50 mmscfd 5 PC H2S Amine Run SS3 R1

– Simulation Report –
Project:
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
Company:
Plant:
Location:
Project:
Description:
File Name:
Run Date:
Run Time:
Product Version:
Engine Build:
GUI Build:
Constructora Subacuatica DIAVAZ S.A. de C.V. / DIAVAZ Servicios de Producción S.A. de C.V.
Gas Sweetener Plant
Dos Bocas, Paraiso, Tabasco, Mexico
Sistema de Endulzamiento y Compresion de Gas Terminal Martitima Dos Bocas para el Sistema
Artifcial de Produccion Bombeo Neumatico
50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
10/11/2022
9:43:00
ProTreat 7.0
7.0.0.001
7.0.0.220
Report Nomenclature:
*
Asterisks denote engine calculated values
Legal Notice:
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Optimized Gas Treating, Inc.
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C:\Users\delarosa.VALKOR\Crosstrails\Operations Documents\05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Flowsheet
Page 2 of 27
Company:
Plant:
Location:
Project:
Constructora Subacuatica DIAVAZ S.A. de C.V. / DIAVAZ Servicios de Producción S.A. de C.V.
Report Date:
10/11/2022
Gas Sweetener Plant
Run Date:
10/11/2022
Dos Bocas, Paraiso, Tabasco, Mexico
Sistema de Endulzamiento y Compresion de Gas Terminal Martitima Dos Bocas para el Sistema Artifcial de Produccion Bombeo Neumatico
Diavaz -DOS BOCAS
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Stream Table
Page 3 of 27
Company:
Plant:
Location:
Project:
Constructora Subacuatica DIAVAZ S.A. de C.V. / DIAVAZ Servicios de Producción S.A. de C.V.
Gas Sweetener Plant
Dos Bocas, Paraiso, Tabasco, Mexico
Sistema de Endulzamiento y Compresion de Gas Terminal Martitima Dos Bocas para el Sistema Artifcial de Produccion Bombeo Neumatico
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Stream Table
Page 4 of 27
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Stream Table
Page 5 of 27
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Material Streams Report
Page 6 of 27
Stream Number
Stream Name
Temperature
Fahrenheit
Pressure
psia
Vapor Fraction
Overall
Molecular Weight
Mass Flow
lb/hr
Liquid Volume Flow
USgal/min
Vapor Volume Flow
MMSCFD
Std Liquid Volume Flow Std USgal/min
Enthalpy
Btu/lb
Entropy
Btu/lb-R
Heat Capacity
Btu/lb-R
Density
lb/cuft
Viscosity
cP
Thermal Conductivity Btu/hr-ft-F
Cp/Cv
ZFactor
Surface Tension
dyne/cm
Vapour Pressure
psia
pH
Components
Nitrogen
mol %
Carbon Dioxide
mol %
Hydrogen Sulfide
mol %
Methane
mol %
Ethane
mol %
Propane
mol %
Isobutane
mol %
n-Butane
mol %
Isopentane
mol %
n-Pentane
mol %
n-Hexane
mol %
Water
mol %
GAS/SPEC SS-3
mol %
Total Flow
lbmol/hr
Custom Special Concentrations
GAS/SPEC SS-3
wt %
Water
mol %
Water
mol %
Carbon Dioxide
Loading
Hydrogen Sulfide
Loading
Hydrogen Sulfide
mol %
Carbon Dioxide
mol %
1
2
3
4
5
6
7
8
9
10
130.0000
1014.7000
1.0000
139.0617
1011.9506
1.0000
174.3657
1014.7000
0.0000E+00
177.1038
89.7000
1.0000
177.1038
89.7000
0.0000E+00
210.0000
84.7000
0.0095
195.0491
34.7000
0.0279
210.9258
24.7000
1.0000
130.0000
19.7000
1.0000
130.0000
19.7000
0.0000E+00
24.1921
1.3282E+05
23.1467
1.1747E+05
31.6322
2.3247E+05
439.8920
30.2600
540.6108
31.6356
2.3193E+05
440.1926
31.6356
2.3193E+05
31.6356
2.3193E+05
25.8216
2.5346E+04
35.0377
1.5754E+04
18.0317
9592.1399
19.4353
50.0000
46.2202
8.9395
4.0949
-1.5305E+01 -8.4991E+00
-2.7523E-01 -2.9110E-01
0.6094
0.6306
4.9625
4.5370
0.0116
0.0115
0.0161
0.0174
1.5821
1.5203
0.7817
0.8035
0.1627
422.1105
-5.9777E+02
-8.2207E-01
0.7204
65.8870
1.9067
0.2547
30.3577
0.0423
0.3497
0.4054
0.0143
0.0145
1.2572
0.9799
421.8789
-5.9925E+02 -5.6838E+02 -5.6837E+02
-8.1171E-01 -7.6178E-01 -7.6219E-01
0.7235
65.6889
24.7980
5.2097
1.8335
0.2550
41.7624
974.4545
7.9444
3.0237
2.9908
4.9847
61.4843
15.1462
8.7776
0.8855
1.8927
0.2499
0.2276
0.0307
0.3062
0.0000E+00
5490.1771
3.2693
0.6377
9.8563E-05
66.3892
16.3497
9.4746
0.9574
2.0439
0.2701
0.2458
0.0331
0.3287
4.4311E-04
5075.1414
0.0012
1.7943
3.7264
0.0851
0.0242
0.0144
3.2543E-04
0.0025
1.8289E-04
3.1800E-04
5.3198E-05
81.9161
12.4349
7349.2360
41.5748
89.7000
7.9267
0.4670
27.8504
16.0735
33.1520
9.1868
5.3288
0.1302
0.9160
0.0701
0.1141
0.0178
6.6919
0.0013
17.8655
1.5447E-05
1.7308
3.6963
0.0045
0.0019
0.0014
8.9861E-06
2.4527E-04
1.2398E-05
4.0768E-05
1.0003E-05
82.0994
12.4652
7331.3705
46.7430
81.9161
0.3062
0.3287
41.6844
0.1014
0.3298
0.0895
0.0144
0.0129
1.3185
0.9900
1.5447E-05
1.7308
3.6963
0.0045
0.0019
0.0014
8.9861E-06
2.4527E-04
1.2398E-05
4.0768E-05
1.0003E-05
82.0994
12.4652
7331.3705
1.5447E-05
1.7308
3.6963
0.0045
0.0019
0.0014
8.9861E-06
2.4527E-04
1.2398E-05
4.0768E-05
1.0003E-05
82.0994
12.4652
7331.3705
1.1612E-04
12.9333
27.6353
0.0338
0.0144
0.0108
6.7886E-05
0.0018
9.3360E-05
3.0524E-04
7.5477E-05
59.3699
9.1360E-11
981.5895
19.1931
