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13505PI
13501PI
13501FI
13501 AFI
13501FT
13502FI
1111I
13501 API
13503PI
13502FT
13502 AFI
13501LI
13501PT
13502PI
13501LT
13504PI
ATM
ATM
ATM
ST
ATM ATM
13501SG
ATM
ATM
111-R-1102111-11124
AI111-11419-1
MP STEAM111-11416
APPLANT AIR
111-11419-1
APPLANT AIR
111-11419-1
AP111-11419-1
111-SP-1105/1106SPENT CATALYST
111-11134
111-K-1101BLOWER AIR
111-11113
CATALYST TRANSFERV-1101 / 1102
111-11134
111-R-1102FRESH CATALYST
111-11124
V-1102CATALYST TRANSFER
111-11134
APPLANT AIR
111-11419-1
V-2504111-11420
APPLANT AIR
111-11419-1
APPLANT AIR
111-11419-1
APPLANT AIR
111-11419-1
SEE PID #B224-FCC-LT-PID-111-11148
GENERAL NOTES
NOTES:
6367 kg/h
13. NO MORE THAN 30° FROM THE VERTICAL.14. CATALYST LOADER CONTROL SYSTEM TO BE INTERFACED. TO DCS FOR MONITORING AND CONTROL.
12. DELETED.11. PLANT AIR PURGING CONNECTION FOR VALVE SEAT AND VALVE STEM.
4. USE NON-INSULATING TYPE PERSONNEL PROTECTION, E.G., SCREENS, CHAIN GUARDS.
2. ALL BENDS IN CATALYST PIPING TO BE MINIMUM OF 9 PIPE DIAMETERS.3. STRAIGHT VERTICAL DROP INTO TRANSFER LINE.
1. FOR CATALYST TRANSFER LINES, PROVIDE 1" VALVED BLAST AIR CONNECTIONS FROM PIPEBOTTOM/SIDE IN ALTERNATIVE / SINGLE DIRECTION TO FLOW AT 45° ANGLE EVERY 6M IN THEHORIZONTAL PIPE RUNS, 3M IN THE VERTICALRUNS AND AT ALL BENDS AND VALVES.
8. DELETED.
10. PI-13501A TO BE READABLE FROM ASSOCIATED GLOBE VALVE.9. FOR CO PROMOTORS OR OTHER ADDITIVES.
7. FOR CONDENSATE REMOVAL.6. ALL CATALYST SERVICE PIPING TO BE SCHEDULE 80 MINIMUM REGARDLESS OF PIPE CLASS.5. PI-13505 & FI-13505 TO BE READABLE FROM ASSOCIATED GLOBE VALVE.
300#
CVF
VF
35
C
16. VENT TO ATMOSPHERE AT A SAFE LOCATION.15. DEBRIS GAURD
25A
2 25B13
17. ELECTRO MECHANICAL LEVEL TRANSMITTER.
20. FOR PLANT AIR INSTRUMENT PURGE DETAILS, REFER DWG. 111-11142 THROUGH 111-11144.
HOL = 21150mm
18. PROVIDE 1/2" WEEP HOLE AT LOW POINT .19. REFER PID 111-11191, FOR DETAIL 'C'.
-
SD/JM
SD/JMAMREVISED FOR BEDP4
SD/JM
5
AM
2
REVISED FOR BEDP
1
3
SD/JMAMREVISED FOR BEDP
REVISED FOR BEDP
15 Jun 2020
VP10 Feb 2020
VP10 Jan 2020
VP20 Dec 2019
VP08 Nov 2019
SD/CCPM VPREVISED FOR BEDP
AM
INTERNAL DIA : 432 mm T-T LENGTH : 3511 mmDESIGN PRESSURE (MAX / MIN) : 5.27 kg/cm^2g / FV@ 65 °C
DESIGN TEMPERATURE (MAX / MIN) : 65 °C / 3.4 °CTRIM : B49A
HOLDS:
DESIGN PRESSURE (MAX / MIN) : 3.5 kg/cm^2g / FV@ 442 °CDESIGN TEMPERATURE (MAX / MIN) : 442 °C / 3.4 °C
16"
2200
0 MM
N+IH
1. PSV-13501A/B QUANTITY, SIZE, INLET / OUTLET LINE SIZE.2. FOR 111-LZ-1106, PACKAGE DETAILS WILL BE FURTHER DEVELOPED BASED ON VENDOR INPUT.
