Thông số dòng và tính toán thiết bị trong hysys
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1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 2
7
8
9
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10
Overall
11
12
Vapour / Phase Fraction
13
Temperature:
14
Pressure:
15
Liquid Phase
0.0000
1.0000
(C)
94.31
94.31
(kPa)
200.0
200.0
Molar Flow
(kgmole/h)
1642
1642
16
Mass Flow
(kg/h)
1.741e+005
1.741e+005
17
Std Ideal Liq Vol Flow
199.6
18
Molar Enthalpy
19
Molar Entropy
20
Heat Flow
21
Liq Vol Flow @Std Cond
(m3/h)
199.6
(kJ/kgmole)
8345
8345
(kJ/kgmole-C)
-12.73
-12.73
(kJ/h)
1.370e+007
1.370e+007
(m3/h)
199.1 *
22
199.1
PROPERTIES
23
Overall
24
25
Molecular Weight
26
Molar Density
27
Mass Density
28
Liquid Phase
106.0
106.0
(kgmole/m3)
7.575
7.575
(kg/m3)
803.1
803.1
Act. Volume Flow
(m3/h)
216.7
216.7
29
Mass Enthalpy
(kJ/kg)
78.71
78.71
30
Mass Entropy
(kJ/kg-C)
-0.1200
-0.1200
31
Heat Capacity
(kJ/kgmole-C)
202.7
202.7
32
Mass Heat Capacity
(kJ/kg-C)
1.912
1.912
33
LHV Vol Basis (Std)
(MJ/m3)
4.378e+006
4.378e+006
34
HHV Vol Basis (Std)
(MJ/m3)
4.581e+006
4.581e+006
35
HHV Mass Basis (Std)
(kJ/kg)
4.321e+004
4.321e+004
36
CO2 Loading
---
---
37
CO2 App ML Con
(kgmole/m3)
---
---
38
CO2 App WT Con
(kgmol/kg)
---
---
39
LHV Mass Basis (Std)
(kJ/kg)
4.130e+004
4.130e+004
40
Phase Fraction [Vol. Basis]
0.0000
1.000
41
Phase Fraction [Mass Basis]
0.0000
1.000
42
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
43
Partial Pressure of CO2
44
Cost Based on Flow
45
Act. Gas Flow
(ACT_m3/h)
---
---
46
Avg. Liq. Density
(kgmole/m3)
8.225
8.225
47
Specific Heat
48
Std. Gas Flow
49
Std. Ideal Liq. Mass Density
50
Act. Liq. Flow
51
Z Factor
52
Watson K
53
User Property
54
Partial Pressure of H2S
55
Cp/(Cp - R)
56
Cp/Cv
57
Heat of Vap.
58
Kinematic Viscosity
59
Liq. Mass Density (Std. Cond)
60
Liq. Vol. Flow (Std. Cond)
61
Liquid Fraction
62
Molar Volume
63
Fluid Package:
0.0000
---
(Cost/s)
0.0000
0.0000
(kJ/kgmole-C)
202.7
202.7
(STD_m3/h)
3.882e+004
3.882e+004
Aspen Technology Inc.
Licensed to: LEGENDS
(kPa)
(kg/m3)
872.1
872.1
(m3/s)
6.020e-002
6.020e-002
8.642e-003
8.642e-003
10.34
10.34
---
---
(kPa)
0.0000
---
1.043
1.043
1.289
1.289
(kJ/kgmole)
3.406e+004
---
(cSt)
0.3620
0.3620
(kg/m3)
874.1
874.1
(m3/h)
199.1
199.1
(m3/kgmole)
1.000
1.000
0.1320
0.1320
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 1 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 2 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
12
Mass Heat of Vap.
13
Phase Fraction [Molar Basis]
14
Surface Tension
15
Thermal Conductivity
16
Viscosity
17
Cv (Semi-Ideal)
(kJ/kg)
18
Mass Cv (Semi-Ideal)
19
Cv
20
Mass Cv
21
Cv (Ent. Method)
22
Mass Cv (Ent. Method)
23
Cp/Cv (Ent. Method)
24
Reid VP at 37.8 C
25
True VP at 37.8 C
Liquid Phase
321.3
---
0.0000
1.0000
(dyne/cm)
21.12
21.12
(W/m-K)
0.1227
0.1227
(cP)
0.2907
0.2907
(kJ/kgmole-C)
194.4
194.4
(kJ/kg-C)
1.833
1.833
(kJ/kgmole-C)
157.2
157.2
(kJ/kg-C)
1.482
1.482
(kJ/kgmole-C)
162.2
162.2
(kJ/kg-C)
1.530
1.530
1.250
1.250
(kPa)
2.723
2.723
(kPa)
2.723
2.723
26
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
199.1
199.1
27
Viscosity Index
-16.58
---
28
COMPOSITION
29
30
Overall Phase
31
32
Fluid Package:
COMPONENTS
33
34
E-Benzene
35
Styrene
36
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
0.0000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
1548.1420
0.9430
164360.0484
0.9443
188.9124
0.9465
91.0982
0.0555
9488.0639
0.0545
10.4399
0.0523
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
37
Benzene
1.2100
0.0007
94.5131
0.0005
0.1071
0.0005
38
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
39
Toluene
1.2271
0.0007
113.0637
0.0006
0.1300
0.0007
40
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Total
1641.6774
1.0000
174055.6891
1.0000
199.5894
1.0000
43
Liquid Phase
44
45
COMPONENTS
46
47
E-Benzene
48
Styrene
49
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
1.000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
1548.1420
0.9430
164360.0484
0.9443
188.9124
0.9465
91.0982
0.0555
9488.0639
0.0545
10.4399
0.0523
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Benzene
1.2100
0.0007
94.5131
0.0005
0.1071
0.0005
51
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
52
Toluene
1.2271
0.0007
113.0637
0.0006
0.1300
0.0007
53
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
54
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
55
Total
1641.6774
1.0000
174055.6891
1.0000
199.5894
1.0000
56
K VALUE
57
58
COMPONENTS
MIXED
LIGHT
HEAVY
59
E-Benzene
0.0000
0.0000
---
60
Styrene
0.0000
0.0000
---
61
Hydrogen
---
---
---
62
Benzene
0.0000
0.0000
63
Aspen Technology Inc.
Licensed to: LEGENDS
Aspen HYSYS Version 7.3 (25.0.0.7336)
---
Page 2 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 2 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10
COMPONENTS
11
MIXED
LIGHT
HEAVY
12
Ethylene
---
---
---
13
Toluene
0.0000
0.0000
---
14
H2O
---
---
---
15
Methane
---
---
---
16
UNIT OPERATIONS
17
FEED TO
18
19
PRODUCT FROM
Heater:
E-100
Mixer:
LOGICAL CONNECTION
MIX-100
20
UTILITIES
21
( No utilities reference this stream )
22
23
PROCESS UTILITY
24
25
26
DYNAMICS
27
28
Pressure Specification
(Inactive):
29
Flow Specification
(Inactive)
200.0 kPa
Molar:
1642 kgmole/h
30
Mass:
1.741e+005 kg/h
Std Ideal Liq Volume:
199.6 m3/h
User Variables
31
32
NOTES
33
34
35
Description
36
37
38
Material Stream: 3
39
40
41
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
42
Overall
43
Vapour Phase
44
Vapour / Phase Fraction
1.0000
45
Temperature:
1.0000
46
Pressure:
47
Molar Flow
(kgmole/h)
1642
1642
48
Mass Flow
(kg/h)
1.741e+005
1.741e+005
49
Std Ideal Liq Vol Flow
50
Molar Enthalpy
51
Molar Entropy
52
Heat Flow
53
Liq Vol Flow @Std Cond
(C)
240.0 *
240.0
(kPa)
170.0 *
170.0
(m3/h)
199.6
199.6
(kJ/kgmole)
7.276e+004
7.276e+004
(kJ/kgmole-C)
136.2
136.2
(kJ/h)
1.195e+008
1.195e+008
(m3/h)
199.1 *
54
199.1
PROPERTIES
55
Overall
56
Vapour Phase
57
Molecular Weight
58
Molar Density
(kgmole/m3)
59
Mass Density
(kg/m3)
4.365
4.365
60
Act. Volume Flow
(m3/h)
3.988e+004
3.988e+004
61
Mass Enthalpy
(kJ/kg)
686.3
686.3
62
Mass Entropy
(kJ/kg-C)
1.285
1.285
63
Aspen Technology Inc.
Licensed to: LEGENDS
106.0
106.0
4.117e-002
4.117e-002
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 3 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 3 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
12
Heat Capacity
13
Vapour Phase
(kJ/kgmole-C)
210.5
Mass Heat Capacity
(kJ/kg-C)
1.985
210.5
1.985
14
LHV Vol Basis (Std)
(MJ/m3)
4.378e+006
4.378e+006
15
HHV Vol Basis (Std)
(MJ/m3)
4.581e+006
4.581e+006
16
HHV Mass Basis (Std)
(kJ/kg)
4.321e+004
4.321e+004
17
CO2 Loading
---
---
18
CO2 App ML Con
(kgmole/m3)
---
---
19
CO2 App WT Con
(kgmol/kg)
---
---
20
LHV Mass Basis (Std)
(kJ/kg)
4.130e+004
4.130e+004
21
Phase Fraction [Vol. Basis]
1.000
1.000
22
Phase Fraction [Mass Basis]
1.000
1.000
23
Phase Fraction [Act. Vol. Basis]
1.000
1.000
24
Partial Pressure of CO2
25
Cost Based on Flow
26
27
28
Specific Heat
29
Std. Gas Flow
30
Std. Ideal Liq. Mass Density
31
Act. Liq. Flow
32
Z Factor
33
Watson K
34
User Property
35
Partial Pressure of H2S
36
Cp/(Cp - R)
37
Cp/Cv
38
Heat of Vap.
