Initial Start Up Procedure RevA
Short Description
initial start up procedure...
Description
PROCEDURE NO:
START UP, SHUT DOWN AND OPERATING MANUAL PETRA RESOURCES SDN BHD (172962-D)
PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
INTRODUCTION Contents Description
Page
1.0
INTRODUCTION
2
2.0
OBJECTIVE
3
3.0
DEFINITIONS
4
4.0
REFERENCES
4
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START UP, SHUT DOWN AND OPERATING MANUAL PETRA RESOURCES SDN BHD (172962-D)
PETRA RESOURCES SDN BHD (172962-D)
1.0
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
INTRODUCTION
This information contained in this manual is intended as an aid to the operation of EOR facilities installed in the following platform:
Sumandak Selatan Integrated Platform (SUPG-B) Samarang Oil Production Platform SMP-B Samarang Drilling Platform SMDP-B Samarang Jacket Platform SMJT-E
It is provided for the guidance and instruction of the platform operators and other personnel concerned with the design intent of the platform and thus will help to ensure the safety and the proper operation of the platform. Samarang Redevelopment Phase 2 EOR project will be undertaken to extend Samarang field life and is anticipated to increase recoverable reserves by as much as 78 mmstb from 17 mmstb to 95 mmstb within 2026. If implemented and executed as recommended, the field will achieve a state of zero continuous venting within 2015, and result in a remaining oil production rate of 6,000 bopd at 2026. Recovery factors from the field will increase from the pre-FDP forecast of 41%, to 51% in 2026. Phase 2 EOR Detail Design work for identified wells consists of infill, water and gas injection facilities (Gravity Assisted Simultaneous Water and Gas - GASWAG). The work involves platform upgrading at existing Sumandak platform SUPG-B, tie-in on existing Samarang platforms (SMP-B / SMDP-B and SMJT-E), and infill drilling on two existing drilling platforms SMDP-B and SMJT-E. Samarang will be utilizing Sumandak SUPG-B water injection (WI) facilities, with 2 new booster pumps installed in series with the existing water injection pumps to meet Samarang water injection pressure. Whereas, for the gas compression facility, there are originally 3 gas compressor trains installed on SUPG-B. However, compressor train A has been removed due to the reduction in export gas amount and SUPG-B is currently operating on 2X100% mode. A new 2 stages compressor train will be installed in place of the existing compressor, as the existing one has limited pressure to meet the required injection pressure in Samarang. A new 6” flexible pipeline (~13.5 km) is required to export the gas injection from SUPG-B to SMP-B. The gas will be further routed to SMDP-B via bridge link piping and the remaining gas will be routed to SMJT-E via new 4” flexible pipeline (~2.3 km). For water injection, a new 6” flexible pipeline (~13.5 km) will be installed from SUPG-B to SMP-B. And new 4” flexible pipeline (~2.3 km) will be installed to transfer water injection from SMP-B to SMJT-E. Safety Procedures and Operating Procedure bulletins issued by the Owner must be considered in conjunction with these guidelines and incorporated into actual procedures to be implemented. Of particular significance are: i.
Structure of the supervisory management in the operating organization and line of communication within.
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PETRA RESOURCES SDN BHD (172962-D)
PETRA RESOURCES SDN BHD (172962-D)
ii.
Experience of Owner’s operator.
iii.
Liaison between Owner’s during initial start-up.
iv.
Detailed operating guidelines for vendor package equipment.
operator and field representatives of equipment manufacturers
The manual is divided into six sections. Each section provides information such as system description, equipment design data, detailed operating sequences and instructions, and equipment / valve location tables, to facilitate proper and safe operation of the facilities. Relevant diagrams are also provided to enhance the understanding of instructions and the operation of Sumandak Selatan Integrated Platform (SUPG-B). Although the manual contains inherent safe operating practices, it is intended to supplement, but not replace, other relevant Carigali approved safety and operating procedures. This manual must be read in conjunction with other relevant Carigali approved safety and operating procedures, including, but not limited to, the following: 1. 2. 3. 4. 5. 6.
Carigali Operating Procedure Bulletins. SUPG-B Emergency Response Procedures Manual(s) and related documentation. Carigali’s approved Vendor/Manufacturer Operating Procedures. Carigali Operations key as-built Drawings (contained within the Blue Books). Carigali HSEMS Manual. Electrical Standing Instructions.
Where applicable, within the operation procedures included in Section 3 and Section 4, for more specific references refer to the Operating Procedure Bulletins and/or to Vendors' / Manufacturers' Operating Procedures. Units of measurement generally conform to the System International (SI) units, followed by the equivalent Imperial units in parentheses e.g. 10 m (32.91 ft).
2. 0 OBJECTIVE The objective of this document to define the scope of work required to re-instate the system and make it ready for Non Hydrocarbon (Water Injection System) and Hydrocarbon (Gas Injection System) introduction. The whole scope of work to be completed in 3 phases;
a) Reinstatement b) System start-up c) System performance monitoring
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PETRA RESOURCES SDN BHD (172962-D)
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DEFINITIONS
COMPANY
: PETRONAS CARIGALI SDN BHD (PCSB)
CONTRACTOR
: PETRA RESOURCES SDN BHD
VENDOR specified
: Party who supplies and manufactures equipment/ materials or services and ordered by CONTRACTOR
SUBCONTRACTOR ordered
: Party who providing subcontracting packages or services specified and by CONTRACTOR
4.0 REFERENCES: PSD-EOR-CO-013-REVB for Start Up, Shut Down and Operating Manual
Attachment List ATTACHMENT 1.0
: Flowchart for Water Injection Black Start
ATTACHMENT 1.1
: Prepare EOR Water Injection Facilities for Black Start-Up
ATTACHMENT 1.2
: USD System
ATTACHMENT 2.0
: Flowchart for Gas Injection Black Start
ATTACHMENT 2.1
: Prepare EOR Gas Injection Facilities for Black Start-Up
ATTACHMENT 2.2 kPag
: Pressurization of Sumandak and Samarang Gas Injection Facility to 7400
ATTACHMENT 2.3
: Start-Up Gas Turbine for Gas Injection Compressor
ATTACHMENT 2.4
: Shutdown of EOR Gas Compression
4
Formatted: Font: (Default) Arial, 10 pt
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PETRA RESOURCES SDN BHD (172962-D)
1.0
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Flowchart for Water Injection Black Start
THIS FLOWCHART IS FOR FIRST BLACK START UP ONLY, NOT DESIGNATED FOR POST ABANDON PLATFORM STARTUP.
Prior to introduction of Non Hydrocarbon, PASR and shall be conducted which include pre startup check in order to ensure Platform readiness for RFSU.
STEP NO.
1
2
3
4
PROCEDURE ACTIVITY
PROCEDURE INSTRUCTION
DRAWING REFERENCE
Power Supply from 6.6kV SG‐7510 (Existing)
09‐SUPG‐B‐E‐ 10001‐1
Vacuum Circuit Breaker (VCB 204)(Existing)
09‐SUPG‐B‐E‐ 10001‐1
Vacuum Circuit Unit (VCU‐214 & 220 spare), 1000KW VCU 214 and 1000KW VCU 220 (Existing) Ensure that all for DMC WI Mechanical (Off Skid + relevant skids) System and checksheets and records are complete and signoff Prepare PASR
09‐SUPG‐B‐E‐ 10001‐1
1.0
5
5
CHECK (/) ONCE TASK IS COMPLETED
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PETRA RESOURCES SDN BHD (172962-D)
REVISION NO: 0
HOOK-UP AND COMMISSIONING
Prepare and CEM Simulation Test
1.1
09‐SUPG‐B‐I‐ 10001‐01‐1
Prepare for SAT P‐4085A/B system 1.1
09‐SUPG‐B‐B‐ 10139‐1‐3
Prepare and Start P‐4085A/B
1.2
09‐SUPG‐B‐B‐ 10139‐1‐3
Prepare and USD Test
1.3
09‐SUPG‐B‐I‐ 10001‐01‐1
Prepare and Endurance Test Pump 1.2 A/B 2 x 72 hours
09‐SUPG‐B‐B‐ 10139‐1‐3
Prepare for Dumping at SMP‐B
1.2
09‐SMP‐B‐P‐0031‐1
Prepare for Dumping at SMJT‐E
1.2
09‐SMP‐E‐P‐0022‐ 1‐3
Stop P‐4085A/B Pump after endurance test
1.2
09‐SUPG‐B‐B‐ 10139‐1‐3
Prepare and restart P‐4085A/B
1.2
09‐SUPG‐B‐B‐ 10139‐1‐3
6
7
8
9
10
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11
12
13
14
15
Prepare for Scaling Inhibitor / Fine 1.2 Stabilizer Injection at SMJT‐E
09‐SMP‐E‐P‐0022‐ 1‐3
Prepare for Water Injection to Wellhead SMJT‐E (SM 74)
1.2
16
09‐SMP‐E‐P‐0001‐ 1‐3‐4
Prepare ESD Test (with GI system)
1.2
09‐SUPG‐B‐I‐ 10001‐01‐1
17
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18
Prepare for Scaling Inhibitor / Fine 1.2 Stabilizer Injection at SMDP‐B
09‐SMDP‐B‐P‐ 0014‐3‐WT
19
Prepare for Water Injection to Wellhead SMDP‐B (SM 50)
09‐SMDP‐B‐P‐ 0001‐3‐WT
1.1
1.2
Prepare EOR Water Injection Facilities for Black Start-Up
1.1.1 Prepare EOR Water Injection Facilities for Black Start‐Up STEP NO.
CHECK ONCE TASK IS COMPLETED
ACTION
1.