21. DELETED.
HOLD 1
HOLD 1
3. NUMBER OF STEAM TRAPS BASED ON PIPING LAYOUT.
HOLD 3
22. FOR FRESH CATALYST LOADER PACKAGE DETAILS REFER PID B224-FCC-LT-PID-111-11135-A.
TYPICAL
TYPICAL
1 2
MW36"
6"
MIN
36"MW
14
15
1
B1A-
ISA1
A-NI
SJAM
076405C
076405C-111-111355076405C-111-PID-0021-1135
11
1-1/2"
2 5
13
FF10
H
3/4"
2
3/4"
163/4"
5.27
3"K4"+
5.27
3"K4"+
VAC
TT-12401TT-12414
DRAFT
FE13502
+
PCV13501
+
111-SP-1136
111-LZ-1106
111-V-1103
LC
6"
6"
1
6"
H
4"
STEAM EJECTOR111-J-1101
RATED CAPACITY:DESIGN PRESSURE (MAX / MIN): 20.4 kg/cm^2g / FV@ 442 °C
DESIGN TEMPERATURE (MAX / MIN) : 442.0 °C / 3.4 °C
5
3
3/4"-CL-111-13501-A1A-IH
2"-SS-111-13501-A1A-NI10"-P-111-13511-B1K-IH
6"-C
T-11
1-13
530-
B49A
-NI
10"-PA-111-11305-A1A-IS
2"-AP-111-13506-A3A-TL
4"-P-111-13522-B1A-NI
10"-CT-111-13502-B49A-IS
8"-P-111-13510-A1A-NI
2"-CT-111-13522-A49A-NI
3"-AP-111-13508-B49A-IS
2"-CT-111-13526-B49A-IS
8"-P-111-13513-B1A-IS
3"-AP-111-13507-A3A-TL
2"-CT-111-13505-A49A-NI
6"-P
-111
-135
14-B
1A-N
I
4"-AP-111-13515-A3A-TL
8"-P-111-13412-B1A-IS
8"-SV-111-13516-A1A-NI
8"-SV-111-13517-A1A-NI
2"-AI-111-41925-A3K-NI
3/4"
03
03
03
1-1/2"
1-1/2"
1-1/2"3/4"
3/4"
11
1-1/2" 1-1/2"11
03
03
1-1/2" 1-1/2"
11
6"-CT-111-13518-B49A-NI
300#
300#
3/4"
FF
20
28
19B
27
12
3/4"16
16
6"
2"
111-J-1101
TO SAFE LOCATION
1
FRESH CATALYST STORAGE HOPPER111-V-1103
INTERNAL DIA : 5500.0 mm T-T LENGTH : 23500.0 mmDESIGN PRESSURE (MAX / MIN) : 5.27 kg/cm^2g / FV@ 65 °C
DESIGN TEMPERATURE (MAX / MIN) : 65.0 °C / 3.4 °CTRIM :B49A
17
126 10
34
SUPERSACK TRANSFER PACKAGE111-LZ-1106
FRESH CATALYST HOPPER CYCLONE111-SP-1136
FF
FF
AP 6"x3"
1-1/2"
1-1/2"
11
19A
111-SP-1141
VAC
4 6
6"x3"
18
13515T
NNF
NNF
A49A-NI
B49A-IS
NITL
B49A-IS A3A-NI
3/4"
PSV13501 B
+
3/4"
LO
PSV13501 A
+
LC
A. FOR PIPING AND INSTRUMENTATION LEGENDS AND SYMBOLS SEE P&IDs. 111-11011 THROUGH 11047.B. ALL INSTRUMENTS ARE PREFIXED WITH THE PLANT CODE "111". THE PREFIX IS NOT SHOWN ON THE P&IDs FOR CLARITY.C. FOR VENT AND DRAIN DETAILS OF CONTROL VALVES AND LEVEL INSTRUMENTS, SEE DWG. 111-11028/111-11029 AND 111-11030/111-11031/111-11043/111-11044/111-11045/111-11046/111-11047 RESPECTIVELY.D. FOR SAMPLE CONNECTION DETAILS, SEE DWG. 111-11022/111-11023/111-11041/111-11042.E. FOR VENT AND DRAIN DETAILS OF PUMPS, EXCHANGER AND FILTERS, SEE DWG. 111-11024/111-11025, 111-11026/111-11027 AND 111-11036 RESPECTIVELY.F. FOR INSTRUMENT/VALVE FLUSHING DETAILS SEE DWG. 111-11037,111-11038 AND 111-11039/111-11040.
