amount

1770 mL 332.4 g

332.4 g

Assays, mg/L.g/t Au

0.48 0.16*

2.72

7. Distribution Au

94.1 5.9

100.0

* average of 0.17, 0.14, 0.17 g/t Au

Total Au recovery by amal. * Cyn * 98.3 7.

Page 165: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 135

Purpose:

Procedure:

Feed:

Conditions:

To conduct a S02 7Air cyanide destruction test on a Zn precipitation barren solution.

The test was conducted in a 500 mL baffled beaker. The sample was fed with a Beckman solution pump. The solution was agitated by a mechanical stirrer. The pH was maintained by a ratiometer pH meter in conjunction with a titrator connected to a magnetic valve controlling the flow of the lime slurry. The SOa/Air mixture was controlled using a Matheson flowmeter. After the 30 minute batch (start-up), the circuit ran continuously for 90 minutes. The solution was collected during the last 30 minutes for analyses. The assay sample was filtered through a 0.45 vim micropore filter.

2.0 litres of preg. solution from Test 129 from which most of the gold had been precipitated with Zn dust.

Feed Rate:Vessel:Retention Time:

PH: S0 2 to CN(T) Ratio:

500 L/30 minutes500 mL30 minutes8.5 maintained with 20 g/L Ca(OH) 2 slurry3.2 g S02 /! g CN(T)

Calculations

Feed Analyses, mg/L:Cu - 3.82 Fe - 0.57 CN(T) - 197 Zn - 5.12

Copper Addition: Start up (batch) per l l itre of solution mg Cu added - 50 - Cu(F)

~ ( 46.18 x 3.93)^ 181.5 mg CuSOM .5H 2 07L~ 90.74 mg CuSOi,.5H 2 07500 mL~ 0.91 mL 107. CuS05 .5H 2 0

Continuous: mg Cu Added 10 - Cu(F) 6.18 mg/L Cu

Strength of Solution:

6.18 mg Cu 19.4 mL

Feed Rate: 1000 mL/60 minutes

Constant Pump Rate: 19.4 mL/h

24.28 mg CuSOM .5H 2 0 19.4 mL

250.3 mg CuSOk .5H 2 0 200 mL

Page 166: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 55 -

jst No. 1 35 - Continued

S02 Addition: per l litre of feed.

l g CN(T) requires 3.2 g of S0 2 197 mg CN(T) requires 630 mg of S02 0.630 g of S0 2 contained in

= 0.630 g x 22.4 ~ 0.221 L at STP 64

~ 0.221 L x 293"C - 0.237 L at NTP 273 C C

0.237 L of S0 2 contained in 0.237 x 1001.5

15.8 L of 1.57. S02 7Air

Retention Time: 60 minutes/litre of feed

Gas Flow:

Flow Meter:

Test Data:

263 cc/min.

62 mm Matheson 602 STST Float

Procedure

Batch Start-up

Continuous

Sample Period jj

Time Min.

005

101520253005

3045607590

Feed Rate mL/min.

0000000016.7

\ t

1.57. S02 / Air , cc/m

0263

\ f

Reag.Vol. Cu,mgAn*

023**

0.10

\A

PH

12.09.38.58.58.58.58.68.68.78.58.58.58.58.78.5

em f mV

M

+4075808090105951001057575757575

mg

Solution Strength 319 mg Cu/litre Batch: 45 ml of 27. Ca(OH) 2 Continuous: 60 mL of 27. Ca(OH) 2

Page 167: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 56 -t No. 135 - Continued

Metallurgical Results

Product

CN Destn: Feed Soln Barren Soln

Assays, mg/L

CN(T)

197 86.6

Cu

3.82 18.9

Fe

0.57 0.57

CNS

302.7 310.9

Zn

5.12 4.15

Au

0.66

Ag

0.05

Ni

1.38

Hg

0.002

Page 168: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 57 -

sts No. 136 and 137

Purpose :

Procedure:

Feed:

Conditions;

To conduct an alkaline chlorination cyanide destruction test on a Zn pptation barren solution.

Barren solution was placed into a baffled vessel. The chlorine was added slowly wile maintaining the pH above 11 with lime. When the emf appeared to have stabilized, it was assumed that the reaction was complete. NaAsOa was then added until the chlorine was no longer detected with Pb(N03 )2 paper.

2 x 500 mL Test 129 pregnant solution (treated with Zn dust),

Chlorine - 67. NaOCl is 28.6 g/L CI

10 : lTest 136 - CI : CN(T)

197 x 0.5 x 10

Test 137 - CI : CN(T)

197 x 0.5 x 7

985 mg CI 34.4 mL NaOCl

689.5 mg CI 24.1 mL NaOCl

Test Data

TimeMin.

CImg

emfmV

PH

Test No. 136, C1:CN(T) - 10:1

00351015

.985 ---

+ 70-

440475495502

12.0.11.811.811.811.8

Test No. 137, C1:CN(T) ~ 7 :1

0035101520

^689--.--

H- 701101551201108580

12.011.811.0

10.9-11.611.511.311.3

Ca(OH) 2

-

0.22.~-

--

0.06---

Page 169: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 58 -

sts No. 136 and 137 - Continued

Metallurgical Results

Solution

CN Destruction:Feed SolutionT- 136 Barren SolnT-137 Barren Soln

Assays, mg/L

CN(T)

1972.939.33

Cu

3.822.473.72

Fe

0.570.540.51

CNS

3030.5O.5

Zn

5.122.700.85

Hg

0.0020.0030.001

Page 170: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 138

Purpose:

Procedure:

Feed:

Grind:

- 59 -

To investigate the recovery of free gold from Composite A prior to cyanidation.

The sample was pulped in a 2 litre bottle with water. Mercury and sodium hydroxide were added and the bottle was placed on the rolls. After 2 hours, the sample was placed in a separatory funnel and the mercury was recovered by elutriation. The tailing was then filtered and retained as feed for cyanidation tests.

l kg sample Composite A, minus 10 mesh.

l kg sample was ground in the lab ball mill for 6.5 minutes at 657. solids.

Metallurgical Results

Product

Amalgam Amalgam. Tailing

Head (calculated)

Amount

1000 g

1000 g

Assays, mg, g/t Au

7.586 2.91

10.5

7. Distribution Au

72.3 27.7

100.0

Page 171: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

jest No. 139

Purpose:

Procedure:

Feed :

Solution Volume:

- 60 -

To investigate the gold recovery from an amalgam tailing with a 12 hour retention time.

The sample was pulped with water in a 2 litre bottle. Preaeration was carried out for six hours with 0.5 g/L Ca(OH) 2 . NaCN was then added and the cyanidation was carried out on rolls in one 12 hour stage. The pulp was filtered and the residue washed three times with water.

333 g Amalgam tailing (Comp. A) from Test 138.

666 mL Pulp Density: 337o solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-44-6

Cyanidation:0-12

Total

Added, Grams

Act NaCN

.--

0.35

0.35

ual Ca(OH) 2

0.330.180.02

0.00

0.58

Equivj NaCN

.--

0.33

0.33

alent CaO

0.250.140.05

0.00

0.44

Residual

Gr i NaCN

.--

0.25

0.25

uns CaO

0.110.200.25

0.23

0.23

Consumed

Gra NaCN

.--

0.08

0.08

ms CaO

0.140.050.00

0.02

0.21

PH

From

11.911.712.0

12.1

To

11.512.012.0

12.1

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.24CaO: 0.63

Metallurgical Results

Product

12 h Preg. Cy Soln 12 h Wash Solution 12 h Cy Residue

Head (calculated)

Amount

570 mL 1480 mL 331.9 g

331.9 g

Assays, mg/L.g/t Au

1.06 0.076 0.67*

2.80

7. Distribution Au

64.5 11.8 23.7

100.0

* average of 0.62, 0.71 g/t Au

Calculated Grades and Recoveries

Combined Solutions 2050 mL 0.35 76 .3

Total Au Recovery by Amal. * Cyn: 93.4 7.

Page 172: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 61 -

est No. 139 - Continued

Screen Analysis

12 h Cyanide Residue

Mesh Size(Tyler)

* 10142028354865

100150200270400

- 400

Total

7. RetainedIndividual

0.11.01.31.21.22.24.18.2

10.111.310.48.7

40.2

100.0

Cumulative

0.11.12.43.64.87.0

11.119.329.440.751.159.8100.0

-

7, PassingCumulative

99.998.997.696.495.293.088.980.770.659.348.940.2

,.

-

Page 173: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

jest No. 140

Purpose:

Procedure:

Feed :

Solution Volume:

- 62 -

To investigate the gold recovery of an amalgam tail, with a s ix hour preaeration and a 16 hour cyanidation retentiontime.

The sample was pulped with water in a 2 litre bottle. Preaeration was carried out for 6 hours with 0.5 g/L Ca(OH) 2 . NaCN was then added and the cyanidation was carried out on rolls in one 16 hour stage. The pulp was filtered and the residue washed three times with water.

333 g Amalgam tailing sample (Comp. A) from Test 138.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-44-6

Cyanidation:0-16

Total

Added, Grams

Act NaCN

---

0.35

0.35

ual Ca(OH) 2

0.330.210.05

0.00

0.59

Equiv, NaCN

---

0.33

0.33

alent CaO

0.250.160.04

0.00

0.45

Residual

Gr,NaCN

---

0.23

0.23

am s CaO

0.090.210.25

0.24

0.24

Consumed

Gr s NaCN

.--

0.10

0.10

ims CaO

0.160.040.00

0.01

0.21

PH

From.

11.912.011.9

12.1

To

11.611.812.0

12.1

Reagent Consumption (kg/t of cyanide feed)

Metallurgical Results

NaCN: 0.30 CaO: 0.62

Product

1. 16 h Preg. Solution 2. 16 h Wash Solution 3. 16 h Cy Residue

Head (calculated)

Amount

600 mL 1240 mL 336.3 g

336.3 g

Assays, mg/L.g/t Au

1.10 0.087 0.67*

2.97

7. Distribution Au

66.0 11.0 23.0

100.0

* Average of 0.57, 0.76 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 1840 mL 0 .42 77 .0

Total Au recovery by amal. + Cyn ~ 9 3.6 7.

Page 174: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 141

Purpose:

Procedure:

Feed:

Solution Volume:

- 63 -

To investigate the gold recovery of an amalgam tailing with a six hour preaeration and a 24 hour cyanidation retention time.

The sample was pulped with water in a 2 litre bottle. Preaeration was carried out on the rolls with 0.5 g/L Ca(OH)2 maintained for 6 hours. NaCN and lime were then added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g Amalgam Tailing sample (Comp. A) from Test 138.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Re ag en t Balanc e :

Time,

Hours

Preaeration:0-22-55-6

Cyanidation:0-24

Added, Grams

Act NaCN

---

0.35t

Total 0.35

ual Ca(OH) 2

0.330.200.07

0.00

0.60

Equiv. NaCN

---

0.33

0.33

alent CaO

0.250.150.05

0.00

0.45

Residual

GrcNaCN

---

0.20

0.20

ims CaO

0.100.200.05

0.23

0.23

Consumed

Gra NaCN

---

0.13

0.13

JT1S

CaO

0.150.050.00

0.02

0.22

PH

From

11.912.011.8

12.0

To

11.611.711.8

12.3

Reagent Consumption (kg/t of cyanide feed)

Metallurgical Results

NaCN: 0.39 CaO: 0.67

Product

1. 24 h Preg. Cy Soln 2. 24 h Wash Solution 3. 24 h Cy Residue

Head (calculated)

Amount

620 mL 1620 mL 330.8 g

330.8 g

Assays, mg/L.g/t Au

1.16 0.065 0.44*

2.96

7. Distribution Au

73.5 11.2 15.3

100.0

* average of 0.52, 0.36 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 2240 mL 0. 37 84. 7

Total Au recovery by Amal. 4- Cyn: 95.8 'L

Page 175: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 6k -

t No. 142

Purpose:

Procedure:

Feed:

Grind:

To recover the free gold from Composite A prior to cyanidation.

As for Test 138.

l kg minus 10 mesh Composite A.

l kg sample ground in the lab ball mill for 5 minutes at 657. solids.

Metallurgical Results

Product

Amalgam Tailing

Head (calculated)

Amount

1000 g

1000 g

Assays, mg, g/t Au

7.317 3.36

10.68

7. Distribution Au

68.5 31.5

100.0

Page 176: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 65 ~

.est No. 143

Purpose:

Procedure:

Feed :

Solution Volume:

To investigate the gold recovery from an amalgam tailing with a coarse grind, 6 hour preaeration and 12 hour cyanidation retention time.

As for Test No. 139.

333 g Amalgam Tailing sample (Comp. A) from Test 142.

666 mL Pulp Density: 337c solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration :0-22-44-6

Cyanidation :0-12

Total

Added , Grams

ActNaCN

.--

0.35

0.35

ual Ca(OH) 2

0.330.200.03

0.00

0.56

Equiv*NaCN

---

0.33

0.33

alent CaO

0.250.150.02

0.00

0.42

Residual

Gr,NaCN

---

0.21

0.21

ims CaO

0.100.230.25

0.24

0.24

Consumed

Gre NaCN

-.-

0.12

0.12

uns CaO

0.150.020.00

0.01

0.18

PH

From

11.911.712.0

12.1

To

11.512.012.0

12.1

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.36CaO: 0.55

Metallurgical Results

Product

1. 12 h Preg. Cy Soln 2. 12 h Wash Soln 3. 12 h Cy Residue

Head (calculated)

Amount

570 mL 1300 mL 327.9 g

327.9 g

Assays, mg/L.g/t Au

1.02 0.081 0.61*

2.71

7. Distribution Au

65.2 12.4 22.4

100.0

* average of 0.57, 0.64 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 1870 mL 0. 37 77. 6

Total Au Recovery of Amal. * Cyn: 92.9 7.

Page 177: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 66 -

No. 143 - Continued

Screen Analysis

12 h Cyanide Residue

Mesh Size(Tyler)

* 10142028354865100150200270400

- 400

Total

'lo RetainedIndividual

0.11.71.92.02.34.07.08.710.58.98.77.6

36.6

100.0

Cumulative

0.11.83.75.78.0

12.019.027.738.247.155.863.4100.0

-

7c PassingCumulative

99.998.296.394.392.088.081.072.361.852.944.236.6-

-

Page 178: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 6? -

st No. 144

Purpose:

Procedure:

Feed:

Solution Volume;

To investigate the gold recovery from an amalgam tailing sample with a coarse grind, 6 hour preaeration and a 16 hour cyanidation retention time.

