4
100.04 psia
1
2637.57 gal/min
89.8831 mmscfd STP
24"
L-1
2
3
V-9
16"
1
2
3
4
5
6
7
8
9
Strm 1
Strm 2
Strm 3
Strm 4
Strm 5
Strm 6
Strm 7
Strm 8
Strm 9
0.6944
0.6946
0.6966
1.0000
1.0000
1.0000
1.0000
01.6781E-005
185.0
185.0
184.6
184.5
184.5
184.1
184.1
184.5
184.5
100.0
99.6
94.6
92.6
92.5
86.9
86.8
92.6
92.6
98.71
98.71
98.71
27.04
27.04
27.04
27.04
263.97
263.97
btu/hr
-70467000 -70445000 -70445000 17638000 17639000 17639000 17640000 -88082000 -88082000
lb/ft3
0.40
0.40
0.38
0.37
0.37
0.35
0.35
0
0.37
lb/ft3
53.77
53.78
53.85
0
0
0
0
53.88
53.88
mmscf/day
89.88
89.91
90.18
90.29
90.29
90.29
90.29
0 6.57E-004
gal/min
2515.40
2514.80
2509.10
0
0
0
0
2506.70
2506.70
0
0
0
0
0
0
0
0
0
lbmol/hr
14215.0
14215.0
14215.0
9914.9
9914.9
9914.9
9914.9
4300.1
4300.1
lb/hr
1403167.0 1403167.0 1403167.0 268060.0 268060.0 268060.0 268060.0 1135107.0 1135107.0
lbmol/hr
5797.6
5797.6
5797.6
5735.1
5735.1
5735.1
5735.1
62.5
62.5
lbmol/hr
1856.2
1856.2
1856.2
1784.8
1784.8
1784.8
1784.8
71.3
71.3
lbmol/hr
1009.0
1009.0
1009.0
914.7
914.7
914.7
914.7
94.2
94.2
lbmol/hr
57.0
57.0
57.0
47.4
47.4
47.4
47.4
9.6
9.6
lbmol/hr
587.4
587.4
587.4
464.5
464.5
464.5
464.5
122.9
122.9
lbmol/hr
65.4
65.4
65.4
42.6
42.6
42.6
42.6
22.8
22.8
lbmol/hr
346.8
346.8
346.8
210.1
210.1
210.1
210.1
136.7
136.7
lbmol/hr
344.5
344.5
344.5
134.8
134.8
134.8
134.8
209.7
209.7
lbmol/hr
102.8
102.8
102.8
22.2
22.2
22.2
22.2
80.6
80.6
lbmol/hr
95.1
95.1
95.1
9.9
9.9
9.9
9.9
85.2
85.2
lbmol/hr
88.3
88.3
88.3
4.3
4.3
4.3
4.3
84.0
84.0
lbmol/hr
4.3
4.3
4.3 9.3E-002 9.3E-002 9.3E-002 9.3E-002
4.2
4.2
lbmol/hr
3305.1
3305.1
3305.1 2.8E-003 2.8E-003 2.8E-003 2.8E-003
3305.1
3305.1
lbmol/hr
150.3
150.3
150.3
146.7
146.7
146.7
146.7
3.6
3.6
lbmol/hr
162.0
162.0
162.0
155.2
155.2
155.2
155.2
6.8
6.8
lbmol/hr
0
0
0
0
0
0
0
0
0
lbmol/hr
0
0
0
0
0
0
0
0
0
lbmol/hr
243.5
243.5
243.5
242.6
242.6
242.6
242.6 8.7E-001 8.7E-001
F
psia
10
Strm 10
0.0020
184.5
87.6
263.97
-88082000
0.35
53.90
7.64E-002
2505.60
0
4300.1
1135107.0
62.5
71.3
94.2
9.6
122.9
22.8
136.7
209.7
80.6
85.2
84.0
4.2
3305.1
3.6
6.8
0
0
8.7E-001
11
Strm 11
0.0020
184.5
87.5
263.97
-88082000
0.35
53.90
7.71E-002
2505.60
0
4300.1
1135107.0
62.5
71.3
94.2
9.6
122.9
22.8
136.7
209.7
80.6
85.2
84.0
4.2
3305.1
3.6
6.8
0
0
8.7E-001
5
20"
L-7
9
6
24"
L-6
10
20" 11
L-8
V-3
20"
7
86.793 psia
90.2877 mmscfd STP
F-2
8
Stream Number
Stream Name
Vapor Fraction
Temperature
Pressure
Molecular Weight
Enthalpy
Vapor Density
Liquid Density
Vapor Flowrate (STP)
Liquid Flowrate (STP)
Water Flowrate (STP)
Total Molar Flowrate
Total Mass FLowrate
METHANE
ETHANE
PROPANE
I-BUTANE
N-BUTANE
I-PENTANE
N-PENTANE
N-HEXANE
N-HEPTANE
N-OCTANE
N-NONANE
N-DECANE
Cut 1
CO2
H2S
WATER
OXYGEN
NITROGEN
24"
L-5
V-4
16"
184.48 F
87.534 psia
2625.36 gal/min
REMOTE SEPARATOR
PA-1101
PP-KU-C
NORMAL CONDITIONS
REVISION 1
June, 2004
Details for Stream 1
Stream 1 (Strm 1)
Thermodynamic Methods
K-Value:
Liquid Visc:
Vapor Visc:
ASOA
NS81
NS81
Enthalpy:
Liquid ThC:
Vapor ThC:
ASOA
NS81
NS81
Density:
Surface Ten:
STD
HADD
Component Name
Total
lbmol/hr
Vapor
lbmol/hr
Liquid 1
lbmol/hr
Liquid 2
lbmol/hr
Total
mole %
K-Value
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
5797.57
1856.15
1008.95
56.968
587.358
65.4025
346.792
344.463
102.818
95.136
88.2919
4.27402
3305.09
150.301
161.959
0
0
243.477
5729.27
1778.67
907.427
46.7139
456.551
41.427
203.677
128.774
21.0132
9.31798
4.03229
0.087512
0.002732
146.373
154.622
0
0
242.518
68.3002
77.4802
101.526
10.2541
130.807
23.9754
143.115
215.689
81.8047
85.818
84.2596
4.18651
3305.08
3.92773
7.33682
0
0
0.959142
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
40.7849
13.0577
7.09781
0.40076
4.13196
0.460095
2.43962
2.42324
0.723306
0.669265
0.621118
0.030067
23.2507
1.05734
1.13935
0
0
1.71282
36.9216
10.1044
3.93402
2.00517
1.53625
0.760538
0.626415
0.262787
0.113062
0.047791
0.021064
0.009201
3.638E-07
16.403
9.27611
0.0838
163.183
111.292
14215
9870.48
4344.52
0
100
Component Name
Total
lb/hr
Vapor
lb/hr
Liquid 1
lb/hr
Liquid 2
lb/hr
Total
mass %
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
93010.3
55810.8
44488.8
3310.98
34137.2
4718.53
25019.6
29683.1
10302.1
10866.8
11323.4
608.091
1060932
6614.72
5519.55
0
0
6820.63
91914.6
53481.1
40012.1
2715.01
26534.7
2988.79
14694.5
11096.7
2105.48
1064.34
517.141
12.4508
0.876986
6441.86
5269.51
0
0
6793.76
1095.74
2329.68
4476.7
595.97
7602.5
1729.73
10325.1
18586.4
8196.67
9802.47
10806.3
595.64
1060932
172.859
