destilacion primaria de crudo (version 1)
TRANSCRIPT
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3D-1009 DECOKING DRUM 3H-1001
CRUDE CHARGE HEAT
DP=25psig DT=600°F 1!" MM #TU $ HR
Autor: Edgar Orellana Rivas.
1 1/2"RW
3FIF-1001
ROTAMETER
3PCV-1001 3D-1009
1"PA
6"PG
3"PD 3PI-1002
1 1/2"MS
AMMONIA CYLINDER 3"LS 3H-1
AT AMBIENT TEMPERATURE
2%-6& ' 5%- 0&
3H-100
PI !FURNISEDWIT PCI#
M()TEAM
M()TEAM
*( )TEAM
FUE* OI*
FUE* OI*
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3PI-1011
2"MS
3PI-1011
3PI-10%3 11/2
FUE* GA)
FUE* OI*
1/2" FPT
M()TEAN
3$& PI*OT GA)
14"PL
3TI-1001 3PI-1003
3TR-1002
3TIC-1002
3TE-1002 3TI-1002 1 1/2"FG 3PI-1010
3/4"TO PILOT
3PI-10& 3PI-100
3TI-1003 3PI-1006 3PT-10&
3PI-100& 3PI'-1009
3PDT-1004 3PC-
3FC-100& 3PT-1009
3PDI-1004 3PCV-100%
3FV-100& 3PV-1009
3PDIC-1004 3FI'-100& 3FV-3001 STRAINER
3PDV-1004 3S$RT-100& 3
3FT-100& 3FR-100& 3FV-1016C
3PSLL-10&% 3FV-1016B 3FT-1006 3S$
3FYV-1016C
BURNERTAIL "A"
IT Y TEN#
LOCATED ONFARTEST BURNER
FRON TE FUEL GASEADER
M()TEAM
P*ANTA AIR
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3T-1001 CRUDE CO*UMN 3P-1001 AND 3P-1001A
CRUDE CO*UMN #OTTOM
DP=50psig 3" U) GPM . PT
DT=A#O/E TRA, 15 525°F #E*O+ TRA, 15 650°F AP=100psig )G=0(02 . MI)C(3500$0 IN) MI)C-3501$1 IN) MI)C-3
3/4-CF
3TI-1004 3TE-100& 1"PG
EACH 4"PL
3TT-100&
DISTRIBUTOR 3TIC-100&
3TR-100& 4"PG
4"PL
3TE-1006
3T-1001 3TT-1006 6"PL
1/4" FPT 3TR-1006 IN TR-1000
3TR-100% 3TI-100% 4"PG
"PL
3TE-100%
4"PG
4"PL
3TE-100
14"PL 3TI-100
3TR-100
3TR-1009
2"MS 3TI-1009 2"PL
3LT-1001
3TE-1009
3LG-T-1001 3PI-1012 3PI-10
3FV-100% 3LS-1001
3LA-1001 3P-1001 3P-1001A
3FC-100% 3LAL-1001
3FT-100% 3LSL-1001 3"PL
FROM3PC-2416 3FI'-100% 3LI'-1001 2"PL
3FR-100% 3LC-1001
/C-300" 1"FG
2"MS
9%-6& ' 6%-0& %-0& ' 15%-0&
3F∑IC-100&/6
)IGNA* FROMPRE))UREINDICATING
CONTRO**ER ATFUE* ),)TEM 6/-
30-03
EAVY DISTILLATE FROMYDROBON-PLATFORMING
UNIT !OT OIL BELT SECTION6Y-30-19#
IN TR-1000
FUE* GA)
FUE* GA)
M()TEAM
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3-I-1001 3E-1001 3P-1005 AND 3P-1005A
CRUDE CHARGE-#OTTOM) CRUDE CO*UMN #OTTOM) COO*ER MIDD*E DI)TI**ATE PUM
ECHANGER 1!55MM #TU$HR AROUND PUMP)