As for Test No. 140.

333 g Amalgam Tailing sample (Comp. A) from Test 142.

666 mL Pulp Density: 337o solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-44-6

Cyanidation:0 - 16

Total

Added, Grams

Act NaCN

---

0.35

0.35

ual Ca(OH) 2

0.330.180.05

0.03

0.59

Equiv NaCN

---

0.33

0.33

alent CaO

0.250.140.04

0.02

0.45

Residual

Gr, NaCN

---

0.19

0.19

ams CaO

0.110.210.23

0.24

0.24

Consumed

GriNaCN

---

0.14

0.14

ims CaO

0.140.040.02

0.01

0.21

PH

From

11.912.011.9

12.1

To

11.811.812.0

12.1

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.42CaO: 0.63

Metallurgical Results

Products

1. 16 h Preg. Cy Soln 2. 16 h Wash Solution 3. 16 h Cy Residue

Head (calculated)

Amount

610 mL 1350 mL 335.2 g

335.2 g

Assays, mg7L,g7t Au

1.23 0.08 0.98*

3.55

7. Distribution Au

63.0 9.2

27.8

100.0

* average of 1.11, 0.84 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 1960 mL 0 .44 72 .2

Total Au Recovery by Amal. + Cyn: 91.2 7.

Page 179: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

t No. 145

Purpose:

Procedure:

Feed:

Solution Volume;

- 68 ~

To investigate the gold recovery from an amalgam tailing sample with a coarse grind and a 24 hour cyanidation retention time.

As for Test No. 141.

333 g Amalgam Tailing sample (Comp. A) from Test 142.

666 mL Pulp Density: 337. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-22-55-6

Cyanidation:0-24

Total

Added, Grams

Act NaCN

---

0.35

0.35

ual Ca(OH) 2

0.330.170.05

0.00

0.56

Equivi NaCN

---

0.33

0.33

ilent CaO

0.250.130.04

0.00

0.42

Residual

Gr*NaCN

---

0.17

0.17

uns CaO

0.120.210.25

0.20

0.20

Consumed

Grf NaCN

--

' -

0.16

0.16

uns CaO

0.130.040.00

0.05

0.22

pH

From

11.912.011.8

12.0

To

11.811.711.8

12.3

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.48CaO: 0.66

Metallurgical Results

Products

1. 24 h Preg. Solution 2. 24 h Wash Solution 3. 24 h Cy Residue

Head (calculated)

Amount

620 mL 1475 mL 333.8 g

333.8 g

Assays, mg7L,g7t Au

1.40 0.069 0.92*

3.83

7. Distribution Au

68.0 7.8

24.2

100.0

* average of 0.90, 0.93 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 2095 mL 0 .46 75 .8

Total Au recovery by amal. -f- cyn: 92.4 7.

Page 180: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 69 -

st No. 147

Purpose:

Procedure:

Feed:

Feed Analysis:

Conditions:

Test A

To investigate the destruction of cyanide using the S02 7Air method.

Three batch CN destruction tests were conducted in a 500 mLbaffled vessel. Agitation was provided by a mechanicalstirrer. The pH was maintained using a radiometer PHM 82pH meter in conjunction with a titrator connected to a magneticvalve controlling the flow of the lime slurry. The SO?/airmixture was controlled using a Matheson flowmeter.At the conclusion of each test, the solution was filteredthrough a 0.45 \m micropore filter and was sent for analysis.

3 x 500 mL comb. preg. soln from Tests 134-141 and 143-145 (treated with Zn dust).

CN(T): 292 mg/L

Vessel: 500 mLRetention Time: 30 minutesMaintained at a pH of 9.0 with 27. Ca(OH) 2 slurryCu addn 50 mg - 2 mL CuSOi,.5H 2 0SOz/CN Ratio: 4.5:1S02 Addition per l litre of Feed:

l g CN(T) requires 4.5 g of S0 2 292 mg CN(T) requires 1.314 g of S0 2 1.314 g of S0 2 contained in

~ 1 .314 g x 22.4 * 0.460 L at STP

Test B

0.460 L x 293'C 273 e C

0.494 L at NTP

0.494 L of S02 contained in 0.494 x 100175

32.93 L of 1.5%/alr

Retention Time: Gas Flow: Flow Meter:

60 minutes/litre of feed549 cc/min.105 mm Matheson 602-STST Float

Vessel: 500 mLRetention Time: 30 minutesMaintained at a pH of 9.0 with 27- Ca(OH) 2 slurryCu addn 50 mg - 2 mL CuSOi,.5H2 0S02 ;CN Ratio: 3.8:1S02 Addition per l litre of feed

l g CN(T) requires 3.8 g of S02 292 mg CN(T) requires 1.11 g of S0 2 1.11 g of S02 contained in

1.11 g 22.4 ~64~

0.389 L x 293"C

0.389 L at STP

0.417 L at NTP273'C

0.417 L of S02 contained in 0.417 x 100T75

27.8 L at 1.5%/alr

Page 181: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

-70-

it No. 147 - Continued

Test B - Cont'd

Test C:

Retention Time: Gas Flow; Flow Meter:

60 min/litre of feed463 cc/min.92 mm Matheson 602 STST Float

Cu Addition 80 mg (78 mg Cu required to complex all the free CN assuming Cu reacts with CN in a 3:1 molar ratio). CN Free: 192 mg/L S0 2 Addition same as Test 147B.

After 30 minutes, 250 mL solution was removed and filtered. The 802/air flow was reduced by half and the test was continued for another 30 minutes,

Test Data:

Procedure

Batch Test No. A

Batch Test No. B

Batch Test C

250 mL SampleRemoved

Time Min.

0006

1015202530

00005

1015202530

000051015202530354045505560

Feed Rate ml/min

^

00000000

0000000000

0-

--

-.

--

----

--

.

-

1.57. S02 / Air .cc/m

549

w

-

463

--

463463463463463463463232232232232232232

Reag.Vol. Cu*

50.------

50--------

79-

78--.-------. -

PH

12.312.2.9.2'9.1

9.09.09.09.0

12.312.212.19.29.29.19.29.29.19.1

12.39.5.

p.

9.09.09.09.19.09.09.09.09.09.09.09.0

emf mV

-180+290

-90110125140260275

-180+250200120130150140140170260

-240*

o

410200160150150150150130190230230250230

Page 182: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 71 -

No. 147 - Continued

Metallurgical Results

Solution

CND Feed Soln0.5 h Barren Soln A0.5 h Barren Soln B0.5 h Barren Soln C1.0 h Barren Soln D

Assays, mg/L

CN(T)

29245.442.736.824.0

Cu

1.691.881.34~-

Fe

^.02*:0.02^.02

--

Zn

11.80.450.22--

CN(Free)

192.---

Page 183: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

is t No. 149

Purpose:

Procedure:

Feed:

Conditions

- 72 -

To investigate the precipitation of gold using zinc dust from cyanidation solutions.

The free cyanide concentration of the feed solution was made up to 0.5 g/L NaCN. The solution was transferred to a separatory funnel and deaerated for 30 minutes with nitrogen. Pb(N0 3 ) 2 and Zn dust were added in slurry form through the top of the funnel. The solution was mixed with nitrogen for 30 minutes. After this time, it was filtered through a micro pore filter with nitrogen being bubbled into it during filtration.

A: 1000 mL Test 112 preg. and wash solutions B: 1000 mL Test 113 preg. and wash solutions

Zn Dust Addition:

NaCNPHZn Dust Addn

Pb(N03 ) 2

0.5 g/L 11.6 100 x

theoretical 0.25xZn

B

0.5 g/L 11.1 50 x

theoretical 0.25xZn

A: b:

Metallurgical Results

1.0 L x 2.34 mg/L Au x 0.332 x 100 = 0.078 g Zn 1.0 L x 2.27 mg/L Au x 0.332 x 50 ^ 0.038 g Zn

Products

A: Feed SolutionBarren Solution

B: Feed SolutionBarren Solution

Assays, mg/LAu

2.340.0122.270.12

Lr\

11.5-

9.94

Page 184: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 73 -

st No. 150

Purpose:

Procedure:

Feed :

Conditions:

Calculations:

Copper Addition:

S0 2 Addition:

To conduct a batch SOj/Air cyanide destruction test on a Zn barren solution.

As per Test 147.

500 mL Zn barren solution from Test 149A.

Batch CN Destruction:

Vessel: . 500 mLRetention Time: 60 minutespH: 8.5 maintained with 20 g/L Ca(OH) 2 slurryCN to Cu Molar Rates: 3:1S0 2 to CN(T) Ratio: 8.0 g of S0 2 /! g CN(T)

Total CN: 238 mg/L Free CN: 236 mg/L

Molar Ratio CN:Cu - 3:1

CN - 26 mg/mole Cu - 63.5 mg/mole

236 mg CN 26 mg/mole 9.077 moles CN

add 3.026 mg moles x 63.5 mg/mg mole s 192 mg Cu/L = 96 mg Cu/500 mL (96 mg Cu+50) x 3.93 * 573.78 mg CuSOi, .5H20/500 mL

~ 5.74 mL 107. CuS0 5 .5H 2 0

per litre of feedl g CN(T) requires 8.0 g S02238 mg/L requires 1.904 mg of SO Z1.904 mg of S0 2 contained in

= 1.904 mg x 22.4 ~ 0 .666 L at STP 64

0.666 L x 293 e C 0.715 L at NTP273 0 C

0.715 L of S0 2 contained in 0.715 x 100r? 47.67 L of 1.57. S0 2 AAir

Retention Time:

Gas Flow:

Flow Meter:

60 minutes/litre of feed

795 cc/minutes

142 mm Matheson 602-STST Float

Page 185: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

No. 150 - Continued

Test Data:

Procedure

Batch Test

250 ml Sample Removed

Time Min.

0005

15202530

354045505560

Feed Rate mL/min.

w-------

--.---

1.57. S0 2 / Air, cc/m

-

142

, f

83

^ f

Reag.Vol. Cu mg

W

146.--..-

- .v.-

pH

11.88.6.8.58.68.68.68.6

8.68.68.68.68.68.6

emf mV

-3604-3 70

.150150260270270

260250270250250250

140 mL of 27. Ca(OH) z slurry added.

Metallurgical Results

Solution

CND Feed Solution CND Barren Soln, 30 min. CND Barren Soln 60 min.

Assays, mg/L

CN(T)

238 2.81 2.33

Cu

2.16 3.15

CN(F)

236

Zn

11.5 0.19 0.35

Au

:

Page 186: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 75 -

t No. 151

Purpose:

Procedure:

Sample :

Grind:

To investigate the recovery of free gold prior to cyanidation.

The sample was pulped into a 4 litre bottle with water. Mercury and sodium hydroxide were added and the bottle was placed on the rolls. After one hour, the pulp was transferred into a separatory funnel and the mercury was removed by elutriation. The mercury was then sent for analyses and the amalgam tail, was filtered and divided into two equal parts for cyanidation.

l kg Composite A, -10 mesh.

l kg sample ground in the lab ball mill at 657. solids for 9 minutes.

Conditions:Mercury: 10 grams/100 grams sample NaOH: 0.5 grams/100 grams of sample.

Metallurgical Results

Products

Amalgam Amal. Tailing

Head (calculated)

Amount

995.1 g

995.1 g

Assays, mg, g/t Au

7.179 5.54

12.7

7o Distribution Au

56.6 43.4

100.0

Page 187: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 152

Purpose:

Procedure:

Feed :

Solution Volume:

- 76 -

To investigate the gold recovery with a lower cyanide concentration and a 16 hour retention time.

As for Test No. 140.

500 g Composite A Amalgam Tail, from Test 151.

1000 mL Pulp Density: 3 37, solids

Solution Composition: 0.40 g/L NaCN0.50 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-33-6

Cyanidation:0-22-16

Total

Added, Grams

Act NaCN

--

0.420.00

0.42

ual Ca(OH) 2

0.500.38

0.160.07

1.11

Equiv* NaCN

--

0.400.00

0.40

il en t CaO

0.380.29

0.120.05

0.84

Residual

Gn NaCN

--

0.400.36

0.36

UT) S

CaO

0.090.26

0.330.34

0.34

Consumed

Gre NaCN

--

0.000.04

0.04

ims CaO

0.290.12

0.050.04

0.50

PH

From

11.611.6

12.012.0

To

11.011.6

12.011.7

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.08CaO: 1.01

Metallurgical Results

Product

1. 16 h Preg. Cy Soln 2. 16 h Wash 3. 16 h Cy Residue

Head (calculated)

Amount

860 mL 1860 mL 495.9 g

495.9 g

Assays, mg/L.g/t Au

2.13 0.20 1.65*

6.09

'L Distribution Au

60.6 12.3 27.1

100.0

* average of 0.41, 3.55, 1.00 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 2720 mL 0 .81 72 .9

Overall Au recovery by Amal. * Cyn: 88.2 7.

Page 188: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- TT -

t No. 152 - Continued

Screen Analysis

16 h Cyanide Residue

Mesh Size(Tyler)

+ 6 5100150200270400400

Total

7o RetainedIndividual

3.33.97.5

11.012.010.851.5

100.0

Cumulative

3.37.2

14.725.737.748.5100.0

-

'lo PassingCumulative

96.792.885.374.362.351.5-

-

Page 189: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

.st No. 153

Purpose:

Procedure:

Feed:

Solution Volume:

- 78 -

To investigate the gold recovery with a lower cyanide concentration and a 24 hour retention time.

As for Test No. 141.

500 g Composite A Amalgam Tail, from Test No. 151.