250.039
0
0
26.8688
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
6.6286
3.97748
3.1706
0.235965
2.43287
0.336277
1.78308
2.11544
0.734207
0.774449
0.806991
0.043337
75.6098
0.471414
0.393363
0
0
0.486088
Total
1403167
265643
1137524
0
100
F
psia
btu/hr
185
100.04
-70466600
0.69437
Total
Vapor
Liquid 1
14215
98.7103
-4957.197
-0.518907
9870.4779
26.9129
1772.4835
2.1807
13.3534
11.1817
1.1942
0.396984
0.980446
185.8759
4344.5221
261.8295
-20246.603
-6.6522
127.4555
117.6823
1.083
53.7731
0.070419
Flowrates
Total
Flowrates
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Flowrate
lbmol/hr
Molecular Weight
Enthalpy
btu/lbmole
Entropy
btu/lbmo/R
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (T-P)
gal/min
Flowrate (STP)
mmscfd
Flowrate (STP)
gal/min
Specific Gravity
GPA STP
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Surface Tension
dyne/cm
Critical Temperature (Cubic EOS)
F
Critical Pressure (Cubic EOS)
psia
2637.5713
89.8831
0.012933
0.020484
887.5
2111.1
2515.353
0.904045
0.892452
0.060039
25.1949
Details for Stream 2
Stream 2 (Strm 2)
Thermodynamic Methods
K-Value:
Liquid Visc:
Vapor Visc:
ASOA
NS81
NS81
Enthalpy:
Liquid ThC:
Vapor ThC:
ASOA
NS81
NS81
Density:
Surface Ten:
STD
HADD
Component Name
Total
lbmol/hr
Vapor
lbmol/hr
Liquid 1
lbmol/hr
Liquid 2
lbmol/hr
Total
mole %
K-Value
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
5797.57
1856.15
1008.95
56.968
587.358
65.4025
346.792
344.463
102.818
95.136
88.2919
4.27402
3305.09
150.301
161.959
0
0
243.477
5729.6
1779.03
907.857
46.7528
457.019
41.4957
204.056
129.129
21.0851
9.35326
4.04803
0.087853
0.00274
146.392
154.656
0
0
242.523
67.9667
77.123
101.096
10.2152
130.339
23.9068
142.736
215.334
81.7328
85.7827
84.2438
4.18617
3305.08
3.90916
7.30292
0
0
0.95433
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
40.7849
13.0577
7.09781
0.40076
4.13196
0.460095
2.43962
2.42324
0.723306
0.669265
0.621118
0.030067
23.2507
1.05734
1.13935
0
0
1.71282
37.0729
10.1444
3.9492
2.01274
1.54202
0.763324
0.628699
0.263718
0.113451
0.04795
0.021132
0.009229
3.645E-07
16.4688
9.31315
0.084147
163.857
111.759
14215
9873.09
4341.91
0
100
Component Name
Total
lb/hr
Vapor
lb/hr
Liquid 1
lb/hr
Liquid 2
lb/hr
Total
mass %
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
93010.3
55810.8
44488.8
3310.98
34137.2
4718.53
25019.6
29683.1
10302.1
10866.8
11323.4
608.091
1060932
6614.72
5519.55
0
0
6820.63
91919.9
53491.8
40031
2717.27
26561.9
2993.75
14721.8
11127.3
2112.69
1068.37
519.16
12.4994
0.879394
6442.68
5270.66
0
0
6793.89
1090.39
2318.93
4457.74
593.709
7575.29
1724.78
10297.8
18555.8
8189.46
9798.44
10804.3
595.591
1060932
172.042
248.884
0
0
26.734
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
6.6286
3.97748
3.1706
0.235965
2.43287
0.336277
1.78308
2.11544
0.734207
0.774449
0.806991
0.043337
75.6098
0.471414
0.393363
0
0
0.486088
Total
1403167
265786
1137381
0
100
F
psia
btu/hr
185
99.628
-70444800
0.69455
Vapor
Liquid 1
9873.0885
26.9202
1773.2438
2.1909
13.3557
11.1847
1.1941
0.39543
0.980517
186.7068
4341.9115
261.9541
-20256.551
-6.6538
127.5118
117.735
1.083
53.7785
0.070156
Flowrates
Total
Flowrates
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Total
Flowrate
lbmol/hr
14215
Molecular Weight
98.7103
Enthalpy
btu/lbmole -4955.6636
Entropy
btu/lbmo/R -0.510709
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (T-P)
gal/min
Flowrate (STP)
mmscfd
Flowrate (STP)
gal/min
Specific Gravity
GPA STP
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Surface Tension
dyne/cm
Critical Temperature (Cubic EOS)
F
887.5
Critical Pressure (Cubic EOS)
psia
2111.1
2636.973
89.9069
0.012932
0.02048
2514.8437
0.904115
0.892592
0.060028
25.2096
Details for Stream 3
Stream 3 (Strm 3)
Thermodynamic Methods
K-Value:
Liquid Visc:
Vapor Visc:
ASOA
NS81
NS81
Enthalpy:
Liquid ThC:
Vapor ThC:
ASOA
NS81
NS81
Density:
Surface Ten:
STD
HADD
Component Name
Total
lbmol/hr
Vapor
lbmol/hr
Liquid 1
lbmol/hr
Liquid 2
lbmol/hr
Total
mole %
K-Value
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
5797.57
1856.15
1008.95
56.968
587.358
65.4025
346.792
344.463
102.818
95.136
88.2919
4.27402
3305.09
150.301
161.959
0
0
243.477
5733.53
1783.16
912.771
47.1943
462.322
42.2695
208.313
133.095
21.8795
9.73618
4.21543
0.091398
0.002784
146.607
155.048
0
0
242.58
64.0414
72.991
96.1823
9.77366
125.036
23.1329
138.478
211.368
80.9384
85.3998
84.0764
4.18262
3305.08
3.69355
6.9108
0
0
0.896924