0("6 MM #TU$HR 4*OCATE IN #A, +ITH 3E-100" 5"6 U) GPM P(T IN)U*ATE AP=5psig
3/4-CF )(G=0(61 . P(T(
1"PG
4"PL
FREE DRAINING 4"PG
4"PL
6"PL
FREE DRAINING 4"PG
4"PL
FREE DRAINING 4"PG
4"PL
LOUVERS
3C-1001 3FI'-1010
3E-10013FR-1010
3TW-1012 2"PL 3TI-1013 3FC-1010
3FR-1009
3FT-100 3FT-1009 3FT-1010 6"PL
3FI-100
3LV-1001
3PI-1014 3PI-101&
3I-1001
3TW-1011
3SC-3003 3SC-3002 3P-1005 3P-1005A
2"PL "PL
2"PL
"PL "PL
1 1/2"PL
LOCATEIN
VIENWOF FI
FUEL OIL TOSTORAGE!6Y-30-09#
SAMPLE COOLER
3T-29213T-2922FUE* OI*
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3T-100 3T-1005 3T-1006 3P-1002 AND 3P-1002A
*ATE *IGHT DI)TI**ATE )TRIPPER HEA/, DI)TI**ATE PRODUCT PUMP)
ECHANGER "3 U) GPM . P(T(
HR IN)U*ATE DP=60psig DP=60ps7ig DP=60psig AP=103 psigDT=500°F DT=500°F DT=650°F )G= 0(6" . P(T(
3/4-CF
1"PG
4"PL
3T-1004
3LV-1002 3FC-1011 3FI'-1011
3FT-1011 3FR-1011
3LI'-1002 3FV-1011 2"MS
3LG-R-1002
3LC-1002 3LT-1002 2"PL
4"PL
3LV-1003 3T-100& 3FC-1012 3FI'-1012
3FT-1012 3FR-1012
3LI'-1003 3FV-1012 2"MS
3LG-R-1003
3LC-1003 3LT-1003
4"PG 3FC-1013 3FI'-1013 6"PL
3LV-1004 3T-1006 3FR-1013
3FT-1013
3LI'-1004 3FV-1013
3LG-R-1004
3I-1003 3LC-1004 3LT-1004 2"PL 3PI-1016 3PI-10
3TW-101&
3P-1002 3P-1002A
3TW-101% 4"PL
2"MS
6"PL 6"PL
6"PL 6"PL
"PL "PL
1 1/2"PL 1 1/2"PL
3%-0& ' 1"%-0& 3%-0& ' 21%-0& 3%-0& ' 20%-0&
EAVY DISTILLATO YDROBO
PLATFORMING U!OT OIL BEL
SECTION#
3T-100
3T-1005
3T-1006
M()TEAM
M()TEA
M()TEA
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3-I-1002 3E-1002
HEA/, DI)TI**ATE CRUDE HEA/, DI)TI**ATE
CHARGE ECHANGER COO*ER
2(0 MM #TU $ HR (21 MM #TU $ HR
IN)U*ATE 4*OCATE IN #A,
3/4-CF +ITH 3E-100"
1"PG
4"PL
6"PL
3E-1002 3"PL
3TI-101
3FR-1014
3"PL 3FI'-1014 3PI-101 3PI-1019
3TW-1016 3FR-101& 1 1/2"PL 3FT-1014
3FI'-101& FC-1014
3FT-101& 3P-1003 3P-1003A
3FC-101& 3FV-1014
3TW-1021 6"PL 3FR-1
3FV-101&
3FI'-1
3"PL
6"PL
2"PL
OPERATEDFRON GRADE
DIESEL TOSTORAGE
LOUVERS
T-291"T-2919
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3-I-1005 3-E-100
MIDD*E DI)TI**ATE MIDD*E DI)TI**ATE
CRUDE CHARGE COO*ER 3(2 MM #TU $ HR
ECHANGER3(0 MM #TU $ HR
3/4-CF
1"PG
4"PL
2"PL
4"PL
3TI-1023
4"CR
A-3E-100
3TW-1019 3I-1005 3E-100A#
3TW-1020 #-3E-100
3"PL 4"CS
3TW-1022 3TI-1024 1 1/2"PL
1 1/2"PL
3FR-101% 3FR-1019 3FR-101
