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Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:49
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2101/2102/2103 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 10.797 in² 9.7176 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
16 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 88.889 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
430 lb 45 in 9 1/2 in
Dim C Dim E Dim F
9 7/16 in 13/16 in 2 1/4 in
Name Plate Capacity Air Water Steam
93612 Nm³/hr - -
26QA12-120
API Letter API Area ASME Area
Q 11.05 in² 12.27 in²
Size Rating Facing
Inlet: 6.0 in 300 # RF
Outlet: 8.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
139617 m³/hr 4179 lbs 122.23 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG)
- Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG) - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 6"-150#RF x 6"-150#RF, because Set. Pressure 18 Barg is too high, maxsimum Set. Pressure for ANSI Class 150# is. 11.4 BarG, so we offer size 6"300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26QA12-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:50
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2101/2102/2103 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
V-001-004 System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
16 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 88.889 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 18 Bar G
Compressible State
Fluid LPG Vapor Molecular Weight 1274.7 Mol Wt Gas Flow Const. 363.5
Req. Flow Cap. 122860 Nm³/hr Specific Gravity 44 sp gr Compressibility 0.01
Calculated Area 10.797 in² Specific Heat Ratio 1.49
Resolved ASME Area: 10.797 in² (Resolved by Maximum) Resolved API Area: 9.7176 in²
Model Selection
Manufacturer Farris API Letter Q Inlet Size 6.0 in Outlet Size 8.0 in
Model Number 26QA12-120 API Area 11.05 in² In. Rating 300 # Out. Rating 150 #
Valve Design Conventional ASME Area 12.27 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 3 NACE No
Name Plate Capacity (Air): 93612 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2101/2102/2103 - Data Sheet
2014-07-21 14:50 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge122860 Nm³/hr 139617 Nm³/hr 35 °C 4179 lbs 122.23 91.671 10.797 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 122860 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.01
Gas Flow Constant C 363.5
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) LPG Vapor
Relief Pressure Prelief 20.813 Bar Abs Specific Gravity Ggas 44 sp gr
Molecular Weight Mvapor 1274.7 Mol Wt Ratio of Specific Heats k 1.49
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 10.797 in²
Tag Notes
1. We assume : - Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG) - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 6"-150#RF x 6"-150#RF, because Set. Pressure 18 Barg is too high, maxsimum Set. Pressure for ANSI Class 150# is. 11.4 BarG, so we offer size 6"300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2101/2102/2103 Data Sheet
Tag +12476: PSV-2101/2102/2103 - Data Sheet
2014-07-21 14:50 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:50
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2301/2302/2303 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 10.797 in² 9.7176 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
16 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 88.889 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
430 lb 45 in 9 1/2 in
Dim C Dim E Dim F
9 7/16 in 13/16 in 2 1/4 in
Name Plate Capacity Air Water Steam
93612 Nm³/hr - -
26QA12-120
API Letter API Area ASME Area
Q 11.05 in² 12.27 in²
Size Rating Facing
Inlet: 6.0 in 300 # RF
Outlet: 8.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
139617 m³/hr 4179 lbs 122.23 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG)
- Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG) - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 6"-150#RF x 6"-150#RF, because Set. Pressure 18 Barg is too high, maxsimum Set. Pressure for ANSI Class 150# is. 11.4 BarG, so we offer size 6"300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26QA12-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:50
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2301/2302/2303 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
V-001-004 System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
16 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 88.889 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 18 Bar G
Compressible State
Fluid LPG Vapor Molecular Weight 1274.7 Mol Wt Gas Flow Const. 363.5
Req. Flow Cap. 122860 Nm³/hr Specific Gravity 44 sp gr Compressibility 0.01
Calculated Area 10.797 in² Specific Heat Ratio 1.49
Resolved ASME Area: 10.797 in² (Resolved by Maximum) Resolved API Area: 9.7176 in²
Model Selection
Manufacturer Farris API Letter Q Inlet Size 6.0 in Outlet Size 8.0 in
Model Number 26QA12-120 API Area 11.05 in² In. Rating 300 # Out. Rating 150 #
Valve Design Conventional ASME Area 12.27 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 1 NACE No
Name Plate Capacity (Air): 93612 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2301/2302/2303 - Data Sheet