Confirm water injection pipeline from SUPG-B to SMP-B is ready for operation.
2.
Confirm water injection pipeline from SMP-B to SMJT-E is ready for operation.
3.
Confirm communication with Samarang via VSF radio/telephone.
4.
Confirm water injection facility at SMP-B, SMDP-B and SMJT-E ready to receive water injection export from SUPGB.
5.
Ensure that all water injection facility PSVs are online (inlet isolation valves car seal open)
6.
Check that check valve VCH-1111/1112 and restriction orifice RO-4086A/B on pump minimum recycle line are installed correctly.
7.
Ensure that all instrumentations are commissioned and online.
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
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8.
Ensure chemical injection system on SUPG-B has been filled with the related chemicals – clay stabilizer and scale inhibitor are ready for operation.
9.
Flush pipes between water injection pump (P-4080A/B/C) discharge line to water injection booster pump (P-4805A/B) suction to remove any construction debris prior to "black start-up" of water injection booster pump. Route the flushed water to overboard via water injection booster pump suction drain valve VBA-1187 / 1188 and VBA-1191 / 1192. Close the drain valves once flushing is completed.
10.
Flush water injection booster pump (P-4805A/B) discharge line to water injection export SDV to remove any construction debris prior to “black start-up” of water injection booster pump. Route the flushed water to overboard via water injection booster pump discharge drain valve VBA-1189 / 1190 and VBA-1193 / 1194. Close the drain valves once flushing is completed.
11.
Check water injection booster pump suction strainer to remove any construction debris prior to “black start-up” of water injection booster pump.
12.
13.
Set water injection booster pump discharge pressure controller PICA-4085 @ 21060 kPag by MCP. Place PICA4085 in MANUAL mode and check PCV-4085 is fully closed. Open bypass valves VBA-1004 & VGL-1001 for pressure equalization. Close VBA-1004 & VGL-1001 once the pressure reaches 21060 kPag.
Set water injection booster pump recycle flow controller FIC4087A/B @ 74 m³/hr in AUTO mode.
Apply start-up override for the following instrumentation trip: 14.
Water injection booster pump suction pressure low low PZALL-4085A/B (LL set @ 2260 kPag) Water injection booster pump discharge flow low low FZALL4087A/B (LL set @ 70 m3/h)
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PETRA RESOURCES SDN BHD (172962-D)
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The start-up override bypasses a process value to allow time for the value to reach a state that does not initiate a trip. The start-up override is cleared automatically when pressure/flow restored above low low set point.
15.
Ensure water injection pump P-4080A/B/C is running and water injection supply header at 8000 kPag (PICA-4081).
16.
Ensure SUPG-B water injection header pressure controller PIC-0908 is at 1200 psig (8274 kPag) in AUTO mode. This is to ensure stable suction pressure for water injection booster pump operation.
17.
Ensure SMP-B water injection dump valve HCV-4060 is 50% open prior to starting water injection booster pump at SUPGB. HCV-4060 to be regulated to desired pressure once water injection arrives at SMP-B. During this procedure, ensure VB-2111 and VB-2112 (guard filter inlet isolation valves) is in close position. This is for flushing pipeline purposes before introducing water injection into guard filter.
18.
Ensure SMDP-B water injection dump valve HCV-4089 is 50% open prior to introducing water injection at Riser Guard. HCV-4089 to be regulated to desired pressure once water injection arrives at SMDP-B. During this procedure, ensure DBB-3009 & DBB-3010 is in closed position.
19.
Ensure water quality at water injection supply header meets required water injection quality.
20.
Ensure all spectacle blinds and valves LC/LO/NC as per P&ID.
21.
Line up the valves as shown in the checklist below.
1.1.2 P‐4085A Valve Status Checklist (Water Injection Black Start‐up) Tag No.
Location/Description
Valve Position
9
Check
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PETRA RESOURCES SDN BHD (172962-D)
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Preparation
Operation
LO
LO
VBA-1001
Discharge header of existing water injection pump
VBA-1141
P-4085A suction isolation valve
Open
Open
XV-4085A
P-4085A suction ON/OFF valve
Open
Open
XV-4086A
P-4085A discharge ON/OFF valve
Open
Open
VBA-1002
P-4085A discharge isolation valve
Open
Open
VBA-1187 / 1188
P-4085A suction drain valves
Open
Close
VBA-1189 / 1190
P-4085A discharge drain valves
Open
Close
VBA-1142
P-4085B suction isolation valve
Close
Open
XV-4085B
P-4085B suction ON/OFF valve
Close
Close
XV-4086B
P-4085B discharge ON/OFF valve
Close
Close
VBA-1003
P-4085B discharge isolation valve
Close
Open
VBA-1191 / 1192
P-4085B suction drain valves
Close
Close
VBA-1193 / 1194
P-4085B discharge drain valves
Close
Close
VBA-1195 / 1196
PCV-4085 inlet isolation valves
Open
Open
VBA-1197 / 1198
PCV-4085 outlet isolation valves
Open
Open
VBA-1004 / VGL-1001
PCV-4085 bypass valves
Open
Close
P
O
1.1.3 P‐4085B Valve Status Checklist (Water Injection Black Start‐up) Valve Position Tag No.
Check
Location/Description Preparation
10
Operation
P
O
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
VBA-1001
Discharge header of existing water injection pump
VBA-1141
LO
LO
P-4085A suction isolation valve
Close
Open
XV-4085A
P-4085A suction ON/OFF valve
Close
Open
XV-4086A
P-4085A discharge ON/OFF valve
Close
Open
VBA-1002
P-4085A discharge isolation valve
Close
Open
VBA-1187 / 1188
P-4085A suction drain valves
Close
Close
VBA-1189 / 1190
P-4085A discharge drain valves
Close
Close
VBA-1142
P-4085B suction isolation valve
Open
Open
XV-4085B
P-4085B suction ON/OFF valve
Open
Close
XV-4086B
P-4085B discharge ON/OFF valve
Open
Close
VBA-1003
P-4085B discharge isolation valve
Open
Open
VBA-1191 / 1192
P-4085B suction drain valves
Open
Close
VBA-1193 / 1194
P-4085B discharge drain valves
Open
Close
VBA-1195 / 1196
PCV-4085 inlet isolation valves
Open
Open
VBA-1197 / 1198
PCV-4085 outlet isolation valves
Open
Open
VBA-1004 / VGL-1001
PCV-4085 bypass valves
Close
Close
Water Injection Launcher L‐4086 at SUPG‐B Valve Position Tag No. XV-4089 VBA-
Check
Location/Description Preparation
Operation
Launcher bypass XV
Open
Open
Water injection line valve to SMP-B
Open
Open
11
P
O
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START UP, SHUT DOWN AND OPERATING MANUAL PETRA RESOURCES SDN BHD (172962-D)
PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
1011 XV-4087 / 4088
Launcher outlet XV
Close
Close
VGL1014 / VBA1014
Launcher kicker line valves
Close
Close
VBA1008
Launcher balance line valve
Close
Close
VBA1005 / 1006 / 1007 / 1010
Launcher drain valves
Close
Close
VBA1015 / VGL1002
Launcher vent valves
Close
Close
Water Injection Receiver R‐4060 at SMP‐B Valve Position Tag No.
Check
Location/Description Preparation
Operation
VB-2025
Incoming water injection supply from SUPG-B
Open
Open
VB-2026 / 2027
Receiver inlet isolation valves
Close
Close
VB-2013 / 2061
Receiver outlet isolation valves
Close
Close
VB-2030
Receiver bypass valve
Open
Open
VB-2028 / VO2014
Receiver bypass pressure equalization valves
Close
Close
VB-2092
Receiver vent valves
Close
Close
12
P
O
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
/ VO2015 VB-2036 / VO2012
Receiver vent valves
Close
Close
VB-2031
Receiver balance line valve
Close
Close
VB-2037 / 2038 / 2039
Receiver drain valves
Close
Close
VB-2105 / 2106
PSV-4060A inlet isolation valves
LO
LO
VB-2107 / 2108
PSV-4060B inlet isolation valves
LC
LC
VB-2109 / 2110
Water injection header dump line isolation valves
Open (Note 1)
Open
VB-2084
Water injection header low point drain
Close
Close
Notes: 1. HCV-4060 (downstream of VB-2109/2110) is 50%-70% open before introduction into guard filter during commissioning or black start. Water Injection Guard Filter F‐4065 at SMP‐B Valve Position Tag No.
Check
Location/Description Preparation
Operation
Close (Note 1)
Open
VB-2111 / 2112
Filter inlet isolation valves
VB-2044
Filter bypass valve
Close
Close
VB-2113 / 2114
Filter outlet isolation valves
Open
Open
VB-2041 / 2042
Filter drain valves
Close
Close
VB-2115 / 2116
Water injection supply to SMDP-B isolation valves
Open
Open
13
P
O
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PETRA RESOURCES SDN BHD (172962-D)
VB-2117 / 2118
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Water injection supply to SMJT-E isolation valves
Open
Open
Notes: 1. To be open after complete water injection dumping. Estimated 1 hour of dumping duration before opening the valves (for reducing filter clogging due to debris and off spec water).
Water Injection Launcher L‐4070 at SMP‐B Valve Position Tag No.