39
Kinematic Viscosity
40
Liq. Mass Density (Std. Cond)
41
Liq. Vol. Flow (Std. Cond)
42
Liquid Fraction
43
Molar Volume
44
Mass Heat of Vap.
45
Phase Fraction [Molar Basis]
46
Surface Tension
47
Thermal Conductivity
48
Viscosity
49
Cv (Semi-Ideal)
50
Mass Cv (Semi-Ideal)
51
Cv
52
Mass Cv
53
Cv (Ent. Method)
54
Mass Cv (Ent. Method)
55
Cp/Cv (Ent. Method)
56
Reid VP at 37.8 C
57
True VP at 37.8 C
58
59
Viscosity Index
(kPa)
0.0000
---
(Cost/s)
0.0000
0.0000
Act. Gas Flow
(ACT_m3/h)
3.988e+004
3.988e+004
Avg. Liq. Density
(kgmole/m3)
8.225
8.225
(kJ/kgmole-C)
210.5
210.5
(STD_m3/h)
3.882e+004
3.882e+004
(kg/m3)
872.1
872.1
(m3/s)
---
---
0.9679
0.9679
10.34
10.34
---
---
(kPa)
0.0000
---
1.041
1.041
1.047
1.047
(kJ/kgmole)
3.450e+004
---
(cSt)
2.373
2.373
(kg/m3)
874.1
874.1
(m3/h)
199.1
199.1
0.0000
0.0000
(m3/kgmole)
24.29
24.29
(kJ/kg)
325.4
---
1.0000
1.0000
(dyne/cm)
---
---
(W/m-K)
2.906e-002
2.906e-002
(cP)
1.036e-002
1.036e-002
(kJ/kgmole-C)
202.2
202.2
(kJ/kg-C)
1.907
1.907
(kJ/kgmole-C)
201.1
201.1
(kJ/kg-C)
1.896
1.896
(kJ/kgmole-C)
---
---
(kJ/kg-C)
---
---
---
---
(kPa)
2.723
2.723
(kPa)
2.723
2.723
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
199.1
199.1
---
---
60
61
62
63
Aspen Technology Inc.
Licensed to: LEGENDS
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 4 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 3 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10
11
Overall Phase
12
13
Fluid Package:
COMPONENTS
MOLAR FLOW
(kgmole/h)
14
15
E-Benzene
16
Styrene
17
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
1.0000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
1548.1420
0.9430
164360.0484
0.9443
188.9124
0.9465
91.0982
0.0555
9488.0639
0.0545
10.4399
0.0523
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
18
Benzene
1.2100
0.0007
94.5131
0.0005
0.1071
0.0005
19
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
20
Toluene
1.2271
0.0007
113.0637
0.0006
0.1300
0.0007
21
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
22
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
23
Total
1641.6774
1.0000
174055.6891
1.0000
199.5894
1.0000
24
Vapour Phase
25
26
COMPONENTS
MOLAR FLOW
(kgmole/h)
27
28
E-Benzene
29
Styrene
30
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
1.000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
1548.1420
0.9430
164360.0484
0.9443
188.9124
0.9465
91.0982
0.0555
9488.0639
0.0545
10.4399
0.0523
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
31
Benzene
1.2100
0.0007
94.5131
0.0005
0.1071
0.0005
32
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
33
Toluene
1.2271
0.0007
113.0637
0.0006
0.1300
0.0007
34
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
35
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
36
Total
1641.6774
1.0000
174055.6891
1.0000
199.5894
1.0000
37
K VALUE
38
COMPONENTS
39
MIXED
LIGHT
HEAVY
40
E-Benzene
---
---
---
41
Styrene
---
---
---
42
Hydrogen
---
---
---
43
Benzene
---
---
---
44
Ethylene
---
---
---
45
Toluene
---
---
---
46
H2O
---
---
---
47
Methane
---
---
---
48
UNIT OPERATIONS
49
FEED TO
50
51
Mixer:
PRODUCT FROM
MIX-101
52
Heater:
LOGICAL CONNECTION
E-100
UTILITIES
53
( No utilities reference this stream )
54
55
PROCESS UTILITY
56
57
58
DYNAMICS
59
60
Pressure Specification
(Active):
61
Flow Specification
(Inactive)
170.0 kPa *
Molar:
1642 kgmole/h
Mass:
1.741e+005 kg/h
Std Ideal Liq Volume:
199.6 m3/h
62
63
Aspen Technology Inc.
Licensed to: LEGENDS
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 5 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 3 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
User Variables
10
11
NOTES
12
13
14
Description
15
16
17
Material Stream: 6
18
19
20
CONDITIONS
21
Overall
22
23
Vapour / Phase Fraction
24
Temperature:
25
Pressure:
26
Vapour Phase
1.0000
1.0000
(C)
722.0 *
722.0
(kPa)
170.0 *
170.0
Molar Flow
(kgmole/h)
3000 *
27
Mass Flow
(kg/h)
28
Std Ideal Liq Vol Flow
29
Molar Enthalpy
30
Molar Entropy
31
Heat Flow
32
Liq Vol Flow @Std Cond
5.405e+004
3000
5.405e+004
(m3/h)
54.15
54.15
(kJ/kgmole)
-2.159e+005
-2.159e+005
(kJ/kgmole-C)
213.2
213.2
(kJ/h)
-6.478e+008
-6.478e+008
(m3/h)
53.26 *
33
53.26
PROPERTIES
34
Overall
35
Vapour Phase
36
Molecular Weight
37
Molar Density
(kgmole/m3)
38
Mass Density
(kg/m3)
0.3703
0.3703
39
Act. Volume Flow
(m3/h)
1.459e+005
1.459e+005
40
Mass Enthalpy
(kJ/kg)
-1.199e+004
-1.199e+004
41
Mass Entropy
(kJ/kg-C)
11.84
11.84
42
Heat Capacity
(kJ/kgmole-C)
41.26
41.26
43
Mass Heat Capacity
(kJ/kg-C)
2.290
2.290
44
LHV Vol Basis (Std)
(MJ/m3)
0.0000
0.0000
45
HHV Vol Basis (Std)
(MJ/m3)
4.101e+004
4.101e+004
46
HHV Mass Basis (Std)
(kJ/kg)
2276
2276
47
CO2 Loading
---
---
48
CO2 App ML Con
(kgmole/m3)
---
---
49
CO2 App WT Con
(kgmol/kg)
---
---
50
LHV Mass Basis (Std)
(kJ/kg)
---
---
51
Phase Fraction [Vol. Basis]
1.000
1.000
52
Phase Fraction [Mass Basis]
1.000
1.000
53
Phase Fraction [Act. Vol. Basis]
1.000
1.000
54
Partial Pressure of CO2
55
Cost Based on Flow
56
57
58
Specific Heat
59
Std. Gas Flow
60
Std. Ideal Liq. Mass Density
61
Act. Liq. Flow
62
63
18.02
18.02
2.056e-002
2.056e-002
(kPa)
0.0000
---
(Cost/s)
0.0000
0.0000
Act. Gas Flow
(ACT_m3/h)
1.459e+005
1.459e+005
Avg. Liq. Density
(kgmole/m3)
55.40
55.40
(kJ/kgmole-C)
41.26
41.26
(STD_m3/h)
7.093e+004
7.093e+004
(kg/m3)
998.0
998.0
(m3/s)
---
---
Z Factor
0.9995
0.9995
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3
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5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 6 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
Vapour Phase
12
Watson K
---
---
13
User Property
---
---
14
Partial Pressure of H2S
15
Cp/(Cp - R)
16
Cp/Cv
17
Heat of Vap.
18
Kinematic Viscosity
19
Liq. Mass Density (Std. Cond)
20
Liq. Vol. Flow (Std. Cond)
21
Liquid Fraction
22
Molar Volume
23
Mass Heat of Vap.