1000 mL Pulp Density: 337. solids

Solution Composition: 0.4 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-33-6

Cyanidation :0-22-24

Total

Added, Grams

Act NaCN

--

0.420.00

0.42

ual Ca(OH) 2

0.500.37

0.160.07

1.10

Equivi NaCN

--

0.400.00

0.40

ilent CaO

0.380.28

0.120.05

0.83

Residual

Gr* NaCN

--

0.400.30

0.30

uns CaO

0.100.26

0.330.35

0.35i

Consumed

Gra NaCN

--

0.000.10

0.10

un s CaO

0.280.12

0.050.03

0.48t

PH

From

11.611.6

12.012.0

To

11.011.6

12.411.6

Reagent Consumption (kg/t of cyanide feed)

Metallurgical Results

NaCN: 0.20 CaO: 0.96

Products

1. 24 h Preg. Cy Soln 2. 24 h Wash Solution 3. 24 h Cy Residue

Head (calculated)

Amount

880 mL 2120 mL 499.2 g

499.2 g

Assays, mg/L.g/t Au

1.86 0.14 1.11*

4.98

7. Distribution Au

65.8 11.9 22.3

100.0

* average of 0.31, 2.70, 0.32 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 3000 mL 0 .64 77. 7

Overall Au Recovery by Amal. -f Cyn: 90.3 7.

Page 190: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 79 -

t No. 154

Purpose:

Procedure:

Sample:

Grind:

Conditions;

To recover the free gold from Composite A prior to cyanidation.

As for Test No. 151.

l kg Composite A, -10 mesh.

l kg sample ground in the lab ball mill at 657o solids for 9 minutes.

Mercury: 10 grams/100 grams of sample NaOH: 0.5 grams/100 grams of sample

Metallurgical Results

Products

Amalgam Amal. Tailing

Head (calculated)

Amount

995.9 g

995.9 g

Assays, mg, g/t Au

6.426 3.91

10.3

7. Distribution Au

62.3 37.7

100.0

Page 191: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

st No. 155

Purpose:

Procedure:

Feed:

Solution Volume:

- 80 -

To investigate the gold recovery with an even lower NaCN concentration and a 16 hour retention time.

As for Test No. 140.

500 g Composite A Amalgam Tail, from Test No. 154.

1000 mL Pulp Density: 337. solids

Solution Composition: 0.2 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-33-6

Cyanidation:0-22-16

Total

Added, Grams

Act NaCN

--

0.210.00

0.21

ual Ca(OH) 2

0.500.42

0.210.07

1.20

Equiv* NaCN

--

0.200.00

0.20

alent CaO

0.380.32

0.160.05

0.91

Residual

Gr* NaCN

.-

0.200.19

0.19

uns CaO

0.060.22

0.330.34

0.34

Consumed

Gr* NaCN

.-

0.000.01

0.01

uns CaO

0.320.16

0.050.04

0.57

PH

From

11.611.6

11.812.0

To

11.011.6

11.811.7

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.02CaO: 1.15

Metallurgical Results

Product

1. 16 h Preg. Solution 2. 16 h Wash 3. 16 h Cy Residue

Head (calculated)

Amount

850 mL 1750 mL 496.6 g

496.6 g

Assays, mg/Ljg/t Au

1.36 0.14 0.86*

3.68

7. Distribution Au

63.2 13.4 23.4

100.0

* average of 1.18, 0.51, 0.88 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 2600 mL 0. 54 76. 6

Overall Au Recovery by Amal. * Cyn: 91.2 7.

Page 192: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

t No. 156

Purpose:

Procedure:

Feed :

Solution Volume:

- 81 -

To investigate the gold recoery with the lower NaCN concentration and a 24 hour retention time.

As for Test No. 141.

500 g Composite A Amalgam Tail, from Test 154.

1000 mL Pulp Density: 337. solids

Solution Composition: 0.2 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time,

Hours

Preaeration:0-33-6

Cyanidation:0-22-24

Total

Added, Grams

Act NaCN

--

0.210.00

0.21

ual Ca(OH) 2

0.500.41

0.240.08

1.23

EquiVi NaCN

--

0.200.00

0.20

alent CaO

0.380.31

0.180.06

0.93

Residual

GriNaCN

--

0.200.18

0.18

uns CaO

0.070.20

0.320.35

0.35

Consumed

Gr*NaCN

--

0.000.02

0.02

uns CaO

0.310.18

0.060.03

0.58

PH

From

11.611.6

11.812.0

To

11.011.6

11.811.6

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.04CaO: 1.16

Metallurgical Results

Products

1. 24 h Preg. Cy Soln 2. 24 h Wash Solution 3. 24 h Cy Residue

Head (calculated)

Amount

850 mL 1890 mL 499.3 g

499.3 g

Assays, mg/L.g/t Au

1.58 0.17 0.80*

4.13

'1, Distribution Au

65.1 15.6 19.3

100.0

* average of 0.65, 1.42, 0.34 g/t Au

Calculated Grades and Recoveries

Products 1 plus 2 2740 mL 0. 61 80. 7

Overall Au recovery by Amal. + Cyn: 92.7 7.

Page 193: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 82 -

st No. 157

Zinc Dust Precipitation

Purpose:

Procedure:

Feed :

Conditions:

Calculations:

To investigate the precipitation of gold from a pregnant cyanide solution by adding zinc dust.

The cyanide strength was made up to 0.5 g/L NaCN and the solution was poured into a separatory funnel. The nitrogen flow was adjusted between 70 and 80 with a 604 flow meter (glass ball) to deaerate the solution. After deaeration, lead nitrate and zinc dust were added to the solution. The reagents were mixed with nitrogen for the required contact time. The solution was then filtered through a micropore filter while nitrogen flowed through the solution.

3.5 litres of pregnant cyanide solution from Tests No. 152, 153, 155 and 156.

Deaeration Time: Contact Time: Zn Dust:

Pb(N03 ) 2 :pH of Barren Soln: .NaCN Soln Strength:

A)

B)

1.35 x -1.74 x 0.332 ? = 0.078 g Zn dust 0.25 x 0.078 - 0.020 g Pb(N03 ) 2

1.3 x 0.37 x 0.332 x " 0 .016 g Zn dust 0.25 x 0.016 s 0.004 g Pb(N03 ) 2

30 minutes60 minutes100 x theoretical requirements(l mole Zn/1 mole Au)0.25 x zinc dust addition11.60.5 g/L NaCN

100

100

Metallurgical Results

Product

Zn Ppt Feed Solution Zn Barren Solution A Zn Barren Solution B

Assays, mg/L

Au

1.74 0.37 0.20

Zn

0.17 15.5 20.0

Cu

2.62

Fe

0.06

CN(T)

2.90

CN(F)

288.9

Page 194: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 83 -

t No. 158

Purpose:

Procedure:

Feed:

Conditions:

To conduct a SOz/Air cyanide destruction test on a Zn barren solution.

As per Test 150.

2.3 litres Zn barren solution from Test 157.

Calculations;

Copper Addn:

Feed Rate:Vessel:Retention Time:

PH:CN:Cu Molar Ratio: S02 to CN(T) Ratio:

Total CN: 290 mg/L Free CN: 289 mg/L

Molar Ratio CN:Cu - 3:1

1000 mL/hour500 mL30 minutes9.0 at 20 g/L Ca(OH) 2 slurry3:16.0 g SC-2/1 g CN(T)

CN - 26 mg/mole

289 mg CN 26 mg/mole

= 1 1.12 moles/L~ 5 .557 moles CN/500 mL

add 1.853 moles Cu x 63.5 mg/mg mole " 117.6 mg Cu 4- 50 ^ 167.6" 659 mg CuS0^.5H 2 0 - 6.6 mL 107. CuSOM .5H 2 0

Strength of Cu Solution:

S0 2 Addition:

Retention Time;

Gas Flow:

Flow Meter:

~ 405 mg CuS04 .5H 2 07l9.4 mL = 4175 mg CuS04 .5H2 07200 mL

per litre of feedl g CN(T) requires 6.0 g S02290 mg/L requires 1.74 g of S02l. 74 g of S02 contained in

- 1.74 g x 22.4 ~ 0 .609 L at STP64

= 0.609L x 293 0 C . 0.654 L at NTP 273 0 C

0.654 L of S02 contained in 0.654 x 100

1.5 50 min/litre of feed

728 cc/min.

134 mm Matheson 602-STST Float

Error in calculations resulted in escess Cu Addn

43.67 L of 1.57. SOz/Air

Page 195: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 8k -

ist No. 158 - Continued

Barren Retreatment (necessary due to excess Cu Addn):

No Cu AdditionS02 :CN(T) - 4:130 Minute Retention Time300 mL x 107 mg/L - 32.1 mg CN

Add 128.4 mg S0 2 - 3.21 L S02 at 1.57. c 107 mL/min.

Test Data:

Procedure

Batch Start-up

Continuous

s Sample Period

V

Sample Retreatment

Time Min.

0005

1520253005

15304560 7590105

030

Feed Rate mL/min.

-------

16.7

^ f--

1.57. S02 7Air cc/min.

.

.728

\ f

107107

Cu Addition mg /m in.

.168

\ i

1.72

^ f--

PH

12.1

9.29.19.19.09.09.09.29.09.29.29.1 9.09.09.09.09.0

emf mV

+90

120120120120120120130140150170120 1008070--

* mg

Ca(OH) 2 Batch Start-up: Continuous:

Metallurgical Results

110 mL Ca(OH) 2 27. 251 mL Ca(OH) 2 27.

Solution

CND Feed SolutionCND Barren SolutionBarren Sample Retreated

CN(T)

2901070.25

As Cu

2.6267.61.78

ssays, m Fe

0.060.04

*:0.02

B/L Zn

20.09.2

0.82

CN(F)

2890.3

N.A.

Page 196: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 85 -

Tel^No. 159

Purpose:

1. Amalgamation

Procedure:

Feed:

Conditions:

To prepare barren solution for simulation of the final barren bleed and tailing from Composite A.

The ground sample was transferred to a 2 L bottle. Mercury and NaOH were added and the bottle was placed on rolls for 2 hours. The mercury was then recovered by elutriation.

l kg minus 10 mesh Composite A.

10 g Hg per 100 grams of sample 2.0 g NaOH

Grind: 10 min/kg in the lab ball mill at 65 7. solids.

Page 197: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 86 -

Ie*2. Cyanidation

Procedure:

. 159 - Continued

Feed :

Solution Volume:

The sample was pulped with water in a four litre bottle. Preaeration was carried out for 6 hours with 0.5 g/L Ca(OH)2, NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

1000 g amalgam tail Composite A.

2000 mL Pulp Density 33 7. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Preaeratio

0-2 2-4 4-6

Cyanidatio

0-2 2-4 4-24

Total

Added , Grams

ActUi NaCN

n

i

1.05 0.11 0.11

1.27

il Ca(OH) 2

1.00 0.79 0.45

0.26 0.24 0.13

2.87

Equi\ NaCN

1.00 0.10 0.10

1.20

alent CaO

0.76 0.60 0.34

0.20 0.18 0.10

2.18

Residual

Gra NaCN

0.90 0.90 0.78

0.78

T1S

CaO

0.16 0.42 0.56

0.58 0.66 0.44

0.44

Consumed

GraNaCN

0.10 0.10 0.22

0.42

us CaO

0.60 0.34 0.20

0.18 0.10 0.32

1.74

PH

11.4-11.4 11.7-11.7 11.8-11.8

11.9-11.7 11.9-11.8 11.9-11.8

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.42 CaO: 1.74

3. Zinc Precipitation

Procedure:

Feed :

Conditions:

The combined pregnant cyanide and wash solutions were transferred to a separatory funnel. Nitrogen was introduced at the bottom of the funnel to deaerate the solution. Lead nitrate and zinc dust were added in slurry form through the top of the funnel and the solution was agitated with the nitrogen gas. After 40 minutes, the solution was filtered through a micropore filter with nitrogen being continually passed through the solution to maintain an oxygen-free environment.

2 x 1200 mL combined pregnant -f wash, solution

Free NaCN:PH:Dearation Time :Zn Dust Addition:Pb(N03 ) 2 :Contact Time:

0.30 g/L11.620 minutes200 x theoretical (0.082 g/1200 mL)0.25 x Zn addition (0.021 g/1200 mL)40 minutes

Page 198: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 87 -

. 159 - Continued

Tests No. 159 and 161 - Flowsheet

Water,

Water-

Watei

Ore

\;Amalgamation

\;Cyanidation

\/

24 h lesidue

amalgam

Preg'n Sol'n

Wash

Wash

Wash

W

Zinc Precipitation

Sample

Barren Solution

Page 199: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 88 -

. 159 - Continued

Metallurgical Results

Product

1. Zn ppt'n barren Sol'n2. 24 h Preg'n+Wash Sol'n3. Amalgam5. 24 h Residue

Head (Calculated)

Amount

2550 ml-

1000.6 g

1000.6 g

Assays, mg/L, g/t

Au

0.0471.03-

0.32

7.57

CNT

125125--

-

Zn

28.20.24--

-

'/c Distribution

Au

1.634.761.04.3

100.0

Calculated Grades and Recoveries

Products 2+3 2550 mL 2.84 - - 95.7

Page 200: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 89 -

Procedure:

Feed:

Conditions:

Grind:

To simulate the barren bleed and tailing from Composite A.

As for test No. 159.

l kg minus 10 mesh Composite A

10 g Hg per 100 grams of sample 2.0 g NaOH

10 min/kg in the lab ball mill at 65 7. solids

Page 201: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 90 -

o. 160 - Continued

2. Cyanidation

Procedure: The sample was pulped with water and preaerated for 6 hours on rolls maintaining 0.5 g/L Ca(OH)2* Cyanide and lime were then added and the cyanidation was carried out in one 24 hour stage. The pulp was filtered and washed with the zinc precipitation barren solution from test 159. The residue was repulped with barren solution and filtered, then washed once with fresh water.

Feed: 1000 g amalgam tailing.

Solution Volume: 2000 mL Pulp IDensity 33 7. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Preaeratio

0-2 2-4 4-6

Cyanidatio

0-3 3-20 20-24

Total

Added, Grams

Actua NaCN

n

n

1.05 0.11 0.35

1.51

1 Ca(OH) 2

1.0 0.45 0.39

0.26 0.13 0.82

3.05

Equiv NaCN

1.00 0.10 0.33

1.43

dent CaO

0.76 0.34 0.30

0.20 0.10 0.62

2.32

Residual

Gr a NaCN

0.90 0.67 0.98

0.98

ns

CaO

0.42 0.46 0.56

0.66 0.14 0.50

0.50

Consumed

Gr* NaCN

0.10 0.33 0.02

0.45

ms CaO

0.34 0.30 0.20

0.10 0.62 0.26

1.82

PH

11.2-11.4 11.6-11.8 11.8-11.8

12.0-11.8 11.8-11.2 11.8-11.6

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.45 CaO: 1.82

3. Zinc Precipitation

Procedure: As for test No. 159.

