Datasheet Inlet Compressor Package ConocoPhillips (Grissik) Ltd.
B-84567-SB-PP0-DSR-ST-23-0009 – Rev. 3 Page 2 of 8
Revision Sheet ConocoPhillips (Grissik) Ltd.
REVISION
DATE
1A
27-Feb-2015
DESCRIPTION OF CHANGE First Issuance Re-Issued for Comment 1.
1B
30-Mar-2015
2. 3. 4.
Revise the 2nd stage section of inlet compressor column for detail Suban compressor configuration. Revise tag no, skid tag no, and driver item tag no. Update Note 13, 15, 16, 17, and 18 Add new page for Prod. Profile Timeline
Issued for Approval 1C
4-May-2015
1. 2. 3.
Rewording content of notes, e.g Note 4, 12, 14, 15 Add new note 19, 20, 21 Update Fuel Gas and Seal Gas properties as per new vendor configurations.
Issued for Use 2
24-June-2015
1. 2. 3.
Rewording content of Note 6 and 12 Update compositions Update Fuel Gas and Seal Gas properties as per new vendor configurations.
Re-Issued for Use 3
29-July-2015
1.
Change process datasheet document numbering become B-84567SB-PP0-DSR-ST-23-0009 “
”
Additional Approvers (If Applicable) Name
Designation
Signature
Date
Process Data Sheet for Centrifugal Compressor Skid No.
: 23SAE-100/200/300/400/500
2
Tag No.
23CAE-100/200/300/400/500 (1st Stage) and 23CAE-101/201/301/401/501 : Location (2nd Stage)
3
Equipment Name
: I nlet Compressor
4 5
Equipment No.
: 5X25%
6
Service Description : Natural Gas
7
Compressor Type
: Centrifugal
Skid Tag No.
: 23SAE-100/200/300/400/500
8
Driver Type
: Gas Turbine
Driver Item Tag No.
: 23CDT-100/200/300/400/500
1
Client
Early Life 9
CASE
Note 2
Case 1 Comp. Suct. Press. 830 PSIG
Unit
st
nd
1 Stage
2 Stage
: ConocoPhillips (Grissik) Ltd. : Suban Gas Plant
Late Life
Beyond PSC Life (Note 3, 19)
Case 4 Comp. Suct. Press. 280 PSIG
Case 5 Comp. Suct. Press. 150 PSIG
Mid life Case 2 Comp. Suct. Press. 490 PSIG st
1 Stage
nd
2 Stage
Case 3 Comp. Suct. Press. 400 PSIG st
nd
1 Stage
st
2 Stage
nd
1 Stage
2 Stage
st
nd
1 Stage
2 Stage
10
OPERATING CONDITIONS
11
Vapour or Gas Handled
12
Oil Free : (Yes/No)
13
Entrainment
14
Corrosive Inlet Gas due to:
15
Hazardous Service : (Yes/No)
16
Liquid Injection Fluid : (Yes/No)
17 18
Volumetric Flow (14.7 psia & 60 F) Mass Flow
19
SUCTION CONDITIONS
20
Pressure
21
Temperature
22
Molecular Weight Cp/Cv Compressibility (Z1) or (Z AVG)
Note 11
1.457
1.501(*)
1.374
1.432 (*)
1.353
1.410 (*)
1.327
1.379 (*)
1.300
1.353 (*)
Note 11
0.889
0.871 (*)
0.930
0.900 (*)
0.941
0.911 (*)
0.957
0.926 (*)
0.975
0.940 (*)
25
Inlet Volume Flow
Note 11
ACFM
10250
8311 (*)
17919
11723 (*)
22080
13464 (*)
22189
11872 (*)
26964
10155 (*)
26
DISCHARGE CONDITIONS AT SKID EDGE
27
Pressure
psig
1031 (*)
1,280
758 (*)
1,280
668 (*)
1,280
542 (*)
(*)
(*)
(*)
(*)
(*)
(*)
Note 11
(*)
(*)
(*)
(*)
(*)
Note 11
(*)
(*)
(*)
(*)
23 24
28
Hydrocarbon Gas Yes (Note 14) 3
Note 8
Wet Gas with H2S (40 ppm), Mercury (750 microgram/Nm ), and CO2 (see gas compositions) Yes No
o
855
855
855
600
400
1,800,663
1,801,354
1,805,990
1,269,420
848,917
Note 11, 17 MMscfd Note 11, 17
lb/hr
psig
830
o
F
Note 11
o
120
120
19.181
19.181 (*)
490
733 (*) (Note 15)
120
120
19.188
19.189 (*)
643 (*) (Note 15)
400 120
120
19.201
19.202 (*)
517 (*) (Note 15)
280 120
150 (Note 3)
120
19.232
405 (*) (Note 15)
120
19.234 (*)
120
19.292
19.285 (*)