12.0532 -9.9613E+02
0.0570 -1.4786E+00
0.2447
0.9991
0.1099
61.5316
0.0143
0.5063
0.0101
0.3541
1.3125
0.9924
53.7485
19.7000
3.9538
2.5350E-04
28.2204
60.2309
0.0738
0.0313
0.0235
1.4820E-04
0.0040
2.0381E-04
6.6637E-04
1.6477E-04
11.4146
1.0925E-18
449.6305
46.8520
82.0994
6.6919
0.1443
0.2997
3.7264
1.7943
1.1117E-09
99.9034
59.3699
0.1389
0.2965
3.6963
1.7308
3.0587E-09
0.0122
0.0843
1.6803E-06
7.8509E-07
4.5210E-07
1.1727E-09
7.1128E-08
1.2561E-09
6.3180E-09
1.0497E-09
99.9034
1.6858E-10
531.9590
11.4146
7.2538E+07
5.0029E+08
0.0843
0.0122
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Material Streams Report
Page 7 of 27
Vapor
Molecular Weight
Mass Flow
lb/hr
Vapor Volume Flow
MMSCFD
Std Liquid Volume Flow Std USgal/min
Enthalpy
Btu/lb
Entropy
Btu/lb-R
Heat Capacity
Btu/lb-R
Density
lb/cuft
Viscosity
cP
Thermal Conductivity Btu/hr-ft-F
Cp/Cv
ZFactor
Surface Tension
dyne/cm
Vapour Pressure
psia
pH
Components
Nitrogen
mol %
Carbon Dioxide
mol %
Hydrogen Sulfide
mol %
Methane
mol %
Ethane
mol %
Propane
mol %
Isobutane
mol %
n-Butane
mol %
Isopentane
mol %
n-Pentane
mol %
n-Hexane
mol %
Water
mol %
GAS/SPEC SS-3
mol %
Total Flow
lbmol/hr
Custom Special Concentrations
GAS/SPEC SS-3
wt %
Water
mol %
Water
mol %
Carbon Dioxide
Loading
Hydrogen Sulfide
Loading
Hydrogen Sulfide
mol %
Carbon Dioxide
mol %
24.1921
1.3282E+05
50.0000
23.1467
1.1747E+05
46.2202
30.2600
540.6108
0.1627
36.9463
2569.7535
0.6334
33.6395
6883.4471
1.8635
25.8216
2.5346E+04
8.9395
35.0377
1.5754E+04
4.0949
-1.5305E+01 -8.4991E+00
-2.7523E-01 -2.9110E-01
0.6094
0.6306
4.9625
4.5370
0.0116
0.0115
0.0161
0.0174
1.5821
1.5203
0.7817
0.8035
30.3577
0.0423
0.3497
0.4054
0.0143
0.0145
1.2572
0.9799
29.4551
0.0105
0.2508
0.4445
0.0169
0.0126
1.3045
0.9796
29.0026
0.0635
0.2637
0.1679
0.0158
0.0122
1.3038
0.9896
41.6844
0.1014
0.3298
0.0895
0.0144
0.0129
1.3185
0.9900
12.0532
0.0570
0.2447
0.1099
0.0143
0.0101
1.3125
0.9924
3.0237
2.9908
4.9847
61.4843
15.1462
8.7776
0.8855
1.8927
0.2499
0.2276
0.0307
0.3062
0.0000E+00
5490.1771
3.2693
0.6377
9.8563E-05
66.3892
16.3497
9.4746
0.9574
2.0439
0.2701
0.2458
0.0331
0.3287
4.4311E-04
5075.1414
0.4670
27.8504
16.0735
33.1520
9.1868
5.3288
0.1302
0.9160
0.0701
0.1141
0.0178
6.6919
0.0013
17.8655
0.0016
52.9358
31.7333
0.4694
0.1976
0.1469
9.4243E-04
0.0251
0.0013
0.0041
9.8340E-04
14.4774
0.0055
69.5538
5.5316E-04
37.5462
36.3112
0.1618
0.0686
0.0515
3.2167E-04
0.0087
4.4293E-04
0.0015
3.5445E-04
25.8415
0.0074
204.6241
1.1612E-04
12.9333
27.6353
0.0338
0.0144
0.0108
6.7886E-05
0.0018
9.3360E-05
3.0524E-04
7.5477E-05
59.3699
9.1360E-11
981.5895
2.5350E-04
28.2204
60.2309
0.0738
0.0313
0.0235
1.4820E-04
0.0040
2.0381E-04
6.6637E-04
1.6477E-04
11.4146
1.0925E-18
449.6305
0.3062
0.3062
0.3287
0.3287
6.6919
6.6919
14.4774
25.8415
59.3699
59.3699
11.4146
11.4146
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Material Streams Report
Page 8 of 27
Aqueous
Molecular Weight
Mass Flow
lb/hr
Liquid Volume Flow
USgal/min
Std Liquid Volume Flow Std USgal/min
Enthalpy
Btu/lb
Entropy
Btu/lb-R
Heat Capacity
Btu/lb-R
Density
lb/cuft
Viscosity
cP
Thermal Conductivity Btu/hr-ft-F
Cp/Cv
ZFactor
Surface Tension
dyne/cm
Vapour Pressure
psia
pH
Components
Nitrogen
mol %
Carbon Dioxide
mol %
Hydrogen Sulfide
mol %
Methane
mol %
Ethane
mol %
Propane
mol %
Isobutane
mol %
n-Butane
mol %
Isopentane
mol %
n-Pentane
mol %
n-Hexane
mol %
Water
mol %
GAS/SPEC SS-3
mol %
Total Flow
lbmol/hr
Custom Special Concentrations
GAS/SPEC SS-3
wt %
Water
mol %
Water
mol %
Carbon Dioxide
Loading
Hydrogen Sulfide
Loading
Hydrogen Sulfide
mol %
Carbon Dioxide
mol %
31.6322
2.3247E+05
439.8920
422.1105
-5.9777E+02
-8.2207E-01
0.7204
65.8870
1.9067
0.2547
31.6356
31.5847
31.5780
2.3193E+05 2.2936E+05 2.2505E+05
440.1926
445.3129
438.3482
421.8789
420.1735
416.4646
-5.9925E+02 -5.7507E+02 -5.8664E+02
-8.1171E-01 -7.7043E-01 -7.8744E-01
0.7235
0.7806
0.7711
65.6889
64.2142
64.0076
1.8335
1.2234
1.4013
0.2550
0.2584
0.2564
18.0317
9592.1399
19.4353
19.1931
-9.9613E+02
-1.4786E+00
0.9991
61.5316
0.5063
0.3541
41.7624
974.4545
7.9444
0.0063
41.5748
89.7000
7.9267
0.0058
39.2887
84.7000
7.6802
0.0024
40.3037
34.7000
7.9509
9.1228E-04
53.7485
19.7000
3.9538
0.0012
1.7943
3.7264
0.0851
0.0242
0.0144
3.2543E-04
0.0025
1.8289E-04
3.1800E-04
5.3198E-05
81.9161
12.4349
7349.2360
1.5447E-05
1.7308
3.6963
0.0045
0.0019
0.0014
8.9861E-06
2.4527E-04
1.2398E-05
4.0768E-05
1.0003E-05
82.0994
12.4652
7331.3705
5.9630E-08
1.2404
3.4278
7.3530E-05
4.7485E-05
5.0718E-05
4.5503E-08
7.6358E-06
2.0289E-07
1.5985E-06
6.7966E-07
82.7471
12.5845
7261.8167
8.8136E-09
0.7026
2.7600
1.0996E-05
7.2731E-06
7.5804E-06
8.9047E-09
1.2163E-06
3.6659E-08
2.7034E-07
1.1381E-07
83.7146
12.8228
7126.7464
3.0587E-09
0.0122
0.0843
1.6803E-06
7.8509E-07
4.5210E-07
1.1727E-09
7.1128E-08