Feed:

Conditions:

2 x 1250 mL combined pregnant + wash solutions

free NaCN:PH:Deaeration Time:Zn dust:Pb(N03 ) 2 :Contact Time:

0.3 g/L11.420 minutes200 x theortical (0.045 g/1250 mL)0.25 x Zn addition (0.011 g/1250 mL)40 minutes

Page 202: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 91 -

. 160 - Continued

Tests No. 160 and 162 - Flowsheet

250 mL Barre Solution

1000 mL Bai Solution

250 mL Water'

Ore

V

Assay Sample^

Amalgamation .Amalgam

Cyanidation

Fil

\Wa

\r en — —^ —— *Rep

— —— -^ \r ' —— -^ — ' Vi

\

Preg'n Sol'n ^--Ler " c--^.

;Wash 1 ^~-sh " - '^^^

;Filtrate ^--'(Ulp ————————— ————— e^^

1Wash 2 _--ish ^—— .

|Tailing

Sample

1360

Assay Sample

200 mL

issay Sample

800 mL

Assay Sample

200 mL

-5*Assay Sample

Zinc Precipitation

yBarren Solution

Page 203: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 92 -

o. 160 - Continued

Metallurgical Results

Product

1. Zn ppt'n Barren Sol'n2. 24 h Preg'n Sol'n3. Wash 14. Filtrate5. Wash 26. Amalgam7. 24 h Residue

Head (Calculated)

Amount

1680 ml255 mL960 mL280 mL-

1000 g

1000 g

Assays, mg/L, g/t

Au

0.0340.800.670.140.08-

0.25

12.1

CNT

.141.3125.3117.3102.7

--

-

Zn

12.0-- ---

-

7. Distribution

Au

0.911.11.41.10.2

84.22.0

100.0

Calculated Grades and Recoveries

ProductsProductsProducts

2-52-52-6

(Calc.)(Direct)

317531753175

mLmLmL

003

.52

.54

.73

~

-

.

7.20-

131398

.8

.8

.0

Additional Assays

Zn ppt'n barren solution; < 0.05 mg/L Ag4.45 mg/L Cu

< 0.3 mg/L Pb

2.16 mg/L Ni

448 mg/L CNS

Page 204: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 93 -

No. 161

Purpose:

1. Amalgamation

Procedure:

Feed:

Conditions:

To prepare barren solution for the simulation of the final barren bleed and tailing from Sample AG-B.

As for test No. 159

l kg minus 10 mesh Sample AG-B.

10 g Hg per 100 grams of sample 2.0 g NaOH

Grind: 8 min/kg in the lab ball mill at 65 7. solids

Page 205: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

i. 161 - continued

'2. Cyanidation

Procedure: As for test No. 159

Feed: 1000 g amalgam tailing sample AG-B.

Solution Volume: 2000 mL Pulp Density 33 7. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Added, Grams

Actu. NaCN

t Preaeration

0-2 2-4 4-6

Cyanidatio

0-3 3-19 19-24

Total

i

1.05 0.25 0.24

1.54

1 Ca(OH) 2

1.00 0.42 0.34

0.32 0.13 0.16

2.37

Equiv NaCN

1.00 0.24 0.23

1.47

alent CaO

0.76 0.32 0.26

0.24 0.10 0.12

1.80

Residual

Gr a NaCN

0.76 0.77 1.00

1.00

ns CaO

0.44 0.50 0.52

0.66 0.64 0.65

0.65

Consumed

Gr f NaCN

0.24 0.23 0

0.47

am s CaO

0.32 0.26 0.24

0.10 0.12 0.11

1.15

PH

11.6-11.6 11.8-11.7 11.8-11.7

11.9-11.6 12.0-12.2 12.2-12.1

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.47 CaO: 1.15

3. Zinc Precipitation

Procedure:

Feed :

Conditions:

As for test No. 159

2 x l200mL combined pregnant+Wash solution

Free NaCN:PH:Deaeration Time:Zn dust addition:Pb(N03 ) 2 addition:Contact Time:

0.40 g/L11.620 minutes200 x theoretical (0.065 g/1200 mL)0.25 x Zn addition (0.016 g/1200 mL)40 minutes

Page 206: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 95 -

o. 161 - Continued

Metallurgical Results

Product

1. Zn ppt'n Barren Sol'n2. 24 h Preg'n+Wash Sol'n3. AmalgamA. 24 h Residue

Head (Calculated)

Amount

.2710 mL-1000.0 g

1000.0 g

Assays, mg/L, g/t

Au

0.500.82-

0.25

6.12

CNT

230240--

-

Zn

45.60.33--

-

7. Distribution

Au

22.136.359.64.1

100.0

Calculated Grades and Recoveries

Products 2 and 3 2710 mL 2.17 - - 95.9

Page 207: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

'No. 162

Purpose:

1. Amalgamation

Procedure:

Feed :

Conditions:

Grind:

2. Cyanidation

Procedure:

Feed:

- 96 -

To simulate the barren bleed and tailing from Sample AG-B.

As for test No. 159.

l kg minus 10 mesh Sample AG-B.

10 g Hg per 100 grams of sample 2.0 g NaOH

8 min/kg in the lab ball mill at 50 7. solids.

As for test No. 161 except the barren solution from test 160 was used for the first wash and repulp.

l kg amalgam tailing

Solution Volume: 2000 mL Pulp Density: 33 7. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Preaeratio

0-2 2-4 4-6

Cyanidatic

0-3 3-20 20-24

Total

Added, Grams,

ActufNaCN

n

-

n

1.05 0.21 0.21

1.47

il Ca(OH) 2

1.0 0.78 0.37

0.16 0.21 0.11

2.63

Equi\ NaCN

-

1.0 0.20 0.20

1.40

alent CaO

076 0.59 0.28

0.12 0.16 0.08

1.99

Residual

Gr E NaCN

-

0.80 0.80 1.00

1.00

ms CaO

0.17 0.48 0.64

0.60 0.68 0.76

0.76

Consumed

Gr aNaCN

-

0.20 0.20 0

0.40

ms CaO

0.59 0.28 0.12

0.16 0.08 0

1.23

PH

11.2-11.2 11.8-11.8 11.8-12.0

12.0-11.8 11.8-11.9 11.9-11.8

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.40 CaO: 1.23

Page 208: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 97 -

Tel^No. 162 - Continued

3. Zinc Precipitation

Procedure:

Feed:

Conditions:

As for test No. 159

2 x 1250 mL comb, preg'n+wash solutions

free NaCN:PH:Deaeration Time:Zn Dust:Pb(N03 ) 2 :Contact Time:

0.40 g/L11.420 minutes200 x theoretical (0.056 g/1250 mL)0.25 x Zn addition (0.014 g/1250 mL)40 minutes

Metallurgical Results

Product

1. Zn ppt'n barren sol'n2. 24 h Preg'n Solution3. Wash 14. Filtrate5. Wash 26. Amalgam7. 24 h Residue

Head (Calc.)

Amount

1720 mL260 mL980 mL280 mL-

1000 g

1000 g

Assays, mg/L, g/t

Au

0.0490.790.790.500.48-

0.18

4.74

CNT

.253.3252.0231.1194.7--

-

Zn

42.0---.--

-

7o Distribution

Au

3.428.74.410.32.8

50.03.8

100.0

Calculated Grades and Recoveries

Products 2-5 (Calc.)Products 2-5 (Direct)Products 2-6

3240 mL3240 mL3240 mL

0.670.671.41

.

237.3-

.15.0-

46.146.196.2

Additional Assays

Zn ppt'n barren solution: < 0.05 mg/L Ag 10.0 mg/L Cu 0.5 mg/L Pb

0.80 mg/L Ni 60.7 mg/L CNS

Page 209: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

. 163

Purpose :

Procedure

Feed :

Conditions:

- 98 -

To investigate the recovery of free gold by amalgamation with mercury prior to cyanidations.

The sample was pulped with water into a two litre bottle. Mercury and sodium hydroxide were then added. The bottle was placed on the rolls for two hours. The sample was transferred to a separatory funnel and the mercury was recovered by elutriation. The amalgam tailing was filtered and split into three for cyanidation tests.

l kg of -10 mesh Composite B.

Mercury: 10 grams per 100 grams of sample NaOH: 2.0 grams

Grind: l kg sample ground in the lab ball mill for 10 minutes at 65 "L s olids,

Metallurgical Results

Product

Amalgam Amalgam Tail.

Head (Gale.)

Amount

1000 g

1000 g

Assays, mg, g ;t

Au

3.492 3.43

6.92

7. Distribution

Au

50.4 49.6

100.0

Page 210: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

TeWNo. 164

Purpose :

Procedure;

- 99 -

To investigate the recovery of gold at 30 "l, solids from Composite B Amalgam tailing.

The sample was pulped with water in a two litre bottle. Preaeration was carried out on the rolls for 6 hours at 0.5 g/L Ca(OH)2. NaCN and lime were then added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

Feed: 333 g Composite B Amalgam tail.

Solution Volume: 777 mL Pulp Density 30 7. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Preaeratio

0-2 2-4 4-6

Cyanidatio

0-3 3-17 17-24

Total

Added, Grams

Actua NaCN

n

n

0.39 0 0

0.39

1 Ca(OH) 2

0.39 0.24 0.09

0.05 0.05 0.09

0.91

Equiv NaCN

0.37 0 0

0.37

ilent CaO

0.30 0.18 0.07

0.04 0.04 0.07

0.70

Residual

Gr e NaCN

0.37 0.37 0.29

0.29

ms CaO

0.12 0.23 0.26

0.26 0.23 0.11

0.11

Consumed

Gr a NaCN

0 0

0.08

0.08

ms CaO

0.18 0.07 0.04

0.04 0.07 0.19

0.59

PH

12.0-11.8 12. -12.0 12.0-12.0

12.1-12.0 12.1-12.0 12.1-12.1

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.24 CaO: 1.77

Page 211: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

No. 164 - continued

Metallurgical Results

- 100 -

Product

24 h Preg'n+Wash 24 h Cy. Residue

Head (Gale.)

Amount

1730 mL 332.9 g

332.9 g

Assays, mg/L, g/t

Au

0.56 0.14*

3.06

7. Distribution

Au

95.1 4.9

100.0

* average of 0.14, 0.14 g/t Au Overall gold recovery by amal + Cyanidation: 97.6 7.

Screen Analyses

24 Hour Cyanide Residue

Mesh Size(Tyler)

* 28354865100150200270400

- 400

Total

7. RetainedIndividual

0.30.10.20.51.64.58.511.311.561.5

100.0

Cumulative

0.30.40.61.12.77.2

15.727.038.5100.0

-

7. PassingCumulative

99.799.699.498.997.392.884.373.061.5

-

-

Page 212: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 101 -

No. 165

Purpose :

Procedure:

Feed :

To investigate the recovery of gold at 40 7. solids from Composite B Amalgam tailing from test No. 163.

The sample was pulped with water in a two litre bottle. Preaeration was carried out on rolls for 6 hours with 0.5 g/L Ca(OH)2. NaCN and lime were then added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

333 g Amalgam tailing (from test 163).

Solution Volume: 500 mL Pulp Density 40 7. solids

Solution Composition: 0.5 g/L NaCN

pH Range: 0.5 g/L Ca90H) 2

Reagent Balance:

Time

Hours

Added , Grams

Actu NaCN

Preaeration

0-2 2-4 4-6

Cyanidatio

0-3 3-17 17-24

Total

i

0.25 0

0.09

0.34

al Ca(OH) 2

0.25 0.18 0.11

0.05 0.04 0.07

0.70

Equiv NaCN

0.24 0

0.09

0.33

alent CaO

0.18 0.14 0.08

0.04 0.03 0.05

0.53

Residual

Gr f NaCN

0.24 0.15 0.24

0.24

ms CaO

0.05 0.11 0.15

0.16 0.14 0.19

0.19

Consumed

Gr i NaCN

0 0.09 0

0.09

ms CaO

0.14 0.08 0.04

0.03 0.05 0

0.34

PH

12.0-11.6 12.0-11.8 11.9-12.0

12.1-12.0 12.1-12.0 12.1-12.1

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.27 CaO: 1.03

Metallurgical Results

Product

24 h Preg'n+Wash 24 h Cyanide Residue

Head (Calculated)

Amount

1400 mL 328.7 g

328.7 g

Assays.mg/L.g/t

Au

1.05 0.18*

4.65

7. Distribution

Au

96.1 3.9

100.0* average of 0.18, 0.18 g/t Au

Overall gold recovery by amalgam + Cyanidation: 98.1 7o

Page 213: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 102 -

No. 166

Purpose: To investigate the recovery of gold at 50 7o solids from Composite BAmalgam tail from test No. 163.

Procedure: The sample was pulped with water in a two litre bottle. Preaeration was carried out on the rolls for 6 hours with 0.5 g/L Ca(OH)z. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

Feed: 333 g Amalgam tail (From test No. 163).

Solution Volume: 333 mL Pulp Density: 50 7, solids

Solution Composition: 0.5 g/L NaCN

pH Range: 0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Added , Grams

Actua, NaCN

i Preaeration

0-2 2-4 4-6

Cyanidatio

0-3 3-17 17-24

Total

n

0.17 0

0.07

0.24

1 Ca(OH) 2

0.17 0.14 0.11

0.07 0.04 0.07

0.60

Equi NaCN

0.16 0

0.07

0.23

/alent CaO

0.13 0.11 0.08

0.05 0.03 0.05

0.45

Residual

Gr a NaCN

0.16 0.09 0.16

0.16

ns CaO

0.02 0.05 0.08

0.10 0.08 0.13

0.13

Consumed

Gra NaCN

0 0.07 0

0.07

ms CaO

0.11 0.08 0.05

0.03 0.05 0

0.32

PH

12.0-11.4 12.0-11.6 11.9-11.9

12.1-12.0 12.1-12.0 12.1-12.1

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.21 CaO: 0.97

Page 214: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

No. 166 - Continued

Metallurgical Results

- 103 -

Product

24 h Preg'n+Wash 24 h Cy. Residue

Head (Calculated)

Amount

1190 mL 330.4 g

330.4 g

Assays, mg/L.g/t

Au

0.68 0.135*

2.57

7. Distribution

Au

95.3 4.7

100.0* average of 0.13, 0.14 g/t Au

Overall Au recovery by amalgam + cyn: 97.7 7,

Page 215: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 104 -

[ No. 167

Purpose: To produce a high grade grade gold concentrate by gravityconcentration and magnetic separation.