24
Phase Fraction [Molar Basis]
25
Surface Tension
26
Thermal Conductivity
27
Viscosity
28
Cv (Semi-Ideal)
29
Mass Cv (Semi-Ideal)
30
Cv
31
Mass Cv
32
Cv (Ent. Method)
33
Mass Cv (Ent. Method)
34
Cp/Cv (Ent. Method)
35
Reid VP at 37.8 C
36
True VP at 37.8 C
37
38
Viscosity Index
(kPa)
0.0000
---
1.252
1.252
1.254
1.254
(kJ/kgmole)
4.028e+004
---
(cSt)
77.84
77.84
(kg/m3)
1015
1015
(m3/h)
53.26
53.26
0.0000
0.0000
(m3/kgmole)
48.64
48.64
(kJ/kg)
2236
---
1.0000
1.0000
(dyne/cm)
---
---
(W/m-K)
8.603e-002
8.603e-002
(cP)
2.883e-002
2.883e-002
(kJ/kgmole-C)
32.95
32.95
(kJ/kg-C)
1.829
1.829
(kJ/kgmole-C)
32.91
32.91
(kJ/kg-C)
1.827
1.827
(kJ/kgmole-C)
---
---
(kJ/kg-C)
---
---
---
---
(kPa)
6.467
6.467
(kPa)
6.467
6.467
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
53.26
53.26
10.58
---
39
COMPOSITION
40
41
Overall Phase
42
43
Fluid Package:
COMPONENTS
44
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
1.0000
LIQUID VOLUME
FRACTION
45
E-Benzene
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
46
Styrene
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
47
Hydrogen
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
48
Benzene
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
49
Ethylene
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
50
Toluene
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
51
H2O
3000.0000 *
1.0000 *
54045.3014 *
1.0000 *
54.1544 *
1.0000 *
52
Methane
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
53
Total
3000.0000
1.0000
54
1.0000
Vapour Phase
55
56
54045.3014
COMPONENTS
57
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
54.1544
1.0000
Phase Fraction
1.000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
58
E-Benzene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
59
Styrene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Benzene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
63
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0.0000
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5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 6 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10
11
Vapour Phase (continued)
12
13
Fluid Package:
COMPONENTS
MOLAR FLOW
(kgmole/h)
14
15
Toluene
16
H2O
17
Methane
18
Total
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
MASS FRACTION
1.000
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
3000.0000
1.0000
54045.3014
1.0000
54.1544
1.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
3000.0000
1.0000
54045.3014
1.0000
54.1544
1.0000
19
K VALUE
20
COMPONENTS
21
MIXED
LIGHT
HEAVY
22
E-Benzene
---
---
---
23
Styrene
---
---
---
24
Hydrogen
---
---
---
25
Benzene
---
---
---
26
Ethylene
---
---
---
27
Toluene
---
---
---
28
H2O
---
---
---
29
Methane
---
---
---
30
UNIT OPERATIONS
31
FEED TO
32
33
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-101
34
UTILITIES
35
( No utilities reference this stream )
36
37
PROCESS UTILITY
38
39
40
DYNAMICS
41
42
Pressure Specification
(Active):
43
Flow Specification
(Active)
170.0 kPa *
Molar:
3000 kgmole/h *
44
Mass:
5.405e+004 kg/h
Std Ideal Liq Volume:
54.15 m3/h
User Variables
45
46
NOTES
47
48
49
Description
50
51
52
Material Stream: 1
53
54
55
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
56
Overall
57
58
Vapour / Phase Fraction
59
Temperature:
60
Pressure:
61
62
63
Fluid Package:
Liquid Phase
0.0000
1.0000
(C)
136.0 *
136.0
(kPa)
200.0 *
200.0
Molar Flow
(kgmole/h)
123.4 *
Mass Flow
(kg/h)
Aspen Technology Inc.
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1.305e+004
123.4
1.305e+004
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3
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5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 1 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
10
Overall
11
12
Std Ideal Liq Vol Flow
13
Molar Enthalpy
14
Molar Entropy
15
Heat Flow
16
Liq Vol Flow @Std Cond
Liquid Phase
(m3/h)
15.00
15.00
(kJ/kgmole)
1.149e+004
1.149e+004
(kJ/kgmole-C)
-20.27
-20.27
(kJ/h)
1.418e+006
1.418e+006
(m3/h)
14.96 *
17
14.96
PROPERTIES
18
Overall
19
20
Molecular Weight
21
Molar Density
22
Mass Density
23
Liquid Phase
105.8
105.8
(kgmole/m3)
7.190
7.190
(kg/m3)
760.3
760.3
Act. Volume Flow
(m3/h)
17.17
17.17
24
Mass Enthalpy
(kJ/kg)
108.6
108.6
25
Mass Entropy
(kJ/kg-C)
-0.1917
-0.1917
26
Heat Capacity
(kJ/kgmole-C)
221.6
221.6
27
Mass Heat Capacity
(kJ/kg-C)
2.095
2.095
28
LHV Vol Basis (Std)
(MJ/m3)
4.371e+006
4.371e+006
29
HHV Vol Basis (Std)
(MJ/m3)
4.575e+006
4.575e+006
30
HHV Mass Basis (Std)
(kJ/kg)
4.326e+004
4.326e+004
31
CO2 Loading
---
---
32
CO2 App ML Con
(kgmole/m3)
---
---
33
CO2 App WT Con
(kgmol/kg)
---
---
34
LHV Mass Basis (Std)
(kJ/kg)
4.133e+004
4.133e+004
35
Phase Fraction [Vol. Basis]
0.0000
1.000
36
Phase Fraction [Mass Basis]
0.0000
1.000
37
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
38
Partial Pressure of CO2
39
Cost Based on Flow
40
Act. Gas Flow
(ACT_m3/h)
---
---
41
Avg. Liq. Density
(kgmole/m3)
8.228
8.228
42
Specific Heat
(kJ/kgmole-C)
221.6
221.6
43
Std. Gas Flow
(STD_m3/h)
2918
2918
44
Std. Ideal Liq. Mass Density
(kg/m3)
870.1
870.1
45
Act. Liq. Flow
(m3/s)
4.768e-003
4.768e-003
46
Z Factor
8.177e-003
8.177e-003
47
Watson K
10.35
10.35
48
User Property
---
---
49
Partial Pressure of H2S
50
Cp/(Cp - R)
51
Cp/Cv
52
Heat of Vap.
53
Kinematic Viscosity
54
Liq. Mass Density (Std. Cond)
55
Liq. Vol. Flow (Std. Cond)
56
Liquid Fraction
57
Molar Volume
58
Mass Heat of Vap.
59
Phase Fraction [Molar Basis]
60
Surface Tension
61
Thermal Conductivity
62
Viscosity
63
Aspen Technology Inc.
Licensed to: LEGENDS
(kPa)
0.0000
---
(Cost/s)
0.0000
0.0000
(kPa)
0.0000
---
1.039
1.039
1.281
1.281
(kJ/kgmole)
3.411e+004
---
(cSt)
0.2754
0.2754
(kg/m3)
872.4
872.4
(m3/h)
14.96
14.96
(m3/kgmole)
(kJ/kg)
1.000
1.000
0.1391
0.1391
322.5
---
0.0000
1.0000
(dyne/cm)
16.77
16.77
(W/m-K)
0.1120
0.1120
0.2094
0.2094
(cP)
Aspen HYSYS Version 7.3 (25.0.0.7336)
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3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 1 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
12
Cv (Semi-Ideal)
13
Mass Cv (Semi-Ideal)
14
Cv
15
Mass Cv
16
Cv (Ent. Method)
17
Mass Cv (Ent. Method)
18
Cp/Cv (Ent. Method)
19
Reid VP at 37.8 C
20
True VP at 37.8 C
Liquid Phase
(kJ/kgmole-C)
213.2
213.2
(kJ/kg-C)
2.016
2.016
(kJ/kgmole-C)
173.0
173.0
(kJ/kg-C)
1.636
1.636
(kJ/kgmole-C)
173.4
173.4
(kJ/kg-C)
1.640
1.640
1.278
1.278
(kPa)
3.009
3.009
(kPa)
3.010
3.010
21
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
14.96
14.96
22
Viscosity Index
-27.14
---
23
COMPOSITION
24
25
Overall Phase
26
27
Fluid Package:
COMPONENTS
28
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
0.0000
LIQUID VOLUME
FRACTION
29
E-Benzene
121.0000 *
0.9804 *
12846.0860 *
0.9842 *
14.7651 *
0.9843 *
30
Styrene
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
31
Hydrogen
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
32
Benzene
1.2100 *
0.0098 *
94.5131 *
0.0072 *
0.1071 *
0.0071 *
33
Ethylene
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
34
Toluene
1.2100 *
0.0098 *
111.4904 *
0.0085 *
0.1281 *
0.0085 *
35
H2O
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
36
Methane
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
37
Total
123.4200
1.0000
38
1.0000
15.0003
Liquid Phase
39
40
13052.0895
COMPONENTS
41
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
1.0000
Phase Fraction
1.000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
42
E-Benzene
121.0000
0.9804
12846.0860
0.9842
14.7651
0.9843
43
Styrene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Benzene
1.2100
0.0098
94.5131
0.0072
0.1071
0.0071
46
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
47
Toluene
1.2100
0.0098
111.4904
0.0085
0.1281
0.0085
48
H2O
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
49
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
50
Total
123.4200
1.0000
13052.0895
1.0000
15.0003
1.0000
51
K VALUE
52
53
COMPONENTS
MIXED
LIGHT
HEAVY
54
E-Benzene
0.0000
0.0000
---
55
Styrene
---
---
---
56
Hydrogen
---
---
---
57
Benzene
0.0000
0.0000
---
58
Ethylene
---
---
---
59
Toluene
0.0000
0.0000
---
60
H2O
---
---
---
61
Methane
---
---
---
62
63
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Page 10 of 236
* Specified by user.