1.2561E-09
6.3180E-09
1.0497E-09
99.9034
1.6858E-10
531.9590
46.7430
81.9161
81.9161
0.1443
0.2997
3.7264
1.7943
46.8520
82.0994
82.0994
0.1389
0.2965
3.6963
1.7308
47.3767
82.7471
48.2841
83.7146
0.0986
0.2724
0.0548
0.2152
1.1117E-09
99.9034
99.9034
7.2538E+07
5.0029E+08
0.0843
0.0122
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Material Streams Report
Page 9 of 27
Liquid
Molecular Weight
Mass Flow
lb/hr
Liquid Volume Flow
USgal/min
Std Liquid Volume Flow Std USgal/min
Enthalpy
Btu/lb
Entropy
Btu/lb-R
Heat Capacity
Btu/lb-R
Density
lb/cuft
Viscosity
cP
Thermal Conductivity Btu/hr-ft-F
Cp/Cv
ZFactor
Surface Tension
dyne/cm
Vapour Pressure
psia
pH
Components
Nitrogen
mol %
Carbon Dioxide
mol %
Hydrogen Sulfide
mol %
Methane
mol %
Ethane
mol %
Propane
mol %
Isobutane
mol %
n-Butane
mol %
Isopentane
mol %
n-Pentane
mol %
n-Hexane
mol %
Water
mol %
GAS/SPEC SS-3
mol %
Total Flow
lbmol/hr
Custom Special Concentrations
GAS/SPEC SS-3
wt %
Water
mol %
Water
mol %
Carbon Dioxide
Loading
Hydrogen Sulfide
Loading
Hydrogen Sulfide
mol %
Carbon Dioxide
mol %
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Material Streams Report
Page 10 of 27
11
12
13
14
15
16
17
18
19
20
21
22
23
249.0409
27.0723
0.0000E+00
250.1352
27.0723
1.0000
250.1352
27.0723
0.0000E+00
250.1725
80.0000
0.0000E+00
210.6097
75.0000
0.0000E+00
135.0000
65.0000
0.0000E+00
136.4643
1289.7000
0.0000E+00
136.4643
1289.7000
0.0000E+00
136.4643
1289.7000
0.0000E+00
177.1037
89.7000
0.0024
130.0000
1006.9506
0.9996
129.9998
1006.9506
1.0000
129.9998
1006.9506
0.0000E+00
29.1443
2.4177E+05
499.7482
18.0995
2.5591E+04
31.4135
2.1618E+05
446.3252
31.4135
2.1618E+05
446.3346
31.4135
2.1618E+05
437.0006
31.4135
2.1618E+05
422.4532
31.4135
2.1618E+05
422.6971
31.3124
2.1712E+05
424.6089
31.3124
2.1712E+05
424.6097
31.6322
2.3247E+05
23.1467
1.1747E+05
23.1480
1.1744E+05
19.3991
36.0504
0.0716
12.8767
462.6782
-5.8119E+02
-7.8373E-01
0.8620
60.3143
0.7188
0.2757
75.1598
0.0560
0.4624
0.0652
0.0129
0.0150
1.3312
0.9861
37.2418
27.0127
8.4020
0.0000E+00
0.0013
0.0085
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
88.9609
11.0294
8295.5321
0.0000E+00
0.0069
0.0364
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
99.8807
0.0760
1413.9095
44.9989
88.9609
46.2202
46.2033
411.7827
411.7827
411.7827
411.7827
411.7827
413.6685
413.6693
0.0706
-5.4383E+02 -5.4364E+02 -5.7676E+02 -6.3849E+02 -6.3366E+02 -6.3526E+02 -6.3526E+02 -5.9778E+02 -1.4290E+01 -1.4007E+01 -9.3596E+02
-7.2156E-01 -7.2710E-01 -7.7681E-01 -8.7871E-01 -8.7695E-01 -8.7957E-01 -8.7957E-01 -8.0973E-01 -3.0205E-01 -3.0172E-01 -1.3820E+00
0.8454
0.8447
0.8291
0.8033
0.8051
0.8059
0.8059
0.6353
0.9390
60.3851
60.3839
61.6736
63.7974
63.7606
63.7519
63.7519
47.7927
4.6479
4.6466
62.7907
0.8439
0.8437
1.2066
3.1535
3.0821
3.0509
3.0509
0.0113
0.5606
0.2603
0.2603
0.2579
0.2480
0.2483
0.2489
0.2489
0.0170
0.3537
1.5475
0.7927
36.3849
36.3822
39.2184
44.3646
44.2678
44.3069
44.3070
52.4177
27.0723
27.0934
12.7953
2.2124
2.3000
2.3027
2.3027
1006.9506
8.3763
8.3759
8.7655
9.6266
9.6083
9.6081
9.6081
7.9638
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0063E-04
0.0027
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.8175
13.1796
6934.1222
0.0000E+00
1.0064E-04
0.0027
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.8176
13.1796
6934.1457
50.2667
86.7173
50.2667
86.7173
50.2667
86.7173
50.2667
86.7173
50.2667
86.7173
50.0485
86.8175
50.0484
86.8176
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
7.6352E-06
2.0818E-04
0.0027
1.0063E-04
7.6360E-06
2.0839E-04
0.0027
1.0064E-04
99.8807
1.1443E-04
7.7079E-04
0.0085
0.0013
0.0012
1.7943
3.7264
0.0851
0.0242
0.0144
3.2543E-04
0.0025
1.8289E-04
3.1800E-04
5.3198E-05
81.9161
12.4349
7349.2360
3.2693
0.6377
9.8563E-05
66.3892
16.3497
9.4746
0.9574
2.0439
0.2701
0.2458
0.0331
0.3287
4.4311E-04
5075.1414
3.2705
0.6376
9.8549E-05
66.4135
16.3557
9.4781
0.9578
2.0446
0.2702
0.2458
0.0332
0.2929
1.2661E-05
5073.2830
0.0019
0.7419
1.3687E-04
0.0690
0.0137
0.0048
1.6136E-04
7.3278E-04
3.0084E-05
4.0022E-05
2.9771E-06
97.9920
1.1756
1.8584
7.2056
97.9920
0.3287
0.2929
0.6311
1.1643E-04
1.3687E-04
0.7419
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Material Streams Report
Page 11 of 27
18.0995
2.5591E+04
12.8767
30.2594
540.5017
0.1627
75.1598
0.0560
0.4624
0.0652
0.0129
0.0150
1.3312
0.9861
23.1480
1.1744E+05
46.2033
23.1480
1.1744E+05
46.2033
30.3587 -1.4007E+01 -1.4007E+01
0.0423 -3.0172E-01 -3.0172E-01
0.3497
0.6353
0.6353
0.4053
4.6466
4.6466
0.0143
0.0113
0.0113
0.0145
0.0170
0.0170
1.2572
1.5475
1.5475
0.9799
0.7927
0.7927
0.0000E+00
0.0069
0.0364
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
99.8807
0.0760
1413.9095
0.4670
27.8480
16.0721
33.1550
9.1876
5.3292
0.1302
0.9161
0.0702
0.1141
0.0178
6.6913
0.0013