3FSLL1016A 3FSLL-1016B 3FT-101% 3FT-1019 3FI'-1019 3FT-101 3FI'-101
3FT-1016B 3FI'-101%
3FT-1016A 3FC-1019 3FC-101
3F$I-1016A 3FV-101% 3FV-1019 3FV-101
3FC-101%
3"PL 2"PL
2"PL 2"PL
6"PL
(EROSENE TO
STORAGE
COO*ING +ATER
COO*ING +ATER
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P-100A 3-E-1015
ATE PRODUCT PUMP) *IGHT DI)TI**ATE
P(T( COO*ER 3(1 MM #TU $ HR
(T(
3/4-CF
1"PG
4"PL
3"PL
3TI-1026 4"CR
A 3E-1015
3E-1015A#
3PI-1020 3PI-1021
# 3E-1015 4"CS
3P-100 3P-100A 3TI-102%
3FI'-1020 3FR-1020
4"PL 3FV-1020 3FC-1020 3FI'-1022 3FR-1022
3FT-1020 3FT-1022 3FC-1022
3FV-1022
3FT-1021 3FR-1021
3FI'-1021
3FC-1021
3FV-1021
LIGT DISTTO
FRACTIONSECTI
3T-29023T-2903T-293T-29
COO*ING +A
COO*ING +AT
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3-P-100 AND 3-P-100A 3-E-1005
CRUDE CHARGE PUMP) CRUDE CO*UMN O/ERHEAD CRUDE C
60 U) GPM . P(T( ECHANGER CONDEN)
AP=390 psig 16(05 MM #TU $ HR 25(1 MM
AG=0(3" . P(T( 4)EE DET
3/4-CF
1"PG
4"PL
10"FL 3PSV-1001
6" 3PR-1034
3PSV-1001-A 3PI'-1034
6"
3PC-1034
6"PL 3PT-1034
6"PL 3I-100
3TW-106 3TW-103
3E-100&
3PSV-1022 1"PL 3-)S-1001 3-)S-100
3C-1
3PI-1032 3PI-1033
3P-100 3P-100A
10"PL
6"PL STARTUP
10"PL
6"PL
3-I-100
CRUDE CHARGEFRON-)TORAGE
OFF-SPEC TOSTORAGE
FREE DRAINING*MINIMURUN OF ORI)ONTAL PIP
!NO POC(ETS#
WAFRAC
WASTE WPLATFO3T-290
3TK 2905
3T-29003T-29013T 10 002
MM
F*ARE
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3-E-1016 3-D-1001 3-P-1006 AND 3-P-1006A
CRUDE CO*UMN O/ERHEAD CRUDE CO*UMN O/ERHEAD PUMP)
TRIN CONDEN)ER RECEI/ER 60 U)( GPM . P(T(
3(1 MM #TU $ HR AP= 9 psig
DP=60psig DT=250°F )G= 066" . P(T(
3/4-CF
4"PL
4"FL 3FV-1024
3PV-1034B
3PV-1034A 2"PG 2"PG
3FC-1024
1 1/2"PG 3FI'-1024
3FT-1024
3FR-1024 2"
3E-1016 3FO-1001
3E-1016A# 4"PG 4"PG
3E-1016 3LS-1006
3D-1001 3PI-1069 3LA-1006
3LI-1006
3LT/LC-1006 3FR-1023
6"PL 3FT-1023 3LV-1006
3LT/LC-100& 3LG-R-1006
3LG-T-100& 3PI-103& 3PI-1036
3LI-100&
3LS-100& 3P-1006 3P-1006$A
10"PL 3TI-1034
3LV-100&
1"WS
1 1/2"WS 1"PL
2"WS 1 1/2"WS
5%-6& '19%-0&
3D-1001
IPING SO TATOT DRAIN BAC(PRESSORS
SPLIT RANGE
WASTE WATER FROMGAS RECOVERY UNIT
F*ARE
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3C-1001 AND 3C-1001A Edgar Orellana Rivas.