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
40.7849
13.0577
7.09781
0.40076
4.13196
0.460095
2.43962
2.42324
0.723306
0.669265
0.621118
0.030067
23.2507
1.05734
1.13935
0
0
1.71282
38.9852
10.638
4.13243
2.10267
1.61008
0.795675
0.655049
0.274196
0.117712
0.049644
0.021833
0.009515
3.668E-07
17.2842
9.76957
0.087897
172.286
117.771
14215
9902.81
4312.19
0
100
Component Name
Total
lb/hr
Vapor
lb/hr
Liquid 1
lb/hr
Liquid 2
lb/hr
Total
mass %
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
93010.3
55810.8
44488.8
3310.98
34137.2
4718.53
25019.6
29683.1
10302.1
10866.8
11323.4
608.091
1060932
6614.72
5519.55
0
0
6820.63
91982.9
53616.1
40247.7
2742.94
26870.1
3049.58
15029
11469.1
2192.28
1112.11
540.629
13.0037
0.893679
6452.17
5284.03
0
0
6795.5
1027.42
2194.69
4241.06
568.045
7267.11
1668.95
9990.67
18214
8109.86
9754.71
10782.8
595.087
1060931
162.553
235.52
0
0
25.1259
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
6.6286
3.97748
3.1706
0.235965
2.43287
0.336277
1.78308
2.11544
0.734207
0.774449
0.806991
0.043337
75.6098
0.471414
0.393363
0
0
0.486088
Total
1403167
267398
1135769
0
100
F
psia
btu/hr
184.64
94.628
-70444800
0.69665
Vapor
Liquid 1
9902.8146
27.0022
1777.2726
2.3082
13.3757
11.2133
1.1928
0.376619
0.981353
197.2212
4312.1854
263.386
-20417.666
-6.7447
128.1095
118.2968
1.0829
53.8485
0.066949
Flowrates
Total
Flowrates
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Total
Flowrate
lbmol/hr
14215
Molecular Weight
98.7103
Enthalpy
btu/lbmole -4955.6636
Entropy
btu/lbmo/R -0.437997
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (T-P)
gal/min
Flowrate (STP)
mmscfd
Flowrate (STP)
gal/min
Specific Gravity
GPA STP
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Surface Tension
dyne/cm
Critical Temperature (Cubic EOS)
F
887.5
Critical Pressure (Cubic EOS)
psia
2111.1
2629.8101
90.1776
0.012912
0.020411
2509.0722
0.90491
0.894653
0.059913
25.3962
Details for Stream 4
Stream 4 (Strm 4)
Thermodynamic Methods
K-Value:
Vapor Visc:
ASOA
NS81
Enthalpy:
Vapor ThC:
ASOA
NS81
Density:
STD
Total
mole %
K-Value
39.8077
10.8501
4.21115
2.14131
1.63931
0.809571
0.666366
0.278697
0.119543
0.050373
0.022134
0.009639
3.679E-07
17.6347
9.96576
0.089504
175.91
120.359
Flowrates
Component Name
Total
lbmol/hr
Vapor Incipient Liquid 1 Liquid 2
lbmol/hr
mol fra
lbmol/hr
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
5735.09
1784.81
914.745
47.3731
464.475
42.5876
210.069
134.757
22.2166
9.89984
4.28722
0.092921
0.002804
146.693
155.204
0
0
242.603
5735.09
1784.81
914.745
47.3731
464.475
42.5876
210.069
134.757
22.2166
9.89984
4.28722
0.092921
0.002804
146.693
155.204
0
0
242.603
0.014531
0.016591
0.021908
0.002231
0.028577
0.005306
0.031795
0.048768
0.018744
0.019822
0.019536
0.000972
0.768607
0.000839
0.001571
0
0
0.000203
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
57.8431
18.0013
9.22596
0.477796
4.68462
0.429531
2.11872
1.35914
0.224072
0.099848
0.04324
0.000937
0.00002828
1.47952
1.56536
0
0
2.44685
9914.9
9914.9
1
0
100
Total
Flowrates
Component Name
Total
lb/hr
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
92007.9
53665.6
40334.8
2753.32
26995.3
3072.53
15155.7
11612.3
2226.05
1130.8
549.836
13.2204
0.899993
6455.95
5289.36
0
0
6796.14
92007.9
53665.6
40334.8
2753.32
26995.3
3072.53
15155.7
11612.3
2226.05
1130.8
549.836
13.2204
0.899993
6455.95
5289.36
0
0
6796.14
0.000883
0.00189
0.00366
0.000491
0.00629
0.00145
0.00869
0.01592
0.00711
0.00858
0.00949
0.000524
0.935
0.00014
0.000203
0
0
0.000022
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
34.3237
20.02
15.0469
1.02713
10.0706
1.14621
5.65384
4.33199
0.830433
0.421846
0.205117
0.004932
0.000336
2.4084
1.9732
0
0
2.53531
268060
268060
1
0
100
F
psia
btu/hr
184.49
92.628
17637600
1
Total
Vapor Incipient Liquid 1 Liquid 2
lb/hr
mass fra
lb/hr
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Flowrate
lbmol/hr
Molecular Weight
Enthalpy
btu/lbmole
Entropy
btu/lbmo/R
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (STP)
mmscfd
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Critical Temperature (Cubic EOS)
F
Critical Pressure (Cubic EOS)
psia
Total
Vapor
9914.9038
27.036
1778.8962
2.3568
9914.9038
27.036
1778.8962
2.3568
13.3841
11.2251
1.1923
0.369079
0.98169
201.7482
90.2877
0.012903
0.020383
83.1
1717.3
Total
mass %
Details for Stream 5
Stream 5 (Strm 5)
Thermodynamic Methods
K-Value:
Vapor Visc:
ASOA
NS81
Enthalpy:
Vapor ThC:
ASOA
NS81
Density:
STD
Total
mole %
K-Value
39.8551
