No Scrubber for Project Flowrate Pressure Temperature Water content Scrubber Size

PSV (N4) (Inch)

1 Scrubber for Ecostation 330 300 12 5 to 8 40 30 40 3 < 0.1 10 um: 99.9 % 12 1.5 mm 4 4 1 1 1 1 1 1 12 Scrubber for package 1 Citereup Bogor 1800 1500 14 10.5 42 32 40 3 < 0.6 10 um: 99 % 12 3 mm 4 4 1 1 1 1 1 1 13 Scrubber for package 1 Indramayu 1800 1500 14.5 10.5 42 32 40 3 <0.6 10 um: 99% 12 3 mm 4 4 1 1 1 1 1 1 14 Scrubber for package 1 Karawang 1800 1500 14 10.5 44 34 40 3 < 0.7 10 um : 99% 12 3 mm 4 4 1 1 1 1 1 1 15 Scrubber for package 1 Subang 1800 1500 14 10.5 44 34 40 3 <0.6 10 um: 99 % 12 3 mm 4 4 1 1 1 1 1 1 16 Scrubber for package 3 Cilegon 4500 3 MMSCFD 14.5 10.5 150 30 40 3 1.03 * 10 um: 99 % 20 3mm 6 6 1 1 1 1 1 1 17 Scrubber for package 3 Jakarta 4500 3 MMSCFD 9.5 6 150 30 40 3 1.03 * 10 um: 99 % 20 0.125 inch 6 6 1 1 1 1 1 1 18 Scrubber for package 4 Bekasi 4500 3 MMSCFD 9.5 6 150 30 40 3 1.03 * 10 um: 99 % 20 0.125 inch 6 6 1 1 1 1 1 1 19 Scrubber for package 4 Purwakarta 5400 4500 14.5 10.5 44 34 40 3 <0.7 10 um: 99 % 20 3 mm 6 6 1 1 1 1 1 1 1

NOTE : 1. 1.03 bar is total pressure drop from inlet scrubber to outlet dryer2. Water content in outlet 3 lbs/MMSCF is designed for dryer not scrubber/coalescer3. Blue colour is VTA (vendor to advice)4. Sketch of Scrubber as below

* DPI, PI and TI is attach in inlet scrubber

Max. Pressure Drop ( bar)

Outlet Allowable

Particle Size

Corrosion Allowance

Inlet Noozle (N1) (Inch)

Outlet Noozle (N2) (Inch)

Drain stage 1 (N3a) (Inch)

Drain stage 2 (N3b) (Inch)

LI (N5,N6,N7,N8)

(Inch)DPI (N9)

(Inch)PI (N10)

(Inch)TI (N11) (Inch)

Design Flow (SM3/hr)Operating Flow

(M3/hr)Design Pressure

BarOperating Pressure

BarDesign Temperature o

C Operating Temperature oCInlet

(lbs/MMSCF)Outlet**

(lbs/MMSCF)Inch (pipe

sch.80)

MECHANICAL REQUIREMENT

No Scrubber for Project INSTRUMENT REQUIREMENT

LIFTING LUG SKIRT / LEG

1 Scrubber for Ecostation

2 Scrubber for package 1 Citereup Bogor

√ √ LEG

3 Scrubber for package 1 Indramayu

√ √ LEG

4 Scrubber for package 1 Karawang

√ √ LEG

5 Scrubber for package 1 Subang

√ √ LEG

6 Scrubber for package 3 Cilegon

√ √ LEG

MAINTENANCE HOLE

7 Scrubber for package 3 Jakarta

√ √ LEG

8 Scrubber for package 4 Bekasi

√ √ LEG

9 Scrubber for package 4 Purwakarta

√ √ LEG

INSTRUMENT REQUIREMENTELEMENT

TI DPI PI LI PSV VENTING

√ √ √ √

√ √ √ √ √

√ √ √ √ √

√ √ √ √ √

√ √ √ √ √

√ √ √ √ √

- Scrubber shall also have elements of glass fiber bonded by a phenolic resin or equivalent filtration material all supported by a suitable stainless steel cage.