CRUDE CO*UMN RECEI/ER NET
GA) COMPRE))OR)
15 )CFM1"(3 #HP
3C-1001$A
3PI-10%4 3PI-10%&
3TI-103& 3TI-103%
3LSL-1016
3LSL-101& 3-LAL-1016 3"PG
3PI-103% 3PI-103
3TA-10&% 3TS-10&% 3LAL-101& 3TS-10& 3TA-10&
3TI-1036 3TI-103
3PSV-100& 3PSV-100&A
3PR-1034
3"
3FR-102&
2"PG 3FT-102&
2"PG
4"PL 4"PL
1"PL 1"PL
2"FL 2"FL
UNICOR IN+ECTIONFROM
FRACTIONATIONSECTION
LOCATE CLOSE
TO 3PR-1034 INCONTROL ROOM
ARRANGE PIPING LI$UID CANNOT
BAC( TO COMPRE
3/4" P BLEED ANDRELIEF VALVE
TAILPIPE DRAIN
F*AREF*ARE
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3-D-1002 3-P-1009 AND 3-P-1009A
DE#UTANI8ER DE#UTANI8ER CHARGE PUMP)
CHARGE )URGE DRUM 295 U) GPM . P(T(
AP= 126 psigDP= 135psig )G= 066 . P(T(
DT=250°F
SPLIT RANGE
3PV-1039B 3PV-1039A
11/2"PG
3PSV-1002 3PC-1039 3PI'-1039
3PT-1039 3PR-1039 3F$I-1026 3FR-1026
3D-1002 3LIC-100%
3FI'-1026 3FC-1026
3LT-100%
3FT-1026 3FV-1026
3LG-T-100% 3LG-R-100
3PI-1040 3PI-1041
3P-1009 3P-1009$A
03
3TI-1039 "PL
6"P
5%-0& '1"%-0&
3 D - 1 0 0 2
DEBUTANI)ER CARGETO FRACTIONATION
SECTION
ION
FUELEM
F*ARE
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3-D-100"
ET FUE* )URGE DRUM
DP= 100psigDPE= 10( psig
DT= 250°F
4"FL 1"FL
2"FL
SPLIT RANGE
3PV-10&9B 3PV-10&9A 1"PG
1"FL
3LS-1013 3LA-1013
4"FL 3PSV-101% 3LSL-1013 3LAL-1013
3PIC-10&9
3D-100" 3LT-10133LIC-1013
3LG-R-101% 3PSV-1024
3LC-1012 3PI-10%2
3LG-T-1016
3PC-10%3
3PV-10%3
3LV-1012
1"GN
2"PL
3FV-10
GA) DE* 3D-1003
3FR-10
3FC-103
3FI'-103
2"PG 1"NG
3%-0& '10%-3&
3 D - 1 0 0 "
BLAN(ETING GASFRON GAS RECOVERY
SECTION
NATURAL GASFRON GASRECOVERY
BLAN(ETING GAS FRONFRACTIONATION
SECTION
F*ARE F*ARE
F*ARE
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-P-101A 3-T-1010
ATING PUMPA) CAU)TIC +A)H
P(T(
DP= 15 psig
(T( DT= 250 °F
2"FL
2"FL 3PSV-1020
2"FL 1*1/2"PL
3LG-T-101
3FT'-1039
3FR-1039
3FC-1039 3T-1010
3FT-1039 1*1/2PL 3FV-1039
3LG-T-1019
3AT-1003
3PI-1061 3AR-1003
DISTRIBUTOR
FLAS POINT
3P-101A RECORDER
NYDROCARBON CAUSTIC FILL
PUMPOUT AND WITNDR
1*1/2"PL
1*1/2"PL
2%-0& '20%-0&
3T-1010
F*ARE
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3-T-100 3-P-1015 AND 3-P-1015A 3-D-1006
+ATER +A)H +ATER PUMP) 10 U) GPM . P(T( +ATER #REAK T
AP= 125 psig
DP= 15 psig )G= 1(0 - 1(0 . P(T( DP= ATM
DT= 250 °F DT= 150 °F
2"FL
3PSV-101
2"FL 1*1/2"PL
3LG-T-1020
3D
3T-100%
3LG-T-1021 3LG-B-1022
1*1/2"TW
DISTRIBUTOR 3PI-1062 3PI-1063
3P-1015 3P1015A
2"TW
AU'ILIARY SEAL PLAN 62
2"
WATER
WITNDRAWAL
1"TW
1*1/2"PL
2"PL
2%-0& ' 20%-0& 2%-0& ' 6%-0&
3T-100
TREATEDWATER
F*ARE
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3-T-100" 3-T-1011
)A*T FI*TER C*A, FI*TER IN)U*ATE
DP= 15 psig DP= 15 psigDT= 250 ° F DT= 250 °F
3"FL 3"FL
3PSV-1021
3PI-1064
3PSV-1019
3T-1011
3T-100
3LT-1014
3LV-1014 2"P
1*1/2"PL
1*1/2"PL
1*1/2"PL
2"TW
2%-0& ' 9%-0& %-0& '15%-"&
3T-1011MA(E
CONNECTION ONVERTICAL LINE
3T-100"
DISTRIBUTOR
MA(ECONNECTION ON
VERTICAL LINE
F*ARE F*ARE
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3-T-1001 3-P-1016 AND 3-P-1016A 3-T
CAU)TIC ME*T TANK CAU)TIC TRAN)FER PUMP) FRE
13 U) GPM . P(T( 90 #
AP= 90 psig
)G= 1(5 . P(T(
Edgar Orellana Rivas.
