LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
25.00 *
1.000 *
0.7520 *
0.5765
3.012e-002
-2.483e+005
1.946
-1.867e+005
3.009e-002 *
Liquid Phase
1.0000
25.00
1.000
0.7520
0.5765
3.012e-002
-2.483e+005
1.946
-1.867e+005
3.009e-002
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.7370 *
0.0008 *
0.0113 *
0.0008 *
0.0011 *
0.0011 *
MOLE FRACTION
0.9800 *
0.0010 *
0.0150 *
0.0010 *
0.0015 *
0.0015 *
MASS FLOW
(kg/h)
23.6134 *
0.0346 *
0.2031 *
0.0331 *
0.0685 *
0.0663 *
MASS FRACTION
0.9831 *
0.0014 *
0.0085 *
0.0014 *
0.0029 *
0.0028 *
LIQUID VOLUME
FLOW (m3/h)
0.0297 *
0.0001 *
0.0002 *
0.0000 *
0.0001 *
0.0001 *
LIQUID VOLUME
FRACTION
0.9852 *
0.0017 *
0.0068 *
0.0014 *
0.0022 *
0.0028 *
Total 0.7520 1.0000 24.0190 1.0000 0.0301 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.7370
0.0008
0.0113
0.0008
0.0011
0.0011
MOLE FRACTION
0.9800
0.0010
0.0150
0.0010
0.0015
0.0015
MASS FLOW
(kg/h)
23.6134
0.0346
0.2031
0.0331
0.0685
0.0663
MASS FRACTION
0.9831
0.0014
0.0085
0.0014
0.0029
0.0028
LIQUID VOLUME
FLOW (m3/h)
0.0297
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9852
0.0017
0.0068
0.0014
0.0022
0.0028
Total 0.7520 1.0000 24.0190 1.0000 0.0301 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Pump: P-100
PRODUCT FROM LOGICAL CONNECTION
Adjust: ADJ-1
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 1 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
25.20
16.78 *
0.7520
0.5765
3.012e-002
-2.482e+005
1.960
-1.867e+005
3.009e-002 *
Liquid Phase
1.0000
25.20
16.78
0.7520
0.5765
3.012e-002
-2.482e+005
1.960
-1.867e+005
3.009e-002
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.7370
0.0008
0.0113
0.0008
0.0011
0.0011
MOLE FRACTION
0.9800
0.0010
0.0150
0.0010
0.0015
0.0015
MASS FLOW
(kg/h)
23.6134
0.0346
0.2031
0.0331
0.0685
0.0663
MASS FRACTION
0.9831
0.0014
0.0085
0.0014
0.0029
0.0028
LIQUID VOLUME
FLOW (m3/h)
0.0297
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9852
0.0017
0.0068
0.0014
0.0022
0.0028
Total 0.7520 1.0000 24.0190 1.0000 0.0301 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.7370
0.0008
0.0113
0.0008
0.0011
0.0011
MOLE FRACTION
0.9800
0.0010
0.0150
0.0010
0.0015
0.0015
MASS FLOW
(kg/h)
23.6134
0.0346
0.2031
0.0331
0.0685
0.0663
MASS FRACTION
0.9831
0.0014
0.0085
0.0014
0.0029
0.0028
LIQUID VOLUME
FLOW (m3/h)
0.0297
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9852
0.0017
0.0068
0.0014
0.0022
0.0028
Total 0.7520 1.0000 24.0190 1.0000 0.0301 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Valve: VLV-100
PRODUCT FROM
Pump: P-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 2 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
25.23
15.10 *
0.7520
0.5765
3.012e-002
-2.482e+005
1.989
-1.867e+005
3.009e-002 *
Liquid Phase
1.0000
25.23
15.10
0.7520
0.5765
3.012e-002
-2.482e+005
1.989
-1.867e+005
3.009e-002
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.7370
0.0008
0.0113
0.0008
0.0011
0.0011
MOLE FRACTION
0.9800
0.0010
0.0150
0.0010
0.0015
0.0015
MASS FLOW
(kg/h)
23.6134
0.0346
0.2031
0.0331
0.0685
0.0663
MASS FRACTION
0.9831
0.0014
0.0085
0.0014
0.0029
0.0028
LIQUID VOLUME
FLOW (m3/h)
0.0297
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9852
0.0017
0.0068
0.0014
0.0022
0.0028
Total 0.7520 1.0000 24.0190 1.0000 0.0301 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.7370
0.0008
0.0113
0.0008
0.0011
0.0011
MOLE FRACTION
0.9800
0.0010
0.0150
0.0010
0.0015
0.0015
MASS FLOW
(kg/h)
23.6134
0.0346
0.2031
0.0331
0.0685
0.0663
MASS FRACTION
0.9831
0.0014
0.0085
0.0014