1250* (Note 1)
430 (*)
1,070
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*) (*)
30
Temperature Cp/Cv Compressibility (Z2)
31
PERFORMANCE
32
Estimated Power Absorbed
hp
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
33
Power Required (including All Losses)
hp
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
34
Speed (N)
rpm
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
35
Estimated Surge Flow (at speed N)
ACFM
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
36
Polytropic Efficiency
%
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
(*)
37
DESIGN CONDITION
38
Design Pressure
39
Design Temperature
40
Compressor Flange Rating
29
Note 11
1006 (*) (Note 15)
F
Note 5
1400 (*)
psig o
F
400 / -20 (*)
#/#
900 / 900 (*)
Max/Min Inlet/Outlet
41 42
NOTES:
43
1. Vendor to advise maximum discharge pressure can be achieved on case 4 by limitation 10% turbin power design margin.
44
2. Vendor to provide the best compressor configuration to meet all 5 cases. Vendor to advise any compressor modification/revamping required to meet the lowest suction pressure of 150 psig to compress 400 MMscfd. Vendor to advise also the lowest possible 3. suction pressure without any revamping/modification to compress 400 MMscfd. 4. The Suban Gas Plant site condition are as follows:
45 46 47
- Air Temperature, Min/Max/Avg
48
- Relative Humidity, Min/Max/Avg
49 50 51 52 53 54 55
o
o
o
o
: 65 F / 100 F / 85 F. Vendor to inform also the performance when 110 F ambient temperature is experienced for sensitivity only. : 60% / 100% / 80%
- Site Elevation : 206.83 ft above MSL. 5. Vendor to provide performance curves including Polytropic Head vs Flow, Polytropic Efficiency vs Flow, suction pressure vs flowrates and Power Curves for various flowrates and compressor speed. These should indicate any expected constraints including surge lines. 6. Vendor to advise the minimum fuel gas pressure and temperature, fuel gas consumption during normal operation and start-up. Fuel gas composition and source condition are as tabulat ed in Pa ge 6. 7. Vendor to advise required seal gas pressure and consumption (including start-up) for selected compressor. Seal gas composition and source condition are tabulated in Page 7. 8. Vendor shall consider the corrosive gas due to H2S, CO2 and mercury content in the selection of material of construction.
56
9. Vendor to advise anti-surge valve sizing requirement and provide Anti-Surge Control System, including hot bypass as required by Dynamic Simulation.
57
10. (*) = Vendor to Confirm / Advise.
58
11. Vendor to calculate the gas properties based on gas composition and operating conditions.
59
12. During Normal operation fuel gas & seal gas are taken from inlet compressor discharge header after going through conditioning system. For back up and during black start up,
60
Fuel Gas and Seal Gas are drawn from sales gas line after going through conditioning system. Barrier gas is supplied from Instrument Air system.
61
13. Vendor to info minimum temperature superheated requirement for Fuel Gas and Seal Gas Supply.
62
14. Incoming inlet gas is wet gas from suction scrubber with removal efficiency of >99% for liquid droplets 10 microns and larger.
