m.t “aquamarine gas”nv-trans.com.vn/storage/tai-lieu/gas-from-c/1. aquamarine gas_… · 1 m.t...

1

M.T “AQUAMARINE GAS”

GAS FORM C

SECTION A

GENERAL INFORMATION

NHAT VIET TRANSPORTATION CORPORATION

06-04-R2 the EverRich Bld, 968 3 thang 2 str, ward 15, Dict 11 - HCM City -VN

Tel: + 84. 8 .22251001 Fax: + 84.8 .22251004 Email: [email protected]

mailto:[email protected]

2

A1 PRINCIPAL SHIP PARTICULARS

1.1 Name of Ship : AQUAMARINE GAS

1.2 Registered Owner : Nhat Viet Transportation Corporation

1.3 Address : Office 06-04-R2,The EVERRICH Building, No.986 - 3 thang 2

street, W.15, D.11, HCM city, Vietnam

Telephone : (84) 08.22251001

Fax : (84) 08.22251004

1.4 Operator : Nhat Viet Transportation Corporation

1.5 Address : Office 06-04-R2 The EVERRICH Building, # 986 - 3 thang 2

street, W.15, D.11, HCM city, Vietnam

1.6 Telephone : (84) 08.22251001

Fax : (84) 08.22251004

1.7 Flag : VIETNAM

1.8 Port of Registry : SAIGON

1.9 Official No. : VNSG-1965-TG

1.10 Call Sign : 3WKN

1.11 Inmarsat C No. : [email protected]

1.12 IMO No. : 8514277

1.13 Previous Name(s) : JAPAN / KOSHIN MARU NO.10

1.14 Builder : JAPAN/ SHINHAMA SHIPBUILDING CO.,LTD

1.15 Date of Delivery : 1985 – RENOVATION 2004 -LEVEL 2SS (1995)

1.16 Classification Society : VIRES (Class No. VR 852215)

1.17 Gross Registered Tonnage : 1358

1.18 Net Registered Tonnage : 506

1.19 Was Ship built in accordance with the

following regulations –

Approval Received

IMO

USCG

RINA

YES YES

YES

YES

YES

YES

3

Other ( NKK )

1.19 IMO certification

Certificate of Fitness - IGC

- A328

- A329

Letter of Compliance

Issued by : VIRES

1.20 Date Questionaire Complied …………………………………………………………

A2 HULL DIMENSIONS

2.1 Length Overall : 71.50 m

2.2 Length Between Perpendiculars : 66.25 m

2.3 Extreme Breadth : 12.00 m

2.4 Extreme Depth : 5.40 m

2.5 Summer Draught : 4.699 m

2.6 Corresponding Deadweight : 1670 T

2.7 Light Displacement : 959.21 T

2.8 Loaded Displacement (Summer) : 1670 T

2.9 Cargo Tank Cubic Capacity (100% full): 1904 m3

2.10 Distance from Keel to Highest Point : 24.00 m

2.11 Air Draught (with normal ballast) : 19.31 m

A3 BALLAST PARTICULARS

Normal Maximum

3.1 Ballast Quantity (Salt Water) : 252 tonnes 405.19 tonnes

3.2 Bunkers, Stores, etc : 92.9 tonnes 125.18 tonnes

3.3 Draught – Forward : 2.43 m 4.91 m

– Aft : 3.74 m 4.12 m

– Mean : 1.31 m 0.79 m

NO YES

YES

YES

YES

NO

4

A4 IMMERSION

4.1 TPC – at Normal Ballast Draught : 5.23 tonnes @ 1.31 m.draught

– at Loaded Draught : 6.05 tonnes @ 4.52 m.draught

A5 LOADED PARTICULARS

Complete the following table:

5.1 Cargo:- Butane Propane Ammonia VCM

5.2 Density:- 0.596 0.583 N/A N/A

5.3

5.4

5.5

5.6

5.7

5.8

5.9

Cargo tones

Bunkers- FO tones

- DO tones

Fresh Water tones

Stores/ Spares tones

Lub Oil tones

Ballast tones

1112.00

98.14

27.04

106.00

14.78

4.42

300.0

1087.80

98.14

27.04

106.00

14.78

4.42

300.0

…………

…………

…………

…………

…………

…………

…………

…………

…………

…………

…………

…………

…………

………….