17.8623
3.2705
0.6376
9.8549E-05
66.4135
16.3557
9.4781
0.9578
2.0446
0.2702
0.2458
0.0332
0.2929
1.2655E-05
5073.2822
3.2705
0.6376
9.8549E-05
66.4135
16.3557
9.4781
0.9578
2.0446
0.2702
0.2458
0.0332
0.2929
1.2661E-05
5073.2830
99.8807
99.8807
6.6913
0.2929
0.2929
0.2929
0.2929
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Material Streams Report
Page 12 of 27
29.1443
2.4177E+05
499.7482
462.6782
-5.8119E+02
-7.8373E-01
0.8620
60.3143
0.7188
0.2757
31.4135
31.4135
31.4135
31.4135
31.4135
31.3124
31.3124
31.6356
19.3986
2.1618E+05 2.1618E+05 2.1618E+05 2.1618E+05 2.1618E+05 2.1712E+05 2.1712E+05 2.3193E+05
36.0653
446.3252
446.3346
437.0006
422.4532
422.6971
424.6089
424.6097
440.1927
0.0716
411.7827
411.7827
411.7827
411.7827
411.7827
413.6685
413.6693
421.8790
0.0706
-5.4383E+02 -5.4364E+02 -5.7676E+02 -6.3849E+02 -6.3366E+02 -6.3526E+02 -6.3526E+02 -5.9925E+02 -9.3598E+02
-7.2156E-01 -7.2710E-01 -7.7681E-01 -8.7871E-01 -8.7695E-01 -8.7957E-01 -8.7957E-01 -8.1171E-01 -1.3820E+00
0.8454
0.8447
0.8291
0.8033
0.8051
0.8059
0.8059
0.7235
0.9391
60.3851
60.3839
61.6736
63.7974
63.7606
63.7519
63.7519
65.6889
62.7906
0.8439
0.8437
1.2066
3.1535
3.0821
3.0509
3.0509
1.8335
0.5605
0.2603
0.2603
0.2579
0.2480
0.2483
0.2489
0.2489
0.2550
0.3537
19.3991
36.0504
0.0716
0.0706
-9.3596E+02
-1.3820E+00
0.9390
62.7907
0.5606
0.3537
37.2418
27.0127
8.4020
0.0018
36.3849
27.0723
8.3763
0.0055
36.3822
27.0934
8.3759
0.0053
39.2184
12.7953
8.7655
0.0050
44.3646
2.2124
9.6266
0.0993
44.2678
2.3000
9.6083
0.0990
44.3069
2.3027
9.6081
0.0990
44.3070
2.3027
9.6081
0.0063
41.5748
89.7000
7.9267
0.0492
52.4181
1006.9506
7.9634
0.0492
52.4177
1006.9506
7.9638
0.0000E+00
0.0013
0.0085
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
88.9609
11.0294
8295.5321
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0140E-04
0.0028
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.7173
13.2798
6881.6227
0.0000E+00
1.0063E-04
0.0027
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.8175
13.1796
6934.1222
0.0000E+00
1.0064E-04
0.0027
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
0.0000E+00
86.8176
13.1796
6934.1457
1.5450E-05
1.7308
3.6964
0.0045
0.0019
0.0014
8.9877E-06
2.4531E-04
1.2400E-05
4.0774E-05
1.0004E-05
82.0994
12.4652
7331.3737
0.0019
0.7419
1.3686E-04
0.0690
0.0137
0.0048
1.6136E-04
7.3279E-04
3.0082E-05
4.0020E-05
2.9768E-06
97.9925
1.1751
1.8592
0.0019
0.7419
1.3687E-04
0.0690
0.0137
0.0048
1.6136E-04
7.3278E-04
3.0084E-05
4.0022E-05
2.9771E-06
97.9920
1.1756
1.8584
44.9989
88.9609
88.9609
1.1443E-04
7.7079E-04
0.0085
0.0013
50.2667
86.7173
86.7173
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
50.2667
86.7173
86.7173
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
50.2667
86.7173
86.7173
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
50.2667
86.7173
86.7173
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
50.2667
86.7173
86.7173
7.6355E-06
2.0819E-04
0.0028
1.0140E-04
50.0485
86.8175
86.8175
7.6352E-06
2.0818E-04
0.0027
1.0063E-04
50.0484
86.8176
86.8176
7.6360E-06
2.0839E-04
0.0027
1.0064E-04
46.8519
82.0994
7.2031
97.9925
0.1389
0.2965
0.6313
1.1647E-04
7.2056
97.9920
97.9920
0.6311
1.1643E-04
1.3687E-04
0.7419
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Material Streams Report
Page 13 of 27
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Column Blocks
Page 14 of 27
Absorber [Column Block]
Convergence
Iterations Specified
Iterations Used
Tolerance Specified
Tolerance Reached
100
6
0.0010
5.1909E-04
Models
OGT Gas Treating Thermodynamics
Reaction Kinetic Model Used for CO2: ProTreat Default used Finite Rate Irreversible
Approach to Equilibrium
Rich/Equilibrium Load CO2
Rich/Sour Pressure CO2
Rich/Equilibrium Load H2S
Rich/Sour Pressure H2S
1.4091
0.9566
0.5124
0.3697
Liquid Hold Up Volume
Section 1
Total
1.8733 cum
1.8733 cum
Internals
Nutter Float Valve
Rate Model Adjustments Applied
Low-Weir-Load Correction
Number of Trays
Tray Spacing
Trayed Height
Number of Passes
Weir Height
DC Clearance
Foam Derating Factor
Diameter *
% Vapor Flood *
% Downcomer Choke *
% Downcomer Backup
DC Choke Correlation:
Tray Active Area As % Column Area *
Tray Active Area *
Inlet DC Area as % Column Area*
Inlet DC Area *
Outlet DC Area as % Column Area*
Outlet DC Area *
Total DC Area As % Column Area *
Total DC Area *
Side DC Width *
Side Weir Length *
Min Weir Load *
Max Weir Load *
Section Pressure Drop*
Highest Liquid Temp*
Segment with Highest Liquid Temp
Lowest Liquid Temp*
Segment with Lowest Liquid Temp
Highest Vapor Temp*
Segment with Highest Vapor Temp
Lowest Vapor Temp*
Segment with Lowest Vapor Temp
20
1.0000
20.0000
1
3.0000
0.0000E+00
0.8000
4.8085
70.0000
70.0000
0.0000E+00
Hydraulic (Default)
70.3957
12.7837
14.8021
2.6880
14.8021
2.6880
29.6043
5.3761