0.0029
0.0028
LIQUID VOLUME
FLOW (m3/h)
0.0297
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9852
0.0017
0.0068
0.0014
0.0022
0.0028
Total 0.7520 1.0000 24.0190 1.0000 0.0301 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Mixer: V-104
PRODUCT FROM
Valve: VLV-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 3 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 4Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
32.96
1.080
0.8997
0.6896
3.604e-002
-2.470e+005
6.078
-2.222e+005
3.601e-002 *
Liquid Phase
1.0000
32.96
1.080
0.8997
0.6896
3.604e-002
-2.470e+005
6.078
-2.222e+005
3.601e-002
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.8832
0.0008
0.0127
0.0008
0.0012
0.0011
MOLE FRACTION
0.9816
0.0008
0.0142
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
28.2998
0.0346
0.2295
0.0331
0.0693
0.0663
MASS FRACTION
0.9849
0.0012
0.0080
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0356
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9868
0.0014
0.0064
0.0012
0.0018
0.0023
Total 0.8997 1.0000 28.7326 1.0000 0.0360 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.8832
0.0008
0.0127
0.0008
0.0012
0.0011
MOLE FRACTION
0.9816
0.0008
0.0142
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
28.2998
0.0346
0.2295
0.0331
0.0693
0.0663
MASS FRACTION
0.9849
0.0012
0.0080
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0356
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9868
0.0014
0.0064
0.0012
0.0018
0.0023
Total 0.8997 1.0000 28.7326 1.0000 0.0360 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Heater: E-100
PRODUCT FROM
Mixer: V-104
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 4 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 5Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
1.0000
250.0 *
14.99 *
0.8997
0.6896
3.604e-002
-1.914e+005
142.6
-1.723e+005
3.601e-002 *
Vapour Phase
1.0000
250.0
14.99
0.8997
0.6896
3.604e-002
-1.914e+005
142.6
-1.723e+005
3.601e-002
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.8832
0.0008
0.0127
0.0008
0.0012
0.0011
MOLE FRACTION
0.9816
0.0008
0.0142
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
28.2998
0.0346
0.2295
0.0331
0.0693
0.0663
MASS FRACTION
0.9849
0.0012
0.0080
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0356
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9868
0.0014
0.0064
0.0012
0.0018
0.0023
Total 0.8997 1.0000 28.7326 1.0000 0.0360 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.8832
0.0008
0.0127
0.0008
0.0012
0.0011
MOLE FRACTION
0.9816
0.0008
0.0142
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
28.2998
0.0346
0.2295
0.0331
0.0693
0.0663
MASS FRACTION
0.9849
0.0012
0.0080
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0356
0.0001
0.0002
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.9868
0.0014
0.0064
0.0012
0.0018
0.0023
Total 0.8997 1.0000 28.7326 1.0000 0.0360 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Equilibrium Reactor: ERV-100
PRODUCT FROM
Heater: E-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 5 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 6AFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
1.0000
365.9
14.99
0.8997
0.6896
3.832e-002
-1.914e+005
190.7
-1.723e+005
3.847e-002 *
Vapour Phase
1.0000
365.9
14.99
0.8997
0.6896
3.832e-002
-1.914e+005
190.7
-1.723e+005
3.847e-002
Liquid Phase
0.0000
365.9
14.99
0.0000
0.0000
0.0000
-1.914e+005
190.7
0.0000
0.0000
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1530
0.3659
0.3779
0.0008
0.0012
0.0011