Procedure: The ground sample was fed over a laboratory table. The tableconcentrate was cleaned once on a Mozley shaking table. The table and Mozley tailings were filtered separately. The final gravity concentrate was further upgraded using a Frantz magnetic separator. The first pass non-mags were repassed at l.OA. The magnetic separation products were assayed in their entirety.

Feed: 2 kg minus 10 mesh Composite B.

Grind: lOmin/Zkg at 65 7. solids in the lab ball mill.

Page 216: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

-105-

O. 167 - Continued

Metallurgical Results

Product

1. Mozley Cone. Non-Mag.2. Mozley Cone. l.OA Mags.3. Mozley Cone. OA Mags.4. Mozley Tailing5. Table Tailing

Head (Calculated)

Amount

0.360.450.292.9895.92

100.00

Assays, g/t

Au

544.164.39.318.11.43

4.72

7. Distribution

Au

41.515.62.4

11.429.1

100.0

Calculated Grades and Recoveries

Products 1Products 1Products' 1

and 2to 3to 4

0.811.104.08

333.255.82.1

57.159.570.9

Screen Analyses

Combined Table Tailing

Mesh Size(Tyler)

+ 142028354865100150200270400

- 400

Total

7. RetainedIndividual

1.50.61.01.64.38.19.710.78.78.87.7

373.

100.0

Cumulative

1.52.13.14.79.017.126.837.546.255.062.7100.0

-

7. PassingCumulative

98.597.996.995.391.082.973.262.553.845.037.3

-

-

Page 217: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

Composite B - Tests 168-175

- 106 -

FLOWSHEET

l kg

Grind

l kg

vGr nd

Amalgamation ——————— * ———————— ^ —— — —— — — — — — — Amaigs(168) (1

Tail \ fy Assay \

Fi:

Creek^^

ter Fi:

\Water ^^^~^~i^. * *^* Wi

Creek^^^^ .Water ^~~~~-^r. Re j

\

SettlingTest(169)

V \l

ish . W*

; \)ulp Rep

\' . ' 1

V vSettling SettlingTest Test(170) (171); i \

Filter Fi:

Creek *~-^^^ J/ ^Water ^^

Water^^^^, \ ^?ej

\

v n ash Wi

; \ lulp Re

; \

mation

Tailjter

^^Xlreek, ^^^ Water

, tgz^"^ Water )ulp

1SettlingTest(172)

ter

, ^^-Creek, jZ^^^ Water ish^27

. -^^"^^ Water )ulp*^

^ 'Preaeration PreaerationCyanidation Cyanidation

(\73) ( 173)V \/

————— Assay Sample\l/

Settling FiltrationTest Test(174) (175)

( ) number in brackets indicate the test number

Page 218: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 107 -

No. 168

Purpose:

Procedure :

Mercury:

Feed:

Grind:

To recover the free gold in Composite B prior to cyanidation.

The samples were pulped with water in four litre bottles. Mercury was added,and the bottles were placed on the rolls for two hours. The mercury was then recovered by elutriation. The amalgam from samples A and B were combined and assayed for gold. The amalgam tailings were separately filtered, washed and repulped with creek water for further testing.

2x30 grams.

2 x l kg Composite B -10 mesh.

l kg sample ground in the lab ball mill at 65 7e solids for 8 minutes.

Metallurgical Results

Product

Amalgam Amal Tailing

Head (Gale.)

Amount

100.0

100.0

Assays, mg, g/t

Au

5.213 2.80

5.41

7. Distribution

Au

48.2 51.8

100.0

Page 219: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 108 -

. 169

Purpose:

Feed:

Lime :

Pulp Volume:

Pulp Weight:

To investigate the settling characteristics of Composite B at 15 7o solids with 1205 g/t lime addition, (pulped with creek water).

Composite B Amalgam Tailing (From test No. 168A).

1205 g/t pH: 10.8

1000 mL

1105.6 g

Specific Gravity of Dry Solids: 2.84

Settling Time Minutes

0123456789

101112

Mudline mL

1000950900850800755705650610560510465420

Settling Time Minutes

13141516171820222428406024 h

i

Mudline mL

370330280230220210195185175170165160160

Observations: Supernatnant was very cloudy which made it very difficult to distinguish mudline. Without any lime, the mudline was impossible to read.

Page 220: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

f3

oD .-1t/

OO

o\ oH

•~\V**

v* l

Page 221: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 110 -

No. 169 - Continued

Thickener Area Requirement Calculations

Feed Concentration Zone

Initial Pulp Density: 1106 g/L

Initial Percent Solids: 15F = 85 l 1 5 * 5.67Final Pulp Density: 1660 g/LFinal Percent Solids: 62.5D . 37.5 ? 62.5 ~ 0.6R s 0.995 metre per hour

A = 0.042 (5.67 - 0.6) j 0 .995= 0 .21 square metre per tonne of dry solids per 24 hours thickener area

required (no safety factor applied)

Entrance to Compression Zone

Initial Pulp Density: 2197 g/LInitial Percent Solids: 36

F - 64 7 36 - 1.78Final Pulp Density: 1660 g/LFinal Percent Solids: 62.5D r: 37.5 7 62.5 z 0.6R = 0 .254 metre per hourA = 0.042 (1.78 - 0.6) f 0 .254

= 0 .2 square metre per tonne of dry solids per 24 hours thickener area required (no safety factor applied)

Page 222: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

\fo. 170

- 111 -

Purpose:

Feed :

Lime :

Pulp Volume:

Pulp Weight:

To investigate the settling characterisitcs of Composite B at 20 7. solids with 870 g/t lime addition (pulped with creek water),

Composite B Amalgam tail from test No. 168A.

870 g/t pH: 10.8

1000 mL

1151.7 g

Specific Gravity of Dry Solids: 2.84

Settling Time Minutes

0123456789

101112

Mud line mL

1000965925895865830800770740710680645615

Settling Time Minutes

1314151617181920

Mud li ne mL

590555530500465435410385

22 34524 ; 32528 i 30032406024 h

270240230225

Observations: As for test No. 169

Page 223: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 112 -

too

•JOo

le.0

IS 55 (.e

Page 224: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 113 -

No. 170 - Continued

Thickener Area Requirement Calculations

Feed Concentration Zone

Initial Pulp Density: 1152 g/LInitial Percent Solids: 20F = 80 / 20 = 4

Final Pulp Density: 1674 g/L

Final Percent Solids: 61.1

D s 38.9 l 6 1.1 a 0.64

R = 0 .661 (metre per hour)

A = 0.042 (4 - 0.64) l 0 .661

= 0.21 square metre per tonne of dry solids per 24 hours thickener area required (no safety factor applied)

Entrance to Compression Zone

Initial Pulp Density: 1300 g/LInitial Percent Solids: 35

F = 65 l 3 5 = 1 .86

Final Pulp Density: 1674 g/L

Final Percent Solids: 61.1

D = 38.9 f 6 1.1 = 0.64

R = 0.156 metre per hourA = 0.042 (1.86 - 0.64) j 0 .156

s* 0 .33 square metre per tonne of dry solids per 24 hours thickener area required (no safety factor applied)

Page 225: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- Ilk -

t No. 171

Purpose:

Feed :

Lime :

Pulp Volume:

Pulp Weight:

To investigate the settling characteristics of Composite B at15 7. solids with a lime addition to pH 11.5 (pulped with creek water),

Composite B Amalgam tailing from test No. 168B.

2410 g/t pH: 11.5

1000 mL

1109 g

Specific Gravity of Dry Solids: 2.84

Settling Time Minutes

0123456789

101112

Mudline Settling Time mL Minutes

1000955905 ;860812765720675630580530485440

1314151617182022242832406024 h

Mudline mL

395350305275260250235220210190185180180

Observations: Supernatant was cloudy but mudline was easily read

Page 226: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

l"t H C l/1

S R S?VJ

1 l

Page 227: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 116 -

No. 171 - Continued

Thickener Area Requirements

Feed Concentration Zone

Initial Pulp Density: 1109 g/L

Initial Percent Solids: 15

F = 85 j 1 5 = 5.67

Final Pulp Density: 1606 g/L

Final Percent Solids: 57.4

D ~ 42.5 7 57.4 ~ 0 .74

R = 0.958 metre per hourA = 0.042 (5.67 - 0.74) l 0 .958

= 0 .22 square metre per tonne of dry solids per 24 hours thickener area required (no safety factor applied)

Entrance to Compression Zone

Initial Pulp Density: 1263 g/L

Initial Percent Solids: 31.7

F - 68.3 l 3 1.7 = 2.15

Final Pulp Density: 1606 g/L

Final Percent Solids: 57.4

D = 42.6 l 5 7.4 * 0.74

R = 0 ;256 metre per hour

A . 0.042 (2.15 - 0.74) J 0 .256

= 0 .23 square metre per tonne of dry solids per 24 hours thickener area required (no safety factor applied)

Page 228: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 117 -

No. 172

Purpose:

Feed :

Lime :

Pulp Volume:

Pulp Weight:

To investigate the settling characteristics of Composite B at20 7. solids with a lime addition to pH 11.5 (pulped with creek water),

Composite B Amalgam Tail from Test No. 168B.

1739 g/t pH: 11.5

1000 mL

1151.8 g

Specific Gravity of Dry Solids: 2.84

Settling Time Minutes

0123456789

k91112

Mud line mL

1000945885850810760720680635590545505460

Settling Time Minutes

1314151617182022242832406024 h

4f

Mud li ne mL

420390365350335325310290275250245240235235

Observations: As for test No. 171.

Page 229: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

rtrc) O

o•5,o

l

CO

r-\

H

l

Page 230: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 119 -

No. 172 - Continued

Thickener Area Requirement Calculations

Feed Concentration Zone

Initial Pulp Density: 1152 g/L

Initial Percent Solids: 20

F = 80 l 20 z 4

Final Pulp Density: 1646 g/L

Final Percent Solids: 59.6

D ~ 40.4 / 59.6 = 0.68

R = 0 .955 metre per hour

A s 0.042 (4 - 0.68) l 0 .955

= 0 .15 square metre per tonne of dry solids per 24 hours thickener

area required (no safety factor applied)

Entrance to Compression Zone

Initial Pulp Density: 1326 g/L

Initial Percent Solids: 37.4

F . 62.6 l 3 7.4 . 1.67

Final Pulp Density: 1646 g/L

Final Percent Solids: 59.6

D = 40.4 j 59.6 s 0.68

R = 0 .168 metre per hour

A = 0.042 (1.67 - 0.68) f 0 .168

= 0 .25 square metre per tonne of dry solids per 24 hours thickener area

required (no safety factor applied)

Page 231: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 120 -

No. 173

Purpose:

Procedure;

Feed :

To investigate the effect of using creek water on the cyanidation response of Composite B.

The thickened pulp from the settling tests was combined with the remaining amal tailings to make up the original 2 x l kg samples and the pulp density was adjusted to 30 7. solids with creek water. Both samples were preaerated for 6 hours with lime. The cyanidations were carried out in a single stage on rolls. After 24 hours, the two pulp samples were combined and an assay sample was removed. The remaining pulp was used for settling and filtration tests.

2 x 1000 g Composite BA - thickened pulp from tests 169 and 170 combined with remaining

amal tailing A B - thickened pulp from tests 171 and 172 combined with remaining

amal tailing B

Solution Volume: 2 x 2333 mL creek water

Pulp Density: 30 'l, solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Page 232: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 121 -

No. 173 - Continued

Reagent Balance A:

Time

Hours

Preaeratio0-2 2-4 4-6

Cyanidatio

0-1.5 1.5-17 17-24

Total

Added , Grams

Actual NaCN Ca(OH) 2

n

n

1.23 0

0.13

1.36

1.17 0.78 0.30

0.18 0

0.18

2.61

Equiv NaCN

-

1.17 0

0.12

1.29

alent CaO

0.89 0.59 0.23

0.14 0

0.14

1.99

Residual

Gr aNaCN

1.17 1.05 1.15

1.15

ns CaO

0

0.30 0.66 0.75

0.89 0.75 0.82

0.82

Consumed

Gr a NaCN

0 0.12 0.02

0.14

ms CaO

0.59 0.23 0.14

0 0.14 0.07

1.17

pH

11.8-11.6 12.0-12.0 12.2-12.2

12.2-12.2 12.2-12.2 12.2-12.2

-

Reagent Balance B:

Preaeratioin

0-2 j -2-44-6

1.12 j -0.820.51 j -

1 ' ?Cyan id at ion i |0-1.5 i 1.23 0.131.5-17 j 017-24 j 0

Total j 1.23

00

2.58

1.1700

1.17

0.850.620.39

0.1000

1.96

w--

1.171.171.05

1.05

0.04

0.270.500.79

0.890.890.86

0.86

—--

00

0.12

0.12

0.620.390.10

00

0.03

1.14

11.8-11.612.0-12.012.2-12.2

12.2-12.212.2-12.212.2-12.2

-

Overall Reagent Consumption (kg/t of cyanide feed) NaCN: 0.13 CaO: 1.16

Page 233: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 122 -

No. 173 - Continued

Metallurgical Results

Product

24 h Preg'n Cy. Solution 24 h Cyanide Residue

Head (Calculated)

Amount

4666 mL 2000 g

Assays, mg/Ljg/t

Au

1.00 0.47*

2000 g j 2.80

7. Distribution

Au

83.3 16.7

100.0

* Average of 0.57, 0.53 and 0.32 g/t Au

Overall Au recovery by amal + cyn: 91.3 *l*

Page 234: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 123 -

No. 174

Purpose:

Feed :

pH:

Pulp Volume:

Pulp Weight:

To investigate the settling characteristics of Composite B cyanide pulp at 30 7. solids.