√ √ √ √ √

√ √ √ √ √

√ √ √ √ √

VESSEL NOZZLE INTERNAL

- Accordance with ASME Section VIII Division 1,- Vessel shall include a 1.5 mm corrosion allowance unless a thicker allowance is called for on the data sheet,- Vertical Type

- All nozzle flanges shall conform to ASME B 16.5- Minimum nozzle size shall be 2 inch NPS.- Nozzles shall be weld neck (WN) with raised face (RF) flange

Bolting for internals shall be 316 SS material (minimum of 0.375 inches diameter)

- Material yang dipakai untuk konstruksi vessel adalah carbon steel- Material untuk tubing instrumentasi menggunakan stainless steel

- All nozzle flanges shall conform to ASME B 16.5- Noozle harus dihitung ketebalannya untuk menentukan perlu tidaknya reinforcement pad

Semua perbautan untuk internal vessel harus menggunakan bahan stainlees steel

- Material yang dipakai untuk konstruksi vessel adalah carbon steel- Material untuk tubing instrumentasi menggunakan stainless steel

- All nozzle flanges shall conform to ASME B 16.5- Noozle harus dihitung ketebalannya untuk menentukan perlu tidaknya reinforcement pad

Semua perbautan untuk internal vessel harus menggunakan bahan stainlees steel

- Material yang dipakai untuk konstruksi vessel adalah carbon steel- Material untuk tubing instrumentasi menggunakan stainless steel

- All nozzle flanges shall conform to ASME B 16.5- Noozle harus dihitung ketebalannya untuk menentukan perlu tidaknya reinforcement pad

Semua perbautan untuk internal vessel harus menggunakan bahan stainlees steel

- Material yang dipakai untuk konstruksi vessel adalah carbon steel- Material untuk tubing instrumentasi menggunakan stainless steel

- All nozzle flanges shall conform to ASME B 16.5- Noozle harus dihitung ketebalannya untuk menentukan perlu tidaknya reinforcement pad

Semua perbautan untuk internal vessel harus menggunakan bahan stainlees steel

- Material yang dipakai untuk konstruksi vessel adalah carbon steel- Material untuk tubing instrumentasi menggunakan stainless steel

- All nozzle flanges shall conform to ASME B 16.5- Noozle harus dihitung ketebalannya untuk menentukan perlu tidaknya reinforcement pad

Semua perbautan untuk internal vessel harus menggunakan bahan stainlees steel

- Material yang dipakai untuk konstruksi vessel adalah carbon steel- Material untuk tubing instrumentasi menggunakan stainless steel

- All nozzle flanges shall conform to ASME B 16.5- Noozle harus dihitung ketebalannya untuk menentukan perlu tidaknya reinforcement pad

Semua perbautan untuk internal vessel harus menggunakan bahan stainlees steel

- Material yang dipakai untuk konstruksi vessel adalah carbon steel- Material untuk tubing instrumentasi menggunakan stainless steel

- All nozzle flanges shall conform to ASME B 16.5- Noozle harus dihitung ketebalannya untuk menentukan perlu tidaknya reinforcement pad

Semua perbautan untuk internal vessel harus menggunakan bahan stainlees steel

- Material yang dipakai untuk konstruksi vessel adalah carbon steel- Material untuk tubing instrumentasi menggunakan stainless steel

- All nozzle flanges shall conform to ASME B 16.5- Noozle harus dihitung ketebalannya untuk menentukan perlu tidaknya reinforcement pad

Semua perbautan untuk internal vessel harus menggunakan bahan stainlees steel

PIPING CLOSURE HYDROTEST

- Welded and designed in compliance to ASME Code B31.3- Piping entering and leaving shall be supported. Vessel, piping and drain lines shall slope in to a manifold.