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
4.9015
16.8554
6.8072
0.0331
0.0693
0.0663
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0251
0.0068
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.8997 1.0000 28.7327 1.0000 0.0383 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1530
0.3659
0.3779
0.0008
0.0012
0.0011
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
4.9015
16.8554
6.8072
0.0331
0.0693
0.0663
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0251
0.0068
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.8997 1.0000 28.7327 1.0000 0.0383 1.0000
Liquid Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.000
1.000
1.000
1.000
1.000
1.000
LIGHT
1.000
1.000
1.000
1.000
1.000
1.000
HEAVY
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 6 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 6A (continued)Fluid Package: Basis-1
Property Package: PRSV
UNIT OPERATIONS
FEED TO
Mixer: MIX-100
PRODUCT FROM
Equilibrium Reactor: ERV-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 6BFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
365.9
14.99
0.0000
0.0000
0.0000
-1.914e+005
190.7
-0.0000
0.0000 *
Vapour Phase
0.0000
365.9
14.99
0.0000
0.0000
0.0000
-1.914e+005
190.7
0.0000
0.0000
Liquid Phase
1.0000
365.9
14.99
0.0000
0.0000
0.0000
-1.914e+005
190.7
0.0000
0.0000
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 7 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 6B (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Liquid Phase (continued) Phase Fraction 1.000
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.000
1.000
1.000
1.000
1.000
1.000
LIGHT
1.000
1.000
1.000
1.000
1.000
1.000
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Mixer: MIX-100
PRODUCT FROM
Equilibrium Reactor: ERV-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 6Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
1.0000
365.9
14.99
0.8997
0.6896
3.832e-002
-1.914e+005
190.7
-1.723e+005
3.847e-002 *
Vapour Phase
1.0000
365.9
14.99
0.8997
0.6896
3.832e-002
-1.914e+005
190.7
-1.723e+005
3.847e-002
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1530
0.3659
0.3779
0.0008
0.0012
0.0011
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
4.9015
16.8554
6.8072
0.0331
0.0693
0.0663
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0251
0.0068
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.8997 1.0000 28.7327 1.0000 0.0383 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
MOLAR FLOW
(kgmole/h)
0.1530
0.3659
0.3779
MOLE FRACTION
0.1700
0.4066
0.4200
MASS FLOW
(kg/h)
4.9015
16.8554
6.8072
MASS FRACTION
0.1706
0.5866
0.2369
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0251
0.0068
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 8 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 6 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Vapour Phase (continued) Phase Fraction 1.000
COMPONENTS
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0008
0.0012
0.0011
MOLE FRACTION
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
0.0331
0.0693
0.0663
MASS FRACTION
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.0011
0.0017
0.0022
Total 0.8997 1.0000 28.7327 1.0000 0.0383 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Cooler: E-101
PRODUCT FROM
Mixer: MIX-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 7Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.5858
135.2 *
14.90 *
0.8997
0.6896
3.832e-002
-2.226e+005
124.2
-2.003e+005
3.847e-002 *
Vapour Phase
0.5858