5.10 Deadweight tones 1662 1638 …… …………

5.11

Draught - Forward

- Aft

- Mean

4,12m

4,91m

4,52 m

4,12m

4,91m

4,52m

…… m

…… m

…… m

………. m

……… m

……… m

A6 PARALLEL MID- BODY DIMENSIONS

m m

m m

MANIFOLD

LOAD DRAFT

BALLAST DRAFT

m m

L.O.A 66.25 m

5

A7 BUNKER CAPACITIES *

7.1 M.E Fuel Oil – Grade : S/G : 0.96

– Capacity @ 98% : 103.00 m3

7.2 Diesel Oil – Grade : GASOIL SG. 0-8383

– Capacity @ 98% : 32.00 m3

A8 FUEL CONSUMPTION DETAILS *

8.1 At Sea (Normal Service Speed) FO : at 270 RPM 5.1 tonnes/day

DO : 0.6 tonnes/day

8.2 In Port, Loading DO : 0.9 tonnes/day

8.3 In Port, Discharging DO : 1.2 tonnes/day

8.4 In Port, Idle DO : 0.6 tonnes/day

(See also consumption Graph on the following page : N/A)

A9 MAIN ENGINE PARTICULARS *

9.1 Main Engine Make and Type HANSHIN DIESEL - GEL32

9.2 No. of Units 6

9.3 Maximum Continuous Rating (MCR) per

Engine 2100 SPH@ 285 RPM

9.4 Total Available Power 2100 HP

9.5 Normal Service Power (85%) 1785 x 270 RPM

A10 AUXILIARY PLANT

10.1 Make and Type of Auxiliary Generators No 01 & No 02 YANMAR S165L – T

P/G: YANMAR 4 K DL

10.2 No. of Units 02

10.3 Maximum Generation Output unit 300 PS

10.4 Total Available Power 695 PS

A11 POWER/SPEED INFORMATION

11.1 Trial Data BHP 2100 PS

MCR 2100 SHP

6

Speed 12.5 knots

Draught 4.699 m

11.2 Normal Service Speed BHP 1785 PS

Speed 11.0 knots

Draught 4.50 m

A12 THRUSTERS (N/A)

12.1 Make and Type …N/A………..

12.2 No. Installed ……………

12.3 Location and Rated Bolled Pull ……………

A13 FRESH WATER

13.1 Capacity of Distilled Tanks N/A m3

13.2 Capacity of Domestic Tank N/A m3

13.3 Daily Consumption – Distilled …………… tonnes

13.4 – Dometic 1.70 tonnes

13.5 Daily Evaporator Output …………… tonnes

A14 BALLAST CAPACITIES AND PUMPS


Tank Capacity (m3)

14.1

14.2

14.3

14.4

14.5

Fore Peak

Wing or Side Tanks

Double Bottoms

Aft Peak

Other (…………………………….)

25.16

77.30

249.52

43.33

14.6 Total 395.31

14.7 Ballast Pump Make and Type VMQ – M/50

DAITO PUMP KOGYO Co., Ltd

7

14.8 No. of Pump 1

14.9 Total Capacity 120/50 m3/hr

14.10 Location ENGINE ROOM

14.11 Control Location ENGINE ROOM

A15 MOORING EQUIPMENT

15.1 ROPES and WIRES

On the diagram below indicate the position of Winch Mounted Wires (W) and Ropes (R) together

with Open (O) and Closed (C ) Fairleads

Mooring Wires (On Drums) Morring Wire Tails

No. Dia Length MBL No. Type Dia Length MBL

Forecastle

For’d Main Deck

Aft Main Deck

Poop

Mooring Ropes (On Drums)

No. Type Dia Length MBL

Forecastle 2 50mm 147

For’d Main Deck

Aft Main Deck 2 50mm 147

Poop 1

8

Other Mooring Lines

No. Type Dia Length MBL

Mooring Wires not on Drums

Mooring Ropes not on Drums 4 50mm 147

Emergency Towing Wires (Fire Wires) 1 6x24 185

MOORING WINCHES

Poop 2 D No Hydraulic 30 KW

15.2 ANCHORS AND WINDLASSES

Windlass Motive Power (e.g. Steam, Hydraulic) Hydraulic

Hauling Power ……9.0 … tonnes

Brake Holding Power ……………… tonnes

Anchor Type ……………..