10.862
4.21545
2.14338
1.64087
0.810296
0.666951
0.278922
0.119632
0.050406
0.022147
0.009644
3.678E-07
17.6543
9.97678
0.089581
176.116
120.511
Flowrates
Component Name
Total
lbmol/hr
Vapor Incipient Liquid 1 Liquid 2
lbmol/hr
mol fra
lbmol/hr
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
5735.09
1784.81
914.745
47.3731
464.475
42.5876
210.069
134.757
22.2166
9.89984
4.28722
0.092921
0.002804
146.693
155.204
0
0
242.603
5735.09
1784.81
914.745
47.3731
464.475
42.5876
210.069
134.757
22.2166
9.89984
4.28722
0.092921
0.002804
146.693
155.204
0
0
242.603
0.014513
0.016573
0.021886
0.002229
0.02855
0.005301
0.031767
0.048728
0.01873
0.019809
0.019524
0.000972
0.768808
0.000838
0.001569
0
0
0.000203
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
57.8431
18.0013
9.22596
0.477796
4.68462
0.429531
2.11872
1.35914
0.224072
0.099848
0.04324
0.000937
0.00002828
1.47952
1.56536
0
0
2.44685
9914.9
9914.9
1
0
100
Total
Flowrates
Component Name
Total
lb/hr
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
92007.9
53665.6
40334.8
2753.32
26995.3
3072.53
15155.7
11612.3
2226.05
1130.8
549.836
13.2204
0.899993
6455.95
5289.36
0
0
6796.14
92007.9
53665.6
40334.8
2753.32
26995.3
3072.53
15155.7
11612.3
2226.05
1130.8
549.836
13.2204
0.899993
6455.95
5289.36
0
0
6796.14
0.000882
0.001887
0.003655
0.000491
0.00628
0.001449
0.00868
0.0159
0.00711
0.00857
0.00948
0.000524
0.935
0.00014
0.000203
0
0
0.000022
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
34.3237
20.02
15.0469
1.02713
10.0706
1.14621
5.65384
4.33199
0.830433
0.421846
0.205117
0.004932
0.000336
2.4084
1.9732
0
0
2.53531
268060
268060
1
0
100
F
psia
btu/hr
184.49
92.515
17638600
1
Total
Vapor Incipient Liquid 1 Liquid 2
lb/hr
mass fra
lb/hr
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Flowrate
lbmol/hr
Molecular Weight
Enthalpy
btu/lbmole
Entropy
btu/lbmo/R
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (STP)
mmscfd
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Critical Temperature (Cubic EOS)
F
Critical Pressure (Cubic EOS)
psia
Total
Vapor
9914.9038
27.036
1778.9991
2.3594
9914.9038
27.036
1778.9991
2.3594
13.3838
11.225
1.1923
0.368617
0.981713
202.001
90.2877
0.012903
0.020382
83.1
1717.3
Total
mass %
Details for Stream 6
Stream 6 (Strm 6)
Thermodynamic Methods
K-Value:
Vapor Visc:
ASOA
NS81
Enthalpy:
Vapor ThC:
ASOA
NS81
Density:
STD
Component Name
Total
lbmol/hr
Vapor
lbmol/hr
Liquid 1
lbmol/hr
Liquid 2
lbmol/hr
Total
mole %
K-Value
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
5735.09
1784.81
914.745
47.3731
464.475
42.5876
210.069
134.757
22.2166
9.89984
4.28722
0.092921
0.002804
146.693
155.204
0
0
242.603
5735.09
1784.81
914.745
47.3731
464.475
42.5876
210.069
134.757
22.2166
9.89984
4.28722
0.092921
0.002804
146.693
155.204
0
0
242.603
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
57.8431
18.0013
9.22596
0.477796
4.68462
0.429531
2.11872
1.35914
0.224072
0.099848
0.04324
0.000937
0.00002828
1.47952
1.56536
0
0
2.44685
42.0466
11.2869
4.33176
2.18505
1.66751
0.816921
0.67039
0.277403
0.11773
0.049063
0.021336
0.009193
3.11E-07
18.4155
10.3695
0.087367
184.729
128.615
9914.9
9914.9
0
0
100
Component Name
Total
lb/hr
Vapor
lb/hr
Liquid 1
lb/hr
Liquid 2
lb/hr
Total
mass %
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
92007.9
53665.6
40334.8
2753.32
26995.3
3072.53
15155.7
11612.3
2226.05
1130.8
549.836
13.2204
0.899993
6455.95
5289.36
0
0
6796.14
92007.9
53665.6
40334.8
2753.32
26995.3
3072.53
15155.7
11612.3
2226.05
1130.8
549.836
13.2204
0.899993
6455.95
5289.36
0
0
6796.14
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
34.3237
20.02
15.0469
1.02713
10.0706
1.14621
5.65384
4.33199
0.830433
0.421846
0.205117
0.004932
0.000336
2.4084
1.9732
0
0
2.53531
268060
268060
0
0
100
F
psia
btu/hr
184.11
86.915
17638600
1
Flowrates
Total
Flowrates
Total
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Flowrate
lbmol/hr
Molecular Weight
Enthalpy
btu/lbmole
Entropy
btu/lbmo/R
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (STP)
mmscfd
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Critical Temperature (Cubic EOS)
F
Critical Pressure (Cubic EOS)
psia
Total
Vapor
9914.9038
27.036
1778.999
2.4813
9914.9038
27.036
1778.999
2.4813
13.3647
11.2165
1.1915
0.346122
0.982807
215.1291
90.2877
0.012886
0.020338
83.1
1717.3
Details for Stream 7
Stream 7 (Strm 7)
Thermodynamic Methods
K-Value:
Vapor Visc:
ASOA
NS81
Enthalpy:
Vapor ThC:
ASOA
NS81
Density:
STD
Total
mole %