135.2
14.90
0.5270
0.4976
2.956e-002
-1.910e+005
158.6
-1.006e+005
3.080e-002
Aqueous Phase
0.4142
135.2
14.90
0.3727
0.1920
8.758e-003
-2.673e+005
75.66
-9.964e+004
8.628e-003
COMPOSITION
Overall Phase Vapour Fraction 0.5858
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1530
0.3659
0.3779
0.0008
0.0012
0.0011
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
4.9015
16.8554
6.8072
0.0331
0.0693
0.0663
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0251
0.0068
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.8997 1.0000 28.7327 1.0000 0.0383 1.0000
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 9 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 7 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Vapour Phase Phase Fraction 0.5858
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0694
0.3632
0.0923
0.0007
0.0003
0.0011
MOLE FRACTION
0.1317
0.6891
0.1752
0.0014
0.0005
0.0021
MASS FLOW
(kg/h)
2.2248
16.7306
1.6634
0.0322
0.0157
0.0651
MASS FRACTION
0.1073
0.8070
0.0802
0.0016
0.0008
0.0031
LIQUID VOLUME
FLOW (m3/h)
0.0028
0.0250
0.0017
0.0000
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.0946
0.8443
0.0564
0.0014
0.0005
0.0028
Total 0.5270 1.0000 20.7317 1.0000 0.0296 1.0000
Aqueous Phase Phase Fraction 0.4142
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0835
0.0027
0.2855
0.0000
0.0009
0.0000
MOLE FRACTION
0.2241
0.0073
0.7661
0.0001
0.0024
0.0001
MASS FLOW
(kg/h)
2.6767
0.1247
5.1438
0.0009
0.0536
0.0012
MASS FRACTION
0.3345
0.0156
0.6429
0.0001
0.0067
0.0002
LIQUID VOLUME
FLOW (m3/h)
0.0034
0.0002
0.0052
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.3841
0.0212
0.5885
0.0001
0.0058
0.0002
Total 0.3727 1.0000 8.0009 1.0000 0.0088 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.5878
94.86
0.2287
24.27
0.2065
37.57
LIGHT
---
---
---
---
---
---
HEAVY
0.5878
94.86
0.2287
24.27
0.2065
37.57
UNIT OPERATIONS
FEED TO
Valve: VLV-101
PRODUCT FROM
Cooler: E-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 8Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.6029
125.6
10.26 *
0.8997
0.6896
3.832e-002
-2.226e+005
125.9
-2.003e+005
3.847e-002 *
Vapour Phase
0.6029
125.6
10.26
0.5424
0.5068
3.002e-002
-1.921e+005
160.8
-1.042e+005
3.120e-002
Aqueous Phase
0.3971
125.6
10.26
0.3573
0.1827
8.300e-003
-2.689e+005
72.97
-9.609e+004
8.179e-003
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 10 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 8 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 0.6029
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1530
0.3659
0.3779
0.0008
0.0012
0.0011
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
4.9015
16.8554
6.8072
0.0331
0.0693
0.0663
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0251
0.0068
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.8997 1.0000 28.7327 1.0000 0.0383 1.0000
Vapour Phase Phase Fraction 0.6029
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0748
0.3643
0.1012
0.0007
0.0003
0.0011
MOLE FRACTION
0.1378
0.6717
0.1865
0.0014
0.0005
0.0021
MASS FLOW
(kg/h)
2.3957
16.7842
1.8226
0.0325
0.0179
0.0656
MASS FRACTION
0.1134
0.7948
0.0863
0.0015
0.0008
0.0031
LIQUID VOLUME
FLOW (m3/h)
0.0030
0.0250
0.0018
0.0000
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.1003
0.8341
0.0608
0.0014
0.0006
0.0028
Total 0.5424 1.0000 21.1185 1.0000 0.0300 1.0000
Aqueous Phase Phase Fraction 0.3971
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0782
0.0015
0.2767
0.0000
0.0009
0.0000
MOLE FRACTION
0.2189
0.0043
0.7743