DETAIL 'C'
STEAM EJECTOR SILENCER111-SP-1141
7
SP13501
FRESH CATALYST LOADER111-LZ-1103
111-LZ-1103
TYPE-O
1-1/2" 1-1/2"
1-1/2"
1-1/2"
11
1/2"
1/2"
11
1-1/2" 1-1/2"11
B1A
A1A
A1A
B2A
B2A
A1A
B2A
A1A
1/2"
9
19
18
13516T
1-1/2"11
1-1/2"
1"-A
P-11
1-13
509-
A3A-
TL
4"-SM-111-13512-B2A-IH
6"-CT-111-13521-A49A-NI
2"-A
P-11
1-13
510-
A49A
-IS
6"-P-111-13515-B1A-NI
3/4"-S
M-11
1-13
513-
B2A-
IH
13502T
13511T
SS / CRWS
B49A
B49AA3A
A3AB49A
B1A
B1A
A1AB1K
A1A
A49A A3A
24 Sep 2021
24 Sep 2021
03NK
VKD
DRZ
1
B224-FCC-LT-PID-111-11135
PETROCHEMICAL FCC UNIT (PFCCU) UNIT 111
FRESH CATALYST STORAGE HOPPERCONVERTER
B224-FCC-LT-PID-111-11135
B1K
B1K
B49A-ISA3A-TLB49A-IS
B49A-ISA3A-TL
A3A-TL B49A-IS
6"
NNF
15
1-1/2
"1-
1/2"
11
SS / CRWS
2"
8"x4"
8"x4"
1-1/2
"
2"-AP-111-13502-A3A-TL
2"-AP-111-13503-A3A-TL
SP13503
A49A
-ISA3
A-TL
HOLD 2
6"
6"
ISNI
300#
FB
FB
B49A-ISA3A-NI
A49A
-ISA3
A-NI
A3A-NI
1-1/2"
1-1/2"
1-1/2"
1-1/2"
1-1/2"
B49A-ISA3A-NI
A3A-NI
1-1/2"
SS
03
03
1"-AP-111-13516-A3A-TL8"
x6"
03
03
03
B49AA49A
B49AA1A
03
0303
03
03
03
03
03
03
10"x8"
03
03
B49AB1A
03
22
1-1/2
"x1/2"
1-1/2
"x1/2"
13510T
13504T
2"-CT-111-13535-B49A-NI
13501T
13507T
13505T
6
6
A3A-TLA49A-NI
2"-C
T -11
1-13
5 56-
A49A
- NI
2"-AP-111-13517-A3A-TL
13512T
1"-CT-111-13557-A49A-NI
2"x1"2"x1-1/2"
1"-AP-111-13518-A3A-TL
13503T
03
3/4"
8"-C
T-11
1-13
501-
B49A
-IS
PSET
=3.52
kg/cm
^2g
03
13508T
16
13514T
16
03
2"-AP-111-13519-A3A-TL
1-1/2"x1"
1-1/2"x1"
22
03
1/2"
1/2"
03
1-1/2"x3/4"
1-1/2"x3/4"
1-1/2"x3/4"
1-1/2"x3/4"
03
1/2"
1/2"
03
1-1/2"x3/4"
1-1/2"x3/4"
03
1-1/2"x3/4"
1-1/2"x3/4"
03
1"
1"
1-1/2"x3/4"
1-1/2"x3/4"
03
1-1/2"x3/4"
1-1/2"x3/4"
03
1-1/2"x3/4"
03
3/4"
3/4"
2"-C
T-11
1-13
558-
A49A
-NI
B49A-IS
3/4"3/4"
4"x3"
03
4"x3"
2"
03
03
3/4"
3/4"
1"03
3/4"
3/4"
03
2"x1"
03
3/4"
3/4"
1"03
13506T
6"-CT-111-13520-A49A-NI
03
AL
L R
IGH
TS
RE
SE
RV
ED
TH
IS D
OC
UM
EN
T A
ND
AN
Y D
AT
A A
ND
INF
OR
MA
TIO
N C
ON
TA
INE
D T
HE
RE
IN A
RE
CO
NF
IDE
NT
IAL
AN
D T
HE
PR
OP
ER
TY
OF
L&
T−C
HIY
OD
A L
IMIT
ED
(L
TC
) A
ND
TH
E C
OP
YR
IGH
T IS
TH
ER
EIN
VE
ST
ED
IN L
TC
. NO
PA
RT
OF
TH
IS D
OC
UM
EN
T, D
AT
A, O
R I
NF
OR
MA
TIO
N S
HA
LL
BE
DIS
CL
OS
ED
TO
OT
HE
RS
OR
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PR