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3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 1 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10
FEED TO
11
12
Fluid Package:
PRODUCT FROM
Mixer:
LOGICAL CONNECTION
MIX-100
13
UTILITIES
14
( No utilities reference this stream )
15
16
PROCESS UTILITY
17
18
19
DYNAMICS
20
21
Pressure Specification
(Active):
22
Flow Specification
(Active)
200.0 kPa *
Molar:
123.4 kgmole/h *
23
Mass:
1.305e+004 kg/h
Std Ideal Liq Volume:
15.00 m3/h
User Variables
24
25
NOTES
26
27
28
Description
29
30
31
Material Stream: 9
32
33
34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35
Overall
36
Vapour Phase
37
Vapour / Phase Fraction
1.0000
38
Temperature:
1.0000
39
Pressure:
40
Molar Flow
(kgmole/h)
4643
4643
41
Mass Flow
(kg/h)
2.281e+005
2.281e+005
42
Std Ideal Liq Vol Flow
43
Molar Enthalpy
44
Molar Entropy
45
Heat Flow
46
Liq Vol Flow @Std Cond
(C)
550.0 *
550.0
(kPa)
135.0 *
135.0
(m3/h)
253.8
253.8
(kJ/kgmole)
-9.070e+004
-9.070e+004
(kJ/kgmole-C)
230.0
230.0
(kJ/h)
-4.211e+008
-4.211e+008
(m3/h)
242.8 *
47
242.8
PROPERTIES
48
Overall
49
Vapour Phase
50
Molecular Weight
51
Molar Density
(kgmole/m3)
52
Mass Density
(kg/m3)
0.9703
0.9703
53
Act. Volume Flow
(m3/h)
2.351e+005
2.351e+005
54
Mass Enthalpy
(kJ/kg)
-1846
-1846
55
Mass Entropy
(kJ/kg-C)
4.682
4.682
56
Heat Capacity
(kJ/kgmole-C)
125.9
125.9
57
Mass Heat Capacity
(kJ/kg-C)
2.564
2.564
58
LHV Vol Basis (Std)
(MJ/m3)
1.548e+006
1.548e+006
59
HHV Vol Basis (Std)
(MJ/m3)
1.646e+006
1.646e+006
60
HHV Mass Basis (Std)
(kJ/kg)
3.351e+004
3.351e+004
61
CO2 Loading
---
---
62
CO2 App ML Con
---
---
63
Aspen Technology Inc.
Licensed to: LEGENDS
(kgmole/m3)
49.13
49.13
1.975e-002
1.975e-002
Aspen HYSYS Version 7.3 (25.0.0.7336)
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3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 9 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
12
CO2 App WT Con
13
LHV Mass Basis (Std)
14
15
Vapour Phase
(kgmol/kg)
---
---
(kJ/kg)
3.151e+004
3.151e+004
Phase Fraction [Vol. Basis]
1.000
1.000
Phase Fraction [Mass Basis]
1.000
1.000
16
Phase Fraction [Act. Vol. Basis]
1.000
1.000
17
Partial Pressure of CO2
18
Cost Based on Flow
19
20
21
Specific Heat
22
Std. Gas Flow
23
Std. Ideal Liq. Mass Density
24
Act. Liq. Flow
25
Z Factor
26
Watson K
27
User Property
28
Partial Pressure of H2S
29
Cp/(Cp - R)
30
Cp/Cv
31
Heat of Vap.
32
Kinematic Viscosity
33
Liq. Mass Density (Std. Cond)
34
Liq. Vol. Flow (Std. Cond)
35
Liquid Fraction
36
Molar Volume
37
Mass Heat of Vap.
38
Phase Fraction [Molar Basis]
39
Surface Tension
40
Thermal Conductivity
41
Viscosity
42
Cv (Semi-Ideal)
43
Mass Cv (Semi-Ideal)
44
Cv
45
Mass Cv
46
Cv (Ent. Method)
47
Mass Cv (Ent. Method)
48
Cp/Cv (Ent. Method)
49
Reid VP at 37.8 C
50
True VP at 37.8 C
51
52
Viscosity Index
(kPa)
0.0000
---
(Cost/s)
0.0000
0.0000
Act. Gas Flow
(ACT_m3/h)
2.351e+005
2.351e+005
Avg. Liq. Density
(kgmole/m3)
18.30
18.30
(kJ/kgmole-C)
125.9
125.9
(STD_m3/h)
1.098e+005
1.098e+005
(kg/m3)
898.8
898.8
(m3/s)
---
---
0.9988
0.9988
10.34
10.34
---
---
(kPa)
0.0000
---
1.071
1.071
1.071
1.071
(kJ/kgmole)
8.017e+004
---
(cSt)
24.56
24.56
(kg/m3)
939.5
939.5
(m3/h)
242.8
242.8
0.0000
0.0000
(m3/kgmole)
50.63
50.63
(kJ/kg)
1632
---
1.0000
1.0000
(dyne/cm)
---
---
(W/m-K)
6.702e-002
6.702e-002
(cP)
2.383e-002
2.383e-002
(kJ/kgmole-C)
117.6
117.6
(kJ/kg-C)
2.394
2.394
(kJ/kgmole-C)
117.6
117.6
(kJ/kg-C)
2.393
2.393
(kJ/kgmole-C)
---
---
(kJ/kg-C)
---
---
---
---
(kPa)
6.882
6.882
(kPa)
208.3
208.3
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
242.8
242.8
5.995
---
53
COMPOSITION
54
55
Overall Phase
56
57
Fluid Package:
COMPONENTS
58
59
E-Benzene
60
Styrene
61
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
1.0000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
1546.8039
0.3331
164217.9837
0.7199
188.7491
0.7438
92.4363
0.0199
9627.4266
0.0422
10.5932
0.0417
Hydrogen
1.3380
0.0003
2.6974
0.0000
0.0386
0.0002
62
Benzene
1.2100
0.0003
94.5136
0.0004
0.1071
63
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Licensed to: LEGENDS
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0.0004
Page 12 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 9 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10
11
Overall Phase (continued)
12
13
Fluid Package:
COMPONENTS
MOLAR FLOW
(kgmole/h)
14
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
1.0000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
15
Ethylene
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
16
Toluene
1.2271
0.0003
113.0694
0.0005
0.1300
0.0005
17
H2O
3000.0000
0.6461
54045.3014
0.2369
54.1544
0.2134
18
Methane
0.0001
0.0000
0.0010
0.0000
0.0000
0.0000
19
Total
4643.0154
1.0000
228100.9933
1.0000
253.7724
1.0000
20
Vapour Phase
21
22
COMPONENTS
MOLAR FLOW
(kgmole/h)
23
24
E-Benzene
25
Styrene
26
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
1.000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
1546.8039
0.3331
164217.9837
0.7199
188.7491
0.7438
92.4363
0.0199
9627.4266
0.0422
10.5932
0.0417
Hydrogen
1.3380
0.0003
2.6974
0.0000
0.0386
0.0002
27
Benzene
1.2100
0.0003
94.5136
0.0004
0.1071
0.0004
28
Ethylene
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
29
Toluene
1.2271
0.0003
113.0694
0.0005
0.1300
0.0005
30
H2O
3000.0000
0.6461
54045.3014
0.2369
54.1544
0.2134
31
Methane
0.0001
0.0000
0.0010
0.0000
0.0000
0.0000
32
Total
4643.0154
1.0000
228100.9933
1.0000
253.7724
1.0000
33
K VALUE
34
35
COMPONENTS
MIXED
LIGHT
HEAVY
36
E-Benzene
---
---
---
37
Styrene
---
---
---
38
Hydrogen
---
---
---
39
Benzene
---
---
---
40
Ethylene
---
---
---
41
Toluene
---
---
---
42
H2O
---
---
---
43
Methane
---
---
---
44
UNIT OPERATIONS
45
FEED TO
46
47
Plug Flow Reactor:
PRODUCT FROM
PFR-101
48
Heater:
LOGICAL CONNECTION
E-101
UTILITIES
49
( No utilities reference this stream )
50
51
PROCESS UTILITY
52
53
54
DYNAMICS
55
56
Pressure Specification
(Active):
57
Flow Specification
(Inactive)
58
135.0 kPa *
Molar:
4643 kgmole/h
Mass:
2.281e+005 kg/h
Std Ideal Liq Volume:
253.8 m3/h
User Variables
59
60
NOTES
61
62
63
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Licensed to: LEGENDS
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Page 13 of 236
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1
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3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 9 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Description
10
11
12
Material Stream: 11
13
14
15
CONDITIONS
16
Overall
17
Vapour Phase
18
Vapour / Phase Fraction
1.0000
19
Temperature:
1.0000
20
Pressure:
21
Molar Flow
(kgmole/h)
4754
4754
22
Mass Flow
(kg/h)
2.281e+005
2.281e+005
23
Std Ideal Liq Vol Flow
24
Molar Enthalpy
25
Molar Entropy
26
Heat Flow
27
Liq Vol Flow @Std Cond
(C)
267.0 *
267.0
(kPa)
110.0 *
110.0
(m3/h)
256.2
256.2
(kJ/kgmole)
-1.173e+005
-1.173e+005
(kJ/kgmole-C)
196.2
196.2
(kJ/h)
-5.575e+008
-5.575e+008
(m3/h)
246.3 *
28
246.3
PROPERTIES
29
Overall
30
Vapour Phase
31
Molecular Weight
47.98
32
Molar Density
(kgmole/m3)
47.98
2.461e-002
2.461e-002
33
Mass Density
(kg/m3)
1.181
1.181
34
Act. Volume Flow
(m3/h)
1.932e+005
1.932e+005
35
Mass Enthalpy
(kJ/kg)
-2444
-2444
36
Mass Entropy
(kJ/kg-C)
4.088
4.088
37
Heat Capacity
(kJ/kgmole-C)
98.10
98.10
38
Mass Heat Capacity
(kJ/kg-C)
2.045
2.045
39
LHV Vol Basis (Std)
(MJ/m3)
1.514e+006
1.514e+006
40
HHV Vol Basis (Std)
(MJ/m3)
1.610e+006
1.610e+006
41
HHV Mass Basis (Std)
(kJ/kg)
3.354e+004
3.354e+004
42
CO2 Loading
---
---
43
CO2 App ML Con
(kgmole/m3)
---
---
44
CO2 App WT Con
(kgmol/kg)
---
---
45
LHV Mass Basis (Std)
(kJ/kg)
3.155e+004
3.155e+004
46
Phase Fraction [Vol. Basis]
1.000
1.000
47
Phase Fraction [Mass Basis]
1.000
1.000
48
Phase Fraction [Act. Vol. Basis]
1.000
1.000
49
Partial Pressure of CO2
50
Cost Based on Flow
51
52
53
Specific Heat
54
Std. Gas Flow
55
Std. Ideal Liq. Mass Density
56
Act. Liq. Flow
57
Z Factor
58
Watson K
59
User Property
60
Partial Pressure of H2S
61
Cp/(Cp - R)
62
Cp/Cv
63
Aspen Technology Inc.