63
15. Pressure drop of 25 psi between 1st stage and 2nd stage inlet compressor is taken to consider the Inlet Compressor Inter Cooler, Interstage scrubber and piping.
64
16. Fuel Gas supply pressure and temperature at outlet of Fuel Gas treatment skid.
3
29-Jul-15
Re-Issued for Use
YMT
JAZ/YHT
MCH
2
24-Jun-15
Issued for Use
YMT
JAZ/YHT
MCH
1C
04-May-15
Re-Issued for Approval
YMT
JAZ/AA
MCH
1B
30-Mar-15
Issued for Approval
YMT
AND/AA
MCH
1A
27-Feb-15
First Issuance
YMT
AA
MCH
REV
DATE
DESCRIPTION
PREPARED
CHECKED
APPROVED
Suban Compression Facilities Process Datasheet for Inlet Compressor ConocoPhillips (Grissik) Ltd.
Doc. No.
: B-84567-SB-PP0-DSR-ST-23-0009 Rev. 3
Page 3 of 8
Process Data Sheet for Centrifugal Compressor 1
Skid No.
:
23SAE-100/200/300/400/500
Client
: ConocoPhillips (Grissik) Ltd.
2
Tag No.
:
23CAE-100/200/300/400/500 (1st Stage) and 23CAE101/201/301/401/501 (2nd Stage)
Location
: Suban Gas Plant
3
Equipment Name
:
Inlet Compressor
4 5
INLET GAS ANALYSIS (1ST STAGE COMPRESSOR) - Note 8
6
GAS ANALYSIS
7
MW
COMPOSITION, %-MOLE (Note 14) Case 1
Case 2
Case 3
Case 4
8
Nitrogen
28
0.1809
0.1805
0.1804
0.1800
Case 5 0.1791
9
Carbon Dioxide
44
5.7330
5.7314
5.7267
5.7169
5.6936
10
Methane
16
88.1607
88.0235
87.9463
87.7671
87.3512
11
Ethane
30
3.3875
3.3880
3.3869
3.3827
3.3695
12
P ropane
44
0.9892
0.9923
0.9931
0.9937
0.9918
13
i -Butane
58
0.2919
0.2939
0.2947
0.2958
0.2963
14
n -Butane
58
0.2892
0.2918
0.2928
0.2944
0.2955
15
i-Pentane
72
0.1575
0.1598
0.1610
0.1631
0.1654
16
n-Pentane
72
0.1001
0.1018
0.1028
0.1044
0.1064
17
n -Hexane
86
0.1529
0.1566
0.1597
0.1659
0.1747
18
Mcyclopentane
84
0.0159
0.0163
0.0167
0.0174
0.0184
19
B enzene
78
0.0549
0.0569
0.0583
0.0609
0.0644
20
Cyclohexane
21
n-Heptane
84
0.0152
0.0157
0.0161
0.0169
0.0181
100
0.0704
0.0716
0.0739
0.0795
0.0894
22
Mcyclohexane
98
0.0194
0.0199
0.0206
0.0222
0.0248
23
Toluene
92
0.0355
0.0369
0.0385
0.0421
0.0481
24
n-Octane
114
0.0438
0.0429
0.0447
0.0499
0.0618
25
m-Xylene
106
0.0072
0.0073
0.0077
0.0088
0.0114
26
p-Xylene
106
0.0073
0.0073
0.0077
0.0088
0.0114
27
o-Xylene
106
0.0035
0.0035