Check
Location/Description Preparation
Operation
VB-2094
Water injection to SMJT-E
Open
Open
VB-2052
Launcher bypass valve
Open
Open
VB-2048 / 2049
Launcher outlet valves
Close
Close
VO2016 / VB-2066
Launcher kicker valves
Close
Close
VB-2047
Launcher balance valve
Close
Close
VB-2046 / 2050 / 2051
Launcher drain valves
Close
Close
VO2017 / VB-2093
Launcher vent valves
Close
Close
P
O
Water Injection Manifold / Flowline at SMDP‐B Valve Position Tag No.
Location/Description Preparation
14
Operation
Check P
O
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
DBB-3009
Water injection to injection well
Close (Note 1)
Open
DBB-3010
Water injection to injection well
Close (Note 1)
Open
VB-3015 / 3016
Water injection dump line isolation valves
Open (Note 2)
Open
Notes: 1. To be open once the water injection meets quality. 2. Set opening of HCV-4089 (downstream of VB-3015/3016) at 50%-70%.
Water Injection Wellhead SM‐50 at SMDP‐B Tag No.
Valve Position
Location/Description
Preparation
Operation
Surface safety valve
Close
Open
Surface controlled subsurface safety valve
Close
Open
Injection choke valve
Close
Open
-
Wing valve
Close
Open
-
Master valve
Close
Open
SSV5051 SCSSV5051 FCV5051
Check P
O
Water Injection Wellhead SM‐49 at SMDP‐B Valve Position Tag No. SSV4951 SCSSV4951
Location/Description Preparation
Operation
Surface safety valve
Close
Open
Surface controlled subsurface safety valve
Close
Open
15
Check P
O
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PETRA RESOURCES SDN BHD (172962-D)
FCV4951
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Injection choke valve
Close
Open
-
Wing valve
Close
Open
-
Master valve
Close
Open
Water Injection Receiver R‐4084 / Manifold at SMJT‐E Valve Position Tag No.
Preparation
Operation
Open
Open
VB-4019
Incoming water injection supply from SMP-B
VB-4046 / 4047
To water injection wellhead SM-48
Close (Note 1)
Open
Water injection header dump line DBB valves
Open (Note 2)
Open
DBB4026
Check
Location/Description
VB-4017 / 4018
Receiver inlet isolation valves
Close
Close
VB-4033 / VO4022
Receiver outlet isolation valves
Close
Close
VB-4020
Receiver bypass valve
Open
Open
VB-4027 / VO4026
Receiver vent valves
Close
Close
VB-4023
Receiver balance line valve
Close
Close
VB-4024 / 4028 / 4031
Receiver drain valves
Close
Close
Notes: 1. Only open when water injection quality met.
16
P
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
2. Set opening of HCV-4084 (downstream of DBB-4026) at 50%-70%. Reduce the opening once quality is met. Water Injection Wellhead SM‐74 at SMJT‐E Tag No.
Location/Description
SSV-7451 SCSSV7451 FCV-7451
Valve Position
Check
Preparati on
Operation
Surface safety valve
Close
Open
Surface controlled Subsurface safety valve
Close
Open
Injection choke valve
Close
Open
P
O
1.2 Black Start-Up EOR Water Injection Facilities STEP NO.
CHECK ONCE TASK IS COMPLETED
ACTION
1.
Prior to starting water injection booster pump P-4085A, ensure Sumandak Water Injection Facilities are prepared.
2.
Ensure communication between Samarang, are established.
3.
Perform line flushing at SMP-B, SMDP-B and SMJT-E.
4.
Start water injection booster pump P-4085A
5.
Check the water is recycling via pump minimum line via recycle pump flow control valve
6.
Ensure pump discharge flow is about 74 m³/hr via flow measurement at FIC-4087A to prevent pump damage
2
platforms,
7.
17
Sumandak
&
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Observe recycle water temperature via temperature measure at TIA4087A on pump recycle line. Temperature should not exceed 60°C. To reduce the temperature, consider gradually open PCV-4085 bypass valves VBA-1004 & VGL-1001. Close the valves once the temperature is manageable.
8.
Check pressure differential across pump suction strainer via PDA4085A.
9.
Once pump discharge flow is stabilized at about 74 m³/hr, open PCV4085 gradually by 5 – 10% opening.
10.
Set water injection booster pump discharge pressure controller PICA4085 in AUTO mode once FCV-4087A is fully closed.
11.
12.
Remove all inhibited trips once the water injection booster pump discharge pressure and flow has stabilized. Start injecting clay stabilizer and scale inhibitor into SUPG-B water injection export header
Monitor pressure at the following location: Water injection booster pump discharge pressure at 21060 kPag (PICA-4085) Water injection export header to SMP-B at SUPG-B (PIA-4092) 13.
Water injection incoming header from SUPG-B at SMP-B (PI-4060) Differential pressure at SMP-B water injection guard filter F-4065 Water injection export header to SMJT-E at SMP-B (PI-4070) Water injection supply header at SMDP-B (PI-4090) Water injection incoming header from SMP-B at SMJT-E (PI-4086)
14.
15
Prior to injecting to wellhead, perform the SLOPE Test. NOTE: Ensure the water injection guard filter is online before performing the SLOPE Test.
Once required pressure at water injection manifold at SMP-B and
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
SMJT-E is achieved, water injection to individual wellhead can proceed.
Water injection to individual wellhead shall be done one wellhead at a time and follows the following sequence: a) Open well SCSSV, manual master valve, manual wing valve and followed by SSV from WHCP unit. b) Manually open injection choke valve at minimum opening and gradually increase as per requirement to introduce water injection into the well.
16.
1.3 Start-Up EOR Water Injection Facilities following USD/PSD/ESD STEP NO.
ACTION
1.
Start-up after USD/PSD/ESD requires operator attendance at the platform
2.
Reason for USD/PSD/ESD has been identified and any correction implemented and conditions cleared.
3.
Ensure all wellhead water injection choke valves and water injection dump valves are closed and confirm pressure in water injection header.
4.
Water injection dump valves shall be open 50% to prevent water hammering during start-up of water injection booster pump and shall be gradually reduce once water injection quality is met.
5.
Confirm pressure in water injection header.
19
CHECK ONCE TASK IS COMPLETED
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Apply start-up override for the following instrumentation trip: Water injection booster pump suction pressure low low PZALL-4085A/B 6.
Water injection booster pump discharge flow low low FZALL-4087A/B The start-up override bypasses a process value to allow time for the value to reach a state that does not initiate a trip. The start-up override is cleared automatically when pressure/flow restored above low low set point.
7.
Follow steps mentioned in section 1.2
1.4 Shutdown EOR Water Injection Facilities CHECK ONCE TASK IS COMPLETED
STEP NO.
ACTION
1.
Monitor pressure at water injection supply header. Open water injection dump valve as necessary to divert the flow overboard.
2.
Slowly reduce water injection supply flow by means of gradually closing wellhead water injection choke valve one by one.
3.
Once all wellhead water injection choke valves are closed, place water injection booster pump discharge pressure controller PICA-4085 in MANUAL mode. Close PCV-4085 gradually by 5% to 10%. By closing of PCV4085 gradually, the water injection flow will be diverted to pump suction via minimum pump recycle line through FCV-4087A.
4.
Close well SSV followed by SCSSV from WHCP unit.
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
5.
Stop the clay stabilizer and scale inhibitor injection into water injection export header at SUPG-B.
6.
Monitor water injection booster pump discharge flow via FIC-4087A
7.
Stop the water injection booster pump P-4085A once PCV-4085 is fully closed.
1.5 Instrument Set Points Water Injection Booster Pump at SUPG‐B Tag No.
Location/Description
Set Point
PZALL-4085A
P-4085A suction pressure low low
2260 kPag
PIAL-4086A
P-4085A suction pressure low
3765 kPag
PIAH-4087A
P-4085A discharge pressure high
22180 kPag
FZALL-4087A
P-4085A discharge flow low low
70 m3/h
FICL-4087A
P-4085A discharge flow low
74 m3/h
TIAH-4087A
P-4085A discharge temperature high
PZALL-4085B
P-4085B suction pressure low low
2260 kPag
PIAL-4086B
P-4085B suction pressure low
3765 kPag
PIAH-4087B
P-4085B discharge pressure high
22180 kPag
FZALL-4087B
P-4085B discharge flow low low
70 m3/h
FICL-4087B
P-4085B discharge flow low
74 m3/h
21
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
TIAH-4087B
P-4085B discharge temperature high
60°C
PICAH-4085
Water Injection Booster Pump discharge header pressure high
22000 kPag
PICAL-4085
Water Injection Booster Pump discharge header pressure low
10450 kPag
Water Injection Launcher at SUPG‐B Tag No.
Location/Description
Set Point
PIAH-4092
Water injection to SMP-B pressure high
22000 kPag
PIAL-4092
Water injection to SMP-B pressure low
10450 kPag
Water Injection Receiver at SMP‐B Tag No. PSV-4060 A/B
Location/Description Water injection to Water Injection Guard Filter pressure safety valves
Set Point 208 barg
Water Injection Guard Filter at SMP‐B Tag No.
Location/Description
Set Point
PSV-4065
Water Injection Guard Filter pressure safety valve
208 barg
PSV-4066
Water injection line to SMDP-B
208 barg
Water Injection Wellheads at SMDP‐B Tag No.