2014-07-21 14:50 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge122860 Nm³/hr 139617 Nm³/hr 35 °C 4179 lbs 122.23 91.671 10.797 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 122860 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.01
Gas Flow Constant C 363.5
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) LPG Vapor
Relief Pressure Prelief 20.813 Bar Abs Specific Gravity Ggas 44 sp gr
Molecular Weight Mvapor 1274.7 Mol Wt Ratio of Specific Heats k 1.49
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 10.797 in²
Tag Notes
1. We assume : - Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG) - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 6"-150#RF x 6"-150#RF, because Set. Pressure 18 Barg is too high, maxsimum Set. Pressure for ANSI Class 150# is. 11.4 BarG, so we offer size 6"300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2301/2302/2303 Data Sheet
Tag +12476: PSV-2301/2302/2303 - Data Sheet
2014-07-21 14:50 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:50
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2101/2102/2103 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 10.797 in² 9.7176 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
16 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 88.889 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
430 lb 45 in 9 1/2 in
Dim C Dim E Dim F
9 7/16 in 13/16 in 2 1/4 in
Name Plate Capacity Air Water Steam
93612 Nm³/hr - -
26QA12-120
API Letter API Area ASME Area
Q 11.05 in² 12.27 in²
Size Rating Facing
Inlet: 6.0 in 300 # RF
Outlet: 8.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
139617 m³/hr 4179 lbs 122.23 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG)
- Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG) - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 6"-150#RF x 6"-150#RF, because Set. Pressure 18 Barg is too high, maxsimum Set. Pressure for ANSI Class 150# is. 11.4 BarG, so we offer size 6"300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26QA12-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:50
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2101/2102/2103 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
V-001-004 System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
16 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 88.889 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 18 Bar G
Compressible State
Fluid LPG Vapor Molecular Weight 1274.7 Mol Wt Gas Flow Const. 363.5
Req. Flow Cap. 122860 Nm³/hr Specific Gravity 44 sp gr Compressibility 0.01
Calculated Area 10.797 in² Specific Heat Ratio 1.49
Resolved ASME Area: 10.797 in² (Resolved by Maximum) Resolved API Area: 9.7176 in²
Model Selection
Manufacturer Farris API Letter Q Inlet Size 6.0 in Outlet Size 8.0 in
Model Number 26QA12-120 API Area 11.05 in² In. Rating 300 # Out. Rating 150 #
Valve Design Conventional ASME Area 12.27 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 1 NACE No
Name Plate Capacity (Air): 93612 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2101/2102/2103 - Data Sheet
2014-07-21 14:50 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge122860 Nm³/hr 139617 Nm³/hr 35 °C 4179 lbs 122.23 91.671 10.797 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 122860 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.01
Gas Flow Constant C 363.5
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) LPG Vapor
Relief Pressure Prelief 20.813 Bar Abs Specific Gravity Ggas 44 sp gr
Molecular Weight Mvapor 1274.7 Mol Wt Ratio of Specific Heats k 1.49
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 10.797 in²
Tag Notes
1. We assume : - Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG) - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 6"-150#RF x 6"-150#RF, because Set. Pressure 18 Barg is too high, maxsimum Set. Pressure for ANSI Class 150# is. 11.4 BarG, so we offer size 6"300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2101/2102/2103 Data Sheet
Tag +12476: PSV-2101/2102/2103 - Data Sheet
2014-07-21 14:50 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:50
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2401/2402/2403 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 10.797 in² 9.7176 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
16 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 88.889 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
430 lb 45 in 9 1/2 in
Dim C Dim E Dim F
9 7/16 in 13/16 in 2 1/4 in
Name Plate Capacity Air Water Steam
93612 Nm³/hr - -
26QA12-120
API Letter API Area ASME Area
Q 11.05 in² 12.27 in²
Size Rating Facing
Inlet: 6.0 in 300 # RF
Outlet: 8.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
139617 m³/hr 4179 lbs 122.23 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG)
- Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG) - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 6"-150#RF x 6"-150#RF, because Set. Pressure 18 Barg is too high, maxsimum Set. Pressure for ANSI Class 150# is. 11.4 BarG, so we offer size 6"300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26QA12-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:51
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2401/2402/2403 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
V-001-004 System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