0.0037
0.0042
0.0056
28
n-Nonane
128
0.0182
0.0167
0.0173
0.0197
0.0268
29
124-Mbenzene
120
0.0018
0.0016
0.0017
0.0020
0.0029
30
n-Decane
142
0.0085
0.0071
0.0072
0.0082
0.0117
31
n-C11
156
0.0034
0.0026
0.0026
0.0029
0.0042
32
n-C12
170
0.0015
0.0010
0.0010
0.0011
0.0015
33
n-C13
184
0.0005
0.0003
0.0003
0.0003
0.0004
34
n-C14
198
0.0001
0.0001
0.0001
0.0001
0.0001
35
n-C15
212
0.0001
0.0000
0.0000
0.0000
0.0000
36
n-C16
226
0.0000
0.0000
0.0000
0.0000
0.0000
37
n-C17
240
0.0000
0.0000
0.0000
0.0000
0.0000
38
n-C18
254
0.0000
0.0000
0.0000
0.0000
0.0000
39
n-C19
268
0.0000
0.0000
0.0000
0.0000
0.0000
40
n-C20
282
0.0000
0.0000
0.0000
0.0000
0.0000
41
H 2O
18
0.2458
0.3684
0.4335
0.5870
0.9718
42
H2S
34
0.0040
0.0040
0.0040
0.0040
0.0040
43
Mercury
44
TOTAL
100.0000
100.0000
100.0000
100.0000
100.0000
45
Average MW
19.181
19.188
19.201
19.232
19.292
750 microgram/Nm3
-
46 47
NOTES:
48
17. The shown value is total gas flowrate.
49
18 Seal Gas supply pressure and temperature at outlet of Seal Gas treatment skid.
50
19. Vendor to provide performance curve during transition prior to revamping.
51
20. Vendor to propose design to meet emission limitations as per Indonesian Regulations (Permen LH No. 13-2009) as below. 3
52
- 320 mg/Nm Nox (as NO 2)
53
- 150 mg/Nm SO2
54 55 56
3
3
- 50 mg/Nm total particulate - Volume of gas is measured at standard condition (25 degC and pressure of 1 atm) and all parameters are corrected with O 2 by 15% in dry state. 21. No modification or revamping is required for Case 1 until Case 4.
57 58 59 60 3
29-Jul-15
Re-Issued for Use
YMT
JAZ/YHT
MCH
2
24-Jun-15
Issued for Use
YMT
JAZ/YHT
MCH
1C
04-May-15
Re-Issued for Approval
YMT
JAZ/AA
MCH
1B
30-Mar-15
Issued for Approval
YMT
AND/AA
MCH
1A
27-Feb-15
First Issuance
YMT
AA
MCH
REV
DATE
DESCRIPTION
PREPARED
CHECKED
APPROVED
Suban Compression Facilities Process Datasheet for Inlet Compressor ConocoPhillips (Grissik) Ltd.
Doc. No
: B-84567-SB-PP0-DSR-ST-23-0009 Rev. 3
Page 4 of 8
Process Data Sheet for Centrifugal Compressor 1
Skid No.
:
23SAE-100/200/300/400/500
Client
: ConocoPhillips (Grissik) Ltd.
2
Tag No.