11.8585
3.8860
109.4118
113.2955
feet
feet
in
feet
feet
sqft
sqft
sqft
sqft
in
feet
USgpm/ft
USgpm/ft
2.7494 psi
188.2274
18
138.8725
1
187.8802
18
139.0657
1
Fahrenheit
Fahrenheit
Fahrenheit
Fahrenheit
Draw stream 3 connects at bottom of column
Draw stream 2 connects at top of column
Feed stream 1 connects below bottom tray
Feed stream 19 connects above top tray
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Column Blocks
Page 15 of 27
Vapor Phase
Sec:Seg
Temperature
Fahrenheit
1:1
1:2
1:3
1:4
1:5
1:6
1:7
1:8
1:9
1:10
1:11
1:12
1:13
1:14
1:15
1:16
1:17
1:18
1:19
1:20
Pressure
psia
139.0657
140.7027
142.5328
144.5560
146.7763
149.1926
151.7984
154.5841
157.5405
160.6654
163.9720
167.4929
171.2714
175.3217
179.5416
183.5961
186.7943
187.8802
184.3290
170.0935
Molec Wt
1:1
1:2
1:3
1:4
1:5
1:6
1:7
1:8
1:9
1:10
1:11
1:12
1:13
1:14
1:15
1:16
1:17
1:18
1:19
1:20
1011.9506
1012.0830
1012.2158
1012.3490
1012.4824
1012.6163
1012.7507
1012.8855
1013.0208
1013.1567
1013.2931
1013.4301
1013.5678
1013.7062
1013.8453
1013.9853
1014.1263
1014.2682
1014.4112
1014.5551
Density
lb/cuft
23.1567
23.1787
23.2041
23.2324
23.2637
23.2980
23.3351
23.3746
23.4163
23.4594
23.5035
23.5482
23.5933
23.6396
23.6882
23.7404
23.7981
23.8657
23.9562
24.1007
Total Flow
Carbon Dioxide
lbmol/hr
lbmol/hr
mol %
5075.1414
32.3625
5096.3250
37.6967
5103.0780
43.7365
5110.7002
50.5357
5119.2403
58.1252
5128.7268
66.5167
5139.1644
75.6960
5150.5308
85.6162
5162.7793
96.1901
5175.8538
107.2826
5189.7266
118.7010
5204.4739
130.1811
5220.3961
141.3607
5238.1448
151.7363
5258.7223
160.6148
5283.1003
167.1240
5311.4406
170.4185
5342.6963
170.1742
5376.0559
167.2386
5416.3574
164.0723
4.5376
4.5189
4.4986
4.4765
4.4527
4.4274
4.4007
4.3728
4.3439
4.3141
4.2831
4.2507
4.2165
4.1808
4.1450
4.1131
4.0922
4.0947
4.1486
4.3355
Viscosity
Cp
cP
Btu/lb-R
0.0115
0.0115
0.0115
0.0116
0.0116
0.0117
0.0117
0.0118
0.0119
0.0119
0.0120
0.0121
0.0121
0.0122
0.0123
0.0124
0.0125
0.0125
0.0125
0.0123
9.9741E-04
0.0012
0.0015
0.0019
0.0024
0.0033
0.0050
0.0091
0.0193
0.0456
0.1117
0.2725
0.6435
1.4416
3.0111
5.7750
10.0822
16.0821
23.8902
34.2841
CO2 Eqm
CO2 Act
psia
psia
0.0448
0.1228
0.2480
0.4395
0.7224
1.1295
1.7023
2.4916
3.5577
4.9716
6.8189
9.2107
12.2988
16.2732
21.2687
27.1009
32.9164
37.0818
37.3570
30.5564
0.6302
0.6287
0.6271
0.6253
0.6234
0.6213
0.6192
0.6171
0.6149
0.6127
0.6105
0.6083
0.6061
0.6040
0.6018
0.5997
0.5977
0.5958
0.5952
0.5937
0.6377
0.7397
0.8571
0.9888
1.1354
1.2969
1.4729
1.6623
1.8631
2.0728
2.2872
2.5013
2.7079
2.8968
3.0543
3.1634
3.2085
3.1852
3.1108
3.0292
Hydrogen Sulfide
lbmol/hr
mol %
0.0050
9.8563E-05
0.0062
1.2182E-04
0.0076
1.4991E-04
0.0095
1.8567E-04
0.0121
2.3635E-04
0.0165
3.2121E-04
0.0253
4.9301E-04
0.0461
8.9497E-04
0.0984
0.0019
0.2327
0.0045
0.5721
0.0110
1.3996
0.0269
3.3144
0.0635
7.4493
0.1422
15.6183
0.2970
30.0890
0.5695
52.8053
0.9942
84.7128
1.5856
126.6102
2.3551
183.0312
3.3792
Enthalpy
Btu/lb
-7.9973E+00
-6.9279E+00
-5.7416E+00
-4.4405E+00
-3.0253E+00
-1.5002E+00
0.1281
1.8522
3.6667
5.5733
7.5836
9.7171
11.9854
14.3546
16.6855
18.6686
19.7339
18.7835
13.2928
8.9526
Equilibrium and Actual Partial Pressure
H2S Eqm
psia
1:1
1:2
1:3
1:4
1:5
1:6
1:7
1:8
1:9
1:10
1:11
1:12
1:13
1:14
1:15
1:16
1:17
1:18
1:19
1:20
H2S Act
psia
8.9505E-04
0.0011
0.0014
0.0017
0.0020
0.0025
0.0033
0.0047
0.0081
0.0172
0.0418
0.1077
0.2750
0.6720
1.5318
3.1921
5.9871
10.0319
14.9743
19.5494
6.4529
7.4862
8.6753
10.0103
11.4960
13.1331
14.9171
16.8370
18.8741
21.0002
23.1764
25.3492
27.4459
29.3646
30.9654
32.0761
32.5384
32.3062
31.5563
30.7329
H2O Eqm
H2O Act
psia
psia
3.2735
3.4054
3.5584
3.7342
3.9356
4.1652
4.4255
4.7188
5.0478
5.4161
5.8296
6.2983
6.8352
7.4526
8.1460
8.8660
9.4802
9.7269
9.1927
7.1255
3.3261
3.4627
3.6236
3.8082
4.0191
4.2588
4.5299
4.8348
5.1766
5.5598
5.9913
6.4812
7.0404
7.6719
8.3522
9.0001
9.4407
9.3696
8.3500
6.0263
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Column Blocks
Page 16 of 27
Liquid Phase
Sec:Seg
Temperature
Fahrenheit
1:1
1:2
1:3
1:4
1:5
1:6
1:7
1:8
1:9
1:10
1:11
1:12
1:13
1:14
1:15
1:16
1:17
1:18
1:19
1:20
Pressure
psia
138.8725
140.4983
142.3070
144.3084
146.5072
148.9027
151.4890
154.2562
157.1946
160.3002
163.5840
167.0774
170.8266
174.8575
179.0925
183.2348
186.6542
188.2274
185.7967
174.3657
Molec Wt
1:1
1:2
1:3
1:4
1:5
1:6
1:7
1:8
1:9
1:10
1:11
1:12
1:13
1:14
1:15
1:16
1:17
1:18
1:19
1:20
1012.0830
1012.2158
1012.3490
1012.4824
1012.6163
1012.7507
1012.8855
1013.0208
1013.1567
1013.2931
1013.4301
1013.5678
1013.7062
1013.8453
1013.9853
1014.1263
1014.2682
1014.4112
1014.5551
1014.7000
Density
lb/cuft
31.3022
31.3119
31.3227
31.3346
31.3477
31.3619
31.3771
31.3931
31.4095
31.4260
31.4422
31.4575
31.4713
31.4834
31.4937
31.5033
31.5149
31.5346
31.5719
31.6322
63.8425
63.8608