16 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 88.889 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 18 Bar G
Compressible State
Fluid LPG Vapor Molecular Weight 1274.7 Mol Wt Gas Flow Const. 363.5
Req. Flow Cap. 122860 Nm³/hr Specific Gravity 44 sp gr Compressibility 0.01
Calculated Area 10.797 in² Specific Heat Ratio 1.49
Resolved ASME Area: 10.797 in² (Resolved by Maximum) Resolved API Area: 9.7176 in²
Model Selection
Manufacturer Farris API Letter Q Inlet Size 6.0 in Outlet Size 8.0 in
Model Number 26QA12-120 API Area 11.05 in² In. Rating 300 # Out. Rating 150 #
Valve Design Conventional ASME Area 12.27 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 1 NACE No
Name Plate Capacity (Air): 93612 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2401/2402/2403 - Data Sheet
2014-07-21 14:51 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge122860 Nm³/hr 139617 Nm³/hr 35 °C 4179 lbs 122.23 91.671 10.797 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 122860 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.01
Gas Flow Constant C 363.5
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) LPG Vapor
Relief Pressure Prelief 20.813 Bar Abs Specific Gravity Ggas 44 sp gr
Molecular Weight Mvapor 1274.7 Mol Wt Ratio of Specific Heats k 1.49
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 10.797 in²
Tag Notes
1. We assume : - Operating Pressure = 16 BarG, 10% lower than Setting Pressure (18 BarG) - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 6"-150#RF x 6"-150#RF, because Set. Pressure 18 Barg is too high, maxsimum Set. Pressure for ANSI Class 150# is. 11.4 BarG, so we offer size 6"300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2401/2402/2403 Data Sheet
Tag +12476: PSV-2401/2402/2403 - Data Sheet
2014-07-21 14:51 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:51
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2411 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 0.41489 in² 0.3734 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
10 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 55.556 % 3.78 Bar G 21 %
Dimensions Weight Dim A Dim B
58 lb 23 in 4 7/8 in
Dim C Dim E Dim F
5 3/8 in 11/16 in 1 5/16 in
Name Plate Capacity Air Water Steam
10910 Nm³/hr - -
26JA10-120
API Letter API Area ASME Area
J 1.287 in² 1.430 in²
Size Rating Facing
Inlet: 2.0 in 150 # RF
Outlet: 3.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
17820 m³/hr 523.78 lbs 113.29 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26JA10-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:51
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2411 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
LPG Tank 0.2T2 System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
10 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 55.556 % Percent Over P. 21 % Over Pressure 3.78 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 22.793 Bar Abs Cold Diff. Test P. 18 Bar G
Compressible State
Fluid LPG Vapor Molecular Weight 1274.7 Mol Wt Gas Flow Const. 363.5
Req. Flow Cap. 5170 Nm³/hr Specific Gravity 44 sp gr Compressibility 0.01
Calculated Area 0.41489 in² Specific Heat Ratio 1.49
Resolved ASME Area: 0.41489 in² (Resolved by Maximum) Resolved API Area: 0.3734 in²
Model Selection
Manufacturer Farris API Letter J Inlet Size 2.0 in Outlet Size 3.0 in
Model Number 26JA10-120 API Area 1.287 in² In. Rating 150 # Out. Rating 150 #
Valve Design Conventional ASME Area 1.430 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 1 NACE No
Name Plate Capacity (Air): 10910 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2411 - Data Sheet
2014-07-21 14:52 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge5170 Nm³/hr 17820 Nm³/hr 35 °C 523.78 lbs 113.29 84.966 0.41489 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 5170 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.01
Gas Flow Constant C 363.5
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) LPG Vapor
Relief Pressure Prelief 22.793 Bar Abs Specific Gravity Ggas 44 sp gr
Molecular Weight Mvapor 1274.7 Mol Wt Ratio of Specific Heats k 1.49
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 0.41489 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2411 Data Sheet
Tag +12476: PSV-2411 - Data Sheet
2014-07-21 14:52 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:52
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2411 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 0.41489 in² 0.3734 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
10 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 55.556 % 3.78 Bar G 21 %
Dimensions Weight Dim A Dim B
58 lb 23 in 4 7/8 in
Dim C Dim E Dim F
5 3/8 in 11/16 in 1 5/16 in
Name Plate Capacity Air Water Steam
10910 Nm³/hr - -
26JA10-120
API Letter API Area ASME Area
J 1.287 in² 1.430 in²
Size Rating Facing
Inlet: 2.0 in 150 # RF
Outlet: 3.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
17820 m³/hr 523.78 lbs 113.29 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26JA10-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:52
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2411 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
LPG Pump Suction System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
