..

r,

A.<>::;==~..JZ<~u~:==6:0<c~Z:J

:,.OC<D.~::;°(1)ro..J

.~U) ..11.COv>

.~

.'..

. "'.;;---,

. -'"," . ,"

.,'c.,.

..

§.....

....-'~

~;

t

~

,

,,- -",,--

,, -,-----

t

%

P:: vi.1 -,-. I-. . -

.~ ! ~m__-. .! ~ ------------.--.---.--... : I i ~ '.---~--~ ~

;-- .1

' :,. ../-

,...

- III

sIIIa:..

!;gIII:-::!>IOI.J-<..<:\1)(0..-<

u

; ,'-" -"""" ." ---

.',... . : "." ., . ... ,",..,. "., ',"" m... .-.----. . . .,,' " . "" " ,. ,,-,...,,-~" ,. ", '.,. "'''-- :"

. '.',.,., ''', . .""'--'~ "'''-- ,"',.;.,

, ". -- ,," """"..",

FIGURE 2 .

. . '. ' .. .'

#2 S'eparator FloWContributors,*

Coker

259.000 gpd

Tank Car & TruckLoading Rack5

29,000 gpd

ISOIJ13X Shops ArealUTl.X

22;000 gpd .187.000gpd

WaterwelIs

1.152,000 gpd

468,000 gpd

Division -B"Tank.Waterdraws108,000 gpd Tank Waterdraws

Isomax CoolingTower

288,000 gpd

#9, #11, #13 CoolingTowers

., Neutralization Pit

360,000 gpd 72,000 gpdMain Pumphouse

36,000 gpd

Fceu

43,000 gpd DFH &. SRU 70

. 36.000 gpdCogeneration! .Condensate I ..

288.000 gpdVRDSISNR

58.000 gpd

#)2 & # 24 CoolingTowers .

#3. #7; #10 Cooling. Towers

115,OOOgpd

#17& #19 Cooling. Towers

130,000 gpd

187,000 gpd

Residuum Stripper

LSFO BoilerBlowdown

7,000 gpd

58.000 gpd

D-406 Drain

36,000 gpd #2 Crude Unit

72.000 gpd

1,008,000 gpd

#2 Separator

Volume =2,050.000 gaL

flow ;5,019,000 gpd

MiscellaneousRefinery Sources

~~__~!U,I~ws ~~~_lc!...~!'..~~g!:__~.i~~i!~s~nt.lybeca~s~_~L~.ariabilityinrefinerysystems9/5/96

,

i ,-"'. '.

-,-",,-,"c '"

':..,".-- . . ""' '"'' "'-.,., """'" -,.--....

. .-. .h..' ... .'- -"h. ,..

'. '-.-'

"FIGORI:3'. . .. .

#4 Separator Flow tont~jbut()rs*

FCCU.'14.0001pd .

. C.820

324,000 9pd

C-40 .

389.000 gpd

Acid Treating Plant60,000 gpd

#3 Separator72,000 gpd

B&STankW"terdraws

180.000 gDdMTBE Plant

6.000 gpd

TAMEPlant4.000 gpd#2 Crude Desalters'

144,000 gpd

I Waterwells403,000 gpd

lSFO Desalters454.ooogDd

AlleyPlant.144,000 gpd

Vacuum TruckTrarisfers(variable)

#2 Crude Unit PumpCase Seal Flush

36,000 gpd

Merox Plant

12.000 gpd

#4 SeparatorVolume= 240,000 gal.Flow = 2,242,000 gpd

!

06.67 .Allflows could change significantly because of variability in refinery systems R,vistd: 10f'.J96

,

. .'--'-'-". ..-,

~

. . .c ..-' '. -. ... ." --.

:\.

.",,"'-""""'"

. .

.FIGURE 4

.Outfall FlowContfibutors*

. .

'1Water tr~~terF= -11 O.QOOgpd

<'.~.0>u:. .CD

~

13 SeparatorV= SO,OOOgal

. F= -72;000 gpd

112 Separator

V:i2,OSO.OOO gal

F= -5,019,000 gpcl

.1Ll.~

~CD.c:~G:>.<D--CO).:-~0iONe '""-.....-~'""

I~..0::

Ez::0::EE8..~z::E

'J:E

i

Groundwater(on or before2Q 1998)F= -777,000 gpd

-- Biomasstooff-site disposal'

To Outfall 001

m-e=='

.!?LI-.I»~

14 Separator

v= 240,000 gal.F=-2,242.000gpd

;~~~:t;~~}._~! I

Row to off-spocaLlXJliaryfacilities

lEGE~Q- Normal Routing

- Off-Spec Flow Routiog

. . . 180. High Flow Routing.All flowscould change significantlybecause of variabilityIn refinerysystems Revised:]01219606.67-----