0.0000
0.0024
0.0000
MASS FLOW
(kg/h)
2.5058
0.0711
4.9845
0.0006
0.0514
0.0007
MASS FRACTION
0.3291
0.0093
0.6546
0.0001
0.0067
0.0001
LIQUID VOLUME
FLOW (m3/h)
0.0031
0.0001
0.0050
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.3794
0.0128
0.6017
0.0001
0.0059
0.0001
Total 0.3573 1.0000 7.6141 1.0000 0.0083 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.6298
155.4
0.2409
36.21
0.2291
60.34
LIGHT
---
---
---
---
---
---
HEAVY
0.6298
155.4
0.2409
36.21
0.2291
60.34
UNIT OPERATIONS
FEED TO
Distillation: T-100
PRODUCT FROM
Valve: VLV-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 11 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: DME ProductFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
45.29
10.00
0.3696
0.4073
2.528e-002
-2.018e+005
84.29
-7.459e+004
2.739e-002 *
Liquid Phase
1.0000
45.29
10.00
0.3696
0.4073
2.528e-002
-2.018e+005
84.29
-7.459e+004
2.739e-002
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.3659
0.0022
0.0007
0.0000
0.0007
MOLE FRACTION
0.0001
0.9900
0.0060
0.0020
0.0000
0.0019
MASS FLOW
(kg/h)
0.0009
16.8551
0.0397
0.0329
0.0000
0.0416
MASS FRACTION
0.0001
0.9932
0.0023
0.0019
0.0000
0.0025
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0251
0.0000
0.0000
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.0000
0.9946
0.0016
0.0017
0.0000
0.0021
Total 0.3696 1.0000 16.9703 1.0000 0.0253 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.3659
0.0022
0.0007
0.0000
0.0007
MOLE FRACTION
0.0001
0.9900
0.0060
0.0020
0.0000
0.0019
MASS FLOW
(kg/h)
0.0009
16.8551
0.0397
0.0329
0.0000
0.0416
MASS FRACTION
0.0001
0.9932
0.0023
0.0019
0.0000
0.0025
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0251
0.0000
0.0000
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.0000
0.9946
0.0016
0.0017
0.0000
0.0021
Total 0.3696 1.0000 16.9703 1.0000 0.0253 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO PRODUCT FROM
Distillation: T-100
LOGICAL CONNECTION
Adjust: ADJ-1
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 12 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 10Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
166.0
10.26
0.5302
0.2823
1.304e-002
-2.615e+005
81.98
-1.386e+005
1.287e-002 *
Aqueous Phase
1.0000
166.0
10.26
0.5302
0.2823
1.304e-002
-2.615e+005
81.98
-1.386e+005
1.287e-002
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1529
0.0000
0.3757
0.0000
0.0012
0.0004
MOLE FRACTION
0.2885
0.0000
0.7085
0.0000
0.0022
0.0008
MASS FLOW
(kg/h)
4.9005
0.0002
6.7675
0.0002
0.0693
0.0247
MASS FRACTION
0.4166
0.0000
0.5753
0.0000
0.0059
0.0021
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4724
0.0000
0.5201
0.0000
0.0051
0.0024
Total 0.5302 1.0000 11.7624 1.0000 0.0130 1.0000
Aqueous Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1529
0.0000
0.3757
0.0000
0.0012
0.0004
MOLE FRACTION
0.2885
0.0000
0.7085
0.0000
0.0022
0.0008
MASS FLOW
(kg/h)
4.9005
0.0002
6.7675
0.0002
0.0693
0.0247
MASS FRACTION
0.4166
0.0000
0.5753
0.0000
0.0059
0.0021
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4724
0.0000
0.5201
0.0000
0.0051
0.0024
Total 0.5302 1.0000 11.7624 1.0000 0.0130 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
---
---
---
---
---
---
HEAVY
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
UNIT OPERATIONS
FEED TO
Valve: VLV-102
PRODUCT FROM
Distillation: T-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 13 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 11Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0502
150.9
6.910 *
0.5302