(kPa)
0.0000
---
(Cost/s)
0.0000
0.0000
Act. Gas Flow
(ACT_m3/h)
1.932e+005
1.932e+005
Avg. Liq. Density
(kgmole/m3)
18.56
18.56
(kJ/kgmole-C)
98.10
98.10
(STD_m3/h)
1.124e+005
1.124e+005
(kg/m3)
890.5
890.5
(m3/s)
---
---
0.9953
0.9953
10.31
10.31
---
---
Licensed to: LEGENDS
(kPa)
0.0000
---
1.093
1.093
1.095
1.095
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 14 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 11 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
12
Heat of Vap.
13
Kinematic Viscosity
14
Liq. Mass Density (Std. Cond)
15
Liq. Vol. Flow (Std. Cond)
16
Liquid Fraction
17
Molar Volume
18
Mass Heat of Vap.
19
Phase Fraction [Molar Basis]
20
Surface Tension
21
Thermal Conductivity
22
Viscosity
23
Cv (Semi-Ideal)
24
Mass Cv (Semi-Ideal)
25
Cv
26
Mass Cv
27
Cv (Ent. Method)
28
Mass Cv (Ent. Method)
29
Cp/Cv (Ent. Method)
30
Reid VP at 37.8 C
31
True VP at 37.8 C
32
33
Viscosity Index
Vapour Phase
(kJ/kgmole)
7.839e+004
---
(cSt)
12.51
12.51
(kg/m3)
926.0
926.0
(m3/h)
246.3
246.3
0.0000
0.0000
(m3/kgmole)
40.63
40.63
(kJ/kg)
1634
---
1.0000
1.0000
(dyne/cm)
---
---
(W/m-K)
3.810e-002
3.810e-002
(cP)
1.478e-002
1.478e-002
(kJ/kgmole-C)
89.79
89.79
(kJ/kg-C)
1.871
1.871
(kJ/kgmole-C)
89.62
89.62
(kJ/kg-C)
1.868
1.868
(kJ/kgmole-C)
---
---
(kJ/kg-C)
---
---
---
---
(kPa)
353.2
353.2
(kPa)
1.802e+004
1.802e+004
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
246.3
246.3
-2.547
---
34
COMPOSITION
35
36
Overall Phase
37
38
Fluid Package:
COMPONENTS
39
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
1.0000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
40
E-Benzene
1435.5929
0.3020
152411.1535
0.6682
175.1786
0.6839
41
Styrene
203.2845
0.0428
21172.4917
0.0928
23.2964
0.0909
42
Hydrogen
111.8507
0.0235
225.4910
0.0010
3.2278
0.0126
43
Benzene
1.2373
0.0003
96.6430
0.0004
0.1095
0.0004
44
Ethylene
0.0273
0.0000
0.7650
0.0000
0.0020
0.0000
45
Toluene
1.5627
0.0003
143.9860
0.0006
0.1655
0.0006
46
H2O
3000.0000
0.6311
54045.3014
0.2369
54.1544
0.2114
47
Methane
0.3356
0.0001
5.3840
0.0000
0.0180
0.0001
48
Total
4753.8909
1.0000
228101.2156
1.0000
256.1522
1.0000
49
Vapour Phase
50
51
COMPONENTS
52
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
1.000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
53
E-Benzene
1435.5929
0.3020
152411.1535
0.6682
175.1786
0.6839
54
Styrene
203.2845
0.0428
21172.4917
0.0928
23.2964
0.0909
55
Hydrogen
111.8507
0.0235
225.4910
0.0010
3.2278
0.0126
56
Benzene
1.2373
0.0003
96.6430
0.0004
0.1095
0.0004
57
Ethylene
0.0273
0.0000
0.7650
0.0000
0.0020
0.0000
58
Toluene
1.5627
0.0003
143.9860
0.0006
0.1655
0.0006
59
H2O
3000.0000
0.6311
54045.3014
0.2369
54.1544
0.2114
60
Methane
0.3356
0.0001
5.3840
0.0000
0.0180
0.0001
61
Total
4753.8909
1.0000
228101.2156
1.0000
256.1522
1.0000
62
63
Aspen Technology Inc.
Licensed to: LEGENDS
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 15 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 11 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
K VALUE
10
COMPONENTS
11
MIXED
LIGHT
HEAVY
12
E-Benzene
---
---
---
13
Styrene
---
---
---
14
Hydrogen
---
---
---
15
Benzene
---
---
---
16
Ethylene
---
---
---
17
Toluene
---
---
---
18
H2O
---
---
---
19
Methane
---
---
---
20
UNIT OPERATIONS
21
FEED TO
22
23
PRODUCT FROM
Cooler:
E-103
Cooler:
LOGICAL CONNECTION
E-102
24
UTILITIES
25
( No utilities reference this stream )
26
27
PROCESS UTILITY
28
29
30
DYNAMICS
31
32
Pressure Specification
(Active):
33
Flow Specification
(Inactive)
110.0 kPa *
Molar:
4754 kgmole/h
34
Mass:
2.281e+005 kg/h
Std Ideal Liq Volume:
256.2 m3/h
User Variables
35
36
NOTES
37
38
39
Description
40
41
42
Material Stream: 12
43
44
45
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
46
Overall
47
Vapour Phase
48
Vapour / Phase Fraction
49
Temperature:
50
Pressure:
51
Molar Flow
(kgmole/h)
4754
4754
52
Mass Flow
(kg/h)
2.281e+005
2.281e+005
53
Std Ideal Liq Vol Flow
54
Molar Enthalpy
55
Molar Entropy
56
Heat Flow
57
1.0000
1.0000
Liq Vol Flow @Std Cond
(C)
180.0 *
180.0
(kPa)
95.00 *
95.00
(m3/h)
256.2
256.2
(kJ/kgmole)
-1.254e+005
-1.254e+005
(kJ/kgmole-C)
181.1
181.1
(kJ/h)
-5.960e+008
-5.960e+008
(m3/h)
246.3 *
58
246.3
PROPERTIES
59
Overall
60
61
Molecular Weight
62
Molar Density
63
Fluid Package:
Aspen Technology Inc.
Licensed to: LEGENDS
(kgmole/m3)
Vapour Phase
47.98
47.98
2.539e-002
2.539e-002
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 16 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 12 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
12
Mass Density
13
Act. Volume Flow
14
Mass Enthalpy
15
Mass Entropy
16
Heat Capacity
17
Vapour Phase
(kg/m3)
1.218
1.218
(m3/h)
1.872e+005
1.872e+005
(kJ/kg)
-2613
-2613
(kJ/kg-C)
3.774
3.774
(kJ/kgmole-C)
87.90
87.90
Mass Heat Capacity
(kJ/kg-C)
1.832
1.832
18
LHV Vol Basis (Std)
(MJ/m3)
1.514e+006
1.514e+006
19
HHV Vol Basis (Std)
(MJ/m3)
1.610e+006
1.610e+006
20
HHV Mass Basis (Std)
(kJ/kg)
3.354e+004
3.354e+004
21
CO2 Loading
---
---
22
CO2 App ML Con
(kgmole/m3)
---
---
23
CO2 App WT Con
(kgmol/kg)
---
---
24
LHV Mass Basis (Std)
(kJ/kg)
3.155e+004
3.155e+004
25
Phase Fraction [Vol. Basis]
1.000
1.000
26
Phase Fraction [Mass Basis]
1.000
1.000
27
Phase Fraction [Act. Vol. Basis]
1.000
1.000
28
Partial Pressure of CO2
29
Cost Based on Flow
30
31
32
Specific Heat
33
Std. Gas Flow
34
Std. Ideal Liq. Mass Density
35
Act. Liq. Flow
36
Z Factor
37
Watson K
38
User Property
39
Partial Pressure of H2S
40
Cp/(Cp - R)
41
Cp/Cv
42
Heat of Vap.