Location/Description
Set Point
PEL-5053
Water injection flowline to wellhead
115.8 barg
PEL-4953
Water injection flowline to wellhead
115.8 barg
Water Injection Wellhead at SMJT‐E
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PETRA RESOURCES SDN BHD (172962-D)
Tag No. PEL-7453
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Location/Description Water injection flowline to wellhead
Set Point 115.8
barg
1.6 SMP-B/SMDP-B The gas from SUPG-B to SMP-B will be further routed to SMDP-B via bridge link piping and injected into two new GI wellheads. Automatic flow control is provided at each gas injection wells. Flow meter will be provided on the common line prior to SMP-B bridge linked to SMDP-B and gas injection export line to SMJT-E, to monitor total gas injection rate. Flow meter is also provided on the line to individual wells. The EOR gas injection facilities at SMP-B consist of: Gas Injection Receiver (R-2940) Item
Specification
Design Pressure
28000 kPag (4060 psig)
Design Temperature
100°C (max) / -20 ºC (min) Diameter: 200 mm / 150 mm
Size (Major Barrel/Minor Barrel)
Length: 1860 mm / 2420 mm
Gas Injection Launcher (L-2950) 1
Item
3
Design Pressure
5
Design Temperature
7
Size (Major Barrel/Minor Barrel)
2 4 6
Specification
28000 kPag (4060 psig) 65 °C (max) / -20 ºC (min)
8
Diameter: 150 mm / 100 mm
9
Length: 1830 mm / 1000 mm
1.6.1 SMJT-E The remaining gas injection from SMP-B will be routed to SMJT-E. New 4” flexible GI pipeline will be installed to transfer injection gas from SMP-B to SMJT-E. Automatic flow control is provided at each gas injection wells.
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
There is no additional equipment installed in SMJT-E for gas injection.The EOR gas injection facilities at SMJT-E consist of: Gas Injection Receiver (R-2910) 10 Item 12 Design Pressure 14 Design Temperature 16 Size (Major Barrel/Minor Barrel)
11 Specification 13 28000 kPag (4060 psig) 15 65 °C (max) / -20 ºC (min) 17 Diameter: 150 mm / 100 mm 18 Length: 2040 mm / 1690 mm
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PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Formatted: Font: Bold
2.0 Flowchart for Gas Injection Black Start
Formatted: Font: (Default) Arial, Bold
THIS FLOWCHART IS FOR FIRST BLACK START UP ONLY, NOT DESIGNATED FOR POST ABANDON PLATFORM STARTUP.
Prior to introduction of Hydrocarbon, PIR-04/PASR and shall be conducted which include pre startup check in order to ensure Platform readiness for RFSU.
STEP NO
1
2
3
PROCEDURE ACTIVITY
PROCEDURE INSTRUCTION
DRAWING REFERENCE
Power Supply from 400V SG SB‐ 7710(Existing)
09‐SUPG‐B‐E‐4012‐1
Air Circuit Breaker (ACB 311)(Existing)
09‐SUPG‐B‐E‐4012‐1
Vacuum Circuit Unit (VCU‐214 & 220 spare), 1000KW VCU 214 and 1000KW VCU 220 (Existing) MCC‐7810 (Existing) 184KW
09‐SUPG‐B‐E‐4012‐1
09‐SUPG‐B‐E‐4012‐1
230V AC UPS DB 7814B (Existing)
09‐SUPG‐B‐E‐4012‐1
IRP 7810 (Existing)
09‐SUPG‐B‐E‐4012‐1
4
5
6
25
CHECK (/) ONCE TASK IS COMPLETED
Formatted: Font: (Default) Arial, Bold Formatted: Font: (Default) Arial, Bold
PROCEDURE NO:
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Ensure that all for RFC GI Mechanical (Off Skid + relevant skids) System and checksheets and records are complete and signoff Prepare PIR‐04
2.0
Prepare PASR
Prepare for CEM Simulation Test
2.0
Prepare for RFSU
Prepare and Pressurization Pipeline from SUPG‐B to SMJT‐E at 72 Barg (System Test)
2.1
09‐SUPG‐B‐B‐10119‐ 1‐3
Prepare for GTC Start Up
2.2
09‐SUPG‐B‐B‐10119‐ 1‐3
Prepare and GTC pressurize 117 Barg to SMJT‐E (System Test)
2.2
14
09‐SUPG‐B‐B‐10120‐ 1‐3
2.2
15
Start GTC Ramp Up Pressure to 234 Barg
09‐SUPG‐B‐B‐10120‐ 1‐3
Prepare for ESD Test
2.4
09‐SUPG‐B‐I‐10001‐ 01‐1
Prepare and Restart Up GTC and Injection to SMJT‐E SM 121 (72 Hours)
2.3
09‐SMJT‐E‐P‐0019‐1‐ 1
7
8
9 09‐SUPG‐B‐I‐10001‐ 01‐1
10
11
12
13
16
17
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REVISION NO: 0
HOOK-UP AND COMMISSIONING
PETRA RESOURCES SDN BHD (172962-D)
PETRA RESOURCES SDN BHD (172962-D)
18
PSP-CS-SMJT-G-002
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
Prepare for Gas Injection into SM 37 & SM 47 at SMDP‐b
2.3
09‐SMDP‐B‐P‐0009‐ 1‐3‐WT
Formatted: Font: Bold
2.1 Prepare EOR Gas Injection Facilities for Black
Formatted: Font: (Default) Arial, Bold
STEP NO.
CHECK ONCE TASK IS COMPLETED
ACTION
1.
Confirm gas injection pipeline to SMP-B is ready for operation
2.
Confirm gas injection facility at SMP-B, SMDP-B and SMJT-E ready to receive gas injection export from SUPG-B
3.
Confirm communication with Samarang via VSF radio/telephone
Check the following utility is ready for operation: 4.
Fuel Gas @ 1860-3450 kPag Instrument Air @ HOLD kPag Power supply
5.
Ensure that all gas injection facility PSVs are online (inlet isolation valves car seal open)
6.
Ensure all check valves and restriction orifices are installed correctly
7.
Ensure that all instrumentations are commissioned and online
27
Formatted: Font: (Default) Arial, Bold Formatted: Font: (Default) Arial, Bold Formatted: Font: Bold
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PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
8.
Ensure gas injection facility piping at SUPG-B, SMP-B, SMDP-B and SMJT-E is already purged and ready prior to hydrocarbon entry. The piping shall be purged and pressurized to 690 kPag with nitrogen.
9.
Ensure gas injection compressor package pre start-up checklist and action item required as stated in Vendor Manual (see vendor doc TPIM 1010) has been completed and complied with.
10.
Verify gas injection compressor casings have been drained.
11.
Set gas injection compressor backpressure controller PICA-2430 @ 23000 kPag and place it in MANUAL mode. Set the controller output to ensure PCV-2430 is fully open.
12.
Set 1st stage compressor suction scrubber level controller LICA2415 on gap control (LCV open @ 650 mm and LCV close @ 400 mm). Place the controller in AUTO mode.
13.
Set 2nd stage compressor suction scrubber level controller LICA2416 on gap control (LCV open @ 650 mm and LCV close @ 400 mm). Place the controller in AUTO mode.
14.
Close all gas injection choke valves via SMQ-A
Apply start-up override for the following instrumentation trip:
15.
1st stage GI compressor scrubber liquid level low low LZALL-2415 1st stage GI compressor suction pressure low low PZALL-2426 1st stage GI compressor suction flow low low FZALL-2425 1st stage GI compressor discharge pressure low low PZAHH-2425 2nd stage GI compressor scrubber liquid level low low LZALL-2416 2nd stage GI compressor suction pressure low low PZALL-2446
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PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
2nd stage GI compressor suction flow low low FZALL-2445 2nd stage GI compressor discharge pressure low low PZAHH-2445 SUPG-B gas injection export header pressure low low PZALL2932A/B/C SMP-B gas injection incoming header pressure low PEL-2940 SMP-B gas injection export header pressure low PEL-2950 SMJT-E gas injection incoming header pressure low PEL-2910 The start-up override bypasses a process value to allow time for the value to reach a state that does not initiate a trip. The start-up override is cleared automatically when pressure/flow restored above low low set point. 16.
Line up the valves as shown in the checklist below.
Gas Injection Preparation Valve Status Checklist
Formatted: Font: (Default) Arial, 11 pt, Bold, English (Malaysia)
Downstream of Gas/Glycol Heat Exchanger at SUPG-B
Formatted: Font: (Default) Arial, 11 pt, Bold, English (Malaysia)
Valve Position Tag No.
Check
Location/Description Prepare
Operation
VDBB1032
Gas supply tie-in DBB
LO
LO
VDBB1033
PSV-2230B inlet DBB
LC
LC
VDBB1034
PSV-2230A inlet DBB
LO
LO
VBA1019
PSV-2230B outlet valve
LO
LO
VBA1017
PSV-2230A outlet valve
LO
LO
P
O
1st Stage Gas Injection Compressor Suction Scrubber V-2415 at SUPG-B Tag No.
Location/Description
Valve Position
29
Check
PROCEDURE NO:
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Prepare
Operation
VBA1059
Suction scrubber inlet isolation valve
Open
Open
SDV2415
Suction scrubber inlet SDV
Close
Open
SDV2416
Suction scrubber inlet bypass SDV
Close
Close
VBA1175 / 1176
PSV-2415A inlet isolation valves
LO
LO
VBA1177 / 1178
PSV-2415B inlet isolation valves
LC
LC
VBA1077
PSV-2415A outlet isolation valve
LO
LO
VBA1145
PSV-2415B outlet isolation valve
LO
LO
VBA1079
Suction scrubber vent valve
LC
LC
VGL1008
Suction scrubber vent valve
NC
NC
VBA1068 / 1069
Suction scrubber drain valves
NC
NC
VBA1070
Suction scrubber instrument drain valve
NC
NC
SDV2417
Suction scrubber outlet SDV
Close
Open
VBA1071 / 1126
LCV-2415 inlet isolation valves
Open
Open
VBA1127 / 1122
LCV-2415 outlet isolation valves
Open
Open
30
P
O
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Valve Position Tag No. VBA1124 / VGL1015
Check
Location/Description Prepare
Operation
NC
NC
LCV-2415 bypass valves
P
O
1st Stage Gas Injection Compressor K-2425 & After Cooler E-2435 at SUPG-B Valve Position Tag No.