Quick Opening Type

Pengujian hydrotest dilakukan 1.3x MAWP sesuai dengan ASME Section VIII Div. 1 UG 95

Pengujian hydrotest dilakukan 1.3x MAWP sesuai dengan ASME Section VIII Div. 1 UG 96

Pengujian hydrotest dilakukan 1.3x MAWP sesuai dengan ASME Section VIII Div. 1 UG 97

Pengujian hydrotest dilakukan 1.3x MAWP sesuai dengan ASME Section VIII Div. 1 UG 98

Pengujian hydrotest dilakukan 1.3x MAWP sesuai dengan ASME Section VIII Div. 1 UG 99

Pengujian hydrotest dilakukan 1.3x MAWP sesuai dengan ASME Section VIII Div. 1 UG 100

Pengujian hydrotest dilakukan 1.3x MAWP sesuai dengan ASME Section VIII Div. 1 UG 101

Pengujian hydrotest dilakukan 1.3x MAWP sesuai dengan ASME Section VIII Div. 1 UG 102

PAINTING AND COATING NDE, WPS & PQR

√

√

√

√

√

- Surface preparation mengacu kepada standard SSPC-SP 10 Surface Preparation Standard Near-White Blast Cleaning atau ISO SA 2 ½- Coating Standard mengacu kepada ISO 12944, Painting Menggunakan traffic yellow RAL 1019

- Surface preparation mengacu kepada standard SSPC-SP 10 Surface Preparation Standard Near-White Blast Cleaning atau ISO SA 2 ½- Coating Standard mengacu kepada ISO 12944, Painting Menggunakan traffic yellow RAL 1020

- Surface preparation mengacu kepada standard SSPC-SP 10 Surface Preparation Standard Near-White Blast Cleaning atau ISO SA 2 ½- Coating Standard mengacu kepada ISO 12944, Painting Menggunakan traffic yellow RAL 1021

- Surface preparation mengacu kepada standard SSPC-SP 10 Surface Preparation Standard Near-White Blast Cleaning atau ISO SA 2 ½- Coating Standard mengacu kepada ISO 12944, Painting Menggunakan traffic yellow RAL 1022

- Surface preparation mengacu kepada standard SSPC-SP 10 Surface Preparation Standard Near-White Blast Cleaning atau ISO SA 2 ½- Coating Standard mengacu kepada ISO 12944, Painting Menggunakan traffic yellow RAL 1023

√

√

√

- Surface preparation mengacu kepada standard SSPC-SP 10 Surface Preparation Standard Near-White Blast Cleaning atau ISO SA 2 ½- Coating Standard mengacu kepada ISO 12944, Painting Menggunakan traffic yellow RAL 1024

- Surface preparation mengacu kepada standard SSPC-SP 10 Surface Preparation Standard Near-White Blast Cleaning atau ISO SA 2 ½- Coating Standard mengacu kepada ISO 12944, Painting Menggunakan traffic yellow RAL 1025

- Surface preparation mengacu kepada standard SSPC-SP 10 Surface Preparation Standard Near-White Blast Cleaning atau ISO SA 2 ½- Coating Standard mengacu kepada ISO 12944, Painting Menggunakan traffic yellow RAL 1026

Gas Composition

HMB For SPBG EcostationUnit dry_gas Water 3

Inlet GasVapour Fraction 1.0000 0.0000 1.0000Temperature C 30.0000 30.0000 29.0795Pressure bar_g 5.0000 5.0000 5.0000Molar Flow MMSCFD 0.2802 0.0002 0.2805Mass Flow kg/h 293.9312 0.2118 294.1430Liquid Volume Flow ft3/hr 27.6250 0.0075 27.6325Heat Flow Btu/hr -1246605.4010 -3185.4347 -1249790.8357Molecular Weight 21.0601 18.0151 21.0575Actual Liquid Flow USGPM - 0.0009 -Specific Gravity rel Air rel_to_air 0.7271 - 0.7270Mass Density lb/ft3 0.3190 62.6602 0.3200Viscosity cP 0.0119 0.7972 0.0119Z Factor 0.9833 0.0043 0.9831Higher Heating Value Btu/SCF 1017.6639 46.4640 1016.8464Cp/Cv 1.2862 1.1500 1.2869Gas CompositionComp Mole Frac (Methane) 0.7870 0.0000 0.7863Comp Mole Frac (Ethane) 0.0406 0.0000 0.0405Comp Mole Frac (Propane) 0.0304 0.0000 0.0304Comp Mole Frac (i-Butane) 0.0059 0.0000 0.0059Comp Mole Frac (n-Butane) 0.0071 0.0000 0.0071Comp Mole Frac (i-Pentane) 0.0023 0.0000 0.0023Comp Mole Frac (n-Pentane) 0.0018 0.0000 0.0018Comp Mole Frac (n-Hexane) 0.0048 0.0000 0.0048Comp Mole Frac (Nitrogen) 0.0550 0.0000 0.0549