Weight ……………… tonnes

Is Spare Carried

Cable Diameter ……………. mm

No. of Shackles Port 6

No. of Shackles Starboard 7

15.3 TOWING EQUIPMENT

Is Ship fitted with a Towing Bracket Aft

If Yes, state SWL ……………… tonnes

Is Towing Chain provided

Dimensions of Towing Wire – Diameter ……………… mm

– Length ……………… m

No

Serving

Single or

Double

Drums

Split

Drums

(Yes/No)

Motive

Power (eg

Steam,

Hydraulic)

Heaving

Power

(tonnes)

Brake

capacity

(tonnes)

Hauling Speed

(m/min)

Forecastle 2 D No Hydraulic 37 KW 5t x 05m/min

For’d Main Deck

Aft Main Deck 4t x 20m/min

YES

YES

YES

9

15.4 WINDAGE

Windage on Ballast Draught – End-on ……………… m2

– Lateral ……………… m2

A16 NAVIGATIONAL EQUIPMENT

Is the following equipment fitted:

16.1 Magnetic Compass

16.2 Gyro Compass and Repeaters

16.3 Radars

16.4 Radar Plotting Equipment

16.5 ARPA

16.6 Echo Sounder

16.7 Speed/Distance Indicator

16.8 Doppler Log

16.9 Speed of Approach Doppler

16.10 Rudder Angle, RPM, Controllable

and Indicators

16.11 Rate of Turn Indicators

16.12 Radio D.F

16.13 Navtex Receiver

16.14 Satellite Navigator

16.15 Decca Navigator

16.16 Omega

NO

YES

YES

NO

NO

NO

NO

NO

NO

NO

NO NO

YES

NO

YES

NO

NO YES

10

16.17 Loran C

16.18 Sextant(s)

16.19 Signal Lamp (Aldis)

16.20 Course Recorder

16.21 Engine Order Printer

16.22 What Chart Outfit Coverage is Provided Worldwide

Or

Limited

If Limited, Indicate areas covered ASIA

……………

16.23 Formal Chart Correction System in use

A17 COMMUNICATIONS EQUIPMENT

Is the following equipment fitted

17.1 Radio Telegraph Main Transmitter including facility

to transmit on Radio Telephone Distress Frequency

17.2 Radio Telephone Main Receiver including facility to

receive on Radio Telephone Distress Freqency

17.3 Radio Telephone Distress Frequency Watch Receiver

17.4 Main Radio Antenna

17.5 Radio Telegraph Reserve Transmitter

17.6 Radio Telegraph Reserve Receiver

17.7 Reserve Radio Antenna

17.8 Are the Main and Reserve Installations electrically

separate and electrically independent of each other

17.9 Radio Telegraph Auto Alarm

17.10 2182 kHz Bridge Watch Receiver

17.11 Alarm Signal Generating Device

17.12 VHF Radio

17.13 Inmarsat Satellite Communications System

If yes, state Identification Number 457427210 / 457427211

NO NO

NO

NO

YES

YES

NO

NO

NO

NO

YES

NO

NO

NO

NO

YES

NO

NO

YES

NO

YES

11

17.14 Telex

If yes, state Identification Number 457427210 / 457427211

17.15 Telefax

If yes, state Identification Number ………………………………………………….

17.16 Weatherfax

17.17 EPIRBS

17.18 At least three Survival Craft two- way radio telephone

apparatus.