10 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 55.556 % Percent Over P. 21 % Over Pressure 3.78 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 22.793 Bar Abs Cold Diff. Test P. 18 Bar G
Compressible State
Fluid LPG Vapor Molecular Weight 1274.7 Mol Wt Gas Flow Const. 363.5
Req. Flow Cap. 5170 Nm³/hr Specific Gravity 44 sp gr Compressibility 0.01
Calculated Area 0.41489 in² Specific Heat Ratio 1.49
Resolved ASME Area: 0.41489 in² (Resolved by Maximum) Resolved API Area: 0.3734 in²
Model Selection
Manufacturer Farris API Letter J Inlet Size 2.0 in Outlet Size 3.0 in
Model Number 26JA10-120 API Area 1.287 in² In. Rating 150 # Out. Rating 150 #
Valve Design Conventional ASME Area 1.430 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 1 NACE No
Name Plate Capacity (Air): 10910 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2411 - Data Sheet
2014-07-21 14:52 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge5170 Nm³/hr 17820 Nm³/hr 35 °C 523.78 lbs 113.29 84.966 0.41489 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 5170 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.01
Gas Flow Constant C 363.5
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) LPG Vapor
Relief Pressure Prelief 22.793 Bar Abs Specific Gravity Ggas 44 sp gr
Molecular Weight Mvapor 1274.7 Mol Wt Ratio of Specific Heats k 1.49
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 0.41489 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2411 Data Sheet
Tag +12476: PSV-2411 - Data Sheet
2014-07-21 14:52 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:52
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-6101 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 12.047 in² 10.843 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
10 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 55.556 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
430 lb 45 in 9 1/2 in
Dim C Dim E Dim F
9 7/16 in 13/16 in 2 1/4 in
Name Plate Capacity Air Water Steam
93612 Nm³/hr - -
26QA12-120
API Letter API Area ASME Area
Q 11.05 in² 12.27 in²
Size Rating Facing
Inlet: 6.0 in 300 # RF
Outlet: 8.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
12222 m³/hr 4029.8 lbs 109.92 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. We can not input Ratio of Specific Heat 0.975, because value of Ratio of Specific Heat must be 1 or 2.5. 3. Based on data sheet, we can not offer size requested 3"-150#RF x 4"-150#RF, due to Required Capacity 12000 Nm3/hr is too large. So we offer size 6"-300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26QA12-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:52
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-6101 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
C-01 Discharge System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
10 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 55.556 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 18 Bar G
Compressible State
Fluid LPG Vapor Molecular Weight 1274.7 Mol Wt Gas Flow Const. 315
Req. Flow Cap. 12000 Nm³/hr Specific Gravity 44 sp gr Compressibility 0.98
Calculated Area 12.047 in² Specific Heat Ratio 1
Resolved ASME Area: 12.047 in² (Resolved by Maximum) Resolved API Area: 10.843 in²
Model Selection
Manufacturer Farris API Letter Q Inlet Size 6.0 in Outlet Size 8.0 in
Model Number 26QA12-120 API Area 11.05 in² In. Rating 300 # Out. Rating 150 #
Valve Design Conventional ASME Area 12.27 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 1 NACE No
Name Plate Capacity (Air): 93612 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-6101 - Data Sheet
2014-07-21 14:52 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge12000 Nm³/hr 12222 Nm³/hr 35 °C 4029.8 lbs 109.92 82.438 12.047 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 12000 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.98
Gas Flow Constant C 315
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) LPG Vapor
Relief Pressure Prelief 20.813 Bar Abs Specific Gravity Ggas 44 sp gr
Molecular Weight Mvapor 1274.7 Mol Wt Ratio of Specific Heats k 1
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 12.047 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. We can not input Ratio of Specific Heat 0.975, because value of Ratio of Specific Heat must be 1 or 2.5. 3. Based on data sheet, we can not offer size requested 3"-150#RF x 4"-150#RF, due to Required Capacity 12000 Nm3/hr is too large. So we offer size 6"-300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-6101 Data Sheet
Tag +12476: PSV-6101 - Data Sheet
2014-07-21 14:52 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:53
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-3001A/B/C No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Liquid (Volume) 2.5392 in² 2.2853 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
13 Bar G 18 Bar G 7 Bar G 0 Bar G 11 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 72.222 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
145 lb 28 1/2 in 6 1/2 in
Dim C Dim E Dim F
6 1/8 in 11/16 in 1 1/2 in
Name Plate Capacity Air Water Steam
- 242.8 m³/hr -
26LA10L-120
API Letter API Area ASME Area
L 2.853 in² 3.170 in²
Size Rating Facing
Inlet: 3.0 in 150 # RF
Outlet: 4.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
324.59 m³/hr 80.883 lbs -