:
23CAE-100/200/300/400/500 (1st Stage) and 23CAE101/201/301/401/501 (2nd Stage)
Location
: Suban Gas Plant
3
Equipment Name
:
Inlet Compressor
4 5
INLET GAS ANALYSIS (2ND STAGE COMPRESSOR) - Note 8, 10
6
GAS ANALYSIS
7
MW
COMPOSITION, %-MOLE (Note 14) Case 1
Case 2
Case 3
Case 4
8
Nitrogen
28
0.1810
0.1807
0.1806
0.1804
Case 5 0.1801
9
Carbon Dioxide
44
5.7346
5.7368
5.7342
5.7298
5.7244
10
Methane
16
88.1866
88.1076
88.0620
87.9673
87.8299
11
Ethane
30
3.3885
3.3912
3.3913
3.3904
3.3878
12
Propane
44
0.9895
0.9932
0.9944
0.9959
0.9970
13
i -Butane
58
0.2920
0.2942
0.2951
0.2964
0.2978
14
n-Butane
58
0.2893
0.2920
0.2932
0.2951
0.2970
15
i-Pentane
72
0.1576
0.1600
0.1612
0.1635
0.1660
16
n-Pentane
72
0.1001
0.1019
0.1029
0.1047
0.1068
17
n-Hexane
86
0.1530
0.1568
0.1599
0.1662
0.1748
18
Mcyclopentane
84
0.0159
0.0164
0.0167
0.0174
0.0184
19
Benzene
78
0.0549
0.0570
0.0583
0.0610
0.0644
20
Cyclohexane
84
0.0152
0.0157
0.0162
0.0170
0.0181
21
n-Heptane
100
0.0705
0.0717
0.0740
0.0796
0.0888
22
Mcyclohexane
98
0.0194
0.0199
0.0206
0.0222
0.0247
23
Toluene
92
0.0355
0.0370
0.0386
0.0421
0.0477
24
n-Octane
114
0.0438
0.0430
0.0447
0.0500
0.0604
25
m-Xylene
106
0.0073
0.0073
0.0077
0.0088
0.0110
26
p-Xylene
106
0.0073
0.0073
0.0077
0.0088
0.0110
27
o-Xylene
106
0.0035
0.0035
0.0037
0.0043
0.0053
28
n-Nonane
128
0.0182
0.0167
0.0173
0.0197
0.0251
29
124-Mbenzene
120
0.0018
0.0016
0.0017
0.0020
0.0026
30
n-Decane
142
0.0085
0.0071
0.0073
0.0082
0.0101
31
n-C11
156
0.0035
0.0026
0.0026
0.0029
0.0030
32
n-C12
170
0.0015
0.0010
0.0010
0.0010
0.0008
33
n-C13
184
0.0005
0.0003
0.0003
0.0003
0.0001
34
n-C14
198
0.0001
0.0001
0.0001
0.0001
0.0000
35
n-C15
212
0.0001
0.0000
0.0000
0.0000
0.0000
36
n-C16
226
0.0000
0.0000
0.0000
0.0000
0.0000
37
n-C17
240
0.0000
0.0000
0.0000
0.0000
0.0000
38
n-C18
254
0.0000
0.0000
0.0000
0.0000
0.0000
39
n-C19
268
0.0000
0.0000
0.0000
0.0000
0.0000
40
n-C20
282
0.0000
0.0000
0.0000
0.0000
0.0000
41
H2O
18
0.2166
0.2734
0.3026
0.3609
0.4428
42
H2S
34
0.0040
0.0040
0.0040
0.0040
0.0040
43
Mercury
44
TOTAL
100.0000
100.0000
100.0000
100.0000
100.0000
45
Average MW
19.181
19.189
19.202
19.234
19.285
750 microgram/Nm3
-
46 47
NOTES:
48 49 50 51 52 53 54 55 56 57 58 59 60 3
29-Jul-15
Re-Issued for Use
YMT
JAZ/YHT
MCH
2
24-Jun-15
Issued for Use
YMT
JAZ/YHT
MCH
1C
04-May-15
Re-Issued for Approval
YMT
JAZ/AA
MCH
1B
30-Mar-15
Issued for Approval
YMT
AND/AA
MCH
1A
27-Feb-15
First Issuance
YMT
AA
MCH
REV
DATE
DESCRIPTION
PREPARED
CHECKED
APPROVED
Suban Compression Facilities Process Datasheet for Inlet Compressor ConocoPhillips (Grissik) Ltd.
Doc. No
: B-84567-SB-PP0-DSR-ST-23-0009 Rev. 3
Page 5 of 8
Process Data Sheet for Centrifugal Compressor 1
Skid No.
:
23SAE-100/200/300/400/500
Client
: ConocoPhillips (Grissik) Ltd.
2
Tag No.