63.8815
63.9047
63.9302
63.9577
63.9869
64.0171
64.0475
64.0772
64.1053
64.1318
64.1590
64.1929
64.2429
64.3207
64.4434
64.6507
65.0469
65.8870
Total Flow
Carbon Dioxide
lbmol/hr
lbmol/hr
mol %
6955.3293
5.3412
6962.0834
11.3820
6969.7070
18.1822
6978.2487
25.7730
6987.7370
34.1660
6998.1767
43.3469
7009.5455
53.2687
7021.7967
63.8444
7034.8740
74.9388
7048.7501
86.3592
7063.5007
97.8413
7079.4267
109.0229
7097.1782
119.4002
7117.7588
128.2802
7142.1405
134.7907
7170.4851
138.0861
7201.7449
137.8423
7235.1076
134.9068
7275.4122
131.7405
7349.2360
131.8693
Viscosity
Cp
cP
Btu/lb-R
2.9609
2.9119
2.8593
2.8030
2.7435
2.6812
2.6165
2.5500
2.4818
2.4119
2.3393
2.2619
2.1770
2.0821
1.9776
1.8697
1.7719
1.7067
1.7149
1.9067
0.8077
0.8056
0.8034
0.8010
0.7984
0.7956
0.7927
0.7898
0.7867
0.7837
0.7807
0.7777
0.7746
0.7711
0.7668
0.7613
0.7541
0.7439
0.7275
0.6956
0.0768
0.1635
0.2609
0.3693
0.4889
0.6194
0.7599
0.9092
1.0652
1.2252
1.3852
1.5400
1.6824
1.8023
1.8873
1.9258
1.9140
1.8646
1.8108
1.7943
Hydrogen Sulfide
lbmol/hr
mol %
0.1917
0.1931
0.1949
0.1975
0.2019
0.2108
0.2315
0.2839
0.4181
0.7575
1.5850
3.4998
7.6349
15.8044
30.2761
52.9942
84.9040
126.8037
183.2264
273.8645
Enthalpy
Sigma
Btu/lb
dyne/cm
-6.3301E+02
-6.3160E+02
-6.3003E+02
-6.2828E+02
-6.2637E+02
-6.2430E+02
-6.2207E+02
-6.1970E+02
-6.1719E+02
-6.1457E+02
-6.1181E+02
-6.0890E+02
-6.0579E+02
-6.0243E+02
-5.9886E+02
-5.9528E+02
-5.9215E+02
-5.9026E+02
-5.9107E+02
-5.9777E+02
0.0028
0.0028
0.0028
0.0028
0.0029
0.0030
0.0033
0.0040
0.0059
0.0107
0.0224
0.0494
0.1076
0.2220
0.4239
0.7391
1.1789
1.7526
2.5184
3.7264
pH
44.1479
44.0406
43.9211
43.7888
43.6431
43.4843
43.3125
43.1283
42.9325
42.7251
42.5053
42.2710
42.0189
41.7470
41.4601
41.1778
40.9425
40.8306
40.9900
41.7624
9.4815
9.3773
9.2795
9.1862
9.0960
9.0083
8.9227
8.8392
8.7576
8.6777
8.5990
8.5200
8.4386
8.3522
8.2598
8.1639
8.0720
7.9942
7.9438
7.9444
Hydraulic Sizing Data
Sec:Seg
1:1
1:2
1:3
1:4
1:5
1:6
1:7
1:8
1:9
1:10
1:11
1:12
1:13
1:14
1:15
1:16
1:17
1:18
1:19
1:20
Cumulative Depth
% Vap Flood
feet
1.0000
2.0000
3.0000
4.0000
5.0000
6.0000
7.0000
8.0000
9.0000
10.0000
11.0000
12.0000
13.0000
14.0000
15.0000
16.0000
17.0000
18.0000
19.0000
20.0000
% DC Choke
62.8000
63.1000
63.3000
63.6000
63.9000
64.2000
64.6000
64.9000
65.3000
65.8000
66.2000
66.7000
67.2000
67.7000
68.3000
68.9000
69.5000
69.9000
70.0000
69.3000
61.6000
61.9000
62.1000
62.4000
62.7000
63.1000
63.5000
63.9000
64.4000
64.9000
65.4000
65.9000
66.6000
67.2000
67.9000
68.7000
69.4000
69.9000
70.0000
69.3000
F-Factor
C-Factor
Dry Tray dP
ft/s*(lb/ft3)^0.5
ft/s
psi
0.8455
0.1098
0.8503
0.1104
0.8544
0.1109
0.8589
0.1114
0.8638
0.1120
0.8692
0.1127
0.8750
0.1134
0.8813
0.1141
0.8880
0.1149
0.8950
0.1158
0.9024
0.1167
0.9102
0.1176
0.9186
0.1187
0.9277
0.1198
0.9376
0.1209
0.9480
0.1222
0.9580
0.1233
0.9661
0.1242
0.9698
0.1243
0.9637
0.1228
0.0238
0.0241
0.0244
0.0246
0.0249
0.0253
0.0257
0.0261
0.0265
0.0270
0.0274
0.0280
0.0285
0.0291
0.0298
0.0305
0.0312
0.0318
0.0321
0.0316
Liq Hold Up Vol
Liq Hold Up Vol
Liq Hold Up Vol
Wet Tray dP
Tot Tray dP
Active Area
Downcomer
Total
psi
psi
cum
cum
cum
0.1086
0.1324
0.0932
3.4757
0.1087
0.1328
0.0933
3.4733
0.1088
0.1331
0.0933
3.4705
0.1089
0.1335
0.0933
3.4674
0.1089
0.1339
0.0934
3.4639
0.1090
0.1343
0.0934
3.4601
0.1091
0.1348
0.0934
3.4560
0.1092
0.1353
0.0935
3.4516
0.1094
0.1359
0.0935
3.4468
0.1095
0.1364
0.0936
3.4418
0.1096
0.1370
0.0936
3.4364
0.1097
0.1377
0.0937
3.4307
0.1098
0.1384
0.0938
3.4245
0.1100
0.1391
0.0938
3.4177
0.1102
0.1400
0.0939
3.4104
0.1104
0.1410
0.0940
3.4029
0.1107
0.1420
0.0941
3.3961
0.1111
0.1430
0.0941
3.3911
0.1118
0.1439
0.0942
3.3896
0.1133
0.1449
0.0941
3.3916
Liq Res Time
Active Area
Seconds
Liq Res Time
Downcomer
Seconds
Liq Res Time
Total
Seconds
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Column Blocks
Page 17 of 27
Component Moles Absorbed
Sec:Seg
6.7210E-04
7.6100E-04
8.5668E-04
9.5627E-04
0.0011
0.0012
0.0012
0.0013
0.0014
0.0014
0.0014
0.0014
0.0013
0.0011
8.2015E-04
4.1510E-04
-3.0787E-05
-3.6988E-04
-3.9895E-04
1.6215E-05
Carbon Dioxide
Hydrogen Sulfide
kmol/s
kmol/s
1.5200E-07
1.8160E-07
2.3174E-07
3.2886E-07
5.5124E-07
1.1167E-06
2.6156E-06
6.5936E-06
1.6922E-05
4.2764E-05
1.0426E-04
2.4126E-04
5.2099E-04
0.0010
0.0018
0.0029
0.0040
0.0053
0.0071
0.0114
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Column Blocks
Page 18 of 27
Regenerator [Column Block]
Convergence
Iterations Specified
Iterations Used
Tolerance Specified
Tolerance Reached
100
5
0.0010
2.5573E-04
Models
OGT Gas Treating Thermodynamics
Reaction Kinetic Model Used for CO2: ProTreat Default used Instantaneous Reversible
Liquid Hold Up Volume
Section 1
Total
2.1984 cum
2.1984 cum
Condenser
Temperature
Pressure *
Pressure Drop
HeatDuty *
Molar Reflux Ratio *