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 7 BarG - Variable Back Pressure = 0 BarG Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26LA10L-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:53
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-3001A/B/C Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
Pump Discharge System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Liquid (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
13 Bar G Operating Temp.
35 °C Constant Back P.
7 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 72.222 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 11 Bar G
Non-Compressible State
Fluid Type LPG Liquid Specific Gravity 0.56 sp gr Viscosity Type Absolute
Req. Flow Cap. 260 m³/hr Viscosity 0.667 Centipoise
Calculated Area 2.5392 in² Reynolds # 1511470
Resolved ASME Area: 2.5392 in² (Resolved by Maximum) Resolved API Area: 2.2853 in²
Model Selection
Manufacturer Farris API Letter L Inlet Size 3.0 in Outlet Size 4.0 in
Model Number 26LA10L-120 API Area 2.853 in² In. Rating 150 # Out. Rating 150 #
Valve Design Conventional ASME Area 3.170 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 3 NACE No
Name Plate Capacity (Water): 242.8 m3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-3001A/B/C - Data Sheet
2014-07-21 14:53 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A LiquidBlocked
Discharge260 m³/hr 324.59 m³/hr 35 °C 80.883 lbs - - 2.5392 in²
Scenario: Case A / Liquid Volume -- Blocked Discharge
Required Flow Capacity Vliquid 260 m³/hr
Specific Gravity Gliquid 0.56 sp gr
Discharge Coeff. (0.9 x Kd) Kliquid 0.6516
Rupture Disk Coefficient KCCF 1
Pset + Pover - Pback P 12.8 Bar G
Liquid Viscosity Factor Ku 1
Liquid Flow Factor Kw -
Fluid Type User Defined Req'd Flow Capacity Qliquid -
Viscosity Type Absolute Discharge Coefficient Kd 0.724
Viscosity 0.667 Centipoise Relief Temperature Trelief 35 °C
Reynolds # R 1511470 ASME Area (Actual) 2.5392 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 7 BarG - Variable Back Pressure = 0 BarG Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-3001A/B/C Data Sheet
Tag +12476: PSV-3001A/B/C - Data Sheet
2014-07-21 14:53 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:53
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-001 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 0.19036 in² 0.17132 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
7 Bar G 15 Bar G 0 Bar G 0 Bar G 15 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 46.667 % 1.5 Bar G 10 %
Dimensions Weight Dim A Dim B
42 lb 19 in 4 1/2 in
Dim C Dim E Dim F
4 1/8 in 1/2 in 1 3/16 in
Name Plate Capacity Air Water Steam
1445.1 Nm³/hr - -
26EA10-140
API Letter API Area ASME Area
E 0.196 in² 0.225 in²
Size Rating Facing
Inlet: 1.0 in 150 # RF
Outlet: 2.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Packed Lever No
Max. Rel. Cap. React. Force Noise
236.4 m³/hr 32.818 lbs 92.783 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG - Ratio of Specific Heat = 1 - Compressibility Factor = 0.9 2. We can not input Setting Pressure 1.5 BarG, lower than Operating Pressure 7 BarG. So we input Setting Pressure 15 BarG. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26EA10-140 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:53
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-001 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
IA Drum System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
7 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 15 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 46.667 % Percent Over P. 10 % Over Pressure 1.5 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 17.513 Bar Abs Cold Diff. Test P. 15 Bar G
Compressible State
Fluid Air Molecular Weight 811.16 Mol Wt Gas Flow Const. 315
Req. Flow Cap. 200 Nm³/hr Specific Gravity 28 sp gr Compressibility 0.98
Calculated Area 0.19036 in² Specific Heat Ratio 1
Resolved ASME Area: 0.19036 in² (Resolved by Maximum) Resolved API Area: 0.17132 in²
Model Selection
Manufacturer Farris API Letter E Inlet Size 1.0 in Outlet Size 2.0 in
Model Number 26EA10-140 API Area 0.196 in² In. Rating 150 # Out. Rating 150 #
Valve Design Conventional ASME Area 0.225 in² In. Facing RF Out. Facing RF
Cap Constrn Packed Lever Test Gag No Quantity 1 NACE No
Name Plate Capacity (Air): 1445.1 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-001 - Data Sheet
2014-07-21 14:53 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge200 Nm³/hr 236.4 Nm³/hr 35 °C 32.818 lbs 92.783 69.587 0.19036 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 200 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.98
Gas Flow Constant C 315
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) Air
Relief Pressure Prelief 17.513 Bar Abs Specific Gravity Ggas 28 sp gr
Molecular Weight Mvapor 811.16 Mol Wt Ratio of Specific Heats k 1
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 0.19036 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG - Ratio of Specific Heat = 1 - Compressibility Factor = 0.9 2. We can not input Setting Pressure 1.5 BarG, lower than Operating Pressure 7 BarG. So we input Setting Pressure 15 BarG. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-001 Data Sheet
Tag +12476: PSV-001 - Data Sheet