XV-2426
Check
Location/Description Preparation
Operation
Open
Close
Hot gas compressor bypass valve
VDBB-1090
PSV-2425A inlet DBB
LO
LO
VDBB-1091
PSV-2425B inlet DBB
LC
LC
VBA-1084
PSV-2425A outlet isolation valve
LO
LO
VBA-1087
PSV-2425B outlet isolation valve
LO
LO
VBA-1083
Compressor vent valve
LC
LC
VGL-1009
Compressor vent valve
NC
NC
VBA-1081 / 1082
After cooler drain valves
NC
NC
XV-2427
Cold gas compressor bypass valve (HOLD)
Open
P
O
Close
2nd Stage Gas Injection Compressor Suction Scrubber V-2416 at SUPG-B Tag No.
Location/Description
Valve Position
31
Check
PROCEDURE NO:
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Preparation
Operation
VBA-1183 / 1184
PSV-2416A inlet isolation valves
LO
LO
VBA-1185 / 1186
PSV-2416B inlet isolation valves
LC
LC
VBA-1037
PSV-2416A outlet isolation valve
LO
LO
VBA-1035
PSV-2416B outlet isolation valve
LO
LO
VBA-1104
Suction scrubber vent valve
LC
LC
VGL-1010
Suction scrubber vent valve
NC
NC
Suction scrubber drain valves
NC
NC
VBA-1043
Suction scrubber instrument drain valve
NC
NC
SDV-2420
Suction scrubber liquid outlet SDV
Close
Open
VBA-1040 / 1128
LCV-2416 inlet isolation valves
Open
Open
VBA-1129 / 1150
LCV-2416 outlet isolation valves
Open
Open
VBA-1125 / VGL1016
LCV-2416 bypass valves
NC
NC
VBA-1041 / 1042
P
O
2nd Stage Gas Injection Compressor K-2426 & After Cooler E-2436 at SUPG-B Valve Position Tag No.
XV-2445
Check
Location/Description Hot gas compressor bypass valve
Preparation
Operation
Open
Close
VDBB-1050
PSV-2426A inlet DBB
LO
LO
VDBB-1051
PSV-2426B inlet DBB
LO
LO
VDBB-1099
PSV-2426C inlet DBB
LC
LC
32
P
O
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
VBA-1051
PSV-2426A outlet isolation valve
LO
LO
VBA-1053
PSV-2426B outlet isolation valve
LO
LO
VBA-1144
PSV-2426C outlet isolation valve
LO
LO
VBA-1110
Compressor vent valve
LC
LC
VGL-1011
Compressor vent valve
NC
NC
VBA-1057 / 1056
After cooler drain valves
NC
NC
XV-2446
Cold gas compressor bypass valve (HOLD)
Open
Close
Gas Injection Compression Discharge Header at SUPG-B Valve Position Tag No.
Preparation
Operation Open
SDV-2435
Compressor discharge header SDV
Close
VBA1155/1203SDV2436
Pipeline pressurisation manual valvesCompressor discharge header bypass SDV
Open
Manual blowdown XV to LP flare
Close
Close
LO
LO
loseOpen
Close
XV-2428VBA1202
Check
Location/Description P
Close
VBA-1136
XV-2428 VBA-1202 outlet isolation valve
BDV-2427
Compression discharge header BDV
VBA-1094
BDV-2428 outlet isolation valve
LO
LO
VBA-1090
Compression discharge header isolation valve
Open
Open
Gas Injection Launcher L-2930 and Compressor Seal Gas Supply at SUPG-B Tag No.
Location/Description
Valve Position
33
Check
O
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Preparation
Operation
Launcher bypass XV
Open
Open
Gas injection line SDV to SMP-B
Open
Open
Launcher outlet XV
Close
Close
VGL1094 / VBA1074
Launcher kicker line valves
Close
Close
VBA1033
Launcher balance line valve
Close
Close
VBA1020 / 1095 / 1034 / 1096 / 1032
Launcher drain valves
Close
Close
VBA1027 / 1098 / 1026
Launcher purging line valves
Close
Close
VBA1021 / 1022
Launcher manual depressurization line valves
Close
Close
BDV2931
Gas injection export header BDV
Close
Close
VBA1030
BDV-2931 outlet isolation valve
LO
LO
VBA1102
BDV-2931 outlet line bleed valve
NC
NC
SDV2932
Gas supply to gas injection turbine compressor seal gas system
Open
Open
VBA-
PCV-2937 inlet isolation valves
Open
Open
XV-2932 SDV2930 XV-2930 / 2931
34
P
O
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
1123 / 1153 VBA1092 / 1155
PCV-2937 outlet isolation valves
Open
Open
VBA1181 / 1182
PSV-2930A inlet isolation valves
LO
LO
VBA1151
PSV-2930A outlet isolation valve
LO
LO
VBA1179 / VBA1181
PSV-2930B inlet isolation valves
LC
LC
VBA1152
PSV-2930B outlet isolation valve
LO
LO
VBA1029 / 1149
Gas injection export pipeline blowdown
Close
Close
Gas Injection Compressor Turbine at SUPG-B Valve Position Tag No.
Preparation
Operation
Compressor turbine utility air supply valve
Open
Open
VBA-1205 / 1206
Compressor turbine instrument air supply valve
Open
Open
VB-24204A
Compressor turbine potable water supply valve
Open
Open
VBA-1210
Engine air inlet duct drain valve
Open
Open
VBA-1207
Lube oil tank drain valve
NC
NC
VBA-1208
Lube oil filter drain-unfiltered valve
NC
NC
VBA-1120
Check
Location/Description
35
P
O
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
VBA-1121
Drip pan oil drain valve
NC
NC
VBA-1209
Engine exhaust collector and combustor drain valve
NC
NC
VBA-1174
Seal gas filter drain valve
Close
Close
LC
LC
Open
Open
VB-59305 / VBA1204
Compressor turbine N2 supply
VBA-1212
TC fuel gas filter inlet
VBA-1211
TC fuel gas filter inlet drain line
NC
NC
VBA-1213
TC fuel gas filter drain point
NC
NC
VBA-1214
TC fuel gas filter depressurisation line
LO
LO
VBA-1216
Potable water supply to high pressure water mist skid
Open
Open
Gas Injection Receiver at SMP-B Valve Position Tag No.
Location/Description Preparation
Operation
ABV-2940
Incoming gas injection supply from SUPG-B
Open
Open
VB-2001 / 2002
Receiver inlet isolation valves
Close
Close
Receiver outlet isolation valves
Close
Close
VB-2007
Receiver bypass valve
Open
Open
VB-2005 / VO-2009
Receiver bypass pressure equalization valves
Close
Close
VB-2009 / 2008
Receiver vent valves
Close
Close
VB-2004
Receiver balance line valve
Close
Close
VBO-2010 / VB-2087
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Check P
O
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PETRA RESOURCES SDN BHD (172962-D)
VB-2101 / 2102
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Receiver purging line valves
Close
Close
Receiver drain valves
Close
Close
VB-2100 / 2099
Future pipeline pressurization line isolation valves
Close
Close
VB-2085
VCH-2001 bypass valve
Close
Close
Gas injection incoming header BDV
Close
Close
LO
LO
VB-2003 / 2010 / 2011
BDV-2941 VB-2012
BDV-2941 outlet isolation valve
DBB-2004
Gas injection to launcher L-2950 DBB valves
Open
Open
DBB-2005
Gas injection to SMDP-B gas injection manifold DBB valves
Open
Open
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Gas Injection Launcher at SMP-B Valve Position Tag No.
Location/Description Preparation
Operation
VB-2091
VC-2002 bypass valve
Close
Close
VB-2014
Launcher bypass valve
Open
Open
VB-2020 / 2021
Launcher outlet isolation valves
Close
Close
VB-2024 / 2023
Header vent valves
Close
Close
Open (Note 1)
Open
ABV2950
Gas injection supply to SMJT-E
Check P
O
Notes: 1. Ensure valve is open after ABV-2910 at SMJT-E is fully open during preparation line up.
Gas Injection Manifold at SMDP-B Valve Position Tag No.
Location/Description Preparation
Operation
ABV-2942
Gas injection supply from SMP-B
Open
Open
DBB-3021
Flowline connection for SM-47
Open
Open
DBB-3022
Flowline connection for SM-61
Open
Open
VB-3007 / 3008
Gas injection manifold drain valves
Close
Close
Gas Injection Flowline Wellhead SM-61 at SMDP-B
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Check P
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PETRA RESOURCES SDN BHD (172962-D)
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Valve Position Tag No.
Location/Description Preparation
Operation
VB-3003 / 3004
Flowline vent valves
Close
Close
SSV-6151
Surface safety valve
Close
Open
Surface controlled subsurface safety valve
Close
Open
SCSSV6151
Check P
O
Gas Injection Flowline Wellhead SM-47 at SMDP-B Tag No. VB-3005 / 3006 SSV-4751 SCSSV4751
Valve Position
Location/Description
Preparation
Operation
Flowline vent valves
Close
Close
Surface safety valve
Close
Open
Surface controlled subsurface safety valve
Close
Open
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Check P
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Gas Injection Receiver at SMJT-E Tag No.