3T-1001 3T-1
1*1/2"PL
3PI-106% 3PI-106
1*1/2"PL
3P-1016 3P-1016A
2"PL 2"CF
1*1/2"TW
2"PL
6%-0& '3%-6&
E
ON ONLINE
FUEL TOTORAGE
3T-1001
-292-292"
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3-T-1003 ),M#O*) ADDED ACCO
IC TANK )PENT CAU)TIC TANK FT, FLOW TRA
90 ##* PDT, PRESSUR
PT, PRESSUR
LT, LEVEL TRAFI', FLOW IND
PI', PRESSUR
TT, TEMPERAT
LSL, LEVEL SW
LAL, LEVEL ALA
PSLL, PRESSUR
FSLL, FLOW SW
FSL, FLOW SW
PSL, PRESSUR
FAL, FLOW ALA
PSL, PRERSSU
F$I, FLOW INT
FYV, SOLENOID
S$*RT*, S$UARE R
RS, RATIO STA
EFR, FLOW REC
SUM, SUMMER
', RELAY
3T-1003 FEIC, FLOW IND
PCV, PRESSUR
PDIC, PRESSUR
)S, VIBRATION
, INSTRUME
, INSTRUME
3LI-101& 3LI-1016 , INSTRUME
1*1/2"PL , TRANSMIT
CRUDO
FUI* OI
DIE)E* O
KERO8E
ET FUI*
GA)O*IN
1*1/2"PL
2 3T-1003
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G TO I)A
ITTER
FERENTIAL TRANSMITTER
ANSMITTER
ITTER
ING MANUAL-AUTOMATIC LOAADING STATION
ICATING MANUAL -AUTOMATIC LOADING STATION
TRANSDUCER
LOW
LOW
ITC LOW !SUT DOWN#
LOW !SUT DOWN#
LOW !SUT DOWN#
ITC LOW !SUT DOWN#
OW
LARM LOW
ATOR VE
E'TRACTOR
ER !SUMMER OF FUEL GAS AND FUEL OIL#
TING CONTROLLER !SUMMER OF FUEL GAS AND FUEL OIL#
NTROL VALVE !SELF-ACTING REGULATOR#
ERENTIAL INDICATING CONTROLLER
ITC
AC( OR BEIND TE BOARD MOUNTED
BOARD MOUNTED !LOCATE IN PROCESS CONTROL ROOM# 3---100&
OCAL MOUNTED 3FYV-101&A
- LOCAL MOUNTED
3FIF-1001 3FR-1006/& 3FR-1009
3PCV-1001 3SUM-1006 3LV-1001
3D-1009 3T-1001 3SC-3003
3-1001 3TI-1004 3SC-3002
3PI-10%3 3TE-100& 3P-100&/A3PI-1002 3TT-100& 3PI-1014
3TI-1001 3TIC-100& 3PI-101&
3PI-1003 3TR-100& 3FT-1010
3TI-1002 3TE-1006 3FR-1010
3TE-1002 3TT-1006 3FC-1010
3TR-1002 3TR-1006 3FI'-1010
3TIC-1002 3TR-100% 3FV-1010
3PI-100& 3TI-100% 3I-1003
3TI-1003 3TE-100% 3TW-1014
3PDT-1004 3TE-100 3TW-101&
3PDIC-1004 3TI-100 3T-10043PDI-1004 3TR-100 3LV-1002
3PDV-1004 3TR-1009 3LI'-1002
3PSLL-10&6 3TI-1009 3LT-1002
3PI-1006 3TE-1009 3LC-1002
3FV-100& 3LT-1001 3LG-R-1002
3FT-100& 3LS-1001 3FV-1011
3FR-100& 3LA-1001 3FT-1011
3S$RT-100& 3LI'-1001 3FC-1011
3FI'-100& 3LSL-1001 3FI'-1011
3PSLL-10&% 3LAL-1001 3FR-1011
3FC-100& 3LC-1001 3T-100&
3FV-100% 3LV-1003
3FT-100% 3LI'-1003
3PT-10& 3FC-100% 3LT-1003
3PI-10& 3FI'-100% 3LC-1003
3PI-1010 3FR-100% 3LG-R-1003