Comp Mole Frac (CO2) 0.0651 0.0000 0.0650Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5Outlet Scrubber Outlet drain

1.0000 0.000029.0222 29.0222

4.9000 4.90000.2805 0.0000

294.1430 0.000027.6325 0.0000

-1249790.8357 0.000021.0575 65.0410

- 0.00000.7270 -0.3146 37.77190.0119 0.18970.9834 0.0253

1016.8464 3542.11591.2866 1.0575

0.7863 0.13180.0405 0.03520.0304 0.09080.0059 0.04330.0071 0.07210.0023 0.05730.0018 0.05870.0048 0.48290.0549 0.0029

0.0650 0.02460.0000 0.00000.0008 0.0004

HMB For SPBG CiteurepUnit dry_gas Water 3

Vapour Fraction 1.0000 0.0000 1.0000Temperature C 32.0000 32.0000 31.0866Pressure bar_g 10.5000 10.5000 10.5000Molar Flow MMSCFD 1.5285 0.0013 1.5297Mass Flow kg/h 1593.6426 1.1551 1594.7977Liquid Volume Flow ft3/hr 148.3756 0.0409 148.4165Heat Flow Btu/hr -6865872.7835 -17360.9544 -6883233.7379Molecular Weight 20.9338 18.0151 20.9313Actual Liquid Flow USGPM - 0.0051 -Specific Gravity rel Air rel_to_air 0.7228 - 0.7227Mass Density lb/ft3 0.6110 62.5763 0.6130Viscosity cP 0.0122 0.7642 0.0122Z Factor 0.9706 0.0082 0.9703Higher Heating Value Btu/SCF 975.8130 46.4640 975.0309Cp/Cv 1.3091 1.1511 1.3099Gas CompositionComp Mole Frac (Methane) 0.7871 0.0000 0.7864Comp Mole Frac (Ethane) 0.0317 0.0000 0.0317Comp Mole Frac (Propane) 0.0243 0.0000 0.0243Comp Mole Frac (i-Butane) 0.0052 0.0000 0.0052Comp Mole Frac (n-Butane) 0.0061 0.0000 0.0061Comp Mole Frac (i-Pentane) 0.0022 0.0000 0.0022Comp Mole Frac (n-Pentane) 0.0015 0.0000 0.0015Comp Mole Frac (n-Hexane) 0.0040 0.0000 0.0040Comp Mole Frac (Nitrogen) 0.0660 0.0000 0.0659Comp Mole Frac (CO2) 0.0719 0.0000 0.0718Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5

1.0000 0.000030.8144 30.814410.0000 10.0000

1.5297 0.00001594.7977 0.0000

148.4165 0.0000-6883233.7379 0.0000

20.9313 61.4449- 0.0000

0.7227 -0.5862 36.74580.0122 0.17000.9715 0.0455

975.0309 3320.73841.3084 1.0595

0.7864 0.17700.0317 0.03470.0243 0.08750.0052 0.04460.0061 0.07150.0022 0.06140.0015 0.05420.0040 0.42840.0659 0.00490.0718 0.03540.0000 0.00000.0008 0.0005