Valve Position
Location/Description
Preparation
Operation
ABV-2910
Gas injection supply from SMP-B
Open
Open
VB-4001 / 4002
Receiver inlet isolation valves
Close
Close
VB-4042 / 4043
Future pipeline pressurization line isolation valves
Close
Close
VB-4003
Receiver bypass valve
Open
Open
VB- 4029
Header vent valves
Close
Close
Check P
O
Gas Injection Manifold at SMJT-E (Error! Reference source not found.33) Tag No. VB-4044 / 4045 VB-4013 / 4014
Valve Position
Location/Description
Prepare
Operation
Flowline connection for SM-7448
Open
Open
Gas injection manifold drain valves
Close
Close
Check P
O
Gas Injection Manifold Wellhead at SMJT-E Tag No.
Valve Position
Location/Description
Prepare
Operation
VB-40438 / 40439
Flowline vent valves
Close
Close
SSV121104851
Surface safety valve
Close
Open
SCSSV121104851
Surface controlled subsurface safety valve
Close
Open
40
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PETRA RESOURCES SDN BHD (172962-D)
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
2.2 Pressurization of Sumandak and Samarang Gas Injection Facility to 7400 kPag CHECK ONCE TASK IS COMPLETED
STEP NO.
ACTION
1.
Line up the following valves at respective platform for pipeline pressurization: (The table focuses on the valves involved in pressurization.)
Downstream of Glycol Heat Exchanger E‐2230 (SUPG‐B) Valve Position Tag No.
Location/Description
VDBB1032
Gas supply tie-in DBB
VDBB1033
PSV-2230B inlet DBB
VDBB1034
PSV-2230A inlet DBB
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Pressurization
Operation
LO
LO
LC
LC
LO
LO
Formatted: Font: (Default) Arial, Bold Formatted: Font: Bold, English (Malaysia)
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
VBA-1017
PSV-2230A outlet valve
LO
LO
VBA-1019
PSV-2230B outlet valve
LO
LO
1st stage Gas Injection Compressor Suction Scrubber V‐2415 (SUPG‐B) Valve Position Tag No.
Location/Description Pressurization
Operation
VBA-1059
Suction scrubber inlet isolation valve
Close
Open
VBA-1155
Pressurization bypass line isolation valve
Open
LC
Gas Injection Compression Discharge Header (SUPG‐B) Valve Position Tag No.
Location/Description Pressurization
Operation
VBA-1203
Pressurization bypass line isolation valve
Open
LC
VBA-1090
Compression discharge header isolation valve
Open
Open
Gas Injection Launcher (SUPG‐B) Valve Position Tag No.
Location/Description Pressurization
Operation
PCV-2430
Launcher pressure control valve
Open
Open
VCH-1003
Launcher check valve
Open
Open
XV-2932
Launcher bypass
Open
Open
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PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
SDV-2930
Gas injection line SDV to SMP-B
Open
Open
BDV-2931
Gas injection export header BDV
Open
Open
VBA-1030
BDV-2931 outlet isolation valve
LO
LO
Gas Injection Receiver (SMP‐B) Valve Position Tag No.
Location/Description Pressurization
Operation
ABV-2940
Incoming gas injection supply from SUPG-B
Open
Open
VB-2005/VO2009
Receiver bypass pressure equalization valves
Open
Close
VCH-2001
Receiver check valve
Open
Open
BDV-2941
Gas injection receiver BDV
Close
Close
DBB-2004
Gas injection to launcher L-2950
Open
Open
DBB-2005
Gas injection to SMDP-B injection manifold via bridge
Open
Open
Gas Injection Export (SMP‐B) Valve Position Tag No.
Location/Description Pressurization
Operation
VC-2002
Export check valve
Open
Open
VB-2014
Launcher bypass valve
Open
Open
VB-2024/23
Header vent valves
Close
Close
ABV-2950
Gas injection supply to SMJT-E
Open
Open
Gas Injection Manifold (SMDP‐B) Tag No.
Location/Description
Valve Position
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PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING Pressurization
Operation
ABV-2942
Gas injection supply from SMP-B
Open
Open
DBB-3021
Connection to SM-47
Close
Open
DBB-3022
Connection to SM-61
Close
Open
VB-3007/08
Manifold drain valves
Close
Close
Gas Injection Receiver (SMJT‐E) Valve Position Tag No.
Location/Description Pressurization
Operation
ABV-2910
Gas injection supply from SMP-B
Open
Open
VB-4001/02
Receiver inlet isolation valves
Close
Close
VB-4050/51
Future pipeline pressurization line isolation valves
Close
Close
Gas Injection Manifold (SMJT‐E) Valve Position Tag No.
Location/Description Pressurization
Operation
VB-4044/45
Connection to SM-74
Close
Open
VB-4013/14
Manifold drain valves
Close
Close
(Continue from step no.1) STEP NO.
2.
CHECK ONCE TASK IS COMPLETED
ACTION
Pressurize the pipeline in 4 stages (each stage accounts for 25% of 7400 kPag): 1850, 3700, 5550, and 7400 kPag. Control the inlet pressure using PCV-2430 in MANUAL mode by setting the control valve to the pressure at each stage. Close VBA-1155 and 1203 to isolate the bypass line at each stage.
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3.
The expected pressure profile is shown in the figure below. A certain time should be reserved for stabilization of pressure and leakage detection upon completion of pressurizing at each stage. Dedicated personnel will be assigned to perform testing (to detect leakage) and remediation at the main valves during pressurization.
4.
Be reminded that the pressure is taken from design value, at discharge of 2nd stage GI compressor. Value may vary during actual pressurization.
5.
Close VBA-1155 and VBA-1203 (LC) when the pressure in the pipeline reaches 74 barg (or the current export pressure). This is to prevent backflow during compressor startup and cause Glycol Contactor C-2220 to overpressure.
6.
Open 1st stage compressor suction scrubber inlet bypass SDV-2416 to start pressurization of gas injection facility to 7400 kPag
7.
Once the pressure is reaches 7400 kPag, place gas injection compressor
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HOOK-UP AND COMMISSIONING
backpressure controller PICA-2430 in AUTO mode (set point: i. 117.0 barg and ii. 234.4 barg). Due to control action, the pressure control valve PCV-2430 will close.
Start cooler fan for 1st stage gas injection compressor after cooler E-2435 and 2nd stage gas injection compressor after cooler E-2436
8.
Line up the following valves for operation prior to compressor start-up: •1st Stage Gas Injection Compressor Suction Scrubber Inlet SDV-2415 •1st Stage Gas Injection Compressor Suction Scrubber Inlet Bypass SDV-2416 •Compressor Discharge Header SDV-2435 •Pipeline pressurisation manual valves VBA-1155 / 1203
9.
Refer to 2.0 for the valve position during operation. NOTE: Refer to Solar Turbines document title Unit-Control Balance of Plant Functional Specification, doc. no. 3Y041-149007 for detailed sequencing of the valves.
2.3 Start-Up Gas Turbine for Gas Injection Compressor STEP NO.
CHECK ONCE TASK IS COMPLETED
ACTION
NOTE: Refer vendor doc. title Turbomachinery Package Installation Guideline: Compressor and Mechanical Drive Units, doc no. TPIM 1010 for further details
1.
Check that fuel gas supply is adequately available for the gas injection compressor turbine driver.
2.
Ensure adequate process gas supply is available from glycol contactor for compressor start up. NOTE : A restart may be initiated one minute after the turbine engine speed drops to 15 percent. In case of a malfunction shutdown, do not attempt another restart until the cause of the malfunction has been determined and the condition has been corrected. After three attempted starts have been unsuccessful, additional troubleshooting
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3.
4. 5. 6.
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
may be required. Select Maintenance display screen and select onscreen FAIL TO LOAD SHUTDOWN ENABLE button. Verify [Fail to Load Enabled] highlights. Select Unit Valves display screen and select onscreen Seal System Auto button. Verify [Auto] highlights for Seal System Status. From Unit Valves display screen, select onscreen Yard Valves Auto button and verify [Auto] highlights for Yard Valves System Status. Select HPC Surge Control display screen and select onscreen Auto button. Verify [Auto] is highlighted for ANTI-SURGE CONTROL.
7.
Select LPC Surge Control display screen and select onscreen Auto button. Verify [Auto] is highlighted for ANTI-SURGE CONTROL.
8.
Verify Operation display screen is selected to monitor package during start.
9.
Press START Switch (S1010) or select Operation display screen onscreen START button.
a. STARTING Light (DS1014) begins flashing and [Starting] is highlighted on Operation display screen. Enclosure vent fan is energized. Backup lube oil pump is tested for operation and pre/post pump starts pre-lubrication cycle. The control system begins a fuel system check. Start system is energized.
b. After pre-lube cycle is complete, engine cranking begins. c.
After starter has cranked engine to 15 percent speed, purge timer provides a preselected period of exhaust system purging via engine air flow. [Purge Crank] is highlighted on Operation display screen. d. After purge cycle is completed, fuel is admitted into combustor chamber where it is mixed with compressed air and ignited. [Ignition] is highlighted on e. Operation display screen. Light off occurs within next few seconds and combustion begins. f. The engine continues to accelerate and engine temperature increases to 400°F (204°C). [Light Off] is highlighted on Operation display screen, fuel ramp is activated, and ignition is de-
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energized. ENGINE HOURS/START COUNTER Meter (M210) registers a successful start.
g. Engine speed increases to starter dropout speed. Engine-driven lube oil pump pressure increases and pre/post lube oil pump stops. Start system is de-energized and starter clutch overruns. Engine speed increases to idle speed. ENGINE HOURS/START COUNTER Meter (M210) begins to log engine operating hours. STARTING Light is extinguished and [Running] is highlighted on Operation display screen.
h. If engine speed remains at idle speed, manually increase engine speed by pressing INCREASE Switch (S1054) until [Ready to Load] is highlighted on Operation display screen.