K-Value
42.3946
11.4971
4.44534
2.25406
1.72393
0.848933
0.698143
0.290925
0.124337
0.052197
0.022854
0.009916
3.63E-07
18.7025
10.5663
0.093659
187.116
128.695
Flowrates
Component Name
Total
lbmol/hr
Vapor Incipient Liquid 1 Liquid 2
lbmol/hr
mol fra
lbmol/hr
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
5735.09
1784.81
914.745
47.3731
464.475
42.5876
210.069
134.757
22.2166
9.89984
4.28722
0.092921
0.002804
146.693
155.204
0
0
242.603
5735.09
1784.81
914.745
47.3731
464.475
42.5876
210.069
134.757
22.2166
9.89984
4.28722
0.092921
0.002804
146.693
155.204
0
0
242.603
0.013644
0.015657
0.020754
0.00212
0.027174
0.00506
0.030348
0.046718
0.018021
0.019129
0.018921
0.000945
0.779046
0.000791
0.001481
0
0
0.00019
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
57.8431
18.0013
9.22596
0.477796
4.68462
0.429531
2.11872
1.35914
0.224072
0.099848
0.04324
0.000937
0.00002828
1.47952
1.56536
0
0
2.44685
9914.9
9914.9
1
0
100
Total
Flowrates
Component Name
Total
lb/hr
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
92007.9
53665.6
40334.8
2753.32
26995.3
3072.53
15155.7
11612.3
2226.05
1130.8
549.836
13.2204
0.899993
6455.95
5289.36
0
0
6796.14
92007.9
53665.6
40334.8
2753.32
26995.3
3072.53
15155.7
11612.3
2226.05
1130.8
549.836
13.2204
0.899993
6455.95
5289.36
0
0
6796.14
0.000821
0.001766
0.003433
0.000462
0.00592
0.001369
0.00821
0.0151
0.00677
0.0082
0.0091
0.000504
0.938
0.000131
0.000189
0
0
0.00002
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
34.3237
20.02
15.0469
1.02713
10.0706
1.14621
5.65384
4.33199
0.830433
0.421846
0.205117
0.004932
0.000336
2.4084
1.9732
0
0
2.53531
268060
268060
1
0
100
F
psia
btu/hr
184.11
86.793
17639700
1
Total
Vapor Incipient Liquid 1 Liquid 2
lb/hr
mass fra
lb/hr
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Flowrate
lbmol/hr
Molecular Weight
Enthalpy
btu/lbmole
Entropy
btu/lbmo/R
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (STP)
mmscfd
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Critical Temperature (Cubic EOS)
F
Critical Pressure (Cubic EOS)
psia
Total
Vapor
9914.9038
27.036
1779.1088
2.4842
9914.9038
27.036
1779.1088
2.4842
13.3644
11.2165
1.1915
0.345631
0.982831
215.4351
90.2877
0.012886
0.020338
83.1
1717.3
Total
mass %
Details for Stream 8
Stream 8 (Strm 8)
Thermodynamic Methods
K-Value:
Liquid Visc:
ASOA
NS81
Enthalpy:
Liquid ThC:
ASOA
NS81
Density:
Surface Ten:
STD
HADD
Liquid 2
lbmol/hr
Total
mole %
K-Value
39.8077
10.8501
4.21115
2.14131
1.63931
0.809571
0.666366
0.278697
0.119543
0.050373
0.022134
0.009639
3.679E-07
17.6347
9.96576
0.089504
175.91
120.359
Flowrates
Component Name
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
Total
Total
Incipient Vapor Liquid 1
lbmol/hr
mol fra
lbmol/hr
62.4831
71.3422
94.2083
9.59495
122.882
22.8149
136.722
209.706
80.6013
85.2361
84.0047
4.1811
3305.08
3.60771
6.75433
0
0
0.874196
0.578431
0.180013
0.09226
0.004778
0.046846
0.004295
0.021187
0.013591
0.002241
0.000998
0.000432
9.372E-06
2.828E-07
0.014795
0.015654
0
0
0.024469
62.4831
71.3422
94.2083
9.59495
122.882
22.8149
136.722
209.706
80.6013
85.2361
84.0047
4.1811
3305.08
3.60771
6.75433
0
0
0.874196
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1.45306
1.65908
2.19084
0.223133
2.85767
0.530567
3.17952
4.87677
1.87441
1.98219
1.95355
0.097233
76.8607
0.083898
0.157074
0
0
0.02033
4300.1
1
4300.1
0
100
Liquid 2
lb/hr
Total
mass %
Flowrates
Component Name
Total
lb/hr
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
1002.42
2145.12
4154.02
557.658
7141.93
1646
9863.98
18070.8
8076.09
9736.01
10773.6
594.87
1060931
158.775
230.188
0
0
24.4892
0.34324
0.2002
0.15047
0.010271
0.10071
0.011462
0.05654
0.04332
0.008304
0.004218
0.002051
0.000049
3.357E-06
0.024084
0.019732
0
0
0.025353
1002.42
2145.12
4154.02
557.658
7141.93
1646
9863.98
18070.8
8076.09
9736.01
10773.6
594.87
1060931
158.775
230.188
0
0
24.4892
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0.08831
0.188979
0.365958
0.049128
0.629185
0.145008
0.868991
1.59199
0.711483
0.857717
0.949126
0.052407
93.4653
0.013988
0.020279
0
0
0.002157
Total
1135107
1
1135107
0
100
F
psia
btu/hr
184.49
92.628
-88082300
0
Incipient Vapor Liquid 1
mass fra
lb/hr
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Total
Liquid 1
Flowrate
lbmol/hr
4300.0962 4300.0962
Molecular Weight
263.9726
263.9726
Enthalpy
btu/lbmole -20483.807 -20483.807
Entropy
btu/lbmo/R
-6.7823
-6.7823
Cp
btu/lbmol/R
128.354
Cv
btu/lbmol/R
118.5265
Cp/Cv
1.0829