2014-07-21 14:53 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:53
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-5001 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Liquid (Volume) 0.24232 in² 0.21809 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
10 Bar G 13.5 Bar G 0 Bar G 0 Bar G 13.5 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 74.074 % 1.35 Bar G 10 %
Dimensions Weight Dim A Dim B
44 lb 19 1/2 in 4 3/4 in
Dim C Dim E Dim F
4 7/8 in 11/16 in 1 1/4 in
Name Plate Capacity Air Water Steam
- 30.662 m³/hr -
26FA10L-120
API Letter API Area ASME Area
F 0.307 in² 0.371 in²
Size Rating Facing
Inlet: 1.5 in 150 # RF
Outlet: 2.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
30.62 m³/hr 3.4186 lbs -
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 1"-150#RF x 2"-150#RF, due to Required Capacity 20 Nm3/hr is too large. So we offer size 1.5"-150#RF x 2"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26FA10L-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:53
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-5001 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
Fire Water Line System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Liquid (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
10 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 13.5 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 74.074 % Percent Over P. 10 % Over Pressure 1.35 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 15.863 Bar Abs Cold Diff. Test P. 13.5 Bar G
Non-Compressible State
Fluid Type Fire Water Specific Gravity 1 sp gr Viscosity Type Absolute
Req. Flow Cap. 20 m³/hr Viscosity 0.86 Centipoise
Calculated Area 0.24232 in² Reynolds # 470694
Resolved ASME Area: 0.24232 in² (Resolved by Maximum) Resolved API Area: 0.21809 in²
Model Selection
Manufacturer Farris API Letter F Inlet Size 1.5 in Outlet Size 2.0 in
Model Number 26FA10L-120 API Area 0.307 in² In. Rating 150 # Out. Rating 150 #
Valve Design Conventional ASME Area 0.371 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 1 NACE No
Name Plate Capacity (Water): 30.662 m3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-5001 - Data Sheet
2014-07-21 14:54 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A LiquidBlocked
Discharge20 m³/hr 30.62 m³/hr 35 °C 3.4186 lbs - - 0.24232 in²
Scenario: Case A / Liquid Volume -- Blocked Discharge
Required Flow Capacity Vliquid 20 m³/hr
Specific Gravity Gliquid 1 sp gr
Discharge Coeff. (0.9 x Kd) Kliquid 0.6516
Rupture Disk Coefficient KCCF 1
Pset + Pover - Pback P 14.85 Bar G
Liquid Viscosity Factor Ku 1
Liquid Flow Factor Kw -
Fluid Type User Defined Req'd Flow Capacity Qliquid -
Viscosity Type Absolute Discharge Coefficient Kd 0.724
Viscosity 0.86 Centipoise Relief Temperature Trelief 35 °C
Reynolds # R 470694 ASME Area (Actual) 0.24232 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. Based on data sheet, we can not offer size requested 1"-150#RF x 2"-150#RF, due to Required Capacity 20 Nm3/hr is too large. So we offer size 1.5"-150#RF x 2"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-5001 Data Sheet
Tag +12476: PSV-5001 - Data Sheet
2014-07-21 14:54 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:54
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2005/2006/2007 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Gas (Volume) 10.797 in² 9.7176 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
16 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 88.889 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
430 lb 45 in 9 1/2 in
Dim C Dim E Dim F
9 7/16 in 13/16 in 2 1/4 in
Name Plate Capacity Air Water Steam
93612 Nm³/hr - -
26QA12-120
API Letter API Area ASME Area
Q 11.05 in² 12.27 in²
Size Rating Facing
Inlet: 6.0 in 300 # RF
Outlet: 8.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
139617 m³/hr 4179 lbs 122.23 dBa
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. We can not input value of Operating Pressure the same with Setting Pressure. So we assume Operating Pressure 16 BarG, minimum 10% lower than Setting Pressure (18 BarG). 3. Based on data sheet, we can not offer size requested 2"-150#RF x 3"-150#RF, due to Required Capacity 122860 Nm3/hr is too large. So we offer size 6"-300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of 26QA12-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:54
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2005/2006/2007 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
Vapor Header Line System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Gas (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
16 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 88.889 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 18 Bar G
Compressible State
Fluid LPG Vapor Molecular Weight 1274.7 Mol Wt Gas Flow Const. 363.5
Req. Flow Cap. 122860 Nm³/hr Specific Gravity 44 sp gr Compressibility 0.01
Calculated Area 10.797 in² Specific Heat Ratio 1.49
Resolved ASME Area: 10.797 in² (Resolved by Maximum) Resolved API Area: 9.7176 in²
Model Selection
Manufacturer Farris API Letter Q Inlet Size 6.0 in Outlet Size 8.0 in
Model Number 26QA12-120 API Area 11.05 in² In. Rating 300 # Out. Rating 150 #
Valve Design Conventional ASME Area 12.27 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 3 NACE No
