Destilacion Primaria de Crudo (Version 1)

8/16/2019 Destilacion Primaria de Crudo (Version 1)

1/28

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*


2/28

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


3/28

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


4/28

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*


5/28

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


6/28

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


7/28

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


8/28

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


9/28

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


10/28

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


11/28

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


12/28

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


13/28

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


14/28

-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


15/28

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


16/28

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


17/28

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"


18/28

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


19/28

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


20/28

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


21/28

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#


22/28

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


23/28

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)


24/28

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


25/28

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


26/28


27/28

RE**ENO , COMPONENTE) DE CAD

DISTRIBUIDOR MOD* %4

RELLENO ESTRUCTURADO

SOPORTE MOD*133

COLECTOR DE LI$UIDO MOD

DISTRIBUIDOR DE LI$UIDO M


SOPORTE MOD*133

DISTRIBUIDOR DE LI$UIDO M


SOPORTE MOD*133


28/28

*ECHA DE *A 3T-1001

OD*2&0

* 33

OD*136

OD*3&0

OD*136

OD*3&0

Date post:	05-Jul-2018
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Destilacion Primaria de Crudo (Version 1)

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