Density
lb/ft3
53.877
Z-Factor
0.065661
Flowrate (T-P)
gal/min
2626.8885
Flowrate (STP)
gal/min
2506.7126
Specific Gravity
GPA STP
0.905234
Viscosity
cP
0.895502
Thermal Conductivity
btu/ft/hr/F
0.059868
Surface Tension
dyne/cm
25.4723
Critical Temperature (Cubic EOS)
F
1048.1
Critical Pressure (Cubic EOS)
psia
331.5
Details for Stream 9
Stream 9 (Strm 9)
Thermodynamic Methods
K-Value:
Liquid Visc:
Vapor Visc:
ASOA
NS81
NS81
Enthalpy:
Liquid ThC:
Vapor ThC:
ASOA
NS81
NS81
Density:
Surface Ten:
STD
HADD
Component Name
Total
lbmol/hr
Vapor
lbmol/hr
Liquid 1
lbmol/hr
Liquid 2
lbmol/hr
Total
mole %
K-Value
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
62.4831
71.3422
94.2083
9.59495
122.882
22.8149
136.722
209.706
80.6013
85.2361
84.0047
4.1811
3305.08
3.60771
6.75433
0
0
0.874196
0.041731
0.012993
0.00666
0.000345
0.003382
0.00031
0.00153
0.000981
0.000162
0.00007208
0.00003121
6.765E-07
2.041E-08
0.001068
0.00113
0
0
0.001763
62.4414
71.3292
94.2016
9.5946
122.879
22.8146
136.721
209.705
80.6012
85.2361
84.0046
4.1811
3305.08
3.60664
6.7532
0
0
0.872433
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1.45306
1.65908
2.19084
0.223133
2.85767
0.530567
3.17952
4.87677
1.87441
1.98219
1.95355
0.097233
76.8607
0.083898
0.157074
0
0
0.02033
39.8265
10.8552
4.21307
2.14227
1.64005
0.809928
0.666658
0.278817
0.119594
0.050393
0.022143
0.009642
3.68E-07
17.643
9.97041
0.089547
175.995
120.416
4300.1
0.072158
4300.02
0
100
Component Name
Total
lb/hr
Vapor
lb/hr
Liquid 1
lb/hr
Liquid 2
lb/hr
Total
mass %
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
1002.42
2145.12
4154.02
557.658
7141.93
1646
9863.98
18070.8
8076.09
9736.01
10773.6
594.87
1060931
158.775
230.188
0
0
24.4892
0.669488
0.39068
0.293663
0.020047
0.19655
0.022371
0.110348
0.084549
0.016208
0.008233
0.004003
0.00009625
6.552E-06
0.046993
0.038507
0
0
0.049385
1001.75
2144.73
4153.73
557.638
7141.73
1645.98
9863.87
18070.7
8076.08
9736
10773.6
594.87
1060931
158.728
230.149
0
0
24.4398
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0.08831
0.188979
0.365958
0.049128
0.629185
0.145008
0.868991
1.59199
0.711483
0.857717
0.949126
0.052407
93.4653
0.013988
0.020279
0
0
0.002157
Total
1135107
1.95113
1135105
0
100
F
psia
btu/hr
184.49
92.584
-88082300
1.6781E-05
Vapor
Liquid 1
0.072158
27.0397
1779.1355
2.3586
13.3858
11.2268
1.1923
0.36895
0.981692
0.001469
4300.024
263.9765
-20484.17
-6.7824
128.3558
118.5282
1.0829
53.8772
0.06563
Flowrates
Total
Flowrates
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Total
Flowrate
lbmol/hr
4300.0962
Molecular Weight
263.9726
Enthalpy
btu/lbmole -20483.797
Entropy
btu/lbmo/R
-6.7822
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (T-P)
gal/min
Flowrate (STP)
mmscfd
Flowrate (STP)
gal/min
Specific Gravity
GPA STP
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Surface Tension
dyne/cm
Critical Temperature (Cubic EOS)
F
1048.1
Critical Pressure (Cubic EOS)
psia
331.5
2626.8756
0.0006571
0.012903
0.020381
2506.703
0.905236
0.8955
0.059868
25.473
Details for Stream 10
Stream 10 (Strm 10)
Thermodynamic Methods
K-Value:
Liquid Visc:
Vapor Visc:
ASOA
NS81
NS81
Enthalpy:
Liquid ThC:
Vapor ThC:
ASOA
NS81
NS81
Density:
Surface Ten:
STD
HADD
Component Name
Total
lbmol/hr
Vapor
lbmol/hr
Liquid 1
lbmol/hr
Liquid 2
lbmol/hr
Total
mole %
K-Value
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
62.4831
71.3422
94.2083
9.59495
122.882
22.8149
136.722
209.706
80.6013
85.2361
84.0047
4.1811
3305.08
3.60771
6.75433
0
0
0.874196
4.74512
1.5613
0.810282
0.042109
0.413209
0.037921
0.187077
0.119989
0.019769
0.008802
0.003808
0.00008246
0.00000246
0.126666
0.13604
0
0
0.174089
57.738
69.7809
93.398
9.55284
122.469
22.7769
136.535
209.586
80.5816
85.2273
84.0008
4.18102
3305.08
3.48104
6.61829
0
0
0.700107
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1.45306
1.65908
2.19084
0.223133
2.85767
0.530567
3.17952
4.87677
1.87441
1.98219
1.95355
0.097233
76.8607
0.083898
0.157074
0
0
0.02033
42.0579
11.4501
4.43977
2.25581
1.72665
0.852005
0.701192
0.292982
0.125549
0.052851
0.023201
0.010093
3.809E-07
18.6215
10.5192
0.094634
186.034
127.253
4300.1
8.38626
4291.71
0
100
Component Name
Total
lb/hr
Vapor
lb/hr
Liquid 1
lb/hr
Liquid 2
lb/hr
Total
mass %
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
1002.42
2145.12
4154.02
557.658
7141.93
1646
9863.98
18070.8
8076.09
9736.01
10773.6
594.87
1060931
158.775
230.188
0
0
24.4892
76.1259
46.945
35.7286
2.44736
24.0157
2.73582