1000 mL of pregnant cyanide pulp from test No. 173 B composite.

11.7

1000 mL

1243.3 g

Specific Gravity of Dry Solids: 2.84

Settling Time Minutes

0123'

45681012141618

Mudline mL

1000975955935915895880840800760720680645

Settling Time Minutes

202224262830354045505762677224 h

Mudline mL

605570535510490470440415395375355345340340340

Observations: Supernatant was slightly cloudy but mudline was easy to read,

Page 235: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

oMV)W*

ftOr

o o oo oV)

83-

Page 236: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 125 -

No. 174 - Continued

Thickener Area Requirement Calculations

Feed Concentration Zone

Initial Pulp Density: 1243 g/L

Initial Percent Solids: 30

F = 70 / 30 = 2.33

Final Pulp Density: 1716 g/L

Final Percent Solids: 63.9

D = 36.1 j 63.9 * 0 .56

R = 0 .424 metre per hour

A = 0.042 (2.33 - 0.56) l 0 .424= 0 .18 square metre per tonne of dry solids per 24 hours thickener

area required (no safety factor applied)

Entrance to Compression Zone

Initial Pulp Density: 1369 g/L

Initial Percent Solids: 41.3F - 58.7 l 4 1.3 = 1.42

Final Pulp Density: 1716 g/LFinal Percent Solids: 63.9

D ~ 36.1 l 6 3.9 = 0.56

R = 0 .131 metre per hour

A = 0.042 (1.42 - 0.56) f 0 .131s 0.28 square metre per tonne of dry solids per 24 hours thickener

area required (no safety factor applied)

Page 237: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 126 -

No. 175

Purpose:

Procedure:

To investigate the filtration characteristics of Composite B which had been pulped at 30 7, solids with creek water and cyanided for 24 hours.

The cyanide pulp was decanted to 50 7, solids and a standard "Pick-up" test was conducted. A form time which would produce a 1/4 to 1/2 inch cake thickeness was selected. Several tests at this form time with equal, double, triple and quadruple dry times were conducted.

Feed :

Cloth Specifications

Media Number

Material

Air-Flow {m 3 /m 2 )

Yarn

Weave

Weight (g/m2 )

Thread Count

Finish

2 kg of cyanide pulp at 50 7. solids (Composite B) (From test No. 173)

POPR-901F

Polypropylene

1.83

Multi-Filament

2/2 Twill

457.8

52 x 35

Heat Set

Page 238: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 127 -

No. 175 - Continued

Test Conditions

Test No.

1

2

3

4

Filter Cloth

POPR-901FPOPR-901FPOPR-901FPOPR-901F

SI 7. Solids

50.5

50.5

50.5

50.5

urry pH

11.8

11.8

11.8

11.8

Temp. 'C

Ambient

Ambient

Ambient

Ambient

Filter Vac Form

508

533.4

508

533.4

. (mm Hg) Dry

508

533.4

508

533.4

Filter Form

30

30

30

30

Time Dry

30

60

90

120

- Sec. Cycle

90

135

180

225

Test Results

Test

No.

1 2 3 4

Cracks No.

0 0 0 0

Thick, mm

15 16 13 15

Filter Ca

Weight - Wet

250 285 198.5 230.8

ke Data

Grams Dry

200.8 233.5 164.9 195.5

7. Moist.

19.7 18.1 16.9 15.3

Rate*

864.6 670.2 355 336.7

Filti

Volume mL

206 271 192 236

•ate Data

Clarity

Excellent Excellent Excellent Excellent

Rate **

886.9 777.9 413.3 406.4

* Dry kg per hour per square metre** Litres per hour per square metre

Page 239: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 128 -

No. 176 A+B

Purpose:

Procedure:

Mercury:

Feed :

Grind:

To recover the free gold in Composite B prior to cyanidation tests.

As for test No. 168.

2 x 30 grams

2 x l kg Composite B -10 mesh

l kg sample ground in the lab ball mill at 65 7, solids for 8 minutes.

Metallurgical Results

Product

Amalgam Amalgam Tailing

Head (Calculated)

Amount

100.00

100.00

Assays .mg/L.g/t

Au

9.948 3.11

8.08

7. Distribution

Au

61.5 38.5

100.0

Page 240: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 129 -

No. 177

Purpose: To investigate the effect of using creek water on the cyanidationresponse of Composite B at 50 7o solids.

Procedure: Each amalgamation tailing sample was washed and repulped with creekwater, then transferred to a 4 litre bottle at 50 7. solids for cyanidation. Preaeration was carried out on the rolls for 6 hours at 0.5 g/L Ca(OH)2- NaCN was added and the cyanidation was carried out on the rolls in one 24 hour stage. The pulp from cyanidations A+B were combined for filtration tests. A pulp sample was taken for assay.

Feed: 2 x 1000 g Composite B Amalgam Tails from test No. 176.

Solution Volume: 2 x 1000 mL creek water Pulp Density 50 7. solids

Solution Composition: 0.5 g/L NaCN0.5 g/L Ca(OH) 2

Reagent Balance A:

Time

Hours

Preaeratio

0-2.5 2.5-4 4-6

Cyanidatio

0-17 17-24

Total

Added , Grams

Actu NaCN

i

i

0.53 0.07

0.60

al Ca(OH) 2

0.50 0.49 0.25

0.29 0.21

1.74

Equi\ NaCN

-

0.50 0.07

0.57

alent CaO

0.38 0.37 0.19

0.22 0.16

1.32

Residual

Gr e NaCN

-

0.43 0.50

0.50

ms CaO

0.01 0.19 0.16

0.22 0.26

0.26

Consumed

Gr sNaCN

-

0.07 0

0.07

.ms CaO

0.37 0.19 0.22

0.16 0.12

1.06

PH

11.8-10.0 11.8-11.6 12.0-11.7

12.2-12.1 12.1-12.1

-

Page 241: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 130 -

No. 177 - Continued

Reagent Balance B:

Time

Hours

Preaeratio

0-2.5 2.5-4 4-6

Cyanidatio

0-16 17-24

Total

Added, Grams

Actua NaCN

n

i

0.53 0

0.53

1 Ca(OH) 2

0..50 0.49 0.36

0.22 0.25

1.82

Equi 1 NaCN

0.50 0

0.50

talent CaO

0.38 0.37 027

0.17 0.19

1.38

Residual

Gr i NaCN

0.50 0.40

0.40

uns CaO

0.01 0.11 0.21

0.19 0.26

0.26

Consumed

GriNaCN

0 0.10

0.10i

ms CaO

0.37 0.27 0.17

0.19 0.12

1.12

PH

11.8-10.0 11.8-11.6 12.0-11.7

12.2-12.1 12.2-12.2

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.09 CaO: 1.09

Metallurgical Results

Product

24 h Preg'n Cy. Sol'n 24 h Cyanide Residue

Head (Calculated)

Amount

2000 mL 2000 g

2000 g

Assays .mg/L^g/t

Au

2.57 0.54*

3.11

7. Distribution

Au

82.6 17.4

100.0

* Average of 0.62, 0.49 and 0.52

Overall Au recovery by amal + cyn: 93.3 7.

Page 242: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 131 -

No. 177 - Continued

Screen Analyses

24 Hour Cyanide Residue

Mesh Size(Tyler)

4- 4865

100150200270400

- 400

Total

7o RetaIndividual

0.81.53.57.1

10.011.210.655.3

100.0

inedCumulative

0.82.35.8

12.922.934.144.7100.0

-

% PassingCumulative

99.297.794.287.177.165.955.3

-

-

Page 243: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 132 -

No. 178

Purpose:

Procedure:

Feed :

To investigate the filtration characteristics of Composite B which had been pulped to 50 7. solids with creek water and cyanided for 24 hours.

A standard "pick-up" leaf test was conducted on cyanide pulp (from test 177).

Cloth Specifications

Media Number

Material

Air-Flow (m 3 /m 2 )

Yarn

Weave

Weight (g/m 2 )

Thread Count

Finish

2 kg of cyanide pulp at 50 'l, solids (Composite B) (from test 177)

PPOR-891F

Polypropylene

1.83

Multi-Filament

2/2 Twill

457.8

52 x 35

Heat Set

Page 244: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 133 -

No. 178 - Continued

Test Conditions

Test No.

1

2

3

4

Filter Cloth

POPR-901FPOPR-901FPOPR-901FPOPR-

7. Solids

50-51

50-51

50-51

50-51

Slurry PH

12.1

12.1

12.1

12.1

Temp. "C

Ambient

Ambient

Ambient

Ambient

Filter Vac Form

533.4

546.1

533.4

533.4

. (mm Hg) Dry

533.4

533.4

533.4

533.4

Filter Form

30

30

30

30

Time - Dry

30

60

90

120

- Sec. Cycle

90

135

180

225

Test Results

Test

No.

1234

Filter Cake Data

CracksNo.

0000

Thick.mm

15151514

WeightWet

271.3258.5261.7249.2

- GramsDry

216.4212.8220.5210.5

7.Moist.

20.217.815.715.5

Rate•it

931.7610.8474.7362.5

Filtrate Data

VolumemL

214256234256

Clarity

Excell.Excell.Excell.Excell.

Rate**

921.4734.8503.8440.9

* Dry kg per hour per square metre** Litres per hour per square metre

Page 245: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

No. 179

Purpose :

Procedure:

Feed:

Grind:

Mercury:

- 131* -

To recover free gold in Composite B prior to cyanidation.

The sample was pulped with water into a 4 litre bottle. Mercuryand sodium hydroxide were added and placed on the rolls for 2hours. The sample was then placed into a separatory funnel andthe mercury was recovered by elutriation. The amalgam tailingwas then split in two and pulped into a 2 litre bottle for cyanidation,

l kg -10 mesh Composite B.

l kg ground in the lab ball mill at 65 'l, solids for 8 minutes.

30 grams

Sodium Hydroxide: l gram

Metallurgical Results

Product

Hg Amalgam Amalgam Tailing

Head (Calculated)

Amount

994.0 g

994.0 g

Assays .mg/L.g/t

Au

4.670 1.87

6.57

7o Distribution

Au

71.5 28.5

100.0

Page 246: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 135 -

it No. 180

Purpose:

Procedure:

Feed:

To investigate the effect of tap water on the recovery of gold from Composite B under standard conditions

The sample was pulped with water in a two litre bottle. Preaeration was carried out on the rolls for 6 hours at 0.5 g/L Ca(OH)a. NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

500 g Composite B amalgam tail (From test 179).

Solution Volume: 1000 mL Pulp Density 33 7. solids

Solution Composition: 0.5 g/L NaCN

0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Preaeratio0-2 2 -A4-6

Cyanidatio

0-18 18-24

Total

Added , Grams

ActuiNaCN

i

i

0.53 0.05

0.58

il Ca(OH) 2

0.50 0.30 0.09

0 0.14

1.03

Equi\ NaCN

0.50 0.05

0.55

ralent CaO

0.38 0.23 0.07

0 0.11

0.79

Residual

Gr* NaCN

0.45 0.50

0.50

uns CaO

0.15 0.31 0.38

0.27 0.38

0.38

Consumed

Gr*NaCN

0.05 0

0.05

ms CaO

0.23 0.07 0

0.11 0

0.41

PH

12.0-11.6 12.0-12.0 12.0-12.0

12.0-11.9 12.0-12.0

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.10 CaO: 0.82

Page 247: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

NO. 180 - Continued

Metallurgical Results

- 136 -

Product

24 h Preg'n+Wash 24 h Cyanide Residue

Head (Calculated)

Amount

2010 mL 497.1 g

497.1 g

Assays, mg/L.g/t

Au

0.43 0.15

1.87

7. DistributionO'all

Au26.4 2.1

28.5

Ind. Au

92.5 7.5

100.0

Overall Au Recovery by Amal +Cyn: 97.9 7o

Page 248: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 137 -

t No. 181

Purpose:

Procedure:

To investigate the effect of creek water on the recovery of gold under standard conditions.

The sample was pulped with creek water in a two litre bottle. Preaeration was carried out on the rolls for 6 hours at 0.5 g/L Ca(OH) 2 . NaCN and lime were added and the cyanidation was carried out on rolls in one 24 hour stage. The pulp was filtered and the residue washed three times with water.

Feed: 500 g Composite B Amalgam Tail. (From test 179)

Solution Volume: 1000 mL Pulp Density 33 7. solids

Solution Composition: 0.5 g/L NaCN

0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Added , Grams

Actut NaCN

i Preaeration0-2 2-4 4-6

Cyanidatio0-18 18-24

Total

n

0.53 0.05

0.58

1 Ca(OH) 2

0,50 0.33 0.08

0.04 0.11

1.06

Equiv NaCN

0.50 0.05

0.55

alent CaO

0.38 0.25 0.06

0.03 0.08

0.80

Residual

Gr* NaCN

0.45 0.48

0.48

trns CaO

0.13 0.32 0.35

0.30 0.38

0.38

Consumed

Gr*NaCN

0.05 0.02

0.07

ms CaO

0.25 0.06 0.03

0.08 0

0.42

PH

12.0-11.5 12.0-12.0 12.0-11.8

12.0-11.9 12.0-12.0

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.14 CaO: 0.85

Page 249: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 138 -

kt No. 181 - Continued

Metallurgical Results

Product

24 h Preg'n + Wash 24 h Cyanide Residue

Head (Calculated)'

Amount

2020 ml 496.9 g

496.9 g

Assays, mg/L.g/t

Au

0.42 0.16

1.87

7. Distribution

O'all Au

26.0 2.5

28.5

Ind. Au

91.4 8.6

100.0

Add: Overall Au recovery by amal -t- cyn: 97.5 'l.

Page 250: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 139 -

No. 182

Purpose:

Procedure;

Feed :

Grind:

Mercury:

To recover free gold in Compsoite B prior to cyanidation.

The sample was pulped with water into a 4 litre bottle. Mercury and sodium hydroxide were added and placed on the rolls for 2 hours. The sample was transferred to a separatory funnel and the mercury was recovered by elutriation. The amalgam tailing was then split into two and pulped into two litre bottles for cyanidation.

l kg sample -10 mesh Composite B.

l kg ground in the laboratory ball mill at 65 7. solids for 8 minutes.

