G.P.L.
|
STOCK INITIAL
|
154,230
|
t
|
|
STOCK FINAL
|
149,532
|
t
|
|
GPL RETRAITE
|
-
|
t
|
|
GPL REINJECTE
|
0,000
|
t
|
|
PRODUCTION
|
2 724,337
|
t
|
|
EXPEDITION MASSE
|
2 729,035
|
t
|
|
EXPEDITION VOLUME
|
5 101,000
|
Sm3
|
|
Teneur -
|
1,89
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%mol
|
|
Teneur C5+
|
0,14
|
%mol
|
|
Densité
|
0,535
|
|
|
P C S
|
25 271
|
kcal/m3
|
|
Richesse de GPL en gaz sec
|
133
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|
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00H 00
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24H 00
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RELEVE AU COMPTEUR LOCAL
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3 575 211
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3 580 312
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|
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|
t
|
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|
g
|
11
|
Wil
|
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FUEL GAS SYSTEM
|
|
|
24/433/07
|
ISSUED FOR DESIGN
|
|
|
|
|
M
|
|
|
01/12/06
|
ISSUED BY SIM
|
|
|
|
|
Mil
|
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p.)., 64,3
c.d. 082-PFD-01
|
Soo.
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|
Rev. .
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|
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|
DATE
|
DESCRIPTOR
|
|
|
|
|
CUB PREMED
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|
|
|
A
F
K
B
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6
J
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1 A 1
V4-5203
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S2-5206 P5-5207
3, y 3,
HEATING OIL STORAGE TANK
HEATING OIL TRANSFER PUMP
019>
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MISC. HOT OIL EOUIPIENT DRAINS
P1-5204A/B/C
·
HEATING OIL CIRCULATION PUMPS
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/
2
2
7E7)--
V4-5208 P1-5209
1 TO TURBINES
HOT OIL
HEATING OIL DRAIN PULP
DRAIN TANK
-- '<TIT>
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12935511
3
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GAS FIRED HOT OIL HEATER (NOTE 11
293551
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MUMMZER REBOILER
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SUPPLY
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1 55824H
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55824
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4
4
E2 --1104
REGENERATION GAS HEATER
TURBINE
EXHAUST
REGENERATION GAS HEATER
#a
H4-5201A
WASTE HEAT HOT OIL HEATER
411)
EtIM
411,
1=1
0
5
5
<288>
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07-15386901
41I)
IEEE
53869
TURBINE
EXHAUST
TRAIN No.1
TRAIN No.2
H4-5201B
WASTE HEAT HOT OIL HEATER
NOTES:
LEGEND:
r-----1 FLOW Ck0/h1
<--> TEMPERATURE I
·C1
1.HEATER RATED FOR REGENERATION OF TWO TRAINS
SIMULTANEOUSLY.
6
zm
81
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4,3
m-
oo
o
10
CONTRACT MI
K F -2 05 8
OWNER NEL
NO.
DATE
REVISIONS
BY
CHKO
APPO
REFERENCES
NO.
RELEASED FOR
BY
GATE
DRAWN BY DATE JIM 03-02-94
~NMI
SONAT RACH
TFT GAS FIELD DEVELOPMENT PROJECT
ISSUE FOR CONSTRUCTION
EYN
/ /
A
PRELIMINARY
/
AS BUILT JANV. 21104
MB
01/01/04
SR
10
ML
B
APP. FOR DESIGN (FEED 1)
DBK
05/05194
"..
· ,,M0 I
CHECKED BY DATE
DATE
APPROVED BY
AS BUILT JAM.20916
FL
01/01/06
IT
11
ML
onvvi
C
ISSUE FOR CONTRACT
JM
a )
N
7
0
PACKAGE NO.
030- lee. S4
DBK
DBK
ISSUE FOR REVIEW
01/13195
UTILITY FLOW DIAGRAM
HOT OIL SYSTEM
APPROVED BY
DATE
E
ISSUE FOR APPROVAL
05/05195
Brown &Root
COST/SCHED-AREA
ISSUE FOR DESIGN
SAF
06/19/95
06/25/96
0
REISSUE FOR DESIGN
EYN
DRAWING --02
REV.
11
SCALE
/ /
e.=
· ritiSILW'STS
|
Brown
& Root
and Chemicals
Petroleum.
|
JOB NO. PURCHASE
SPECIFICATION REVISION PAGE
|
BF-4749 ITEM NO. E2-1402 1 2402
|
|
|
ORDER
NO_
1
|
NO.