Molar Stripping Ratio *
Reflux Flow Rate *
% Reflux Return
130.0000
19.7000
5.0000
-1.0420E+01
1.3330
1.4610
531.9590
100.0000
Fahrenheit
psia
psi
MMBtu/hr
Reboiler
Temperature *
Pressure *
Pressure Drop
HeatDuty *
Boilup Ratio (Molar)*
250.1352
27.0723
0.0000E+00
24.8670
0.2055
Fahrenheit
psia
psi
MMBtu/hr
Internals
Number of Trays
Tray Spacing
Trayed Height
Number of Passes
Weir Height
DC Clearance
Foam Derating Factor
Nutter Float Valve
Diameter *
% Vapor Flood *
% Downcomer Choke *
% Downcomer Backup
DC Choke Correlation:
Tray Active Area As % Column Area *
Tray Active Area *
Inlet DC Area as % Column Area*
Inlet DC Area *
Outlet DC Area as % Column Area*
Outlet DC Area *
Total DC Area As % Column Area *
Total DC Area *
Side DC Width *
Side Weir Length *
Min Weir Load *
Max Weir Load *
5.3801
70.0000
70.0000
0.0000E+00
Hydraulic (Default)
81.4301
18.5120
9.2850
2.1108
9.2850
2.1108
18.5699
4.2216
9.5980
3.8280
5.6021
130.5529
Section Pressure Drop*
20
2.0000
40.0000
1
2.0000
0.0000E+00
0.8000
lbmol/hr
feet
feet
in
feet
feet
sqft
sqft
sqft
sqft
in
feet
USgpm/ft
USgpm/ft
2.3723 psi
Highest Liquid Temp*
Segment with Highest Liquid Temp
Lowest Liquid Temp*
Segment with Lowest Liquid Temp
Highest Vapor Temp*
Segment with Highest Vapor Temp
Lowest Vapor Temp*
Segment with Lowest Vapor Temp
249.0409
20
209.5819
1
249.1653
20
210.9322
1
Feed stream 7 connects above tray
3
Fahrenheit
Fahrenheit
Fahrenheit
Fahrenheit
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Column Blocks
Page 19 of 27
Vapor Phase
Sec:Seg
Temperature
Fahrenheit
1:1
1:2
1:3
1:4
1:5
1:6
1:7
1:8
1:9
1:10
1:11
1:12
1:13
1:14
1:15
1:16
1:17
1:18
1:19
1:20
Liquid Phase
Sec:Seg
1:1
1:2
1:3
1:4
1:5
1:6
1:7
1:8
1:9
1:10
1:11
1:12
1:13
1:14
1:15
1:16
1:17
1:18
1:19
1:20
Pressure
psia
210.9322
213.3973
224.6967
235.3943
239.9015
242.2107
243.6124
244.5639
245.2647
245.8164
246.2757
246.6755
247.0362
247.3700
247.6851
247.9866
248.2782
248.5624
248.8437
249.1653
Temperature
Fahrenheit
24.7000
24.7707
24.8426
24.9502
25.0668
25.1883
25.3120
25.4367
25.5620
25.6875
25.8131
25.9389
26.0648
26.1907
26.3166
26.4425
26.5685
26.6945
26.8204
26.9464
Total Flow
Carbon Dioxide
Hydrogen Sulfide
lbmol/hr
lbmol/hr
mol %
lbmol/hr
mol %
981.5895
126.9524
12.9333
271.2651
27.6353
1023.6892
126.9138
12.3977
271.0148
26.4743
759.3420
41.0713
5.4088
175.5458
23.1181
1040.3143
30.6947
2.9505
135.0090
12.9777
1197.1785
21.9201
1.8310
94.1719
7.8662
1273.3108
15.4282
1.2117
64.1693
5.0396
1313.1483
10.8436
0.8258
43.9121
3.3440
1336.8382
7.6447
0.5718
30.4801
2.2800
1352.4652
5.4125
0.4002
21.5246
1.5915
1363.5824
3.8484
0.2822
15.4614
1.1339
1371.9863
2.7466
0.2002
11.2757
0.8219
1378.6796
1.9662
0.1426
8.3263
0.6039
1384.2601
1.4108
0.1019
6.2063
0.4483
1389.0973
1.0138
0.0730
4.6545
0.3351
1393.4265
0.7292
0.0523
3.5005
0.2512
1397.3991
0.5245
0.0375
2.6306
0.1882
1401.1160
0.3771
0.0269
1.9676
0.1404
1404.6469
0.2706
0.0193
1.4577
0.1038
1408.0377
0.1937
0.0138
1.0628
0.0755
1411.2935
0.1380
0.0098
0.7554
0.0535
24.7707
24.8426
24.9502
25.0668
25.1883
25.3120
25.4367
25.5620
25.6875
25.8131
25.9389
26.0648
26.1907
26.3166
26.4425
26.5685
26.6945
26.8204
26.9464
27.0723
Total Flow
Carbon Dioxide
lbmol/hr
lbmol/hr
mol %
574.0121
0.0264
575.0337
0.0535
7922.0071
30.6987
8078.8592
21.9243
8154.9749
15.4331
8194.7984
10.8490
8218.4779
7.6504
8234.1003
5.4187
8245.2140
3.8548
8253.6153
2.7532
8260.3065
1.9730
8265.8856
1.4177
8270.7217
1.0208
8275.0501
0.7362
8279.0225
0.5315
8282.7392
0.3840
8286.2700
0.2776
8289.6607
0.2006
8292.9165
0.1450
8295.5324
0.1047
Pressure
psia
209.5819
213.2115
217.7999
231.6087
237.9295
241.0934
242.9158
244.0974
244.9346
245.5712
246.0853
246.5214
246.9066
247.2575
247.5846
247.8949
248.1928
248.4815
248.7633
249.0409
0.0046
0.0093
0.3875
0.2714
0.1892
0.1324
0.0931
0.0658
0.0468
0.0334
0.0239
0.0172
0.0123
0.0089
0.0064
0.0046
0.0033
0.0024
0.0017
0.0013
Hydrogen Sulfide
lbmol/hr
mol %
0.1983
0.3294
135.1828
94.3484
64.3491
44.0947
30.6644
21.7109
15.6490
11.4645
8.5157
6.3961
4.8445
3.6906
2.8207
2.1577
1.6479
1.2531
0.9456
0.7052
0.0346
0.0573
1.7064
1.1678
0.7891
0.5381
0.3731
0.2637
0.1898
0.1389
0.1031
0.0774
0.0586
0.0446
0.0341
0.0261
0.0199
0.0151
0.0114
0.0085
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Control Blocks
Page 20 of 27
Control [Control Block]
Total Flow
GAS/SPEC SS-3
425.0000 USgal/min
50.0000 wt %
Make-up values
Water
GAS/SPEC SS-3
945.3297 lb/hr
2.9710 lb/hr
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Flash Blocks
Page 21 of 27
Flash Tank [Flash Block]
Convergence
Maximum Iterations
Iterations Used*
Tolerance Specified
Tolerance Reached*
Sizing
Residence Time
Drum Diameter*
Drum Length*
Flash Results
Flash Type
Vapor Fraction*
Outlet Temperature*
Temperature Change*
Outlet Pressure*