HMB For SPBG IndramayuUnit dry_gas Water 3

Vapour Fraction 1.0000 0.0000 1.0000Temperature C 32.0000 32.0000 31.0866Pressure bar_g 10.5000 10.5000 10.5000Molar Flow MMSCFD 1.5285 0.0013 1.5297Mass Flow kg/h 1593.6426 1.1551 1594.7977Liquid Volume Flow ft3/hr 148.3756 0.0409 148.4165Heat Flow Btu/hr -6865872.7835 -17360.9544 -6883233.7379Molecular Weight 20.9338 18.0151 20.9313Actual Liquid Flow USGPM - 0.0051 -Specific Gravity rel Air rel_to_air 0.7228 - 0.7227Mass Density lb/ft3 0.6110 62.5763 0.6130Viscosity cP 0.0122 0.7642 0.0122Z Factor 0.9706 0.0082 0.9703Higher Heating Value Btu/SCF 975.8130 46.4640 975.0309Cp/Cv 1.3091 1.1511 1.3099Gas CompositionComp Mole Frac (Methane) 0.7871 0.0000 0.7864Comp Mole Frac (Ethane) 0.0317 0.0000 0.0317Comp Mole Frac (Propane) 0.0243 0.0000 0.0243Comp Mole Frac (i-Butane) 0.0052 0.0000 0.0052Comp Mole Frac (n-Butane) 0.0061 0.0000 0.0061Comp Mole Frac (i-Pentane) 0.0022 0.0000 0.0022Comp Mole Frac (n-Pentane) 0.0015 0.0000 0.0015Comp Mole Frac (n-Hexane) 0.0040 0.0000 0.0040Comp Mole Frac (Nitrogen) 0.0660 0.0000 0.0659Comp Mole Frac (CO2) 0.0719 0.0000 0.0718Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5

1.0000 0.000030.8144 30.814410.0000 10.0000

1.5297 0.00001594.7977 0.0000

148.4165 0.0000-6883233.7379 0.0000

20.9313 61.4449- 0.0000

0.7227 -0.5862 36.74580.0122 0.17000.9715 0.0455

975.0309 3320.73841.3084 1.0595

0.7864 0.17700.0317 0.03470.0243 0.08750.0052 0.04460.0061 0.07150.0022 0.06140.0015 0.05420.0040 0.42840.0659 0.00490.0718 0.03540.0000 0.00000.0008 0.0005

HMB For SPBG KarawangUnit dry_gas Water 3

Vapour Fraction 1.0000 0.0000 1.0000Temperature C 34.0000 34.0000 33.0901Pressure bar_g 10.5000 10.5000 10.5000Molar Flow MMSCFD 1.5285 0.0013 1.5297Mass Flow kg/h 1593.6426 1.1551 1594.7977Liquid Volume Flow ft3/hr 148.3756 0.0409 148.4165Heat Flow Btu/hr -6860053.6598 -17351.5110 -6877405.1707Molecular Weight 20.9338 18.0151 20.9313Actual Liquid Flow USGPM - 0.0051 -Specific Gravity rel Air rel_to_air 0.7228 - 0.7227Mass Density lb/ft3 0.6066 62.4817 0.6086Viscosity cP 0.0123 0.7332 0.0123Z Factor 0.9712 0.0081 0.9709Higher Heating Value Btu/SCF 975.8130 46.4640 975.0309Cp/Cv 1.3075 1.1522 1.3083Gas CompositionComp Mole Frac (Methane) 0.7871 0.0000 0.7864Comp Mole Frac (Ethane) 0.0317 0.0000 0.0317Comp Mole Frac (Propane) 0.0243 0.0000 0.0243Comp Mole Frac (i-Butane) 0.0052 0.0000 0.0052Comp Mole Frac (n-Butane) 0.0061 0.0000 0.0061Comp Mole Frac (i-Pentane) 0.0022 0.0000 0.0022Comp Mole Frac (n-Pentane) 0.0015 0.0000 0.0015Comp Mole Frac (n-Hexane) 0.0040 0.0000 0.0040Comp Mole Frac (Nitrogen) 0.0660 0.0000 0.0659Comp Mole Frac (CO2) 0.0719 0.0000 0.0718Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5

1.0000 0.000032.8214 32.821410.0000 10.0000

1.5297 0.00001594.7977 0.0000

148.4165 0.0000-6877405.1707 0.0000

20.9313 60.5495- 0.0000

0.7227 -0.5819 36.28700.0123 0.16200.9721 0.0451

975.0309 3268.98751.3068 1.0596

0.7864 0.18720.0317 0.03580.0243 0.08880.0052 0.04480.0061 0.07140.0022 0.06070.0015 0.05330.0040 0.41540.0659 0.00530.0718 0.03680.0000 0.00000.0008 0.0005