Name Plate Capacity (Air): 93612 Nm3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2005/2006/2007 - Data Sheet
2014-07-21 14:54 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A GasBlocked
Discharge122860 Nm³/hr 139617 Nm³/hr 35 °C 4179 lbs 122.23 91.671 10.797 in²
Scenario: Case A / Gas Volume -- Blocked Discharge
Required Flow Capacity Vgas 122860 Nm³/hr
Relief Temperature Trelief 35 °C
Compressibility Z 0.01
Gas Flow Constant C 363.5
Discharge Coeff. (0.9 x Kd) KGas 0.8577
Flow Flow Critical
Rupture Disk Coefficient KCCF 1 Fluid Type (User Defined) LPG Vapor
Relief Pressure Prelief 20.813 Bar Abs Specific Gravity Ggas 44 sp gr
Molecular Weight Mvapor 1274.7 Mol Wt Ratio of Specific Heats k 1.49
Vapor Flow Factor Kb 1 Discharge Coefficient Kd 0.953
Vapor Flow Factor Kv - ASME Area (Actual) 10.797 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. We can not input value of Operating Pressure the same with Setting Pressure. So we assume Operating Pressure 16 BarG, minimum 10% lower than Setting Pressure (18 BarG). 3. Based on data sheet, we can not offer size requested 2"-150#RF x 3"-150#RF, due to Required Capacity 122860 Nm3/hr is too large. So we offer size 6"-300#RF x 8"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2005/2006/2007 Data Sheet
Tag +12476: PSV-2005/2006/2007 - Data Sheet
2014-07-21 14:54 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:54
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2004/2003/3002 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Liquid (Volume) 18.097 in² 16.287 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
16 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 88.889 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
750 lb 54 1/2 in 11 in
Dim C Dim E Dim F
10 7/8 in 13/16 in 2 7/16 in
Name Plate Capacity Air Water Steam
- 2758 m³/hr -
H26TA12L-120
API Letter API Area ASME Area
T 26.00 in² 28.94 in²
Size Rating Facing
Inlet: 8.0 in 300 # RF
Outlet: 10.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
415.79 m³/hr 1016.8 lbs -
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. We can not input value of Operating Pressure the same with Setting Pressure. So we assume Operating Pressure 16 BarG, minimum 10% lower than Setting Pressure (18 BarG). 3. Based on data sheet, we can not offer size requested 2"-150#RF x 3"-150#RF, due to Required Capacity 260 Nm3/hr is too large. So we offer size 8"-300#RF x 10"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of H26TA12L-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:54
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2004/2003/3002 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
LPG Header Line System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Liquid (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
16 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 88.889 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 18 Bar G
Non-Compressible State
Fluid Type LPG Liquid Specific Gravity 44 sp gr Viscosity Type Absolute
Req. Flow Cap. 260 m³/hr Viscosity 0.5 Centipoise
Calculated Area 18.097 in² Reynolds # 5.243e+7
Resolved ASME Area: 18.097 in² (Resolved by Maximum) Resolved API Area: 16.287 in²
Model Selection
Manufacturer Farris API Letter T Inlet Size 8.0 in Outlet Size 10.0 in
Model Number H26TA12L-120 API Area 26.00 in² In. Rating 300 # Out. Rating 150 #
Valve Design Conventional ASME Area 28.94 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 3 NACE No
Name Plate Capacity (Water): 2758 m3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2004/2003/3002 - Data Sheet
2014-07-21 14:54 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A LiquidBlocked
Discharge260 m³/hr 415.79 m³/hr 35 °C 1016.8 lbs - - 18.097 in²
Scenario: Case A / Liquid Volume -- Blocked Discharge
Required Flow Capacity Vliquid 260 m³/hr
Specific Gravity Gliquid 44 sp gr
Discharge Coeff. (0.9 x Kd) Kliquid 0.6516
Rupture Disk Coefficient KCCF 1
Pset + Pover - Pback P 19.8 Bar G
Liquid Viscosity Factor Ku 1
Liquid Flow Factor Kw -
Fluid Type User Defined Req'd Flow Capacity Qliquid -
Viscosity Type Absolute Discharge Coefficient Kd 0.724
Viscosity 0.5 Centipoise Relief Temperature Trelief 35 °C
Reynolds # R 5.243e+7 ASME Area (Actual) 18.097 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. We can not input value of Operating Pressure the same with Setting Pressure. So we assume Operating Pressure 16 BarG, minimum 10% lower than Setting Pressure (18 BarG). 3. Based on data sheet, we can not offer size requested 2"-150#RF x 3"-150#RF, due to Required Capacity 260 Nm3/hr is too large. So we offer size 8"-300#RF x 10"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2004/2003/3002 Data Sheet
Tag +12476: PSV-2004/2003/3002 - Data Sheet
2014-07-21 14:54 Page 2
Pressure Relief Valve Reference Drawing Date Prepared: 2014-07-21 14:54
PSV Identification Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Tag # Tag Description P / ID NACE
PSV-2001 No
ASME Code Fluid State Resolved ASME Area Resolved API Area Rupture Disk Coeff.
ASME Sec. VIII Liquid (Volume) 18.097 in² 16.287 in² No Rupture Disk, 1
Operating Pressure Set Pressure Constant Back P. Variable Back P. Cold Diff. Test P.
16 Bar G 18 Bar G 0 Bar G 0 Bar G 18 Bar G
Operating Temp. Relief Temp. Operating to Set % Over Pressure Percent Over P.