:
23CAE-100/200/300/400/500 (1st Stage) and 23CAE101/201/301/401/501 (2nd Stage)
Location
: Suban Gas Plant
3
Equipment Name
:
Inlet Compressor
4 5
FUEL GAS SUPPLY - Note 6, 8, 12 FUEL GAS COMPOSITION, %-MOLE
6 GAS ANALYSIS
MW
7
Case 1
Case 2
Case 3
Case 4
Case 5
Black Start and/or Back up
8
Nitrogen
28
0.1810
0.1807
0.1806
0.1804
0.1801
0.1870
9
Carbon Dioxide
44
5.7350
5.7368
5.7342
5.7307
5.7244
3.5099
10
Methane
16
88.1922
88.1076
88.0620
87.9820
87.8299
91.0220
11
Ethane
30
3.3887
3.3912
3.3913
3.3910
3.3878
3.4499
12
Propane
44
0.9896
0.9932
0.9944
0.9961
0.9970
0.9700
13
i-Butane
58
0.2920
0.2942
0.2951
0.2965
0.2978
0.2690
14
n-Butane
58
0.2893
0.2920
0.2932
0.2951
0.2970
0.2540
15
i-Pentane
72
0.1576
0.1600
0.1612
0.1635
0.1660
0.1190
16
n-Pentane
72
0.1001
0.1019
0.1029
0.1047
0.1068
0.0694
17
n-Hexane
86
0.1530
0.1568
0.1599
0.1662
0.1748
0.0694
18
Mcyclopentane
84
0.0159
0.0164
0.0167
0.0174
0.0184
0.0066
19
Benzene
78
0.0549
0.0570
0.0583
0.0610
0.0644
0.0210
20
Cyclohexane
21
n-Heptane
22
Mcyclohexane
98
0.0194
0.0199
0.0206
0.0222
0.0247
0.0051
23
Toluene
92
0.0355
0.0370
0.0386
0.0421
0.0477
0.0072
24
n-Octane
114
0.0438
0.0430
0.0447
0.0500
0.0604
0.0061
25
m-Xylene
106
0.0073
0.0073
0.0077
0.0088
0.0110
0.0007
26
p-Xylene
106
0.0073
0.0073
0.0077
0.0088
0.0110
0.0000
27
o-Xylene
106
0.0035
0.0035
0.0037
0.0043
0.0053
0.0000
28
n-Nonane
128
0.0182
0.0167
0.0173
0.0197
0.0251
0.0000
29
124-Mbenzene
120
0.0018
0.0016
0.0017
0.0020
0.0026
0.0000
30
n-Decane
142
0.0085
0.0071
0.0073
0.0082
0.0101
0.0000
31
n-C11
156
0.0035
0.0026
0.0026
0.0029
0.0030
0.0000
32
n-C12
170
0.0015
0.0010
0.0010
0.0010
0.0008
0.0000
33
n-C13
184
0.0005
0.0003
0.0003
0.0003
0.0001
0.0000
34
n-C14
198
0.0001
0.0001
0.0001
0.0001
0.0000
0.0000
35
n-C15
212
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
36
n-C16
226
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
n-C17
240
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
n-C18
254
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
n-C19
268
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
n-C20
282
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
H 2O
18
0.2103
0.2734
0.3026
0.3443
0.4428
0.0100
42
H2S
34
0.0040
0.0040
0.0040
0.0040
0.0040
0.0000
43
Mercury
44
TOTAL
100.0000
100.0000
100.0000
100.0000
100.0000
100.0000
45
Average MW
19.181
19.189
19.202
19.234
19.285
18.231
Case 4
Case 5
Black Start and/or Back up
84
0.0152
0.0157
0.0162
0.0170
0.0181
0.0056
100
0.0705
0.0717
0.0740
0.0797
0.0888
0.0182
-
< 1 microgram/Nm3
46 47
FUEL GAS CONDITION SUPPLY CONDITION
48 49
Supply Pressure, Psig
(Note 10, 16)
50
Supply Temperature, F
o
(Note 13, 16)
51
Hydrocarbon Dew Point, F
52
Water Dew Point, F
53
Fuel Gas LHV, Btu/scf
o
o
Case 1
Case 2
Case 3
180.7
167.9
167.9
167.3
167.7
170.3
130.9
118.1
118.0
117.4
117.7
24.9
89.7
98.3
101.7
106.1
114.9
8.2
932.9
932.7
933.1
934.3
936.0
939.1
350
54 55
NOTES:
56 57 58 59 60 3
29-Jul-15
Re-Issued for Use
YMT
JAZ/YHT
MCH
2
24-Jun-15
Issued for Use
YMT
JAZ/YHT
MCH
1C
04-May-15
Re-Issued for Approval
YMT
JAZ/AA
MCH
1B
30-Mar-15
Issued for Approval
YMT
AND/AA
MCH
1A
27-Feb-15
First Issuance
YMT
AA
MCH
REV
DATE
DESCRIPTION
PREPARED
CHECKED
APPROVED
Suban Compression Facilities Process Datasheet for Inlet Compressor ConocoPhillips (Grissik) Ltd.