43
Kinematic Viscosity
44
Liq. Mass Density (Std. Cond)
45
Liq. Vol. Flow (Std. Cond)
46
Liquid Fraction
47
Molar Volume
48
Mass Heat of Vap.
49
Phase Fraction [Molar Basis]
50
Surface Tension
51
Thermal Conductivity
52
Viscosity
53
Cv (Semi-Ideal)
54
Mass Cv (Semi-Ideal)
55
Cv
56
Mass Cv
57
Cv (Ent. Method)
58
Mass Cv (Ent. Method)
59
Cp/Cv (Ent. Method)
60
Reid VP at 37.8 C
61
True VP at 37.8 C
62
63
Aspen Technology Inc.
(kPa)
0.0000
---
(Cost/s)
0.0000
0.0000
Act. Gas Flow
(ACT_m3/h)
1.872e+005
1.872e+005
Avg. Liq. Density
(kgmole/m3)
18.56
18.56
(kJ/kgmole-C)
87.90
87.90
(STD_m3/h)
1.124e+005
1.124e+005
(kg/m3)
890.5
890.5
(m3/s)
---
---
0.9931
0.9931
10.31
10.31
---
---
(kPa)
0.0000
---
1.104
1.104
1.108
1.108
(kJ/kgmole)
7.820e+004
---
(cSt)
9.943
9.943
(kg/m3)
926.0
926.0
(m3/h)
246.3
246.3
0.0000
0.0000
(m3/kgmole)
39.38
39.38
(kJ/kg)
1630
---
1.0000
1.0000
(dyne/cm)
---
---
(W/m-K)
2.904e-002
2.904e-002
(cP)
1.211e-002
1.211e-002
(kJ/kgmole-C)
79.58
79.58
(kJ/kg-C)
1.659
1.659
(kJ/kgmole-C)
79.36
79.36
(kJ/kg-C)
1.654
1.654
(kJ/kgmole-C)
---
---
(kJ/kg-C)
---
---
---
---
(kPa)
353.2
353.2
(kPa)
1.802e+004
1.802e+004
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
246.3
246.3
Licensed to: LEGENDS
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 17 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 12 (continued)
7
8
9
Overall
11
Viscosity Index
Property Package:
Peng-Robinson
Vapour Phase
-46.01
---
13
COMPOSITION
14
15
Overall Phase
16
17
Basis-1
PROPERTIES
10
12
Fluid Package:
COMPONENTS
MOLAR FLOW
(kgmole/h)
18
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
1.0000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
19
E-Benzene
1435.5929
0.3020
152411.1535
0.6682
175.1786
0.6839
20
Styrene
203.2845
0.0428
21172.4917
0.0928
23.2964
0.0909
21
Hydrogen
111.8507
0.0235
225.4910
0.0010
3.2278
0.0126
22
Benzene
1.2373
0.0003
96.6430
0.0004
0.1095
0.0004
23
Ethylene
0.0273
0.0000
0.7650
0.0000
0.0020
0.0000
24
Toluene
1.5627
0.0003
143.9860
0.0006
0.1655
0.0006
25
H2O
3000.0000
0.6311
54045.3014
0.2369
54.1544
0.2114
26
Methane
0.3356
0.0001
5.3840
0.0000
0.0180
0.0001
27
Total
4753.8909
1.0000
228101.2156
1.0000
256.1522
1.0000
28
Vapour Phase
29
30
COMPONENTS
MOLAR FLOW
(kgmole/h)
31
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
1.000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
32
E-Benzene
1435.5929
0.3020
152411.1535
0.6682
175.1786
0.6839
33
Styrene
203.2845
0.0428
21172.4917
0.0928
23.2964
0.0909
34
Hydrogen
111.8507
0.0235
225.4910
0.0010
3.2278
0.0126
35
Benzene
1.2373
0.0003
96.6430
0.0004
0.1095
0.0004
36
Ethylene
0.0273
0.0000
0.7650
0.0000
0.0020
0.0000
37
Toluene
1.5627
0.0003
143.9860
0.0006
0.1655
0.0006
38
H2O
3000.0000
0.6311
54045.3014
0.2369
54.1544
0.2114
39
Methane
0.3356
0.0001
5.3840
0.0000
0.0180
0.0001
40
Total
4753.8909
1.0000
228101.2156
1.0000
256.1522
1.0000
41
K VALUE
42
COMPONENTS
43
MIXED
LIGHT
HEAVY
44
E-Benzene
---
---
---
45
Styrene
---
---
---
46
Hydrogen
---
---
---
47
Benzene
---
---
---
48
Ethylene
---
---
---
49
Toluene
---
---
---
50
H2O
---
---
---
51
Methane
---
---
---
52
UNIT OPERATIONS
53
FEED TO
54
55
Cooler:
56
PRODUCT FROM
E-104
Cooler:
LOGICAL CONNECTION
E-103
UTILITIES
57
( No utilities reference this stream )
58
59
PROCESS UTILITY
60
61
62
63
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Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 18 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 12 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
DYNAMICS
10
11
Pressure Specification
(Active):
12
Flow Specification
(Inactive)
95.00 kPa *
Molar:
4754 kgmole/h
13
Mass:
2.281e+005 kg/h
Std Ideal Liq Volume:
256.2 m3/h
User Variables
14
15
NOTES
16
17
18
Description
19
20
21
Material Stream: 13
22
23
24
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
25
Overall
26
27
Vapour / Phase Fraction
28
Temperature:
29
Pressure:
30
Molar Flow
31
Mass Flow
32
Std Ideal Liq Vol Flow
33
Molar Enthalpy
34
Molar Entropy
35
Heat Flow
36
Liq Vol Flow @Std Cond
Vapour Phase
0.0413
Liquid Phase
Aqueous Phase
0.0413
0.3413
0.6174
(C)
65.00 *
65.00
65.00
65.00
(kPa)
80.00 *
80.00
80.00
80.00
(kgmole/h)
4754
196.2
1623
2935
(kg/h)
2.281e+005
3763
1.715e+005
5.287e+004
(m3/h)
256.2
7.124
196.0
52.98
(kJ/kgmole)
-1.742e+005
-6.929e+004
9982
-2.831e+005
(kJ/kgmole-C)
48.03
147.9
7.961
63.50
(kJ/h)
-8.283e+008
-1.359e+007
1.620e+007
-8.309e+008
4615
195.6
52.10
(m3/h)
246.3 *
37
PROPERTIES
38
Overall
39
40
Molecular Weight
41
Molar Density
42
Mass Density
43
Vapour Phase
Liquid Phase
Aqueous Phase
47.98
19.19
105.7
18.02
(kgmole/m3)
0.6661
2.852e-002
7.880
54.20
(kg/m3)
31.96
0.5473
832.6
976.5
Act. Volume Flow
(m3/h)
7137
6877
205.9
54.15
44
Mass Enthalpy
(kJ/kg)
-3631
-3611
94.47
-1.572e+004
45
Mass Entropy
(kJ/kg-C)
1.001
7.708
7.534e-002
3.525
46
Heat Capacity
(kJ/kgmole-C)
114.5
43.91
188.8
78.10
47
Mass Heat Capacity
(kJ/kg-C)
2.386
2.288
1.787
4.335
48
LHV Vol Basis (Std)
(MJ/m3)
1.514e+006
6.497e+005
4.356e+006
0.3456
49
HHV Vol Basis (Std)
(MJ/m3)
1.610e+006
7.094e+005
4.555e+006
4.101e+004
50
HHV Mass Basis (Std)
(kJ/kg)
3.354e+004
3.698e+004
4.311e+004
2276
51
CO2 Loading
---
---
---
---
52
CO2 App ML Con
(kgmole/m3)
---
---
---
---
53
CO2 App WT Con
(kgmol/kg)
---
---
---
---
54
LHV Mass Basis (Std)
(kJ/kg)
3.155e+004
3.386e+004
4.122e+004
1.919e-002
55
Phase Fraction [Vol. Basis]
2.781e-002
2.781e-002
0.7654
0.2068
56
Phase Fraction [Mass Basis]
1.650e-002
1.650e-002
0.7517
0.2318
57
Phase Fraction [Act. Vol. Basis]
0.9636
0.9636
2.885e-002
7.587e-003
58
Partial Pressure of CO2
59
Cost Based on Flow
60
Act. Gas Flow
(ACT_m3/h)
6877
6877
---
---
61
Avg. Liq. Density
(kgmole/m3)
18.56
27.53
8.277
55.40
62
Specific Heat
114.5
43.91
188.8
78.10
63
Aspen Technology Inc.
Licensed to: LEGENDS
(kPa)
0.0000
---
---
---
(Cost/s)
0.0000
0.0000
0.0000
0.0000
(kJ/kgmole-C)
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 19 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 13 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
12
Std. Gas Flow
13
Std. Ideal Liq. Mass Density
14
Act. Liq. Flow
15
Z Factor
16
Watson K
17
User Property
18
Partial Pressure of H2S
19
Cp/(Cp - R)
20
Cp/Cv
21
Heat of Vap.