HMB For SPBG SubangUnit dry_gas Water 3

Vapour Fraction 1.0000 0.0000 1.0000Temperature C 34.0000 34.0000 33.0901Pressure bar_g 10.5000 10.5000 10.5000Molar Flow MMSCFD 1.5285 0.0013 1.5297Mass Flow kg/h 1593.6426 1.1551 1594.7977Liquid Volume Flow ft3/hr 148.3756 0.0409 148.4165Heat Flow Btu/hr -6860053.6598 -17351.5110 -6877405.1707Molecular Weight 20.9338 18.0151 20.9313Actual Liquid Flow USGPM - 0.0051 -Specific Gravity rel Air rel_to_air 0.7228 - 0.7227Mass Density lb/ft3 0.6066 62.4817 0.6086Viscosity cP 0.0123 0.7332 0.0123Z Factor 0.9712 0.0081 0.9709Higher Heating Value Btu/SCF 975.8130 46.4640 975.0309Cp/Cv 1.3075 1.1522 1.3083Gas CompositionComp Mole Frac (Methane) 0.7871 0.0000 0.7864Comp Mole Frac (Ethane) 0.0317 0.0000 0.0317Comp Mole Frac (Propane) 0.0243 0.0000 0.0243Comp Mole Frac (i-Butane) 0.0052 0.0000 0.0052Comp Mole Frac (n-Butane) 0.0061 0.0000 0.0061Comp Mole Frac (i-Pentane) 0.0022 0.0000 0.0022Comp Mole Frac (n-Pentane) 0.0015 0.0000 0.0015Comp Mole Frac (n-Hexane) 0.0040 0.0000 0.0040Comp Mole Frac (Nitrogen) 0.0660 0.0000 0.0659Comp Mole Frac (CO2) 0.0719 0.0000 0.0718Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5

1.0000 0.000032.8214 32.821410.0000 10.0000

1.5297 0.00001594.7977 0.0000

148.4165 0.0000-6877405.1707 0.0000

20.9313 60.5495- 0.0000

0.7227 -0.5819 36.28700.0123 0.16200.9721 0.0451

975.0309 3268.98751.3068 1.0596

0.7864 0.18720.0317 0.03580.0243 0.08880.0052 0.04480.0061 0.07140.0022 0.06070.0015 0.05330.0040 0.41540.0659 0.00530.0718 0.03680.0000 0.00000.0008 0.0005

HMB For SPBG CilegonUnit dry_gas Water 3

Vapour Fraction 1.0000 0.0000 1.0000Temperature C 30.0000 30.0000 29.0773Pressure bar_g 10.5000 10.5000 10.5000Molar Flow MMSCFD 3.8211 0.0032 3.8244Mass Flow kg/h 3932.1698 2.8886 3935.0584Liquid Volume Flow ft3/hr 369.8676 0.1022 369.9698Heat Flow Btu/hr -16764601.1972 -43437.3613 -16808038.5585Molecular Weight 20.6609 18.0151 20.6586Actual Liquid Flow USGPM - 0.4344 -Specific Gravity rel Air rel_to_air 0.7133 - 0.7133Mass Density lb/ft3 0.6071 62.6707 0.6091Viscosity cP 0.0121 0.7972 0.0121Z Factor 0.9705 0.0082 0.9702Higher Heating Value Btu/SCF 973.4676 46.4640 972.6872Cp/Cv 1.3123 1.1499 1.3131Gas CompositionComp Mole Frac (Methane) 0.7927 0.0000 0.7920Comp Mole Frac (Ethane) 0.0323 0.0000 0.0323Comp Mole Frac (Propane) 0.0245 0.0000 0.0245Comp Mole Frac (i-Butane) 0.0058 0.0000 0.0058Comp Mole Frac (n-Butane) 0.0050 0.0000 0.0050Comp Mole Frac (i-Pentane) 0.0014 0.0000 0.0014Comp Mole Frac (n-Pentane) 0.0021 0.0000 0.0021Comp Mole Frac (n-Hexane) 0.0025 0.0000 0.0025Comp Mole Frac (Nitrogen) 0.0680 0.0000 0.0679Comp Mole Frac (CO2) 0.0657 0.0000 0.0656Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5