OD
UC
ED
IN A
NY
MA
NN
ER
OR
US
ED
FO
R A
NY
PU
RP
OS
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OE
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R, E
XC
EP
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TH
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RIO
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RIT
TE
N P
ER
MIS
SIO
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F L
TC
.
A
1
SH.
REV.APP BY:
CHK BY:
DATE TITLE:
SIGN: DATE:
CODE 1 - NO COMMENTSPROCEED WITH MANUFACTURE / FABRICATION /CONSTRUCTION AS PER THE DOCUMENT
SIGN: DATE:NAME: DISCIPLINE:
DOCUMENT STATUS
STATEMENT OF SUB: 1st
FINAL FOR CODE -1
AS BUILT
CONSTRUCTION
ISSUED FOR
EIL REVIEW/APPROVAL CODE: VPTL NO:
SCH. DATE OF SUBMISSION
DRG. CATEGORY:(USE TICK MARK)
DWG. NO :
PC
PIPING AND INSTRUMENT DIAGRAM
DRN BY:
DEPT:
PROJECT:
PWO NO.:
DRG. NO.:
INFORMATION
REVIEW
AS BUILT
2nd 3rd
R I
CODE 2 - PROCEED WITHMANUFACTURE / FABRICATION / CONSTRUCTION AS PER THECOMMENTED DOCUMENT, REVISED DOCUMENT REQUIREDCODE 3 - DOCUMENT DOES NOTCONFORM TO BASIC REQUIREMENTS AS MARKED.RESUBMIT FOR REVIEW.
CODE R - DOCUMENT IS RETAINED FOR RECORDS.PROCEED WITH MANUFACTURE / FABRICATION
CODE V - VOID
2 3 4 5 6 7 8 9 10 11 12
1 2 3 4 5 6 7 8 9 10 11 12
B
C
D
E
F
G
H
A
B
C
D
E
F
G
H
ENGINEERS
(A Govt. of India Undertaking)
EPC / LSTKCONTRACTOR : L&T Hydrocarbon EngineeringPMC :
ई.आई.एलइंजीिनयस
इंिडया िलिमटेड का सरकार( भारत उप म )
INDIA LIMITED
HPCL RAJASTHAN REFINERY LIMITEDRAJASTHAN REFINERY PROJECT
PACHPADRA, BARMER, RAJASTHANEPCC 03 PACKAGE PETROCHEMICAL FLUDIZED CATALYTIC
CRACKING UNIT AND PROPYLENE RECOVERY UNIT
OWNER:
ENGINEERINGSUB-CONTRACTOR : L&T - CHIYODA LIMITED
PROJECT NUMBER REVISIONTECHNIPFMC NUMBER
PROCESS BY DRAWN BYCLIENT NUMBER
ENGINEERS
(A Govt. of India Undertaking)
ई.आई.एलइंजीिनयस
इंिडया िलिमटेड का सरकार( भारत उप म )
INDIA LIMITED
INFORMATION CONTAINED IN THIS DOCUMENT IS THE WORK PRODUCT OF ONE OR MORE LEGAL ENTITIESOF THE TECHNIPFMC PROCESS TECHNOLOGY BUSINESS UNIT AND EMBODIES CONFIDENTIAL AND
PROPRIETARY INFORMATION OF THE APPLICABLE ENTITY AND/OR ITS CLIENT.USE OF THIS INFORMATION IS RESTRICTED IN ACCORDANCE WITH CONDITIONS SPECIFIED BY THE CONTRACT.