NOTE: Refer to Solar Turbines document title Unit-Control Balance of Plant Functional Specification, doc. no. 3Y041-149007 for detailed sequencing of the valves. NOTE: Refer to Solar Turbines document title Unit-Control Balance of Plant Functional Specification, doc. no. 3Y041-149007 for detailed sequencing of the valves.
2.3 .1 Start-Up Gas Turbine for Gas Injection Compressor STEP NO.
CHECK ONCE TASK IS COMPLETED
ACTION
1.
Confirm that gas injection compressor is in stable operation
2.
Monitor flow, pressure and temperature at the following location: 1st stage GI compressor suction pressure (PIA-2425) via GI compressor TCP 1st stage GI compressor discharge pressure (PIA-2426) via GI
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HOOK-UP AND COMMISSIONING
compressor TCP 1st stage GI compressor discharge temperature (TIA-2426) via GI compressor TCP 2nd stage GI compressor suction pressure (PIA-2445) via GI compressor TCP 2nd stage GI compressor discharge pressure (PIA-2448) via GI compressor TCP 2nd stage GI compressor discharge temperature (TIA-2446) via GI compressor TCP 2nd stage GI compressor after cooler outlet temperature (TIA-2457) GI injection export header flow (FQI-2435)
3.
4.
5.
With closed PCV-2430 due controller action, 2nd stage GI compressor discharge pressure is expected to build up to 23000 kPag. Upon reaching this pressure, PCV-2430 will start to open to pressurize the pipeline further from 74 barg to reach required operating landing pressure at SMP-B and SMJT-E depending on GI injection well consumption.
Once required pressure at gas injection manifold at SMP-B and SMJT-E is achieved, gas injection to individual wellhead can proceed.
Gas injection to individual wellhead shall be done one wellhead at a time and follows the following sequence: a. Ensure the header valves are fully open. b. Ensure the master and wing valves are fully open. c. Open well SCSSV and followed by SSV from WHCP unit. d. Open injection choke valve to introduce gas injection into the well
2.4 Shutdown of EOR Gas Compression 49
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
NOTE: Refer vendor doc. title Turbomachinery Package Installation Guideline: Compressor and Mechanical Drive Unit, doc no. TPIM 1010 for further details This subsection describes the shutdown procedures for the turbine package. There are four types of shutdown procedures; normal stop, pressurized fast stop, emergency stop, and control system stop. Once the turbine is shutdown, operator at SMG-A to stop gas injection at SMDP-B and SMJT-E as necessary by closing the wellhead gas injection choke valves. Close injector well SSV followed by SCSSV from well control-o-maticWHCP unit.
2.4.1 NORMAL STOP NOTE: Refer to Solar Turbines document title Unit-Control Balance of Plant Functional Specification, doc. no. 3Y041-149007 for more details.
This subsection describes the procedures to initiate a normal stop from the control console. A normal stop shutdown sequence includes a cooldown period, which allows the engine to run with no load for a preset period before the engine is stopped. 1. Press NORMAL STOP Switch (S1011) or select Operation display screen onscreen STOP button. The following events occur: a. COOLDOWN Light (DS1013) illuminates, surge control valve is opened, and [Cooldown] highlights on Operation display screen. b. Engine slows to idle speed and continues to run for a preset cooldown cycle. NOTE : Engine may be restarted during cooldown cycle by pressing ACKNOWLEDGE Switch, RESET Switch, and then START Switch or by selecting Operation display screen onscreen RESET and START buttons. c.
After preset cooldown cycle, fuel system valves close, combustion ceases, and engine begins to decelerate. COOLDOWN Light (DS1013) extinguishes and [Cooldown] indication reverts to normal video. d. When engine speed decreases below 25%, Slow Roll Time counts down under TIME REMAINING on Operation display screen.
NOTE : The Variable Frequency Drive (VFD) commands the starter motor to a speed of ~2 to 3.5% NGP. As the engine speed continues to slow from 25%, the overrunning clutch continues to overrun until the engine speed matches the starter speed. The clutch engages and the starter maintains the commanded speed until the slow roll timer times out.
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e. After preset slow roll cycle, start motor is de-energized. STOPPING Light (DS1011) illuminates, and [Stopping] highlights on Operation display screen. f. Gas compressors suction valves and discharge valves close and vent valves remains closed to maintain pressure in gas compressors and process piping for a preselected pressurization hold time period. g. [Running] indication reverts to normal video. ENGINE HOURS/START COUNTER Meter (M210) stops logging operating time. h. After engine coasts to a stop and rundown timer expires, a preset post lubrication cycle will be initiated. i. After preselected pressurization hold time period ends, vent valves open to depressurize compressors and process piping and seal system is de- energized.
2.4.2 PRESSURIZED FAST STOP NOTE: Refer vendor doc. title Unit-Control Balance of Plant Functional Specification, doc no. 3Y041-149008 for further details A pressurized fast stop causes the unit to stop with the compressors pressurized, and vent valves and blowdown valves remain closed. To initiate a pressurized fast stop, press the customerfurnished FAST STOP (REMOTE) Switch (S513). The following events occur: 1. Compressor suction valves close, discharge valves close, vent valves, and blowdown valves remain closed to maintain pressure in gas compressors and process piping for a preselected pressurization hold time period. 2. Engine shuts down immediately with no cooldown cycle. Slow roll cycle is bypassed, STOPPING Light (DS1011) illuminates, and [Stopping] highlights on Operation display screen. 3. ENGINE HOURS/START COUNTER Meter (M210) stops logging operating time. 4. After engine coasts to a stop and rundown timer expires, a preset post lubrication cycle will be initiated. 5. After pre-selected pressurization hold time period ends, vent valves and blowdown valves open to depressurize compressors and process piping and seal system is de-energized.
2.4.2 EMERGENCY STOP NOTE: Refer to Solar Turbines document title Unit-Control Balance of Plant Functional Specification, doc. no. 3Y041-149007 for more details. An emergency stop does not include a cool down period, which allows the engine to run with no load for a preset period before the engine is stopped. The emergency stop shutdown should only be used when plant conditions require an immediate shutdown.
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An emergency stop prevents package operation until the emergency stop shutdown is acknowledged and reset by pressing the local ACKNOWLEDGE and RESET switches and the backup relay system is reset. NOTE : In the following procedures, display screen indications that highlight in (reverse video) are shown in brackets [ ]. To initiate an emergency stop, press either the EMERGENCY STOP Switch (S1012) located on the turbine control panel or the EMERGENCY STOP Switch (S312) located on the enclosure twin control station. The following events occur: 1. Pressurized hold sequence is bypassed. Compressor suction valves close, discharge valves close, and vent valves open. 2. Engine shuts down immediately with no cool down cycle. Slow roll cycle is bypassed, STOPPING Light (DS1011) illuminates, and [Stopping] highlights on Operation display screen. 3. ENGINE HOURS/START COUNTER Meter (M210) stops logging operating time. 4. After engine coasts to a stop and rundown timer expires, a preset post lubrication cycle will be initiated.
2.4.3 CONTROL SYSTEM STOP NOTE: Refer to Solar Turbines document title Unit-Control Balance of Plant Functional Specification, doc. no. 3Y041-149007 for more details. There are two types of control system stops; cool down stop and fast stop. If an unsafe operating condition is detected by the control system, the control system will initiate a shutdown. Depending upon the severity of the shutdown, the control system will initiate either a cool down stop or a fast stop. If the control system stop was initiated due to a condition that is self-correcting, the engine can be restarted after the condition returns to normal. If the control system stop was initiated due to a condition that is not self-correcting, contact maintenance personnel to perform corrective actions.
Cooldown Stop If a cooldown stop has been initiated, the compressors are unloaded and the engine is shut down in the same manner as a normal stop. There are two types of cooldown stops; cooldown lockout and cooldown nonlockout.
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Cooldown Nonlockout (CN) - Cooldown nonlockout shutdowns reduce engine speed to idle for a preset cooldown period before initiating a shutdown. Cooldown nonlockout shutdowns include operator initiated normal stops, operating conditions that reached a shutdown limit because maintenance was not performed, a momentary disruption that causes an out-oflimits condition, and operating conditions that exceed alarm levels but are not serious enough to cause any immediate damage. Cooldown nonlockout shutdowns can be reset after corrective action has been taken or operating conditions revert to normal using either the local or remote acknowledge and reset switches. Cooldown Lockout (CL) - Cooldown lockout shutdowns reduce engine speed to idle for a preset cooldown period before initiating a shutdown. Cooldown lockout shutdowns typically result from a component failure and not because operating conditions have exceeded alarm or shutdown levels. Cooldown lockout shutdowns may not present immediate danger, but corrective action must be taken to avoid damage resulting from a component failure. Cooldown lockout shutdowns prevent package operation until the shutdown is acknowledged and reset using the local acknowledge and reset switches.