1.0000 0.000028.8046 28.804610.0000 10.0000

3.8244 0.00003935.0584 0.0000

369.9698 0.0000-16808038.5585 0.0000

20.6586 56.4031- 0.0000

0.7133 -0.5824 35.32880.0121 0.14940.9714 0.0437

972.6872 3041.49941.3115 1.0627

0.7920 0.21780.0323 0.04280.0245 0.10610.0058 0.05990.0050 0.07020.0014 0.04680.0021 0.09070.0025 0.31970.0679 0.00630.0656 0.03900.0000 0.00000.0008 0.0006

HMB For SPBG JakartaUnit dry_gas Water 3

Vapour Fraction 1.0000 0.0000 1.0000Temperature C 30.0000 30.0000 29.1135Pressure bar_g 6.0000 6.0000 6.0000Molar Flow MMSCFD 3.8211 0.0032 3.8244Mass Flow kg/h 4122.0917 2.8886 4124.9803Liquid Volume Flow ft3/hr 389.2566 0.1022 389.3588Heat Flow Btu/hr -18532377.0391 -43438.5220 -18575815.5611Molecular Weight 21.6588 18.0151 21.6557Actual Liquid Flow USGPM - 0.0127 -Specific Gravity rel Air rel_to_air 0.7478 - 0.7477Mass Density lb/ft3 0.3847 62.6621 0.3859Viscosity cP 0.0117 0.7972 0.0117Z Factor 0.9779 0.0050 0.9777Higher Heating Value Btu/SCF 1085.0160 46.4640 1084.1417Cp/Cv 1.2803 1.1500 1.2810Gas CompositionComp Mole Frac (Methane) 0.7838 0.0000 0.7831Comp Mole Frac (Ethane) 0.0553 0.0000 0.0553Comp Mole Frac (Propane) 0.0437 0.0000 0.0437Comp Mole Frac (i-Butane) 0.0079 0.0000 0.0079Comp Mole Frac (n-Butane) 0.0099 0.0000 0.0099Comp Mole Frac (i-Pentane) 0.0027 0.0000 0.0027Comp Mole Frac (n-Pentane) 0.0023 0.0000 0.0023Comp Mole Frac (n-Hexane) 0.0032 0.0000 0.0032Comp Mole Frac (Nitrogen) 0.0119 0.0000 0.0119Comp Mole Frac (CO2) 0.0793 0.0000 0.0792Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5

1.0000 0.000028.8064 28.8064

5.5000 5.50003.8244 0.0000

4124.9803 0.0000389.3588 0.0000

-18575815.5611 0.000021.6557 59.2726

- 0.00000.7477 -0.3582 36.42490.0117 0.16340.9792 0.0264

1084.1417 3220.68681.2793 1.0611

0.7831 0.14470.0553 0.05150.0437 0.13750.0079 0.06040.0099 0.10410.0027 0.06890.0023 0.07640.0032 0.32310.0119 0.00070.0792 0.03230.0000 0.00000.0008 0.0004