Pressure Drop
Heat Duty
Entropy Change
200.0000
2.0000
1.0000E-04
3.1073E-05
20.0000 Minutes
9.4959 feet
33.2358 feet
QP
0.0024
177.1038
9.0183E-05
89.7000
0.0000E+00
0.0000E+00
0.0593
Fahrenheit
Fahrenheit
psia
psi
MMBtu/hr
J/K-s
Flash-1 [Flash Block]
Convergence
Maximum Iterations
Iterations Used*
Tolerance Specified
Tolerance Reached*
Sizing
Residence Time
Drum Diameter*
Drum Length*
Flash Results
Flash Type
Vapor Fraction*
Outlet Temperature*
Temperature Change*
Outlet Pressure*
Pressure Drop
Heat Duty
Entropy Change
200.0000
19.0000
1.0000E-04
5.5095E-05
300.0000 Seconds
0.3265 feet
1.1428 feet
QP
0.9996
129.9998
-1.6928E-04
1006.9506
0.0000E+00
0.0000E+00
-6.3818E-03
Fahrenheit
Fahrenheit
psia
psi
MMBtu/hr
Btu/R-hr
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
HeatX Blocks
Page 22 of 27
Lean/Rich Exch [HeatX Block]
Convergence
Max Iterations
Iterations Used*
Tolerance Specified
Tolerance Reached*
Exchanger Results
Shell Side Inlet Stream
Shell Side Outlet Stream
Tube Side Inlet Stream
Tube Side Outlet Stream
Calculation Mode
Minimum Temp Approach*
Temp Approach (Shell Out vs Tube In)*
Temp Approach (Shell Out vs Tube Out)*
Temp Approach (Shell In vs Tube Out)*
Heat Duty*
UA*
U*
Area*
Fouling Resistance
Effective U
LMTD*
LMTD Correction Factor
Effective LMTD*
Shell Side Results
Inlet Stream
Outlet Stream
Pressure Drop
Outlet Pressure*
Shell Outlet Temperature*
Shell Temperature Change*
Shell Heat Duty*
Shell Outlet Vapor Fraction*
Shell Outlet Degrees Subcooled*
Shell Outlet Degrees Superheated*
Tube Side Results
Inlet Stream
Outlet Stream
Pressure Drop
Outlet Pressure*
Tube Outlet Temperature
Tube Temperature Change*
Tube Heat Duty*
Tube Outlet Vapor Fraction*
Tube Outlet Degrees Subcooled*
Tube Outlet Degrees Superheated*
200.0000
2.0000
0.0010
8.3417E-04
14.0000
15.0000
6.0000
7.0000
Simple Energy Balance
33.5059
33.5059
0.6097
40.1725
7.1585
1.9485E+05
Fahrenheit
Fahrenheit
Fahrenheit
Fahrenheit
MMBtu/hr
Btu/hr-F
Btu/hr-sqft-F
sqft
36.7384 Fahrenheit
1.0000
36.7384 Fahrenheit
14.0000
15.0000
5.0000
75.0000
210.6097
-3.9563E+01
-7.1585E+00
0.0000E+00
102.6510
6.0000
7.0000
5.0000
84.7000
210.0000
32.8962
7.1585
0.0095
psi
psia
Fahrenheit
Fahrenheit
MMBtu/hr
Fahrenheit
Fahrenheit
psi
psia
Fahrenheit
Fahrenheit
MMBtu/hr
Fahrenheit
Fahrenheit
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Heater Blocks
Page 23 of 27
Heater-1 [Heater Block]
Outlet Pressure*
Pressure Drop
Outlet Temperature
Temperature Change*
Heat Duty*
Outlet Vapor Fraction*
Outlet Degrees Subcooled*
Outlet Degrees Superheated*
Lean Amine Cooler [Heater Block]
Outlet Pressure*
Pressure Drop
Outlet Temperature
Temperature Change*
Heat Duty*
Outlet Vapor Fraction*
Outlet Degrees Subcooled*
Outlet Degrees Superheated*
1006.9506
5.0000
130.0000
-9.0617E+00
-6.8018E-01
0.9996
psia
psi
Fahrenheit
Fahrenheit
MMBtu/hr
Fahrenheit
Fahrenheit
65.0000
10.0000
135.0000
-7.5610E+01
-1.3342E+01
0.0000E+00
168.6455
psia
psi
Fahrenheit
Fahrenheit
MMBtu/hr
Fahrenheit
Fahrenheit
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Inlet Blocks
Page 24 of 27
Inlet Gas [Inlet Block]
Temperature
Pressure
Total Flow
130.0000 Fahrenheit
1000.0000 psig
50.0000 MMSCFD
Components Specified as Composition
Water Saturation %
Nitrogen
Carbon Dioxide
Hydrogen Sulfide
Methane
Ethane
Propane
Isobutane
n-Butane
Isopentane
n-Pentane
n-Hexane
Water
100.0000
3.0330
3.0000
5.0000
61.6732
15.1927
8.8046
0.8882
1.8985
0.2507
0.2283
0.0308
mol %
mol %
mol %
mol %
mol %
mol %
mol %
mol %
mol %
mol %
mol %
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Pump Blocks
Page 25 of 27
Solution Pump [Pump Block]
Pressure
Efficiency %
Power Input*
1275.0000 psig
75.0000
402.4060 Horsepower
Booster Pump [Pump Block]
Pressure
Efficiency %
Power Input*
80.0000 psia
75.0000
18.3734 Horsepower
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Recycle Blocks
Page 26 of 27
Recycle [Recycle Block]
Temperature
Pressure
Max Iterations
Iterations Used
Convergence Tolerance
Tolerance Reached
Total Flow
125.0000 Fahrenheit
1100.0000 psig
20.0000
1.0000
0.0020
3.5073E-06
400.0000 USgal/min
Components Specified as Composition
Carbon Dioxide
Hydrogen Sulfide
GAS/SPEC SS-3
0.0150 Loading
0.0010 Loading
50.0000 wt %
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor
Equipment Report
Valve Blocks
Page 27 of 27
Valve-1 [Valve Block]
Outlet Pressure
Max Line Velocity
Pressure Drop*
Vapor Fraction*
Line Size*
LCV [Valve Block]
Outlet Pressure
Max Line Velocity
Pressure Drop*
Vapor Fraction*
Line Size*
75.0000 psig
ft/s
925.0000 psi
0.0024
feet
20.0000
3.0000
50.0000
0.0279
2.2910
psig
ft/s
psi
feet
C:\Users\delarosa.VALKOR\Crosstrails\Operations - Documents\
05 BD Prospects\50 mmscfd 5 PC H2S Amine Run SS3 R1.ptr
ProTreat® Version 7.0
Licensed by Crosstrails Engineering - Valkor