30 grams

Sodium Hydroxide: l gram

Metallurgical Results

Product

Hg Amalgam Amalgam Tailing

Head (Calculated)

Amount

1000.0 g

1000.0 g

Assays, mg7L,g7t

Au

4.154 2.76

6.91

7. Distribution

Au

60.0 40.0

100.0

Page 251: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- n*o -

t No. 183

Purpose: To repeat test No. 180.

Procedure: As for test No. 180.

Feed: 500 g Composite B Amalgam Tail (From test No. 182)

Solution Volume: 1000 mL Pulp Density 33 7. solids

Solution Composition: 0.5 g/L NaCN

0.5 g/L Ca(OH) 2

Reagent Balance:

Time

Hours

Added , Grams

Actua NaCN

Preaer'ation0-2 2-4 4-6

Cyanidatio

0-15 15-24

Total

n

0.53 0.07

0.60

1 Ca(OH) 2

0.5 0.33 0.13

0.07 0.16

1.19

Equi NaCN

0.50 0.07

0.57

ralent CaO

0.38 0.25 0.10

0.05 0.12

0.90

Residual

Gr.NaCN

0.43 0.49

0.49

ims CaO

0.13 0.28 0.33

0.26 0.38

0.38

Consumed

Gr NaCN

0.07 0.01

0.08

UT) S

CaO

0.25 0.10 0.05

0.12 0

0.52

PH

11.8-11.75 12.0-11.8 12.0-12.0

12.1-12.0 12.0-12.0

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.16 CaO: 1.04

Metallurgical Results

Product

24 h Preg'n 4- Wash 24 h Cyanide Residue

Head (Calculated)

Amount

2060 mL 498.5 g

498.5 g

Assays .mg/L.g/t

Au

0.60 0.24*

2.75

7. Distribution

O'all Au

36.5 3.5

40.0

Ind. Au91.2 8.8

100.0

* average of 0.27, 0.20 and 0.24 g/t Au

Overall Recovery 96.57o(amal 4- cyn.)

Page 252: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- lUl -

it No. 184

Purpose: To repeat test No. 181.

Procedure: As for test No. 181.

Feed: 500 g Composite B Amalgam Tailing from Test No. 182,

Solution Volume: 1000 ml Pulp Density 33 7. solids

Solution Composition: 0.5 g/L NaCN

0.5 with Ca(OH) 2

Reagent Balance:

Time

Hours

Preaeratio0-2 2-4 4-6

Cyanidatio

0-15 15-24

Total

Added , Grams

Actu NaCN

n

n

0.53 0

0.53

al Ca(OH) 2

0.5 0.32 0.12

0.07 0.08

1.09

Equi\ NaCN

0.50 0

0,50

alent CaO

0.38 0.24 0.09

0.05 0.06

0.82

Residual

Gr 1 NaCN

0.49 0.45

0.45

ins CaO

0.14 0.29 0.33

0.32 0.38

0.38

Consumed

Gr NaCN

0.01 0.04

0.05

ams CaO

0.24 0.09 0.05

0.06 0

0.44

PH

11.8-11.75 12.0-12.0 12.0-12.0

12.1-12.0 12.0-12.0

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 0.10 CaO: 0.89

Page 253: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 1U2 -

No. 184 - Continued

Metallurgical Results

Product

24 h Preg'n+Wash Sol'n 24 h Cyanide Residue

Head (Calculated)

Amount

2200 ml 495.6 g

495.6 g

Assays, mg/L.g/t

Au

0.58 0.18*

2.76

7. Distribution

O'all Au

37.4 2.6

40.0

Ind. Au

93.4 6.6

100.0average of 0.18, 0.20 and 0.15 g/t Au

Overall Au Recovery by Amal + Cyn: 97.4 'l.

Page 254: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

No. 185

Purpose:

Procedure:

Feed:

Grind:

To recover the free gold from Composite B by gravity separation.

The sample was ground and passed over a Wilfley table. The concentrate and tailing were collected and filtered. The concentrate was reserved for cyanidation.

2000 grams minus 10 mesh Composite B.

12 minutes/2 kg at 65 percent solids in a lab ball mill.

Metallurgical Results

Product

Table Concentrate Table Tailing

Head (Calculated)

Amount

3.5 96.5

100.0

Assays, g/t

Au

49.1 1.59

3.25

7. Distribution

Au

52.8 47.2

100.0

Screen Analyses

Table Tailing

Mesh Size(Tyler)

* 142028354865100150200270400

- 400

Total

7o RetainedIndividual

0,30.50.60.82.45.08.710.110.310.38.542.5

100.0

Cumulative

0.30.81.42.24.69.618.328.438.749.057.5100.0

-

7o PassingCumulative

99.799.298.697.895.490.481.771.661.351.042.5

-

-

Page 255: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

No. 186

Purpose:

Procedure;

To investigate the recovery of gold from Test No. 185 table concentrate by intensive cyanidation.

The concentrate was pulped with water in a 2 litre plastic jar. NaCN was added and the sample was agitated using an Agitair cell. Oxygen was circulated in the sample throughout the test. The cyanidation was carried out in one 24 hour stage. Solution samples were taken at 6 and 16 hours. The pulp was filtered and the residue washed three times with water.

Feed: 75 g table concentrate, test 185.

Solutino Volume: 300 ml Pulp Density 20 'l, solids

Solution Composition: 30 g/L NaCN

Reagent Balance:

Time

Hours

0-24

Total

Added , Grams

Actua NaCN

9.47

9.47

1 Ca(OH) 2

-

-

Equi NaCN

9.00

9.00

valent CaO

-

-

Residual

Gr J NaCN

0.73

0.73

ims CaO

-

-

Consumed

Gr NaCN

8.27

8.27

ims CaO

-

-

PH

11.3-10.8

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 121

Metallurgical Results

Product

24 h Preg'n Solution 24 h Wash Solution24 h Residue

Head (Calculated)

Amount

210 mL 720 mL68.1 g

68.1 g

Assays, mg/L, g/t

Au

10.8 0.06715.1

49.10

7. Distribution

Ind. Au

67.81.4

30.8

100.0

O'all Au

35.8 0.716.3

52.8

Additional Assays: 6 h pregnant solution: Au - 16.4 mg/L16 h pregnant solution: Au - 10.5 mg/L

Page 256: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

it No. 187

Purpose:

Procedure:

Feed :

Grind:

To repeat test No. 185 but regrind the concentrate before cyanidation.

As for test No. 185.

2000 grams minus 10 mesh Composite B.

12 minutes/2 kg at 65 percent solids in a lab ball mill.

Metallurgical Results

Product

Table Concentrate Table CI. Tail. Table Tailing

Head (Calc.)

Weight

•u

5.4 6.3

88.3

100.0

Assays, g/t

Au

81.97 2. 41 1.00

5.46

7. Distribution

Au

81.0 2.8

16.2

100.0

Calculated Grades and Recoveries

Products 2 and 3 94.6 1.09 19.0

Page 257: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

No. 188

Purpose: To investigate the effect of a regrind on the recovery of gold from testl87 table.concentrate by intensive cyanidation.

Procedure: As for test No. 186.

Feed: 105 g table concentrate test 187.

Solution Volume: 420 mL Pulp Density 20 7. solids

Solution Composition: 30 g/L NaCN

Grind: 10 minutes in a lab pebble mill.

Reagent Balance:

Time

Hours

0-24

Total

Added, Grams

Actu NaCN

13.26

13.26

al Ca(OH) 2

-

-

Equi NaCN

12.60

12.60

valent CaO

-

-

Residual

Gr i NaCN

0.52

0.52

mis CaO

-

-

Consumed

Grai NaCN

12.08

12.08

ns CaO

-

-

PH

11.0-10.6

-

Reagent Consumption (kg/t of cyanide feed) NaCN: 116

Metallurgical Results

Product

24 h Preg'n Solution 24 h Wash Solution24 h Residue

Head (Calculated)

Amount

490 mL 1200 mL104.4 g

104.4 g

Assays .mg/Ljg/t

Au

15.3 0.80.97

81.97

7o Distribution

Ind. Au

87.6 11.21.2

100.0

O'all Au

70.9 9.11.0

81.0

Calculated Grades and Recoveries

Products 1 and 2 420 mL - 98.8 80.0

Additional Assays: 6 h pregnant solution: Au - 19.4 mg/L16 h pregnant solution: Au - 22.4 mg/L

Page 258: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

t No. 189

Purpose:

Procedure:

Feed:

Grind:

To collect free gold by gravity separation followed by intensive cyanidation on the concentrate.

A 2000 gram minus 10 mesh Composite A sample was ground for 15 minutes at 65 percent solids in a lab ball mill. The sample was passed over a Wilfey table. The tailing was collected and filtered, The concentrate was pulped with water in a two litre plastic jar. NaCN was added and the cyanidation was carried out in one 6 hour stage using an Agitair cell for agitation. Oxygen was directed into the pulp throughout the test. The pulp was filtered and the residue washed three times with water.

2000 g -10 mesh Composite A

15 minutes in lab ball mill.

Cyanidation Conditions

Feed: —90 g table concentrate test 189

Solution Volume: 360 mL Pulp Density 20 7. solids

Solution Composition: 30.0 g/L NaCN

Grind: 10 minutes in a pebble mill.

Reagent Balance:

Time

Hours

0-6

Added, Grams

Actu NaCN

11.37

al Ca(OH) 2

-

Equiv NaCN

10.80

alent CaO

-

Residual

Gr i NaCN

1.76

ims CaO

-

Consumed

GrsNaCN

9.04

ims CaO

-

PH

11.1-12.2

Page 259: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 1U8 -

No. 189 - Continued

Metallurgical Results

Product

1. 6 h Preg'n+Wash Sol'n 2. 6 h Residue 3. Table Tailing

Head (Calculated)

Amount

1000 mL 74.6 g 1912.6 g

1987.2 g

Assays .mg/Ljg/t

Au

6.58 1.87 2.52

5.81

7. Distribution

Au

57.0 1.2

41.8

100.0

Calculated Grades and Recoveries

Products 1 and 2 74 .6 g 90. 1 -

Au recovery by intensive cyanidation of the table concentrate: 97.9 7.

Screen Analyses

Table Tailing

Mesh Size(Tyler)

* 142028354865

100150200270400

- 400

Total

7. RetainedIndividual

0.20.20.20.41.23.67.2

10.711.810.610.343.6

100.0

Cumulative

0.20.40.61.02.25.8

13.023.735.546.156.4

100.0

-

7. PassingCumulative

99.899.699.499.097.894.287.076.364.553.943.6

-

' -

Page 260: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 1U9 -

No. 190

Purpose:

Procedure:

Feed:

Grind:

To produce a high grade gold concentrate by gravity concentration and magnetic separation.

The sample was fed over a laboratory Wilfley table. The table concentrate was cleaned on a Mozley shaking table. The two table tailings were filtered separately and assayed. The final gravity concentrate was further upgraded using a Frantz magnetic separator, The first pass non-magnetics were repassed at 0.1A.

2 kg minus 10 mesh Composite A.

I2minf2 kg at 65 7. solids in lab ball mill.

Metallurgical Results

Product

1. Mozley Non-Mags2. Mozley 0-lA Mags3. Mozley OA Mags4. Mozley Tailing5. Wilfley Tailing

Head (Calculated)

Weight

7.

0.660.120.494.21

94.52

100.00

Assays, g/t

Au

54129936.517.82.48

7.20

7, Distribution

Au

49.65.02.5

10.432.5

100.0

Calculated Grades and Recoveries

Products 1 and 2Products 1 to 3Products 1 to 4

0.781.275.48

50432388.6

54.657.168.5

Page 261: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 150 -

Test No. 190 - Continued

.eralog)

The magnetic separation products were examined mineralogically to determine the size and distribution of the gold.

Grain Count Results:

Product

Non-Magnetics 0.1A Mags DA Magnetics

Product

Non-Mags 0.1A Mags DA Mags

'/. Au Distr.

93.306.650.05

100.00

7. FreeGold

7. Middlings99.3 9.8

73.4

0.790.2

100.0

26.6

Size of Au in non-mags: 3-70 urn

Non-Magnetics: Mineral

non-opaquespyritemarcasite/aspy

Total

Particle 'L

84115

100 7.

At least 80 7. of the sulphides were liberatedThere was a trace of pyrrhotite as middlings with pyrite

Screen Analyses

Combined Tailings

Mesh Size(Tyler)

* 2028354865100150200270400

- 400

Total

7. RetainedIndividual

1.31.32.14.17.5

10.211.210.39.18.7

34.2

100.0

Cumulative

1.32.64.78.816.326.537.748.057.165.8100.0

-

7. PassingCumulative

98.797.495.391.283.773.562.352.042.934.2

-

-

Page 262: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 151 -

Bond Ball Mill Closed Circuit Grindability Test

Sample:

Mesh of Grind:

Feed:

Composite A

Minus 6 mesh

14.67. passing 100 mesh

Cycle

12345

New Feed

g

1316.400.5379.7361.5388.8

Number of

Revolutions

100153153162154 .

Grams of Minus 100 mesh

In MillProduct

400.5379.7361.5388.8377.4

In MillFeed

192.158.555.452.856.8

NetProduct

208.4321.2306.1336.0320.6

Net perRevolution

2.082.102.002.072.08

Unit Volume (700 mL) =

Ideal potential product * Average of last 3 periods

Bond's Formula

1316 g in mill : Equivalent to 1880 kg/m 3 at -100 mesh

- 376.4 g

375.9 g : 250.37. circulating load2.05 net g minus 100 mesh per revolution

where:

Wi

Wi

P lGbp

,, t- , (v x 44.5 l ( P ) f v (Gbp) O.82 10 10

Work Index

Screen size test in microns

Net grams of undersize produced per revolution of test millSize in microns which 80 percent of test product passesSize in microns which 80 percent of test feed passes

10.821472.05

109.55

1873

Page 263: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

i41-1

*"

3 IK

in

-. 'jm

i WM

VMW

:I 'MfitnrM

M D

in.w

nr.in

HO

"! J1V

H3IU

OI

01 X

SlIO

At)

7.