Doc. No
: B-84567-SB-PP0-DSR-ST-23-0009 Rev. 3
Page 6 of 8
Process Data Sheet for Centrifugal Compressor 1
Skid No.
:
23SAE-100/200/300/400/500
Client
: ConocoPhillips (Grissik) Ltd.
2
Tag No.
:
23CAE-100/200/300/400/500 (1st Stage) and 23CAE-101/201/301/401/501 (2nd Stage)
Location
: Suban Gas Plant
3
Equipment Name
:
Inlet Compressor
4 5
SEAL GAS SUPPLY - Note 7, 8, 12, 18 SEAL GAS COMPOSITION, %-MOLE
6 GAS ANALYSIS
MW
7
Case 1
Case 2
Case 3
Case 4
Case 5
Black Start and/or Back up
8
Nitrogen
28
0.1810
0.1807
0.1806
0.1804
0.1801
0.1870
9
Carbon Dioxide
44
5.7350
5.7368
5.7342
5.7307
5.7244
3.5099
10
Methane
16
88.1922
88.1076
88.0620
87.9820
87.8299
91.0220
11
Ethane
30
3.3887
3.3912
3.3913
3.3910
3.3878
3.4499
12
Propane
44
0.9896
0.9932
0.9944
0.9961
0.9970
0.9700
13
i-Butane
58
0.2920
0.2942
0.2951
0.2965
0.2978
0.2690
14
n-Butane
58
0.2893
0.2920
0.2932
0.2951
0.2970
0.2540
15
i-Pentane
72
0.1576
0.1600
0.1612
0.1635
0.1660
0.1190
16
n-Pentane
72
0.1001
0.1019
0.1029
0.1047
0.1068
0.0694
17
n-Hexane
86
0.1530
0.1568
0.1599
0.1662
0.1748
0.0694
18
Mcyclopentane
84
0.0159
0.0164
0.0167
0.0174
0.0184
0.0066
19
Benzene
78
0.0549
0.0570
0.0583
0.0610
0.0644
0.0210
20
Cyclohexane
21
n-Heptane
22
Mcyclohexane
98
0.0194
0.0199
0.0206
0.0222
0.0247
0.0051
23
Toluene
92
0.0355
0.0370
0.0386
0.0421
0.0477
0.0072
24
n-Octane
114
0.0438
0.0430
0.0447
0.0500
0.0604
0.0061
25
m-Xylene
106
0.0073
0.0073
0.0077
0.0088
0.0110
0.0007
26
p-Xylene
106
0.0073
0.0073
0.0077
0.0088
0.0110
0.0000
27
o-Xylene
106
0.0035
0.0035
0.0037
0.0043
0.0053
0.0000
28
n-Nonane
128
0.0182
0.0167
0.0173
0.0197
0.0251
0.0000
29
124-Mbenzene
120
0.0018
0.0016
0.0017
0.0020
0.0026
0.0000
30
n-Decane
142
0.0085
0.0071
0.0073
0.0082
0.0101
0.0000
31
n-C11
156
0.0035
0.0026
0.0026
0.0029
0.0030
0.0000
32
n-C12
170
0.0015
0.0010
0.0010
0.0010
0.0008
0.0000
33
n-C13
184
0.0005
0.0003
0.0003
0.0003
0.0001
0.0000
34
n-C14
198
0.0001
0.0001
0.0001
0.0001
0.0000
0.0000
35
n-C15
212
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
36
n-C16
226
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
n-C17
240
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
38
n-C18
254
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