HMB For SPBG BekasiUnit dry_gas Water 3

Vapour Fraction 1.0000 0.0000 1.0000Temperature C 30.0000 30.0000 29.1135Pressure bar_g 6.0000 6.0000 6.0000Molar Flow MMSCFD 3.8211 0.0032 3.8244Mass Flow kg/h 4122.0917 2.8886 4124.9803Liquid Volume Flow ft3/hr 389.2566 0.1022 389.3588Heat Flow Btu/hr -18532377.0391 -43438.5220 -18575815.5611Molecular Weight 21.6588 18.0151 21.6557Actual Liquid Flow USGPM - 0.0127 -Specific Gravity rel Air rel_to_air 0.7478 - 0.7477Mass Density lb/ft3 0.3847 62.6621 0.3859Viscosity cP 0.0117 0.7972 0.0117Z Factor 0.9779 0.0050 0.9777Higher Heating Value Btu/SCF 1085.0160 46.4640 1084.1417Cp/CV 1.2803 1.1500 1.2810Gas CompositionComp Mole Frac (Methane) 0.7838 0.0000 0.7831Comp Mole Frac (Ethane) 0.0553 0.0000 0.0553Comp Mole Frac (Propane) 0.0437 0.0000 0.0437Comp Mole Frac (i-Butane) 0.0079 0.0000 0.0079Comp Mole Frac (n-Butane) 0.0099 0.0000 0.0099Comp Mole Frac (i-Pentane) 0.0027 0.0000 0.0027Comp Mole Frac (n-Pentane) 0.0023 0.0000 0.0023Comp Mole Frac (n-Hexane) 0.0032 0.0000 0.0032Comp Mole Frac (Nitrogen) 0.0119 0.0000 0.0119Comp Mole Frac (CO2) 0.0793 0.0000 0.0792Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5

1.0000 0.000028.8064 28.8064

5.5000 5.50003.8244 0.0000

4124.9803 0.0000389.3588 0.0000

-18575815.5611 0.000021.6557 59.2726

- 0.00000.7477 -0.3582 36.42490.0117 0.16340.9792 0.0264

1084.1417 3220.68681.2793 1.0611

0.7831 0.14470.0553 0.05150.0437 0.13750.0079 0.06040.0099 0.10410.0027 0.06890.0023 0.07640.0032 0.32310.0119 0.00070.0792 0.03230.0000 0.00000.0008 0.0004

HMB For SPBG PurwakartaUnit dry_gas Water 3

Vapour Fraction 1.0000 0.0000 1.0000Temperature C 34.0000 34.0000 33.1370Pressure bar_g 10.5000 10.5000 10.5000Molar Flow MMSCFD 4.5854 0.0039 4.5892Mass Flow kg/h 4946.5100 3.4662 4949.9762Liquid Volume Flow ft3/hr 467.1079 0.1227 467.2305Heat Flow Btu/hr -22226978.8375 -52065.8886 -22279044.7262Molecular Weight 21.6588 18.0151 21.6557Actual Liquid Flow USGPM - 0.0152 -Specific Gravity rel Air rel_to_air 0.7478 - 0.7477Mass Density lb/ft3 0.6314 62.4817 0.6333Viscosity cP 0.0120 0.7332 0.0119Z Factor 0.9654 0.0081 0.9651Higher Heating Value Btu/SCF 1085.0160 46.4640 1084.1417Cp/Cv 1.2940 1.1522 1.2948Gas CompositionComp Mole Frac (Methane) 0.7838 0.0000 0.7831Comp Mole Frac (Ethane) 0.0553 0.0000 0.0553Comp Mole Frac (Propane) 0.0437 0.0000 0.0437Comp Mole Frac (i-Butane) 0.0079 0.0000 0.0079Comp Mole Frac (n-Butane) 0.0099 0.0000 0.0099Comp Mole Frac (i-Pentane) 0.0027 0.0000 0.0027Comp Mole Frac (n-Pentane) 0.0023 0.0000 0.0023Comp Mole Frac (n-Hexane) 0.0032 0.0000 0.0032Comp Mole Frac (Nitrogen) 0.0119 0.0000 0.0119Comp Mole Frac (CO2) 0.0793 0.0000 0.0792Comp Mole Frac (H2S) 0.0000 0.0000 0.0000Comp Mole Frac (H2O) 0.0000 1.0000 0.0008

4 5

1.0000 0.000032.8397 32.839710.0000 10.0000

4.5892 0.00004949.9762 0.0000

467.2305 0.0000-22279044.7262 0.0000

21.6557 56.5670- 0.0000

0.7477 -0.6055 35.19980.0119 0.14400.9665 0.0434

1084.1417 3064.80041.2931 1.0619

0.7831 0.17400.0553 0.05710.0437 0.14380.0079 0.06070.0099 0.10270.0027 0.06540.0023 0.07140.0032 0.28640.0119 0.00090.0792 0.03700.0000 0.00000.0008 0.0005