17.19 Emergency lifeboat Transmitter

17.20 Full set of Publications

NO

YES

YES

NO

NO

YES

12

SECTION B

CARGO SYSTEMS

13

B1 CARGO- GENERAL INFORMATION

1.1 List Products which the ship is certified LPG

to carry

Transport and Carriage Conditions

1.2 Minimum allowable tank temperature 0.00 oC

1.3 Maximum permissible tank pressure 15.6 Barg

1.4 List grades which can be transported 1 GRADE ONLY

simultaneously

1.5 List grades which can be loaded or 1 GRADE ONLY

discharged simultaneously

1.6 State natural tank segregations NONE

(NB. Separation must be by the removal

of spools or the insertion of blanks)

1.7 Number of products that can be conditioned N/A

by reliquefaction simultaneously

B2 CARGO TANKS

2.1 Type of Cargo Tanks STEEL-PLATEWELDING, HORIZONTAL

CYLINKAL TYPE WITH HEMISPHERICAL

AND PLATE

2.2 Maximum Allowable Relief Valve Setting 18.0 kg/cm2

2.3 Safety valve set pressure – if variable give 15.6 kg/cm2

rang for pilot valves

2.4 Maximum vacuum 0.00

2.5 Maximum cargo density 0.97 kg/m3

2.6 State any limitations regarding partially None

filled tanks

2.8 State allowable combinations of filled NO LIMITATIONS

and empty tanks

B3 CARGO TANK CAPACITIES


Tank Capacity

m3 (100%)

Butane Propane Ammonia VCM ………………… …………………

Tonnes oC Tonnes

oC Tonnes

oC Tonnes

oC Tonnes

oC Tonnes

oC

1 760 360 15 358 15

2 1.140 360 15 358 15

3

14

4

5

6

7

8

Total 1900 720 716

B4 LOADING RATES

4.1 From Refrigerated Storage: Product Rate (m3/hr)

With Vapour

Return

Without Vapour

Return

Butane 635 m3/hr Depending on

Shore Condition Propane 635 m3/hr

4.2 From Pressure Storage: Product Rate (m3/hr)

With Vapour

Return

Without Vapour

Return

Butane 0-30oC

600 m3/hr

Depending on

Shore Condition

Propane 0 o

C

10 oC

20 oC

30 oC

4.3 Special Remarks:

B5 DISCHARGING – GENERAL

Cargo Pumps

5.1 Types of pumps ELECTRIC MOTOR DRIVEN,VERTICAL CENTRIFUGAL

DEEP- WELL TYPE

5.2 Number per tank 1

5.3 Rate (per pump) 400 m3/hr

5.4 Delivery head mlc

5.5 Maximum density 12 (120m) kg/m3

Booster Pump

5.6 Type of pump DH – M15

5.7 Number per tank No 2 P,S TANK ( FO)

5.8 Rate (per pump) 0.7 m3/hr

5.9 Delivery head ……………………… mlc

15

5.10 Maximum density 0,57………………… kg/m3

Pumps Curves

Insert in the space below copies of pumping Curves for cargo Pumps and Booster Pumps:

B6 DISCHARGE PERFORMANCE

Fulll Cargo Discharge Times (using all main pumps):

6.1 Fully Refrigerated:

Manifold Back

Pressure

Hours

With Vapour Return Without Vapour

Return

6.2 1 Bar

6.3 5 Bar

6.4 10 Bar

6.5 Pressurized:

Manifold Back

Pressure

Hours

With Vapour Return With Vapour Return

6.6 1 Bar N/A 5

6.7 5 Bar OK 5

6.8 10 Bar OK 10

B7 UNPUMPABLES

Tank No 1 2 3 4 5 6 7 8 Total tonnes

7.1 Vapour 16 25 41

7.2 Liquid 396 583 979

7.3 Total liquid vapour 1020

B8 VAPORISING UNPUMPABLES

8.1 Process used time to vaporise liquid ……………………………

unpumpables remaining after cargo discharge

8.2 - Propane …………………………… hrs

8.3 - Butane …………………………… hrs

8.4 - Ammonia …………………………… hrs

16

B9 RELIQUEFACTION PLANT (N/A)

9.1 Plant design conditions – Air temperature …………………………… oC

9.2 – Sea temperature …………………………… oC

Plant Type

9.3 Single stage/direct

9.4 Two stage/direct

9.5 Simple cascade

9.6 Coolant type ……………………………

Compressors

9.7 Type LPGOS – 97A, VERTICAL ONE STAGE WATER COOLED

9.8 Number 2

9.9 Capacity (per unit) 460 m3/hr

9.10 Are they oil- free

B10 COOLING CAPACITY ( N/A)