13.4968
10.3397
1.98083
1.00538
0.488401
0.011732
0.00079
5.57457
4.63625
0
0
4.87683
926.29
2098.17
4118.29
555.211
7117.91
1643.27
9850.48
18060.4
8074.11
9735.01
10773.1
594.859
1060931
153.2
225.551
0
0
19.6124
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0.08831
0.188979
0.365958
0.049128
0.629185
0.145008
0.868991
1.59199
0.711483
0.857717
0.949126
0.052407
93.4653
0.013988
0.020279
0
0
0.002157
Total
1135107
230.41
1134877
0
100
F
psia
btu/hr
184.48
87.584
-88082300
0.00195025
Vapor
Liquid 1
8.3863
27.4747
1806.7206
2.5596
13.5761
11.4212
1.1887
0.35455
0.981958
0.180518
4291.7099
264.4347
-20527.354
-6.7909
128.5662
118.7243
1.0829
53.8971
0.062171
Flowrates
Total
Flowrates
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Total
Flowrate
lbmol/hr
4300.0962
Molecular Weight
263.9726
Enthalpy
btu/lbmole -20483.797
Entropy
btu/lbmo/R
-6.7726
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (T-P)
gal/min
Flowrate (STP)
mmscfd
Flowrate (STP)
gal/min
Specific Gravity
GPA STP
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Surface Tension
dyne/cm
Critical Temperature (Cubic EOS)
F
1048.1
Critical Pressure (Cubic EOS)
psia
331.5
2625.3763
0.076367
0.012829
0.020195
2505.5817
0.905459
0.895331
0.059806
25.5531
Details for Stream 11
Stream 11 (Strm 11)
Thermodynamic Methods
K-Value:
Liquid Visc:
Vapor Visc:
ASOA
NS81
NS81
Enthalpy:
Liquid ThC:
Vapor ThC:
ASOA
NS81
NS81
Density:
Surface Ten:
STD
HADD
Component Name
Total
lbmol/hr
Vapor
lbmol/hr
Liquid 1
lbmol/hr
Liquid 2
lbmol/hr
Total
mole %
K-Value
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
62.4831
71.3422
94.2083
9.59495
122.882
22.8149
136.722
209.706
80.6013
85.2361
84.0047
4.1811
3305.08
3.60771
6.75433
0
0
0.874196
4.79162
1.57748
0.818791
0.042553
0.417567
0.038321
0.189052
0.121256
0.019978
0.008895
0.003848
0.00008333
2.486E-06
0.127962
0.137453
0
0
0.175567
57.6915
69.7647
93.3895
9.55239
122.465
22.7765
136.533
209.585
80.5814
85.2272
84.0008
4.18102
3305.08
3.47974
6.61688
0
0
0.698629
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1.45306
1.65908
2.19084
0.223133
2.85767
0.530567
3.17952
4.87677
1.87441
1.98219
1.95355
0.097233
76.8607
0.083898
0.157074
0
0
0.02033
42.0811
11.4563
4.44213
2.25699
1.72755
0.852443
0.701551
0.29313
0.125612
0.052877
0.023212
0.010097
3.81E-07
18.6316
10.5249
0.094687
186.139
127.324
4300.1
8.47043
4291.63
0
100
Component Name
Total
lb/hr
Vapor
lb/hr
Liquid 1
lb/hr
Liquid 2
lb/hr
Total
mass %
2 : METHANE
3 : ETHANE
4 : PROPANE
5 : I-BUTANE
6 : N-BUTANE
7 : I-PENTANE
8 : N-PENTANE
10 : N-HEXANE
11 : N-HEPTANE
12 : N-OCTANE
13 : N-NONANE
14 : N-DECANE
100 : Cut 1
49 : CO2
50 : H2S
62 : WATER
47 : OXYGEN
46 : NITROGEN
1002.42
2145.12
4154.02
557.658
7141.93
1646
9863.98
18070.8
8076.09
9736.01
10773.6
594.87
1060931
158.775
230.188
0
0
24.4892
76.8718
47.4318
36.1038
2.47315
24.269
2.76471
13.6394
10.4489
2.00174
1.01598
0.493547
0.011855
0.000798
5.63161
4.68442
0
0
4.91822
925.544
2097.68
4117.92
555.185
7117.66
1643.24
9850.34
18060.3
8074.09
9735
10773.1
594.859
1060931
153.143
225.503
0
0
19.571
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0.08831
0.188979
0.365958
0.049128
0.629185
0.145008
0.868991
1.59199
0.711483
0.857717
0.949126
0.052407
93.4653
0.013988
0.020279
0
0
0.002157
Total
1135107
232.761
1134875
0
100
F
psia
btu/hr
184.48
87.534
-88082200
0.00196982
Vapor
Liquid 1
8.4704
27.4792
1807.0043
2.5617
13.578
11.4232
1.1886
0.354409
0.98196
0.182433
4291.6257
264.4393
-20527.773
-6.7909
128.5683
118.7263
1.0829
53.8973
0.062137
Flowrates
Total
Flowrates
Properties
Temperature
Pressure
Enthalpy
Vapor Fraction
Total
Flowrate
lbmol/hr
4300.0962
Molecular Weight
263.9726
Enthalpy
btu/lbmole -20483.778
Entropy
btu/lbmo/R
-6.7725
Cp
btu/lbmol/R
Cv
btu/lbmol/R
Cp/Cv
Density
lb/ft3
Z-Factor
Flowrate (T-P)
ft3/sec
Flowrate (T-P)
gal/min
Flowrate (STP)
mmscfd
Flowrate (STP)
gal/min
Specific Gravity
GPA STP
Viscosity
cP
Thermal Conductivity
btu/ft/hr/F
Surface Tension
dyne/cm
Critical Temperature (Cubic EOS)
F
1048.1
Critical Pressure (Cubic EOS)
psia
331.5
2625.3612
0.077134
0.012828
0.020193
2505.5702
0.905461
0.89533
0.059806
25.5539
Line Module 1 (L-1)
Properties
Vapor Flowrate
Liquid Flowrate
Pipe Roughness
Pipe Drag Factor
Internal Diameter
Outside Diameter
Nominal Diameter
Pipe Wall Thickness Code
scf/hr
gal/hr
ft
inches
inches
inches
3745100
150920
0.00015
1
27.25
28
28
STD
Pressure Drop Table for Nominal Diameter 28.000 inches
Line