NOTE : Remote acknowledge and reset switches cannot acknowledge or reset cooldown lockout shutdowns. Fast Stop If a fast stop has been initiated, the compressors are unloaded and the engine is shut down in the same manner as an emergency stop. There are two types of fast stops; fast stop lockout and fast stop non lockout. WARNING : When a fast stop shutdown has been initiated due to fire detection, the postlube oil pump will remain energized for a preset rundown period. After the preset rundown period expires, the postlube oil pump will be deenergized for 20 minutes. After the 20 minute time period expires, the postlube pump will cycle on and off for a preset postlube period. If unsafe conditions still exist, the operator must manually abort the post lube cycle by opening the facility contactors for the postlube and backup lube oil pumps.
Fast Stop Nonlockout (FN) - Fast stop nonlockout shutdowns initiate an immediate shutdown of the engine. Fast stop nonlockout shutdowns typically result from a disruption in operation due to abnormal operating conditions and may not require corrective action. Fast stop nonlockout shutdowns can be reset when operating conditions revert to normal using either the local or remote acknowledge and reset switches. Fast Stop Lockout (FL) - Fast stop lockout shutdowns initiate an immediate shutdown of the engine. Fast stop lockout shutdowns prevent package operation until the shutdown is acknowledged and reset using the local acknowledge and reset switches. In addition to using the local acknowledge and reset switches, fast stop lockout shutdowns initiated due to a microprocessor failure, fire detection, backup overspeed, or pressing of emergency stop switch will require the backup relay system to be reset. Fast stop lockout shutdowns
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
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are the most severe shutdown types and require corrective action before the package can be restarted. NOTE : Remote acknowledge and reset switches cannot acknowledge or reset fast stop lockout shutdowns. Shutdown Initiators Any of the following process abnormality signals will result an export compressor USD. 1st stage GI compressor scrubber liquid level high high LZAHH-2415 1st stage GI compressor suction pressure low low PZALL-2426 1st stage GI compressor suction flow low low FZALL-2425 1st stage GI compressor discharge pressure high high PZAHH-2427 1st stage GI compressor discharge pressure low low PZAHH-2425 1st stage GI compressor after cooler inlet temperature high high TZAHH-2427A/B 1st stage GI compressor after cooler outlet temperature high high TZAHH-2436 2nd stage GI compressor scrubber liquid level high high LZAHH-2416 2nd stage GI compressor suction pressure low low PZALL-2446 2nd stage GI compressor suction flow low low FZALL-2445 2nd stage GI compressor discharge pressure high high PZAHH-2447 2nd stage GI compressor discharge pressure low low PZAHH-2445 2nd stage GI compressor after cooler inlet temperature high high TZAHH-2447A/B 2nd stage GI compressor after cooler outlet temperature high high TZAHH-2456 PSD ESD In addition to this a number of machine related signals can give a USD. For details on this refer to vendors operation and maintenance manuals. In the event of crash shutdown is initiated check the following actions occur. 1. Check lube oil supply from run down tank is maintained during speed down. 2. Check that fuel gas SABDV has closed. 3. Check that compressor inlet, outlet valves have closed and compressor has been depressurised.
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Check lube oil pumps and air coolers are shutdown and isolate all motor breakers.
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
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2.42.5 Instrument Set Points Downstream of Gas/Glycol Heat Exchanger at SUPG-B Tag No. TIAH-2230
PSV-2230 A/B
Location/Description
Set Point
Downstream of Gas/Glycol Heat Exchanger temperature high Gas/Glycol Heat Exchanger pressure safety valves
65°C 8740 kPag (1267 psig)
1st Stage Gas Injection Compressor Suction Scrubber V-2415 at SUPG-B Tag No.
Location/Description
Set Point
LZAHH-2415
1st Stage Gas Injection Compressor Suction Scrubber level high high
800mm from vessel bottom tangent line
LZALL-2415
1st Stage Gas Injection Compressor Suction Scrubber level low low
250mm from vessel bottom tangent line
LICAH-2415
1st Stage Gas Injection Compressor Suction Scrubber level high
700mm from vessel bottom tangent line
LICAL-2415
1st Stage Gas Injection Compressor Suction Scrubber level low
350mm from vessel bottom tangent line
PSV-2415 A/B
1st Stage Gas Injection Compressor Suction Scrubber pressure safety valves
13700 kPag (1986.5 psig)
1st Stage Gas Injection Compressor K-2425 & After Cooler E-2435 at SUPG-B Tag No. PZALL-2426
Location/Description 1st Stage Gas Injection Compressor suction pressure low low
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Set Point 5250 kPag (761 psig)
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PETRA RESOURCES SDN BHD (172962-D)
Tag No.
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Location/Description
Set Point
FZALL-2425
1st Stage Gas Injection Compressor suction flow low low
PZALL-2425
1st Stage Gas Injection Compressor discharge pressure low low
8870 kPag (1286 psig)
PZAHH-2427
1st Stage Gas Injection Compressor discharge pressure high high
13500 kPag (1975.6 psig)
TZAHH-2427A
1st Stage Gas Injection Compressor discharge temperature high high
115°C
TZAHH-2427B
1st Stage Gas Injection Compressor discharge temperature high high
115°C
TZAHH-2436
1st Stage Gas Injection Compressor After Cooler outlet temperature high high
60°C
PSV-2425 A/B
1st Stage Gas Injection Compressor pressure safety valves
HOLD
15000 kPag (2175 psig)
Gas Injection Launcher L-2930 and Compressor Seal Gas Supply at SUPG-B Tag No.
Location/Description
Set Point
PZAHH-2932
Seal gas pressure high high
17080 kPag (2477 psig)
PSV-2930 A/B
Seal gas line pressure safety valves
18200 kPag (2639 psig)
2nd Stage Gas Injection Compressor Suction Scrubber V-2416 at SUPG-B Tag No.
Location/Description
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Set Point
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PETRA RESOURCES SDN BHD (172962-D)
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
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LZAHH-2416
2nd Stage Gas Injection Compressor Suction Scrubber level high high
800mm from vessel bottom tangent line
LZALL-2416
2nd Stage Gas Injection Compressor Suction Scrubber level low low
250mm from vessel bottom tangent line
LICAH-2416
2nd Stage Gas Injection Compressor Suction Scrubber level high
700mm from vessel bottom tangent line
LICAL-2416
2nd Stage Gas Injection Compressor Suction Scrubber level low
350mm from vessel bottom tangent line
PSV-2416 A/B
2nd Stage Gas Injection Compressor Suction Scrubber pressure safety valves
17350 kPag (2516 psig)
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PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
2nd Stage Gas Injection Compressor K-2426 & After Cooler E-2436 at SUPG-B Tag No.
Location/Description
Set Point
PZALL-2446
2nd Stage Gas Injection Compressor suction pressure low low
6600 kPag (960 psig)
FZALL-2445
2nd Stage Gas Injection Compressor suction flow low low
PZALL-2445
2nd Stage Gas Injection Compressor discharge pressure low low
20000 kPag (2900 psig)
PZAHH-2447
2nd Stage Gas Injection Compressor discharge pressure high high
25200 kPag (3654 psig)
TZAHH-2447A
2nd Stage Gas Injection Compressor discharge temperature high high
123°C
TZAHH-2447B
2nd Stage Gas Injection Compressor discharge temperature high high
123°C
PSV-2426 A/C
2nd Stage Gas Injection Compressor pressure safety valves
28000 kPag (4060 psig)
PSV-2426 B
2nd Stage Gas Injection Compressor pressure safety valve
29400 kPag (4264 psig)
TZAHH-2456
2nd Stage Gas Injection Compressor After Cooler outlet temperature high high
80°C
TIAH-2457
2nd Stage Gas Injection Compressor After Cooler outlet temperature high
75°C
HOLD
Gas Injection Launcher L-2930 and Compressor Seal Gas Supply at SUPG-B Tag No.
Location/Description
Set Point
PICAH-2430
Gas injection compression discharge header pressure high
24150 kPag (3503 psig)
PICAL-2430
Gas injection compression discharge header pressure low
21850 kPag (3170 psig)
Gas injection to SMP-B pressure low
18952 kPag (2720 psig)
PIAL-2931
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Tag No.
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Location/Description
Set Point
PZALL-2932 A/B/C
Gas injection to SMP-B pressure low low
16408 kPag (2380 psig)
PZAHH-2932
Gas supply to compressor turbine seal gas system
17080 kPag (2477 psig)
Gas Injection Receiver at SMP-B Tag No.
Location/Description
Set Point
PEL-2940
Pressure Alarm Low for Gas Injection from SUPG-B
148 barg (2146.6 psig)
Gas Injection Launcher at SMP-B Tag No. PEL-2950
Location/Description Pressure Alarm Low for Gas Injection to SMJT-E
Set Point 148 barg (2146.6 psig)
Gas Injection Manifold at SMDP-B Tag No.
Location/Description
Set Point
PEL-6151
Pressure Alarm Low for Gas Injection to SMDP-B
144.8 barg
PEL-4751
Pressure Alarm Low for Gas Injection to SMDP-B
144.8 barg
Gas Injection Receiver at SMJT-E Tag No. PEL-2910
Location/Description Pressure Alarm Low for Gas Injection from SMP-B
Gas Injection Manifold at SMJT-E
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Set Point 145.6 barg (2111.8 psig)
PROCEDURE NO:
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PETRA RESOURCES SDN BHD (172962-D)
Tag No. PEL-1214853
PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-018 REVISION NO : A
HOOK-UP AND COMMISSIONING
Location/Description Pressure Alarm Low for Gas Injection at SMJT-E
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Set Point 144.8
barg
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PSP-CS-SMJT-G-002 REVISION NO: 0
PROCEDURE NO : PSP-EOR-CO-013 REVISION NO : A
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