n-C19
268
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
40
n-C20
282
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
H 2O
18
0.2103
0.2734
0.3026
0.3443
0.4428
0.0100
42
H 2S
34
0.0040
0.0040
0.0040
0.0040
0.0040
0.0000
43
Mercury
44
TOTAL
100.0000
100.0000
100.0000
100.0000
100.0000
100.0000
45
Average MW
19.181
19.189
19.202
19.234
19.285
18.231
Case 5
Black Start and/or Back up
84
0.0152
0.0157
0.0162
0.0170
0.0181
0.0056
100
0.0705
0.0717
0.0740
0.0797
0.0888
0.0182
< 1 microgram/Nm3
-
46 SEAL GAS CONDITION
47 SUPPLY CONDITION
48
Case 1
Case 2
Case 3
Case 4
49
Supply Pressure, Psig
(Note 10, 18)
1225
1225
1225
1195
1015
1264
50
Supply Temperature, F
o
(Note 13, 18)
215.1
203.8
203.8
202.4
196.3
203.7
51
Hydrocarbon Dew Point, F
-70.1
o
98.1
90.8
92.0
97.8
111.7
52
Water Dew Point, F
123.4
133.7
137.8
142.4
148.0
28.1
53
Seal Gas LHV, Btu/scf
932.9
932.7
933.1
934.3
936.0
939.1
o
54 55
NOTES:
56 57 58 59 60 3
29-Jul-15
Re-Issued for Use
YMT
JAZ/YHT
MCH
2
24-Jun-15
Issued for Use
YMT
JAZ/YHT
MCH
1C
04-May-15
Re-Issued for Approval
YMT
JAZ/AA
MCH
1B
30-Mar-15
Issued for Approval
YMT
AND/AA
MCH
1A
27-Feb-15
First Issuance
YMT
AA
MCH
REV
DATE
DESCRIPTION
PREPARED
CHECKED
APPROVED
Suban Compression Facilities Process Datasheet for Inlet Compressor ConocoPhillips (Grissik) Ltd.
D oc . N o
: B -8 45 67- SB -P P0 -D SR -S T- 23 -0 00 9 R ev . 3
Page 7 of 8
Process Data Sheet for Centrifugal Compressor 1
Skid No.
:
23SAE-100/200/300/400/500
Client
: ConocoPhillips (Grissik) Ltd.
Tag No.
:
23CAE-100/200/300/400/500 (1st Stage) and 23CAE-101/201/301/401/501 (2nd Stage)
Location
: Suban Gas Plant
2 Equipment Name : Inlet Compressor 3 PRODUCTION PROFILE TIMELINE 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 NOTES 60 61 62 63 64 29-Jul-15 3 24-Jun-15 2 04-May-15 1C 30-Mar-15 1B 27-Feb-15 1A REV DATE
ConocoPhillips (Grissik) Ltd.
Re-Issued for Use Issued for Use Re-Issued for Approval Issued for Approval First Issuance DESCRIPTION
Doc. No
YMT JAZ/YHT YMT JAZ/YHT YMT JAZ/AA YMT AND/AA YMT AA PREPARED CHECKED Suban Compression Facilities Process Datasheet for Inlet Compressor : B-84567-SB-PP0-DSR-ST-23-0009 Rev. 3
MCH MCH MCH MCH MCH APPROVED
Page 8 of 8