22
Kinematic Viscosity
23
Liq. Mass Density (Std. Cond)
24
Liq. Vol. Flow (Std. Cond)
25
Liquid Fraction
26
Molar Volume
27
Mass Heat of Vap.
28
Phase Fraction [Molar Basis]
29
Surface Tension
30
Thermal Conductivity
31
Viscosity
32
Cv (Semi-Ideal)
33
Mass Cv (Semi-Ideal)
34
Cv
35
Mass Cv
36
Cv (Ent. Method)
37
Mass Cv (Ent. Method)
38
Cp/Cv (Ent. Method)
39
Reid VP at 37.8 C
40
True VP at 37.8 C
Vapour Phase
Liquid Phase
Aqueous Phase
(STD_m3/h)
1.124e+005
4638
3.837e+004
(kg/m3)
890.5
528.3
874.6
998.0
(m3/s)
7.225e-002
---
5.720e-002
1.504e-002
(kPa)
6.940e+004
---
0.9976
3.611e-003
5.250e-004
10.31
12.87
10.31
47.59
---
---
---
---
0.0000
---
---
---
1.078
1.234
1.046
1.119
1.166
1.003
1.236
1.300
(kJ/kgmole)
7.799e+004
---
---
---
(cSt)
---
23.90
0.4561
0.4402
(kg/m3)
926.0
0.8154
876.7
1015
(m3/h)
246.3
4615
195.6
52.10
0.9587
0.0000
1.000
1.000
1.501
35.06
0.1269
1.845e-002
(m3/kgmole)
(kJ/kg)
1625
---
---
---
0.0413
0.0413
0.3413
0.6174
(dyne/cm)
---
---
24.41
65.06
(W/m-K)
---
7.774e-002
0.1309
0.6581
(cP)
---
1.308e-002
0.3798
0.4298
(kJ/kgmole-C)
106.2
35.59
180.5
69.79
(kJ/kg-C)
2.213
1.855
1.708
3.874
(kJ/kgmole-C)
114.1
35.51
145.2
66.98
(kJ/kg-C)
2.378
1.851
1.375
3.718
(kJ/kgmole-C)
---
---
152.3
64.03
(kJ/kg-C)
---
---
1.442
3.554
---
---
1.239
1.220
(kPa)
353.2
---
3.779
43.21
(kPa)
1.802e+004
---
62.31
43.21
41
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
4863
4615
195.6
52.10
42
Viscosity Index
-8.601
---
---
---
43
COMPOSITION
44
45
Overall Phase
46
47
COMPONENTS
48
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
0.0413
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
49
E-Benzene
1435.5929
0.3020
152411.1535
0.6682
175.1786
0.6839
50
Styrene
203.2845
0.0428
21172.4917
0.0928
23.2964
0.0909
51
Hydrogen
111.8507
0.0235
225.4910
0.0010
3.2278
0.0126
52
Benzene
1.2373
0.0003
96.6430
0.0004
0.1095
0.0004
53
Ethylene
0.0273
0.0000
0.7650
0.0000
0.0020
0.0000
54
Toluene
1.5627
0.0003
143.9860
0.0006
0.1655
0.0006
55
H2O
3000.0000
0.6311
54045.3014
0.2369
54.1544
0.2114
56
Methane
0.3356
0.0001
5.3840
0.0000
0.0180
0.0001
57
Total
4753.8909
1.0000
228101.2156
1.0000
256.1522
1.0000
58
Vapour Phase
59
60
COMPONENTS
61
62
E-Benzene
63
Aspen Technology Inc.
Licensed to: LEGENDS
MOLAR FLOW
(kgmole/h)
20.6725
MOLE FRACTION
0.1054
MASS FLOW
(kg/h)
Phase Fraction
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
0.5832
2.5226
2194.7213
Aspen HYSYS Version 7.3 (25.0.0.7336)
4.126e-002
LIQUID VOLUME
FRACTION
0.3541
Page 20 of 236
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1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 13 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10
11
Vapour Phase (continued)
12
13
Fluid Package:
COMPONENTS
14
15
Styrene
16
Hydrogen
17
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
4.126e-002
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
2.1029
0.0107
219.0192
0.0582
0.2410
0.0338
111.5006
0.5684
224.7853
0.0597
3.2177
0.4517
Benzene
0.1104
0.0006
8.6218
0.0023
0.0098
0.0014
18
Ethylene
0.0256
0.0001
0.7185
0.0002
0.0019
0.0003
19
Toluene
0.0536
0.0003
4.9380
0.0013
0.0057
0.0008
20
H2O
61.3597
0.3128
1105.4020
0.2937
1.1076
0.1555
21
Methane
0.3293
0.0017
5.2824
0.0014
0.0176
0.0025
22
Total
196.1547
1.0000
3763.4886
1.0000
7.1239
1.0000
23
Liquid Phase
24
25
COMPONENTS
26
27
E-Benzene
28
Styrene
29
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
0.3413
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
1414.9203
0.8719
150216.4322
0.8761
172.6560
0.8807
201.1817
0.1240
20953.4726
0.1222
23.0554
0.1176
Hydrogen
0.3459
0.0002
0.6973
0.0000
0.0100
0.0001
30
Benzene
1.1269
0.0007
88.0211
0.0005
0.0998
0.0005
31
Ethylene
0.0017
0.0000
0.0465
0.0000
0.0001
0.0000
32
Toluene
1.5091
0.0009
139.0480
0.0008
0.1598
0.0008
33
H2O
3.6210
0.0022
65.2321
0.0004
0.0654
0.0003
34
Methane
0.0063
0.0000
0.1015
0.0000
0.0003
0.0000
35
Total
1622.7128
1.0000
171463.0513
1.0000
196.0468
1.0000
36
Aqueous Phase
37
38
COMPONENTS
39
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
0.6174
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
40
E-Benzene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
41
Styrene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
42
Hydrogen
0.0042
0.0000
0.0085
0.0000
0.0001
0.0000
43
Benzene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
44
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
45
Toluene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
46
H2O
2935.0193
1.0000
52874.6673
1.0000
52.9814
1.0000
47
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
48
Total
2935.0235
1.0000
52874.6758
1.0000
52.9815
1.0000
49
K VALUE
50
51
COMPONENTS
MIXED
LIGHT
HEAVY
52
E-Benzene
0.3395
0.1209
53
Styrene
0.2429
8.647e-002
-----
54
Hydrogen
7401
2667
3.980e+005
55
Benzene
2.276
0.8103
---
56
Ethylene
359.4
127.9
---
57
Toluene
0.8252
0.2938
---
58
H2O
0.4852
140.2
0.3128
59
Methane
1209
430.4
2.688e+007
60
61
62
63
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Licensed to: LEGENDS
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 21 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 13 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
UNIT OPERATIONS
10
FEED TO
11
12
Fluid Package:
PRODUCT FROM
Component Splitter:
X-100
Cooler:
LOGICAL CONNECTION
E-104
13
UTILITIES
14
( No utilities reference this stream )
15
16
PROCESS UTILITY
17
18
19
DYNAMICS
20
21
Pressure Specification
(Active):
22
Flow Specification
(Inactive)
80.00 kPa *
Molar:
4754 kgmole/h
23
Mass:
2.281e+005 kg/h
Std Ideal Liq Volume:
256.2 m3/h
User Variables
24
25
NOTES
26
27
28
Description
29
30
31
Material Stream: 22
32
33
34
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
CONDITIONS
35
Overall
36
Aqueous Phase
37
Vapour / Phase Fraction
0.0000
38
Temperature:
1.0000
39
Pressure:
40
Molar Flow
(kgmole/h)
3000
3000
41
Mass Flow
(kg/h)
5.405e+004
5.405e+004
42
Std Ideal Liq Vol Flow
43
Molar Enthalpy
44
Molar Entropy
45
Heat Flow
46
Liq Vol Flow @Std Cond
(C)
65.00 *
65.00
(kPa)
200.0 *
200.0
(m3/h)
54.15
54.15
(kJ/kgmole)
-2.831e+005
-2.831e+005
(kJ/kgmole-C)
63.50
63.50
(kJ/h)
-8.493e+008
-8.493e+008
(m3/h)
53.26 *
47
53.26
PROPERTIES
48
Overall
49
50
Molecular Weight
51
Molar Density
52
Mass Density
53
Aqueous Phase
18.02
18.02
(kgmole/m3)
54.20
54.20
(kg/m3)
976.5
976.5
Act. Volume Flow
(m3/h)
55.35
55.35
54
Mass Enthalpy
(kJ/kg)
-1.571e+004
-1.571e+004
55
Mass Entropy
(kJ/kg-C)
3.525
3.525
56
Heat Capacity
(kJ/kgmole-C)
78.10
78.10
57
Mass Heat Capacity
(kJ/kg-C)
4.335
4.335
58
LHV Vol Basis (Std)
(MJ/m3)
0.0000
0.0000
59
HHV Vol Basis (Std)
(MJ/m3)
4.101e+004
4.101e+004
60
HHV Mass Basis (Std)
(kJ/kg)
2276
2276
61
CO2 Loading
---
---
62
CO2 App ML Con
---
---
63
Aspen Technology Inc.