35 °C 35 °C 88.889 % 1.8 Bar G 10 %
Dimensions Weight Dim A Dim B
750 lb 54 1/2 in 11 in
Dim C Dim E Dim F
10 7/8 in 13/16 in 2 7/16 in
Name Plate Capacity Air Water Steam
- 2758 m³/hr -
H26TA12L-120
API Letter API Area ASME Area
T 26.00 in² 28.94 in²
Size Rating Facing
Inlet: 8.0 in 300 # RF
Outlet: 10.0 in 150 # RF
Valve Design Cap Constrn Test Gag
Conventional Screwed Cap No
Max. Rel. Cap. React. Force Noise
415.79 m³/hr 1016.8 lbs -
Materials Body (1)
Carbon Steel (SA-216 Gr. WCB)
Bonnet (2)
Carbon Steel (SA-216 Gr. WCB)
Nozzle (5)
316 SS
Disc (4)
316 SS
Guide (8)
316 SS
Spring (18)
Chrome Alloy
Bellows (15)
N/A
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC)
- Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. We can not input value of Operating Pressure the same with Setting Pressure. So we assume Operating Pressure 16 BarG, minimum 10% lower than Setting Pressure (18 BarG). 3. Based on data sheet, we can not offer size requested 3/4"-150#RF x 1"-150#RF, due to Required Capacity 260 Nm3/hr is too large. So we offer size 8"-300#RF x 10"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of H26TA12L-120 Valve Reference Drawing
Pressure Relief Valve Data Sheet Date Prepared: 2014-07-21 14:55
General Job Data Customer Requisition # Job # Job Description
PT. PP (Persero) +12476 Terminal LPG Banyuwangi
Prepared By Checked By Approved By Job Status Revision #
System Admin Sizing/Selecting 0
PSV Identification Tag # Tag Description Tag Status P / ID Discharge To Revision #
PSV-2001 Valve Selected 0
Plant # Drawing # Index # Issue For Service Inlet Line # Outlet Line # Revised By
Threstle LPG Line System Admin
Sizing Basis ASME Code Cause of Over Pressure Fluid State Rupture Disk Coeff. NACE
ASME Sec. VIII Blocked Discharge Liquid (Volume) No Rupture Disk, 1 No
Process Parameters
MAWP - Bar G Max. Design T. - °C Min. Design T. - °C
Operating Pressure
16 Bar G Operating Temp.
35 °C Constant Back P.
0 Bar G
Set Pressure 18 Bar G Relief Temp. 35 °C Variable Back P. 0 Bar G
Operating to Set % 88.889 % Percent Over P. 10 % Over Pressure 1.8 Bar G
Atm Pressure 1.0133 Bar Abs Relief Pressure 20.813 Bar Abs Cold Diff. Test P. 18 Bar G
Non-Compressible State
Fluid Type LPG Liquid Specific Gravity 44 sp gr Viscosity Type Absolute
Req. Flow Cap. 260 m³/hr Viscosity 0.5 Centipoise
Calculated Area 18.097 in² Reynolds # 5.243e+7
Resolved ASME Area: 18.097 in² (Resolved by Maximum) Resolved API Area: 16.287 in²
Model Selection
Manufacturer Farris API Letter T Inlet Size 8.0 in Outlet Size 10.0 in
Model Number H26TA12L-120 API Area 26.00 in² In. Rating 300 # Out. Rating 150 #
Valve Design Conventional ASME Area 28.94 in² In. Facing RF Out. Facing RF
Cap Constrn Screwed Cap Test Gag No Quantity 1 NACE No
Name Plate Capacity (Water): 2758 m3/hr
Model Materials
Body Carbon Steel (SA-216 Gr. WCB) Bonnet Carbon Steel (SA-216 Gr. WCB)
Nozzle 316 SS Disc 316 SS
Guide 316 SS Spring Chrome Alloy
Bellows N/A
Tag +12476: PSV-2001 - Data Sheet
2014-07-21 14:55 Page 1
Sizing Scenarios
ScenarioFluidState
Cause ofOver P.
Relief LoadCapacity
Max Rel Cap Relief T. React. ForceNoise
Atm (dBa)Noise
Flare (dBa)Required
Area
Case A LiquidBlocked
Discharge260 m³/hr 415.79 m³/hr 35 °C 1016.8 lbs - - 18.097 in²
Scenario: Case A / Liquid Volume -- Blocked Discharge
Required Flow Capacity Vliquid 260 m³/hr
Specific Gravity Gliquid 44 sp gr
Discharge Coeff. (0.9 x Kd) Kliquid 0.6516
Rupture Disk Coefficient KCCF 1
Pset + Pover - Pback P 19.8 Bar G
Liquid Viscosity Factor Ku 1
Liquid Flow Factor Kw -
Fluid Type User Defined Req'd Flow Capacity Qliquid -
Viscosity Type Absolute Discharge Coefficient Kd 0.724
Viscosity 0.5 Centipoise Relief Temperature Trelief 35 °C
Reynolds # R 5.243e+7 ASME Area (Actual) 18.097 in²
Tag Notes
1. We assume : - Operating Temp. = 35 degC, equal with Relieving Temp. (35 degC) - Constant Back Pressure = 0 BarG - Variable Back Pressure = 0 BarG 2. We can not input value of Operating Pressure the same with Setting Pressure. So we assume Operating Pressure 16 BarG, minimum 10% lower than Setting Pressure (18 BarG). 3. Based on data sheet, we can not offer size requested 3/4"-150#RF x 1"-150#RF, due to Required Capacity 260 Nm3/hr is too large. So we offer size 8"-300#RF x 10"-150#RF. Please customer to verify and confirm for data above.
SizeMaster 4.3.2.13, DB: D:\DATA SIZE MASTER\SM JAS 2013-lf End of PSV-2001 Data Sheet
Tag +12476: PSV-2001 - Data Sheet
2014-07-21 14:55 Page 2
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