State Cooling Capacity (in kcal/hr) for-

10.1 Propane @ -42 oC ……………………… kcal/hr

10.2 @ -20 oC ……………………… kcal/hr

10.3 @ -5 oC ……………………… kcal/hr

10.4 Butane @ -5 oC ……………………… kcal/hr

10.5 …………… @ …… oC ……………………… kcal/hr

10.6 …………… @ …… oC ……………………… kcal/hr

B11 CARGO TEMPERATURE LOWERING CAPABILITY (AT SEA)

Time taken to lower the temp. of:

11.1 Propane from …… oC to -42

oC ……………………… hrs

11.2 -5 oC to -42

oC ……………………… hrs

11.3 -38 oC to -42

oC ……………………… hrs

11.4 +20oC to -0.5

oC ……………………… hrs

11.5 +10oC to -0.5

oC ……………………… hrs

11.6 Butane from +20oC to -0.5

oC ……………………… hrs

11.7 +10oC to -0.5

oC ……………………… hrs

11.8 +10oC to -5

oC ……………………… hrs

11.9 …………from…………to……………… ……………………… hrs

11.10 …………from…………to……………… ……………………… hrs

11.11 …………from…………to……………… ……………………… hrs

11.12 …………from…………to……………… ……………………… hrs

NO YES

NO YES

NO YES

NO

17

B12 INERT GAS

Main I.G Plant

12.1 Type of System ………………………

12.2 Capacity ……………………… m3/hr

12.3 Composition of I.G ………………………

………………………

12.4 Lowest dewpoint achievable ……………………… oC

12.5 Used for ………………………

Auxiliary I.G. Plant

12.6 Type of System ………………………

12.7 Capacity ……………………… m3/hr

12.8 Composition of I.G ………………………

………………………

12.9 Lowest dewpoint achievable ……………………… oC

12.10 Used for ………………………

Nitrogen

12.11 Liquid storage capacity ……………………… m3

12.12 Daily boil- off loss ……………………… m3

12.13 Maximum supply pressure ……………………… kg/cm2

12.14 Supply capacity ……………………… m3/hr

12.15 Used for ………………………

………………………

B13 CARGO TANK INERTING/DE- INERTING

WITH N2 FROM SHORE

13.1 Time taken from fresh air under 5% O2, at –25oC hrs

dewpoint

Time taken from cargo vapour to fully inert at

-25oC dewpoint when:

13.2 - I.G density less than product hrs

- I.G density greater than product ……………………… hrs

B14 GAS FREEING TO FRESH AIR

14.1 Plant used ………………………

14.2 Time taken from fully inerted condition

to fully breathable fresh air ……………………… hrs

18

B15 CHANGING CARGO GRADES

In the table below, show the number of hours needed to changed grades from the removal of

unpumpables to tanks fit to load. Also indicate quantity of inert gas consumed during the

operation:

To Propane Butane Ammonia VCM

From

Time

(hours)

I.G. used

(m3)

Time

(hours)

I.G. used

(m3)

Time

(hours)

I.G. used

(m3)

Time

(hours)

I.G. used

(m3)

Propane

Butane

Ammonia

VCM

Note any operation thet cannot be carried out at sea: ………………………………………

………………………………………

………………………………………

B16 DECK TANK CAPACITIES

16.1 Propane capacity 39 m3

16.2 Butane capacity 34 m3

16.3 Ammonia capacity 13 m3

B17 PRE-LOADING COOLDOWN

In the table below, show time and quantity of coolant required to cooldown cargo tanks from

ambient temperature and fully gassed up state sufficient to allow loading to commence

Product

Quantity of

Coolant

Required (m3

)

Time (hours)

With Vapour

Return Line

Without Vapour

Return Line

17.1 Propane

17.2 Butane

17.3 Ammonia

17.4 VCM

B18 VAPORISER

18.1 Type of vaporiser ……………………………

18.2 Number fitted ……………………………

19

18.3 Capacity (per unit) ………………………….. m3/hr Vapour

18.4 Liquid supply rate ………………………….. m3/hr Liquid

18.5 Delivery temperature …………………………… oC

B 19 BLOWER

19.1 Type of Blower …………………………………….

19.2 Rated capacity …………………… ……………… m3/hr

19.3 Delivery pressure …………………… ……………… kg/m2

B20 CARGO RE-HEATER

20.1 Tyre of Re-heater ………………………………………………

20.2 Number fitted ………………………………………………

20.3 Heating medium ………………………………………………

Discharge rates with sea water at 15oC to raise

Product temperture:

20.4 - for Propane from –42oC to –5

oC ……………………………………… m

3/hr

20.5 - for Ammonia from –33oC to 0

oC ……………………………………… m

3/hr

20.6 Cargo Heater Curve:

Seawater Density: 1.015t/m3

Back Pressure: 3-5 bars

20

20

18

16

14

12

Sea Water 10

Temperature

oC 8

6

4

2

20 40 60 80 100 120 140 160 180

Discharge Rate tonnes/hr

Ammonia/Propane Discharge @ -10oC

B21 HYDRATE CONTROL

21.1 Freezing point temperature of Depressant ………………………………………… oC

21.2 Quantity of Depressant carried …………metanol……………………………… litres

21.3 Means of injection …………………………………………

B 22 CARGO MESUREMENT

Level Gauges

22.1 Are level gauges local or remote

22.2 Manufactuer ENRAF NONRUS

22.3 Type m

22.4 Rated accuracy +/- 10 mm

22.5 Certifying authority SGS RED WOOD

Temperature Gauges

22.6 Manufacturer JAPAN

22.7 Type meter

22.8 Rated accuracy +/- 0.30o

C

22.9 Certifying authority Division for standardization metrology and quality

LOCAL REMOTE

21

Control of Hai phong city - Vietnam

Pressure Gauges


22.11 Type meter

22.12 Rated accuracy 1.5

22.13 Certifying authority Division for standardization metrology and quality

Control of Hai phong city - Vietnam

Oxygen Analyser


22.15 Type meter

Gas Analyser


22.17 Type meter

B23 CARGO SAMPLING

23.1 In the table below, indicate whether samples may be obtained from the levels specified:

Cargo Tank:- 1 2 3 4 5 6 7 8

Sample Level

Top

Middle

Bottom

23.2 Can samples be drawn from _ Tank vapour outlet

_ Manifold liquid line

_ Manifold vapour line

_ Pump discharge line

23.3 State Connection Type and Size ………………………………………………..

YES

NO

NO

YES

22

B 24 CARGO MEASUREMENT


BOW …33….. m STERN 33 m

A B C D E F G H

16.6 m 7.10 m

16.70 m

16.75 m 7.25 m

16.8 m 7.30 m

Notes 1. Indicate liquid, vapour and Nitrogen lines

2. Indicate pipe groupings for separate systems

3. Indicate fuel oil connections

4. Indicate flange rating

5. Show any cross manifolding arrangements

6. Indicate distances from centreline of manifold

Pipe

Flange

Duty Rating Size Raised (R) or

Flat (F) Face

A Liquid 60-1800 mm Center

B Liquid 1730 – 3500 mm P’side S’side

C Vapour 3 4 F

D liquid 8 8 F

E vapour 4 4 F

F liquid 3430 – 5200 mm Center

G Liquid 5130 – 6900mm Center

H Liquid 6830 – 8600 mm Center

14.00

b

-------------

a 1050 a Height above uppermost

------------------ continuous deck 1.05 m

b Distance from ship’s side 1.4 m

c d c Height above load W/L 1.2 m

d Height above light W/L m

Load W/L ………

Light W/L ……………………

23

B25 CARGO MANIFOLD REDUCERS

State number of reducers carried on board and their

flange rating and size:

25.1 WHAT REDUCER ON BOARD ? ASA 8B x ASA 8B = 1 ANSI 300

ASA 6B x ASA 6B = 1 ANSI 300




B 26 MANIFOLD DERRICK/CRANE

26.1 Is manifold derrick provided

26.2 Is manifold crane provided

26.3 Is lifting equipment same port and starboard

If No, give detail ………………………………………………………………

26.4 State SWL at maximum outreach ……………………………………………………………… tonnes

B27 STONES HANDLING

27.1 Stones crane/derrick location and SWL ……………………………NIL………………..

………………………………………………………………

………………………………………………………………

YES

YES

YES

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