Licensed to: LEGENDS
(kgmole/m3)
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 22 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 22 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
PROPERTIES
10
Overall
11
12
CO2 App WT Con
13
LHV Mass Basis (Std)
14
Aqueous Phase
(kgmol/kg)
---
(kJ/kg)
---
---
Phase Fraction [Vol. Basis]
0.0000
1.000
15
Phase Fraction [Mass Basis]
0.0000
1.000
16
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
17
Partial Pressure of CO2
18
Cost Based on Flow
19
Act. Gas Flow
(ACT_m3/h)
---
---
20
Avg. Liq. Density
(kgmole/m3)
55.40
55.40
21
Specific Heat
22
Std. Gas Flow
23
Std. Ideal Liq. Mass Density
24
Act. Liq. Flow
25
Z Factor
26
Watson K
27
User Property
28
Partial Pressure of H2S
29
Cp/(Cp - R)
30
Cp/Cv
31
Heat of Vap.
32
Kinematic Viscosity
33
Liq. Mass Density (Std. Cond)
34
Liq. Vol. Flow (Std. Cond)
35
Liquid Fraction
36
Molar Volume
37
Mass Heat of Vap.
38
Phase Fraction [Molar Basis]
39
Surface Tension
40
Thermal Conductivity
41
Viscosity
42
Cv (Semi-Ideal)
43
Mass Cv (Semi-Ideal)
44
Cv
45
Mass Cv
46
Cv (Ent. Method)
47
Mass Cv (Ent. Method)
48
Cp/Cv (Ent. Method)
49
Reid VP at 37.8 C
50
True VP at 37.8 C
51
52
Viscosity Index
---
(kPa)
0.0000
---
(Cost/s)
0.0000
0.0000
(kJ/kgmole-C)
78.10
78.10
(STD_m3/h)
7.093e+004
7.093e+004
(kg/m3)
998.0
998.0
(m3/s)
1.537e-002
1.537e-002
1.312e-003
1.312e-003
---
---
---
---
(kPa)
0.0000
---
1.119
1.119
1.166
1.166
(kJ/kgmole)
4.003e+004
---
(cSt)
0.4402
0.4402
(kg/m3)
1015
1015
(m3/h)
53.26
53.26
1.000
1.000
(m3/kgmole)
1.845e-002
1.845e-002
(kJ/kg)
2222
---
0.0000
1.0000
(dyne/cm)
65.06
65.06
(W/m-K)
0.6581
0.6581
(cP)
0.4298
0.4298
(kJ/kgmole-C)
69.78
69.78
(kJ/kg-C)
3.874
3.874
(kJ/kgmole-C)
66.98
66.98
(kJ/kg-C)
3.718
3.718
(kJ/kgmole-C)
---
---
(kJ/kg-C)
---
---
---
---
(kPa)
6.467
6.467
(kPa)
6.467
6.467
Liq. Vol. Flow - Sum(Std. Cond) (m3/h)
53.26
53.26
-11.35
---
53
COMPOSITION
54
55
Overall Phase
56
57
Fluid Package:
COMPONENTS
58
MOLAR FLOW
(kgmole/h)
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
0.0000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
59
E-Benzene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
60
Styrene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
61
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
62
Benzene
0.0000
0.0000
0.0000
0.0000
0.0000
63
Aspen Technology Inc.
Licensed to: LEGENDS
Aspen HYSYS Version 7.3 (25.0.0.7336)
0.0000
Page 23 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 22 (continued)
7
8
9
Basis-1
Property Package:
Peng-Robinson
COMPOSITION
10
11
Overall Phase (continued)
12
13
Fluid Package:
COMPONENTS
MOLAR FLOW
(kgmole/h)
14
MOLE FRACTION
MASS FLOW
(kg/h)
Vapour Fraction
0.0000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
15
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
16
Toluene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
17
H2O
3000.0000
1.0000
54045.3014
1.0000
54.1544
1.0000
18
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
19
Total
3000.0000
1.0000
54045.3014
1.0000
54.1544
1.0000
20
Aqueous Phase
21
22
COMPONENTS
MOLAR FLOW
(kgmole/h)
23
MOLE FRACTION
MASS FLOW
(kg/h)
Phase Fraction
1.000
MASS FRACTION
LIQUID VOLUME
FLOW (m3/h)
LIQUID VOLUME
FRACTION
24
E-Benzene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
25
Styrene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
26
Hydrogen
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
27
Benzene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
28
Ethylene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
29
Toluene
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
30
H2O
3000.0000
1.0000
54045.3014
1.0000
54.1544
1.0000
31
Methane
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
32
Total
3000.0000
1.0000
54045.3014
1.0000
54.1544
1.0000
33
K VALUE
34
35
COMPONENTS
MIXED
LIGHT
HEAVY
36
E-Benzene
---
---
---
37
Styrene
---
---
---
38
Hydrogen
---
---
---
39
Benzene
---
---
---
40
Ethylene
---
---
---
41
Toluene
---
---
---
42
H2O
0.0000
---
0.0000
43
Methane
---
---
---
44
UNIT OPERATIONS
45
FEED TO
46
PRODUCT FROM
Pump:
47
48
LOGICAL CONNECTION
P-100
UTILITIES
49
( No utilities reference this stream )
50
51
PROCESS UTILITY
52
53
54
DYNAMICS
55
56
Pressure Specification
(Active):
57
Flow Specification
(Inactive)
58
200.0 kPa *
Molar:
3000 kgmole/h
Mass:
5.405e+004 kg/h
Std Ideal Liq Volume:
54.15 m3/h
User Variables
59
60
NOTES
61
62
63
Aspen Technology Inc.
Licensed to: LEGENDS
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 24 of 236
* Specified by user.
1
2
LEGENDS
Burlington, MA
USA
3
4
5
Case Name:
TEST FINAL.HSC
Unit Set:
SI
Date/Time:
Mon Dec 10 20:32:46 2018
6
Material Stream: 22 (continued)
7
8
9
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Fluid Package:
Basis-1
Property Package:
Peng-Robinson
Description
10
11
12
Material Stream: 24
13
14
15
CONDITIONS
16
Overall
17
Liquid Phase
18
Vapour / Phase Fraction
0.0000
19
Temperature:
1.0000
90.75
20
Pressure:
90.75
200.0 *
21
Molar Flow
(kgmole/h)
1521
200.0
1521
22
Mass Flow
(kg/h)
1.613e+005
1.613e+005
23
Std Ideal Liq Vol Flow
184.9
24
Molar Enthalpy
25
Molar Entropy
26
Heat Flow
27
Liq Vol Flow @Std Cond
(C)
(kPa)
(m3/h)
184.9
(kJ/kgmole)
8090
8090
(kJ/kgmole-C)
-12.30
-12.30
(kJ/h)
1.230e+007
1.230e+007
(m3/h)
184.4 *
28
184.4
PROPERTIES
29
Overall
30
31
Molecular Weight
32
Molar Density
33
Mass Density
34
Liquid Phase
106.0
106.0
(kgmole/m3)
7.606
7.606
(kg/m3)
806.6
806.6
Act. Volume Flow
(m3/h)
199.9
199.9
35
Mass Enthalpy
(kJ/kg)
76.29
76.29
36
Mass Entropy
(kJ/kg-C)
-0.1160
-0.1160
37
Heat Capacity
(kJ/kgmole-C)
201.1
201.1
38
Mass Heat Capacity
(kJ/kg-C)
1.896
1.896
39
LHV Vol Basis (Std)
(MJ/m3)
4.379e+006
4.379e+006
40
HHV Vol Basis (Std)
(MJ/m3)
4.582e+006
4.582e+006
41
HHV Mass Basis (Std)
(kJ/kg)
4.320e+004
4.320e+004
42
CO2 Loading
---
---
43
CO2 App ML Con
(kgmole/m3)
---
---
44
CO2 App WT Con
(kgmol/kg)
---
---
45
LHV Mass Basis (Std)
(kJ/kg)
4.129e+004
4.129e+004
46
Phase Fraction [Vol. Basis]
0.0000
1.000
47
Phase Fraction [Mass Basis]
0.0000
1.000
48
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
49
Partial Pressure of CO2
50
Cost Based on Flow
51
Act. Gas Flow
(ACT_m3/h)
---
---
52
Avg. Liq. Density
(kgmole/m3)
8.225
8.225
53
Specific Heat
54
Std. Gas Flow
55
Std. Ideal Liq. Mass Density
56
Act. Liq. Flow
57
Z Factor
58
Watson K
59
User Property
60
Partial Pressure of H2S
61
Cp/(Cp - R)
62
Cp/Cv
63
Aspen Technology Inc.
Licensed to: LEGENDS
(kPa)
0.0000
---
(Cost/s)
0.0000
0.0000
(kJ/kgmole-C)
201.1
201.1
(STD_m3/h)
3.595e+004
3.595e+004
(kg/m3)
872.2
872.2
(m3/s)
5.553e-002
5.553e-002
8.690e-003
8.690e-003
10.34
10.34
---
---
(kPa)
0.0000
---
1.043
1.043
1.291
1.291
Aspen HYSYS Version 7.3 (25.0.0.7336)
Page 25 of 236
* Specified by user.