TECHNIPFMC PROCESS TECHNOLOGY AND ITS AFFILIATES DISCLAIM ANY AND ALL LIABILITIES FOR ANYCHANGES OR MODIFICATIONS TO THIS DOCUMENT WHICH ARE MADE BY ANY PERSON OTHER THAN
THE ENTITY THAT ISSUED THE DOCUMENT UNDER THE APPLICABLE CLIENT CONTRACT.
REVISION DESCRIPTIONREV DATE CHECKED APPROVED PROJ APR
LICENSOR:
DESCRIPTIONREV DATE DRN CHECKED APPROVED
FCC
B224
SCALE
AL
L R
IGH
TS
RE
SE
RV
ED
TH
IS D
OC
UM
EN
T A
ND
AN
Y D
AT
A A
ND
INF
OR
MA
TIO
N C
ON
TA
INE
D T
HE
RE
IN A
RE
CO
NF
IDE
NT
IAL
AN
D T
HE
PR
OP
ER
TY
OF
L&
T−C
HIY
OD
A L
IMIT
ED
(L
TC
) A
ND
TH
E C
OP
YR
IGH
T IS
TH
ER
EIN
VE
ST
ED
IN L
TC
. NO
PA
RT
OF
TH
IS D
OC
UM
EN
T, D
AT
A, O
R I
NF
OR
MA
TIO
N S
HA
LL
BE
DIS
CL
OS
ED
TO
OT
HE
RS
OR
RE
PR
OD
UC
ED
IN A
NY
MA
NN
ER
OR
US
ED
FO
R A
NY
PU
RP
OS
E W
HA
TS
OE
VE
R, E
XC
EP
T W
ITH
TH
E P
RIO
R W
RIT
TE
N P
ER
MIS
SIO
N O
F L
TC
.
A
1
SH.
REV.APP BY:
CHK BY:
DATE TITLE:
SIGN: DATE:
CODE 1 - NO COMMENTSPROCEED WITH MANUFACTURE / FABRICATION /CONSTRUCTION AS PER THE DOCUMENT
SIGN: DATE:NAME: DISCIPLINE:
DOCUMENT STATUS
STATEMENT OF SUB: 1st
FINAL FOR CODE -1
AS BUILT
CONSTRUCTION
ISSUED FOR
EIL REVIEW/APPROVAL CODE: VPTL NO:
SCH. DATE OF SUBMISSION
DRG. CATEGORY:(USE TICK MARK)
DWG. NO :
PC
PIPING AND INSTRUMENT DIAGRAM
DRN BY:
DEPT:
PROJECT:
PWO NO.:
DRG. NO.:
INFORMATION
REVIEW
AS BUILT
2nd 3rd
R I
CODE 2 - PROCEED WITHMANUFACTURE / FABRICATION / CONSTRUCTION AS PER THECOMMENTED DOCUMENT, REVISED DOCUMENT REQUIREDCODE 3 - DOCUMENT DOES NOTCONFORM TO BASIC REQUIREMENTS AS MARKED.RESUBMIT FOR REVIEW.