3PI-1011 3LG-T-1001 3FV-1012
3PI'-1009 3P-1001/A 3FT-1012
3PT-1009 3PI-1012 3FC-1012
3PC-1009 3PI-1013 3FI'-1012
3PV-1009 3I-1001 3FR-1012
3RS-100& 3TI-1010 3T-1006
3LSS-1009 3TW-1011 3LV-1004
3FR-1006 3E-1001 3LI'-1004
3S$RT-1006 3TW-1012 3LT-1004
3FT-1006 3FT-100 3LC-1004
3FYV-1016C 3FI-100 3LG-R-1004
3FV-1016C 3TI-1013 3FV-1013
3FV-1016B 3C-1001 3FT-1013
3FIC-100&/6 3FT-1009 3FC-1013
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TAG - DE *A U( DE CRUDO
Edgar O.R.
3FI'-1013 3FV-101% 3TW-1031 3TI-103% 3PSV-1024 3T.-1002
3FR-1013 3FT-101 3TI-1032 3LSL-1016 3PI-10%2 3LI-101&
3P-1002/A 3FR-101 3C-1002 3LAL-1016 3PV-10%3 3T.-1003
3PI-1016 3FI'-101 3)S-1001 3PI-103 3PC-10%3 3LI-1016
3PI-101% 3FC-101 3)S-1002 3TS-10& 3FV-103 3FC-1039
3TW-101% 3FV-101 3E-1016AB 3TA-10& 3FT-103 3LG-R-101%
3I-1002 3FT-1019 3TI-1033 3TI-103 3FR-103 3PCV-100%
3TW-1016 3FR-1019 3D-1001 3PSV-100&A 3FC-103 3FV-3001
3E-1002 3FI'-1019 3LT/LC-100& 3PSV-100& 3FI'-103 3VC-300
3TI-101 3FC-1019 3LI-100& 3FR-102& 3TI-1069 3LIC-100%
3FT-1014 3FV-1019 3LA-100& 3FT-102& 3P-101%/A 3FR-1004
3FR-1014 3P-1004/A 3LS-100& 3PR-1034 3PI-1060
3FI'-1014 3PI-1020 3LG-T-100& 3D-1002 3PI-1061
3FC-1014 3PI-1021 3LV-100& 3PV-1039B 3FT-1039
3FV-1014 3TW-102& 3PI-1069 3PV-1039A 3FR-1039
3FT-101& 3E-101&AB 3LT/LC-1006 3PSV-1002 3FI'-1039
3FR-101& 3TI-1026 3LS-1006 3PT-1039 3FV-1039
3FI'-101& 3TI-102% 3LA-1006 3PR-1039 3AT-1003
3FC-101& 3FT-1020 3LI-1006 3PI'-1039 3AR-1003
3FV-101& 3FR-1020 3LV-1006 3PC-1039 3T-1010
3P-1003/A 3FI'-1020 3LG-R-1006 3LG-T-100% 3PSV-1020
3PI-101 3FC-1020 3PV-1034A 3LT-100% 3LG-T-101
3PI-1019 3FV-1020 3PV-1034B 3P-1009/A 3LG-T-1019
3TW-1021 3FT-1021 3FT-1024 3PI-1040 3T-100%
3I-100& 3FR-1021 3FR-1024 3PI-4041 3PSV-101
3TW-1019 3FI'-1021 3FI'-1024 3TI-1039 3LG-T-1020
3TW-1020 3FC-1021 3FC-1024 3FT-1026 3LG-T-1021
3TW-1022 3FV-1021 3FV-1024 3FC-1026 3P-101&/A
3FT-1016A 3FT-1022 3P-1006/A 3FR-1026 3PI-10623FSLL-1016A 3FR-1022 3PI-103& 3F$I-1026 3PI-1063
3FAL-1016A 3FI'-1022 3PI-1036 3FI'-1026 3D-1006
3FSL-1016A 3FC-1022 3TI-1034 3FV-1026 3LV-1014
3FR-1016A 3FV-1022 3FT-1023 3D-100 3LT-1014
3FI'-1016A 3P-100%/A 3FR-1023 3PV-10&9B 3LG-B-1022
3FC-1016A 3PSV-1022 3FO-1001 3PV-10&9A 3T-100