Segment
0
1
2
3
4
5
6
7
8
9
10
Length
ft
Elevation
ft
Pressure
psia
Delta P Friction
psi
Delta P Elevation
psi
Temperature
F
Velocity
ft/sec
Liquid
Holdup
fraction
Flow
Regime
0
10
20
30
40
50
60
70
80
90
100
0
0
0
0
0
0
0
0
0
0
0
100.04
100
99.96
99.92
99.88
99.83
99.79
99.75
99.71
99.67
99.63
0.04
0.04
0.04
0.04
0.04
0.04
0.04
0.04
0.04
0.04
0
0
0
0
0
0
0
0
0
0
185
185
185
185
185
185
185
185
185
185
185
47.3
47.4
47.4
47.4
47.4
47.4
47.5
47.5
47.5
47.5
47.6
0.0306
0.1234
0.1233
0.1233
0.1233
0.1232
0.1232
0.1232
0.1231
0.1231
0.1231
INTE
INTE
INTE
INTE
INTE
INTE
INTE
INTE
INTE
INTE
INTE
Estimated Sonic Velocity In Gas Phase for Nominal Diameter 28.000 inches
Inlet Conditions
Outlet Conditions
ft/sec
ft/sec
1168.1
1167.9
Line Module 5 (L-5)
Properties
Vapor Flowrate
Liquid Flowrate
Pipe Roughness
Pipe Efficiency Factor
Internal Diameter
Outside Diameter
Nominal Diameter
Pipe Wall Thickness Code
scf/hr
gal/hr
ft
inches
inches
inches
3762000
0
0.00015
1
23.25
24
24
STD
Pressure Drop Table for Nominal Diameter 24.000 inches
Line
Segment
0
1
2
3
4
5
6
7
8
9
10
Length
ft
Elevation
ft
Pressure
psia
Delta P Friction
psi
Delta P Elevation
psi
Temperature
F
Velocity
ft/sec
Liquid
Holdup
fraction
Flow
Regime
0
10
20
30
40
50
60
70
80
90
100
0
0
0
0
0
0
0
0
0
0
0
92.63
92.62
92.61
92.59
92.58
92.57
92.56
92.55
92.54
92.53
92.51
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0
0
0
0
0
0
0
0
0
0
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
68.4
68.4
68.4
68.5
68.5
68.5
68.5
68.5
68.5
68.5
68.5
0
0
0
0
0
0
0
0
0
0
0
TURB
TURB
TURB
TURB
TURB
TURB
TURB
TURB
TURB
TURB
TURB
Estimated Sonic Velocity In Gas Phase for Nominal Diameter 24.000 inches
Inlet Conditions
Outlet Conditions
ft/sec
ft/sec
1165.5
1165.5
Line Module 6 (L-6)
Properties
Vapor Flowrate
Liquid Flowrate
Pipe Roughness
Pipe Efficiency Factor
Internal Diameter
Outside Diameter
Nominal Diameter
Pipe Wall Thickness Code
scf/hr
gal/hr
ft
inches
inches
inches
3762000
0
0.00015
1
23.25
24
24
STD
Pressure Drop Table for Nominal Diameter 24.000 inches
Line
Segment
0
1
2
3
4
5
6
7
8
9
10
Length
ft
Elevation
ft
Pressure
psia
Delta P Friction
psi
Delta P Elevation
psi
Temperature
F
Velocity
ft/sec
Liquid
Holdup
fraction
Flow
Regime
0
10
20
30
40
50
60
70
80
90
100
0
0
0
0
0
0
0
0
0
0
0
86.91
86.9
86.89
86.88
86.87
86.85
86.84
86.83
86.82
86.81
86.79
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0.01
0
0
0
0
0
0
0
0
0
0
184.1
184.1
184.1
184.1
184.1
184.1
184.1
184.1
184.1
184.1
184.1
73
73
73
73
73
73
73
73
73
73.1
73.1
0
0
0
0
0
0
0
0
0
0
0
TURB
TURB
TURB
TURB
TURB
TURB
TURB
TURB
TURB
TURB
TURB
Estimated Sonic Velocity In Gas Phase for Nominal Diameter 24.000 inches
Inlet Conditions
Outlet Conditions
ft/sec
ft/sec
1166.1
1166.1
Line Module 7 (L-7)
Properties
Vapor Flowrate
Liquid Flowrate
Pipe Roughness
Pipe Efficiency Factor
Internal Diameter
Outside Diameter
Nominal Diameter
Pipe Wall Thickness Code
scf/hr
gal/hr
ft
inches
inches
inches
0
150400
0.00015
1
19.25
20
20
STD
Pressure Drop Table for Nominal Diameter 20.000 inches
Line
Segment
0
1
2
3
4
5
6
7
8
9
10
Length
ft
Elevation
ft
Pressure
psia
Delta P Friction
psi
Delta P Elevation
psi
Temperature
F
Velocity
ft/sec
Liquid
Holdup
fraction
Flow
Regime
0
10
20
30
40
50
60
70
80
90
100
0
0
0
0
0
0
0
0
0
0
0
92.63
92.62
92.62
92.61
92.61
92.61
92.6
92.6
92.59
92.59
92.58
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
2.9
2.9
2.9
2.9
2.9
2.9
2.9
2.9
2.9
2.9
2.9
1
1
1
1
1
1
1
1
1
1
1
PART
PART
PART
PART
PART
PART
PART
PART
PART
PART
PART
Line Module 8 (L-8)
Properties
Vapor Flowrate
Liquid Flowrate
Pipe Roughness
Pipe Drag Factor
Internal Diameter
Outside Diameter
Nominal Diameter
Pipe Wall Thickness Code
scf/hr
gal/hr
ft
inches
inches
inches
3182
150330
0.00015
1
19.25
20
20
STD
Pressure Drop Table for Nominal Diameter 20.000 inches
Line
Segment
0
1
2
3
4
5
6
7
8
9
10
Length
ft
Elevation
ft
Pressure
psia
Delta P Friction
psi
Delta P Elevation
psi
Temperature
F
Velocity
ft/sec
Liquid
Holdup
fraction
Flow
Regime
0
10
20
30
40
50
60
70
80
90
100
0
0
0
0
0
0
0
0
0
0
0
87.58
87.58
87.57
87.57
87.56
87.56
87.55
87.55
87.54
87.54
87.53
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
184.5
3
3
3
3
3
3
3
3
3
3
3
0.9701
0.9701
0.97
0.97
0.97
0.9699
0.9699
0.9699
0.9698
0.9698
0.9698
INTE
INTE
INTE
INTE
INTE
INTE
INTE
INTE
INTE
INTE
INTE
Estimated Sonic Velocity In Gas Phase for Nominal Diameter 20.000 inches
Inlet Conditions
Outlet Conditions
ft/sec
ft/sec
1154.7
1154.6