CODE R - DOCUMENT IS RETAINED FOR RECORDS.PROCEED WITH MANUFACTURE / FABRICATION
CODE V - VOID
2 3 4 5 6 7 8 9 10 11 12
1 2 3 4 5 6 7 8 9 10 11 12
B
C
D
E
F
G
H
A
B
C
D
E
F
G
H
ENGINEERS
(A Govt. of India Undertaking)
EPC / LSTKCONTRACTOR : L&T Hydrocarbon EngineeringPMC :
ई.आई.एलइंजीिनयस
इंिडया िलिमटेड का सरकार( भारत उप म )
INDIA LIMITED
HPCL RAJASTHAN REFINERY LIMITEDRAJASTHAN REFINERY PROJECT
PACHPADRA, BARMER, RAJASTHANEPCC 03 PACKAGE PETROCHEMICAL FLUDIZED CATALYTIC
CRACKING UNIT AND PROPYLENE RECOVERY UNIT
OWNER:
ENGINEERINGSUB-CONTRACTOR : L&T - CHIYODA LIMITED
PROJECT NUMBER REVISIONTECHNIPFMC NUMBER
PROCESS BY DRAWN BYCLIENT NUMBER
ENGINEERS
(A Govt. of India Undertaking)
ई.आई.एलइंजीिनयस
इंिडया िलिमटेड का सरकार( भारत उप म )
INDIA LIMITED
INFORMATION CONTAINED IN THIS DOCUMENT IS THE WORK PRODUCT OF ONE OR MORE LEGAL ENTITIESOF THE TECHNIPFMC PROCESS TECHNOLOGY BUSINESS UNIT AND EMBODIES CONFIDENTIAL AND
PROPRIETARY INFORMATION OF THE APPLICABLE ENTITY AND/OR ITS CLIENT.USE OF THIS INFORMATION IS RESTRICTED IN ACCORDANCE WITH CONDITIONS SPECIFIED BY THE CONTRACT.
TECHNIPFMC PROCESS TECHNOLOGY AND ITS AFFILIATES DISCLAIM ANY AND ALL LIABILITIES FOR ANYCHANGES OR MODIFICATIONS TO THIS DOCUMENT WHICH ARE MADE BY ANY PERSON OTHER THAN
THE ENTITY THAT ISSUED THE DOCUMENT UNDER THE APPLICABLE CLIENT CONTRACT.
REVISION DESCRIPTIONREV DATE CHECKED APPROVED PROJ APR
LICENSOR:
DESCRIPTIONREV DATE DRN CHECKED APPROVED
FCC
B224
SCALE
1-1/2"x3/4"
SP13401
03
6
SP13401
03
03
03
SP13401
03
SP13401
03
1"
SP12401
1
03
SP13401
03
SP13401
03
SP13401
03
SP13401
1" 1"
SP12402
SP12402
03
03
503
AKPAKPAKPAKP
24 Sep 202103 Jul 2021
11 May 202110 Mar 2021
NKVKDDRZINCORPORATING HAZOP RECOMMENDATION03NKVKDDRZISSUED FOR HAZOP02NKVKDDRZISSUED FOR REVIEW01NKVKDDRZISSUED FOR REVIEW00
03 03 03
3/4"-S
V-11
1-13
518-
A1A-
NI3/4
"-SV-
111-
1351
9-A1
A-NI
SP13401
03
SP13402
03
6"-C
T-11
1-13
525-
A49A
-NI
23
03
2"-SV-111-13521-A1A-NI
23. AS PER EDB (DOC. NO.: EDB-B224-999-16-43-EDB-1001), CLAUSE NO. 3.2.10, POINT NO. 5, PIPE STEAMTRAP SHALL BE OF COMPACT TYPE (VENDOR FURNISHED).
03
FE13501
+
SS / CRWS
SS / CRWS
4. PRV ROUTING SHOULD NOT BE MORE THAN 1 m.
24. COP & CATALYST HOPPER CONNECTIONS SHOULD JOIN HEADER LINE AT 45° ANGLE. IN THE DIRECTIONOF FLOW.
03
2424
HOLD 4
MIN.
03
HOLD 4SS / CRWS
2"-SV-111-13520-A1A-NI
16 16
HOLD 4
SS / CRWS13513
T
13509T
HOLD 4
03
18
18
18
18
03A INTERNAL ISSUE 11 OCT 2021
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