3F$I-1016A 3PI-1032 3C-1001/A 3PSV-101% 3PSV-1019
3FV-1016A 3PI-1033 3PI-10%4 3PIC-10&9 3T-1011
3FT-1016B 3PSV-1001 3TI-103& 3LV-1012 3PSV-1021
3FSLL-1016B 3PSV-1001-A 3LSL-101& 3LC-1012 3PI-1064
3E-1004AB 3PT-1034 3LAL-101& 3LG-T-1016 3PV-106&
3TI-1023 3PR-1034 3PI-103% 3LT-1013 3PI-10663TI-1024 3PI'-1034 3TA-10&% 3LIC-1013 3PC-106&
3FT-101% 3PC-1034 3TS-10&% 3LSL-1013 3T.-1001
3FR-101% 3I-100% 3TI-1036 3LS-1013 3P-1016/A
3FI'-101% 3TW-106 3PSV-100& 3LA-1013 3PI-106%
3FC-101% 3E-100& 3PI-10%& 3LAL-1013 3PI-106
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3D-1009 DECOKING DRUM 3H-1001
CRUDE CHARGE HEATE
DP=25psig DT=600°F 1!" MM #TU $ HR
Autor: Edgar Orellana Rivas.
1 1/2"RW RAN+
3FIF-1001
ROTAMETER
3PCV-1001
1"PA
6"PG
3"PD 3PI-1002
M( )TEAM 1 1/2"MS
AMMONIA CYLINDER *()TEAM 3"LS
AT AMBIENT TEMPERATURE
FUE* OI*
FUE* OI*
M()TEAM 1
2%-6& ' 5%- 0&
3H-1001
PI !FURNISEDWIT PCI#
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Edgar Orellana Rivas.
3/4"AS
3PI-1011
2"MS M* STEAM
3PI-1011
3PI-10%3 11/2"FP
PLANTA AIR FUE* GA)
FUE* OI*
1/2" FPT
M()TEAN
3$& PI*OT GA)
14"PL
3TI-1001 3PI-1003
3TR-1002
3TIC-1002
3TE-1002 3TI-1002 1 1/2"FG 3PI-1010
3/4"TO PILOT
3PI-10& 3PI-100
3PI-1006 3PT-10&
3PI-100& 3PI'-1009
3PDT-1004 3PC-10
3FC-100& 3PT-1009
3PDI-1004 3PV-100% 3Y
3PV-1009 3PV-1009
3PDIC-1004 3FI'-100& FV-3001 STRAINER
3PDV-1004 3S$RT-100& 3RS
3FT-100& 3FR-100& 3PV-1016C
3PSLL-10&% 3FV-1016B 3FT-1006 3S$RT
3FYV-1016C 3FT-1006
BURNERTAIL "A"IT Y TEN#
LOCATED ONFARTEST BURNER
FRON TE FUEL GASEADER
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3T-1001 CRUDE CO*UMN 3P-1001 AND 3P-1001A
CRUDE CO*UMN #OTTOM
DP=50psig 3" U) GPM . PT
DT=A#O/E TRA, 15 525°F #E*O+ TRA, 15 650°F AP=100psig )G=0(02 . MI)C(3500$0 IN) MI)C-3501$1 IN) MI)C-3
3/4-CF
3TI-1004 3TE-100& 1"PG
EACH 4"PL
3TT-100&
DISTRIBUTOR 3TIC-100&
3TR-100& 4"PG
4"PL
3TE-1006
3TF-1006 6"PL
1/4" FPT 3TR-1006 IN TR-1000
3TI-100% 3TI-100% 4"PG
"PL
3TE-100%
4"PG
4"PL
3TE-100
14"PL 3TI-100
3TR-100
3TR-1009
2"MS 3TI-1009 2"PL
3LT-1001
3TE-1009
3LGT-1001 3PI-1012 3PI-10
3FV-100% 3LS-1001
3LA-1001 3P-1001 3P-1001A
3FC-100% 3LAL-1001
3FT-100% 3LSL-1001 3"PL
3FEIC-100&/6
FROM3PC-2416 3FI'-100% 3LI'-1001 2"PL