Page 264: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

- 153 -

Ball Mill Closed Circuit Grindability Test - Cont'd

Screen Analyses - Oversize

Mesh Size(Tyler)

* 810142028354865100

- 100

Total

7. RetainedIndividual

6.011.410.37.28.38.713.917.215.91.1

100.0

Cumulative

6.017.427.734.943.251.965.883.098.9100.0

-

7. PassingCumulative

94.082.672.365.156.848.134.217.01.1-

-

Head, Composite A

* 6810142028354865

100150200270400

- 400

Total

0.18.7

18.518.112.59.66.25.14.02.62.31.91.71.37.4

100.0

0.18.827.345.457.967.573.778.882.885.487.789.691.392.6100.0

-

99.991.272.754.642.132.526.321.217.214.612.310.48.77.4-

-

Page 265: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

Ball Mill Closed Circuit Grindability Test - Cont'd

Screen Analysis

Undersize

Mesh Size(Tyler)

* 100150200270400

- 400

Total

7. RetainedIndividual

2.020.014.710.79.7

42.9

100.0

Cumulative

2.022.036.747.457.1100.0

-

7. PassingCumulative

98.078.063.352.642.9-

-

LAKEFIELD RESEARCHA Division of Falconbridge LimitedLakefield, OntarioApril 17, 1985 l s lk, tmg

Page 266: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

5 o

uiO'tfil

00*

lOOt

"Ml

w Ml

-Sil

* fill

1*081

•Ui

•oot

Page 267: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past
Page 268: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

N

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Page 269: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

*V1*1. Om

1

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* * * S S f fi B- S K -S ?

Mtl

m AMoy. Au fm* O m*ftr*

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BELL CREEK J .V. ——— WETMORE PROPERTY ————

Mtltt TttMntMy, DNl

•"l 045 1 IciK MOOO j OIK tp'll' 14

Page 270: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

1 ——

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Page 271: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

Au yfti mtti't

IN It ti**** *'*IM tr* 10*

BELL CREEK J.VUirlMII (Ml) B trtulan Klif (SROVtln lent

MorlMII S Iroulon K*tf l __ ______ lorn t.), an

^o) 049 l tolt |i|000 [cm *pru'a*

Page 272: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

too*

tnm

MSB

(TBM

IBOiK

It5 W

lOOl*

TS*

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045-0*-t 9

8

Page 273: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INCDRILL SECTION .-5292 E

i 4ri I.On •mtrvlt*.

BELL CREEK J.V.

ALLERSTON - M. BOUNDARYmft T..mult, o*t.

Page 274: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

990 M

g l

3 l8 i

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•OO

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H

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TOO

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Page 275: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

———r-

l

7

049-OI-tO* r t97.0m

(H* AlMyt 00*1 OOt

gfMU l**p* •l4Ni* *rt 10*

CANAMAX RESOURCES INC.

DRILL SECTION. Un, 375 w

Bell Cr**k J.V.

-—— Roit Option .—

Prt| Q4S |i|000[oan April B

Page 276: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

1001

too*

I IS*

tOOm

176*

160*

lOOm

TBM

60 w

Page 277: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

l O4S-OI-Z08

OO: tt.

CANAMAX RESOURCES INC.

DRILL SECTION: Um. 375 w

Ajuy: Aa pni miter*

Oe

Bill Crttk J.V.

- —— Rtit Option

045 |SM I.:|,|000|0... April' 84

Page 278: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

N oe*

m oot

M flit

M O

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M B

tC

H O

OS

M C

i*

M O

OZ

o o

Page 279: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

e tt i Au p ffi

in* t tr iv* i ,O m

CANAMAX RESOURCES INC.DRILL SECTION : tint 375m w

Btll Crtvk J.V.

111,1! T....H.. 0.1.'H

' frol.i 0^5^ [ sttft ; I 'lbo6[ bot 83

Page 280: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

BOO*

ITS*

04S-OI-2O6

Inrburfe*

tSO*

tun

tOOm

.o,.o m -^

Flmt*.

iaoi

its*

lOOm

•ram

•On

It*s

S

Page 281: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

20*

Ctalu

PSZSZ7*

Claim

PS2SZTS

CANAMAX RESOURCES INC.

DRILL SECTION: L36E

K

8: *u ytii •HUri

fli* tr* I.OMI •IkirvlM.

BELL CREEK J .V. CANAMAX C LAIM

Pr*j: 04S l tolt: t-BOO l Dolt: April'M

Page 282: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past
Page 283: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

101.01

CANAMAX RESOURCES INC

DRILL SECTION. L36E

Page 284: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

s Io

o

3s

o i

1291

75 W

SOW aw

ooe

Page 285: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

048-OI-tOJ

VT •t

\

\

Au ynt

toll lotK lUWl W( l.(B w IMIitIM tlivdM

CANAMAX RESOURCES INC.DRILL SECTION: 125 N

BELL CREEK J.V.MARLHILL Z ONE

Mgrlklll A Irtvltn ^rtpNtfl* TtvM th i* , On)

Page 286: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

104

H

tOO

H

±00

H

ICO

*)

Page 287: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC

DRILL SECTION :L150W

Page 288: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

1s

tnm

190m

t t6m

ITS m

ISO m

ISA o

100m

80m

18m

!

m0 j

xS

~*

li

m0n

1200m

Page 289: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

CANAMAX RESOURCES INC

DRILL SECTION: L sowBELL CREEK J .V

M t Ml VCINSHtrlftill

Htyt* T*f . O ut

l ton |ilOQO[ Pan

Page 290: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

TOWNSHIPTOWNSHIP

B

n i t e

B

B BuffaloAnkeri t a

Au nor

RESOURCES INC

BELL CREEK PROSPECT

LOCATION MAP (Tirhmins Area)

.5 M.t

42A11SE0064 6 3,4-158 HOYLE 200

Page 291: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

59

00

N

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e M

ain

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s fo

r N

orth

and

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l C

reek

Zon

es

gold

dep

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(c

alc

ite

, Fe

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mite,

quart

z, p

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, to

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.G.)

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ngly

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arbo

nate

d V

olca

nics

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nfo

rmable

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onta

ct

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sedim

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to

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then

th

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AA

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Fa

ult-

Fr

om

D.D.

H. D

ata

or f

rom

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. S

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ccia

ted ,

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lly

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phiti

c

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ike

ft D

ip o

f P

olys

ut.

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w

ith B

eddi

ng.

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ow F

acin

gsS

trik

e a

Dip

of

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arin

g

Geo

logi

cal

Con

tact

s Se

en

or In

ferr

ed

-(A

lso

def

inin

g m

iner

aliz

ed

zone

s

Geo

logi

cal

Con

tact

s fr

om

D.D

.H.

da

ta

(pro

ject

ed

to

250m

ele

vatio

n)

Gra

datio

nal

Alte

ratio

n

Bou

ndar

ies

Out

crop

B

ound

arie

s

Sha

llow

Tr

ench

es o

r P

its

on

Qua

rtz

Vei

ns

Gla

cial

Str

ia.

OD

rill

Ho

les

I96

0

-- 80-2

0

198

l t

81-1

8se

ries

series

19

82 -

84

t

10

0-

210

incl

. se

ries

5200

N

Pro

pose

d S

ite f

or

Ver

tical

S

haft

Z. 2

7 t

.85

met

ers

drill

core

sam

ples

)

RE

SO

UR

C

t2A11SE00B4 63.4458 HOYLE

BE

LL

C

RE

EK

-

J.V.

P

roje

ct

045

Pla

n of

Surf

ace

Q

D

ri'II

H

ole

G

eolo

gy "

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e

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nsh

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rio

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le

l IO

OO

Da

te

: Ju

ne

I98

4

Page 292: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

5850 N

oID ^-in

LUO Oin in

o in in in

LUooCOin

LLJOinCOin

LLJOo r^ in

o in r^ in

LLJO Ooo in

5800 N

5750 N

5700 N

117

5650 N

Diobase Dike

194

O 187

5600 N

193

5550 N

O177

5500 N

o184

5450 N

o9m

CM

O

1

w se

42AMSE0064 63.4458 HOYLE 220

LUOtnTtin

LLJO Oin in

oCO (D

v/iLUO Ooc

ITS

Page 293: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

TOWNSHIP

Scale: l'20,000

BR ' Broulan R**f Hoi**

BRW Roiorlo Wlnki* H olt*

AQDrill Ho l* i

100 - 212: Canomai BO He l* i

I9S4 D iamond Drill Hoi**

1.173.Se HI Vtln

l.Aft

MARLHILL ZONE- WEST PART

LO MM-80-9

TL 1*0 S

42A11SE0064 63.4458 HOYLE S30

CANAMAX RESOURCES INC.

DRILL PLAN VERTICAL PROJECTION

MARLHILL Z ONES

HOYLE TOWNSHIP , ONT .

SELL. CREEK J.V.

Scole:l'IOOO but* April f 1983

Page 294: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

Branching Ml qv'l

10 -30 e n Mid* Aspy.py, Tour,

M2 Qv'flo -40cm wid* o V 0. Aipy-py-Tour

M2 qti vtm*

BRl qt 20-40cm wide V.9 -Alpy-Tour

Ml qtl

30.40cm wid* VO -Aapy.py-Tour CARBONATED

PILLOW LANiAS

CARBONATED -

PILLOW LAVAS

CARBONATED PILLOW LAVAS

CARBONATED

PILLOW LAVAS

CARBONATED PILLOW LAVAS

—--. — —-O-

CARBONATED PILLOW LAVAS

bREEN SCHISTOSE

LAVAS

SCALE 1:100042A11SEe064 63.445B HOYLE

LEGEND

Baaolt - Pillowed 81 C arbonatet3

Gr*ir Schistose Leucoxene Basalt

Komatilric Basalt- Carbonated

SYMBOLS

Auriferous Quartz VeinsMl-M2-M3-M4 S BRi Quartz VeinsV G - Arienopynte- Pyrite- Tourmaline

Narro* QU artz Vein or Stringer

-^-'-T Strongly Schistose or Sheared Zones

Trench Outlines with Outcrop Boundaries

Surface Pro] e c f i on of Vft In g (from drilling or from trenching;

Strike of Showed Basait-Toos Sojtn

Ke 9 Di p of Sch!3TC5ity

CorDonated

Win Ter Roods

9 93 Assay - Au gms (Split Core) meters

Area of i984 Stripping

CANAMAX RESOURCES

GEOLOGY AND TRENCH LAYOUT

BELL CREEK JOINT VENTURE

(B'oulan M arlhlll properties)

NTS o-A-ii D*TE R*v. Dec 1984

OFFICE 1-0 ACCOMPANY REPORT ON MAHtHILL STfflPP NG

Page 295: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

5O N 5O N

4O N

30 N

\— 2O N

!0 N

O •O

IO S

Approx. Elevation ; 2 87m

0.5m S hear W/narrow q tz. veuis

N

Surveyed BL O f A Cnd)

Channels Sample^-/

A A 0 8426 \J/ AC 8427 A' 8428

B 84291 8430y 843 1 B' 8432

C 8433

NC

c

v C

84348435843684378438

/ 8 439 8440

) 844184428443

f 6 444 )' 8445

E 8446^ 8447 E' 8448

Tr A 0 7976

\

79777978797979807981

* 7982Tr' 7983

Sample Width

I.Om 1. Om 1. 0 m

I.Om1. 0 m1. Om I.Om

I.OmI.Om1,0ml. 0 mI.OmI.OmI.Om I.Om

I.OmI.Om1.0 mI.Om 1 Om

I.OmI.OmI.Om

I.OmI.OmI.OmI.OmI.OmI.Om I.Om1. Om

Au Assay ( gms.)

342 .97

1 .66

.01

.03Ni 1 .03

.03.05

9 80.35.96.65.25

Nil

.03Ni 1

.0666 .67

.031 .40 .03

.551 .466.325.023.46

.16

.14

.15

BRW-6

1980-Winkie Hole gms Aumerer s

o*

IO S to s

LEGEND

V7-PL.-cb Carbonated Pillowed Basalt

Auriferous Ml 9 M2 Quartz VeinfO. 10-0.40 cm wide Aspy,Dy,tour QVG )

Narrow Quartz Stringers ( i - 3 cm wtae

Sen is tosi ty Trends,

CANAMAX RESOURCES INC

BELL CREEK J.V.

MARLHILL - M! a M2 VEIN SYSTEMS with SAMPLE LOCATIONS

TT" Redding Trends of F'illow LavaFacing South)

Scale : l - IOO Date ; Nov. 1984

42AI1SE0054 63.4458 HOYLE 250

Page 296: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

-M-

HOYLE TOWNSHIP

Broulan

N-

Lot 9 . x \^s\\\SCone. M\\

MarthfH

Scole; I--20,QOC

LEGEND

ASSAYS i a.ift * omt Au l.03 m*r*rt

BR : Broulon R**f Holvi

BRW: Rotorio Wink.* Hole*

MH 80-2, ai-40 ' Rotorio AQ Drill Hvtti

lOt - 2l2i C dnonox BQ Holts

1984 D iomvnd Drill Ho1*t

1.173.36 : Ml Vtin

2.0 : BRI Vein

MARLHILL ZONE -CAST PART

CANAMAX RESOURCES INC.

WILL PLAN VERTICAL PROJECTION

MARLHILL Z ONESHOYLE T OWNSHIP, ONT .

BELL CREEK J.V.

Project 043 Dote. April/ 1 983

Page 297: PROGRESS RPT 1984 PROGRAM BELL CREEK PROJ · 1984 PROGRAM BELL CREEK PROJECT PROJECT 045 MURPHY S HOYLE ... 205 and 206 ... During the course of the past

LUOin to in

LUOo t^- in

LUOinr*- in

LUo o00in

LU Oin oo in

5850 N

5800 N

5750 N

5700 N

5650 N

6IT4

5600 N

13T

5550 N

5500 N

Note:

- 'A' Horizon Intercept*

6 ^

CANAMAX RESOURCES INC.

DRILL HOLE DEVIATION PLAN

BELL CREEK - J.V.

North Zone

Vertical Projection of 'A 1 Horizon InterceptsHoyle Twp., Ont.

Proj ' 045 Scale: l : 5OO Date: Rev. July'84

5450 N