1
|
NO. 4749-100-117-4-P-88
|
|
|
100-0 3- P-117-004
|
|
SHELL- AND- TUBE HEAT EXCHANGER
DATA SHEET
METRIC
UNITS
|
DATE SEPTEMBER 27, 1996
|
|
OF
|
2 BY V M PATEL
|
|
|
|
a'
4"--" g
·-RFI* t4 Fig"- '
712'-gP A 2Ni:in 24;
· 477.P; V 42 71 t4 2A 22tig
g:
CI VI
|
APPLICABLE TO Q INQUIRY 3 PURCHASE Q AS BUILT
|
|
|
SERVICE OF DNIT DEETHANIZER REBOILER
MANUFACTURER FABSCO
|
|
|
CUSTOMER SONATRACH LOCATION TIN FM/YE TABANKORT ALGERIA
|
|
|
SIZE 787.4 mm / 13203 mm X 5490 m TYPE EKG (3)
CkI, HORM 0 VERT CONNECTED IN ONE PARALLEL ONE SERIES
|
|
|
SURF/UNIT 0 GROSS ( EFF. 201.9 m' SHELLSrUN/T
ONE SURF/SHELL GROSS 3 EFF. 201,9 41-0
|
|
|
PERFORMANCE OF ONE UNIT
|
|
|
F L LNG ALLOCATION
|
SHELL SIDE
|
TUBE SIDE
|
|
|
FL ui 0 NAme
|
GE ETHANIZER BOTTOMS
|
Nor OIL
|
|
|
FLU to 04JANTITy, TOTAL, kiln,
|
120,494 {21
|
55.824
|
|
|
VAPOR 0 NraUT)
|
-
|
5851
|
|
|
|
|
LIQUID
|
120,09
|
81 944
|
55.624
|
55.824
|
|
|
STEAM
|
|
|
|
|
|
|
WATER
|
|
|
|
|
|
|
HONCONOENSABLES
|
|
|
|
|
|
|
Tad.PERATuRE 0N/bun. .c
|
713.
|
82
|
245
|
113.3
|
|
|
DENSITY LN, kalm.
|
447.71
|
451 9 /4747
|
733
|
855
|
|
|
VISCOSITY LN, cP
|
0.0118/
|
0.072410.0111
|
0.830
|
4.00
|
|
|
MOLECULAR WEIGHT, VAPOR
|
|
47.7
|
|
|
|
|
MOLECULAR WEIGHT, NONcoNDENSABLE
|
|
|
|
|
|
|
SPECIFIC HEAT CAPACITY LN, kr...2A; 'C
|
0.783/
|
0.802/0.574
|
0 843
|
0.533
|
|
|
THERMAL CONDUCTIVITY LN kin Vp.- m 'C
|
0.0824 .1
|
0.0803 / 0.0231
|
0.114 AVG
|
0,114 AVG.
|
|
|
LATENT HEAT. kcallkg 431 *C
|
|
|
|
|
|
|
|
|
|
INLET PRESSURE, e411(1)
|
19.86
|
|
|
|
VELOCIM m/s
|
|
|
|
|
PRESSURE DROP, ALLOW/CA LC.. bra'
|
1 NEGL
|
0.890 1 0.134
|
|
|
FOULING RESISTANCE (MIN). mr"
·-C-Nksal
|
0.0304
|
0.0004
|
|
|
HEAT EXCHANGED 4.323,C0O x 1.1 k..all'h lin,
(CORRECTED' 79.8 'C
|
|
|
TRANSFER RATE, kcagh- m'-"C SERVICE 2115 .8 CLEAN 14-czLT-
.-C
|
|
|
CONSTRUCTION CF ONE SHELL
|
SKETCH (BuNaL / NOME ORIE'NTADDN)
|
|
|
SHELLSIOE
|
TUBESIDE
|
_
|
|
|
DESIGN PRESSURE. bar(o)
|
32
|
10
|
|
DESIGN TEMPERATURE/ MOW, 'C
|
110 I
· 5
|
330 1 $
|
|
NO. OF PASSES PER SHELL
|
KETTLE
|
SIX
|
|
CORROSION ALLOWANCE, mm
|
1.5
|
i,5
|
|
CONNECTIONS
w_E A-1%i D
RATING
|
IN NPS
|
Br Jr 3006 RF
|
5' / 3030 SF
|
|
OUT NPS
|
113- VAP, 8' UR/303F RF
|
EF Jr 303( RF
|
|
INTERM. NPS
|
3000 RF
|
3000 RF
|
|
TUBE NO. 297 11 ] 00 19.05 mm 1-1-11C1( 3 MIN AVG.
211 mm
|
LENGTH 54190 m PITCH 25.4 mm
|
|
|
TUBE TYPE BARE MATERIAL SA 214 0 WLD Q
smi.s
|
· p
· . 30'
· ..
· C. m
, Kr t iv
|
|
|
SHELL COVER MATERIAL SA-316-70 GI INTECi.
REMOV.
|
|
|
CHANNEL COVER MATERIAL
SA-510-70
|
|
|
|
|
PROTECTION 0 YES NO
% Cur: 0 cZs:L.---o AREA ;SPACING:Gfc
1575
|
mm
|
|
|
nun
|
|
|
|
|
|
· C
|
|
|
pv. INLET NOZZLE BUNDLE ENTRANCE BUNDLE
EXIT TUBES
|
|
|
GASKETS: SH ELLSIPE (1) TUBE SIDE (1) FLOATING HEAD
|
|
|
CODE ASME AGmE SECT. Vitt 41V,1 STAMP 3 YES NO
riArh. BOARD REG. (I YES 0 NO TEMA CLASS:
|
FI
|
|
WEIGHTS' DRY FILLER WITH WATER BUNDLE
|
kg
|
|
INSULATION 3 YES Q NO THICKNESS 301100 rnm
INSULATION SUPPORTS R EQUIRED 3 SHELLS:DE. 3 TUEESIDE
|
|
|
PAINT REOUIRED Ct SHELL5IDE 0 TustESIDE spECrFICATION OF
-4I 749-000-020-G-1943-021
|
|
|
REMARKS (11 304 SS SPIRAL WOUND (2) STRAGIAT LINE VAPORIZATION
(3) WITH WEIR
|
|
|
(4) SADDLES ARE TO BE FIREPROOFED (5)
TWO UNITS ARE R EOLIREO
|
|
|
|
|
|
|
|