3FR-100% 3LC-1001
/C-300" 1"FG
2"MS
FUE* GA)
9%-6& '6%-0& %-0& '15%-0&
)IGNA* FROMPRE))UREINDICATING
CONTRO**ER ATFUE* ),)TEM 6/-
30-03
EAVY DISTILLATE FROMYDROBON-PLATFORMING
UNIT !OT OIL BELT SECTION6Y-30-19#
IN TR-1000
M()TEAM
FUE* GA)
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3-I-1001 3E-1001 3P-1005 AND 3P-1005A
CRUDE CHARGE-#OTTOM) CRUDE CO*UMN #OTTOM) COO*ER MIDD*E DI)TI**ATE PUMP
ECHANGER 1!55MM #TU$HR AROUND PUMP)
0("6 MM #TU$HR 4*OCATE IN #A, +ITH 3E-100" 5"6 U) GPM P(T
IN)U*ATE AP=5psig
3/4-CF )(G=0(61 . P(T(
1"PG
4"PL
FREE DRAINING 4"PG
4"PL
6"PL
FREE DRAINING 4"PG
4"PL
FREE DRAINING 4"PG
4"PL
LOUVERS
3C-1001 3FI'-1010
3FR-1010
3TW-1012 2"PL 3TI-1013 3FC-1010
3FR-1009
3FT-100 3FT-1009 3FT-1010 6"PL
3FI-100
3LV-1001
3PI-1014 3PI-101&
3I-1001
3TW-1011
3P-1005 3P-1005A
2"PL "PL
2"PL
"PL "PL
1 1/2"PL
2"PL
LOCATEIN
VIENWOF FI
FUEL OIL TOSTORAGE!6Y-30-09#
SAMPLE COOLER
3T-29213T-2922
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3T-100 3T-1005 3T-1006 3P-1002 AND 3P-1002A
*ATE *IGHT DI)TI**ATE )TRIPPER HEA/, DI)TI**ATE PRODUCT PUMP)
ECHANGER "3 U) GPM . P(T(
HR IN)U*ATE DP=60psig DP=60ps7ig DP=60psig AP=103 psigDT=500°F DT=500°F DT=650°F )G= 0(6" . P(T(
3/4-CF
1"PG
4"PL
3LV-1002 3FC-1011 3FI'-1011
3FT-1011 3FR-1011
3LI'-1002 3FV-1011 2"MS
3LGR-1002
3LC-1002 3LT-1002 2"PL
4"PL
3LV-1003 3FC-1012 3FI'-1012
3FT-1012 3FR-1012
3LI'-1003 3FV-1012 2"MS
3LGR-1003
3LC-1003 3LT-1003
4"PG 3FC-1013 3FI'-1013 6"PL
3LV-1004 3FR-1013
3FT-1013
3LI'-1004 3FV-1013
3LGR-1004
3I-1003 3LC-1004 3LT-1004 2"PL 3PI-1016 3PI-10
3TW-101&
3P-1002 3P-1002A
3TW-101% 4"PL
2"MS
6"PL 6"PL
6"PL 6"PL
"PL "PL
1 1/2"PL 1 1/2"PL
3%-0& '1"%-0& 3%-0& '21%-0& 3%-0& '20%-0&
EAVY DISTILLATTO YDROBON
PLATFORMING UN!OT OIL BELT
SECTION#
3T-100
3T-1005
3T-1006
M()TEAM
M()TEAM
M()TEAM
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RE**ENO , COMPONENTE) DE CAD
DISTRIBUIDOR MOD* %4
RELLENO ESTRUCTURADO
SOPORTE MOD*133
COLECTOR DE LI$UIDO MOD
DISTRIBUIDOR DE LI$UIDO M
RELLENO ESTRUCTURADO
SOPORTE MOD*133
DISTRIBUIDOR DE LI$UIDO M
RELLENO ESTRUCTURADO
SOPORTE MOD*133
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*ECHA DE *A 3T-1001
OD*2&0
* 33
OD*136
OD*3&0
OD*136
OD*3&0