0.2823
1.304e-002
-2.615e+005
82.08
-1.386e+005
1.287e-002 *
Vapour Phase
0.0502
150.9
6.910
2.663e-002
1.620e-002
7.868e-004
-2.174e+005
158.7
-5790
7.800e-004
Aqueous Phase
0.9498
150.9
6.910
0.5036
0.2661
1.225e-002
-2.638e+005
78.03
-1.329e+005
1.209e-002
COMPOSITION
Overall Phase Vapour Fraction 0.0502
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1529
0.0000
0.3757
0.0000
0.0012
0.0004
MOLE FRACTION
0.2885
0.0000
0.7085
0.0000
0.0022
0.0008
MASS FLOW
(kg/h)
4.9005
0.0002
6.7675
0.0002
0.0693
0.0247
MASS FRACTION
0.4166
0.0000
0.5753
0.0000
0.0059
0.0021
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4724
0.0000
0.5201
0.0000
0.0051
0.0024
Total 0.5302 1.0000 11.7624 1.0000 0.0130 1.0000
Vapour Phase Phase Fraction 5.022e-002
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0130
0.0000
0.0133
0.0000
0.0000
0.0003
MOLE FRACTION
0.4865
0.0002
0.5007
0.0001
0.0012
0.0114
MASS FLOW
(kg/h)
0.4151
0.0002
0.2402
0.0001
0.0019
0.0176
MASS FRACTION
0.6149
0.0003
0.3558
0.0002
0.0028
0.0260
LIQUID VOLUME
FLOW (m3/h)
0.0005
0.0000
0.0002
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.6630
0.0004
0.3059
0.0002
0.0023
0.0283
Total 0.0266 1.0000 0.6751 1.0000 0.0008 1.0000
Aqueous Phase Phase Fraction 0.9498
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1400
0.0000
0.3623
0.0000
0.0011
0.0001
MOLE FRACTION
0.2780
0.0000
0.7195
0.0000
0.0022
0.0002
MASS FLOW
(kg/h)
4.4854
0.0000
6.5273
0.0001
0.0674
0.0071
MASS FRACTION
0.4046
0.0000
0.5887
0.0000
0.0061
0.0006
LIQUID VOLUME
FLOW (m3/h)
0.0056
0.0000
0.0065
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4601
0.0000
0.5339
0.0000
0.0052
0.0007
Total 0.5036 1.0000 11.0873 1.0000 0.0123 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.750
132.6
0.6958
38.01
0.5273
46.50
LIGHT
---
---
---
---
---
---
HEAVY
1.750
132.6
0.6958
38.01
0.5273
46.50
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 14 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 11 (continued)Fluid Package: Basis-1
Property Package: PRSV
UNIT OPERATIONS
FEED TO
Distillation: T-101
PRODUCT FROM
Valve: VLV-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 12Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
122.5
6.800
6.664e-003
5.356e-003
2.802e-004
-2.319e+005
52.76
-1545
2.794e-004 *
Vapour Phase
0.0000
122.5
6.800
1.478e-008
1.210e-008
6.348e-010
-1.987e+005
135.4
-2.937e-003
6.327e-010
Liquid Phase
1.0000
122.5
6.800
6.664e-003
5.356e-003
2.802e-004
-2.319e+005
52.76
-1545
2.794e-004
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0061
0.0000
0.0001
0.0000
0.0000
0.0004
MOLE FRACTION
0.9179
0.0007
0.0169
0.0007
0.0000
0.0638
MASS FLOW
(kg/h)
0.1960
0.0002
0.0020
0.0002
0.0000
0.0247
MASS FRACTION
0.8783
0.0010
0.0091
0.0009
0.0000
0.1107
LIQUID VOLUME
FLOW (m3/h)
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.8791
0.0012
0.0073
0.0009
0.0000
0.1116
Total 0.0067 1.0000 0.2232 1.0000 0.0003 1.0000
Vapour Phase Phase Fraction 2.218e-006
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.9084
0.0054
0.0057
0.0018
0.0000
0.0788
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.8533
0.0073
0.0030
0.0023
0.0000
0.1341
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.8518
0.0086
0.0024
0.0024
0.0000
0.1348
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0061
0.0000
0.0001
0.0000
0.0000
0.0004
MOLE FRACTION
0.9179
0.0007
0.0169
0.0007
0.0000
0.0638
MASS FLOW
(kg/h)
0.1960
0.0002
0.0020
0.0002
0.0000
0.0247
MASS FRACTION
0.8783
0.0010
0.0091
0.0009
0.0000
0.1107
LIQUID VOLUME
FLOW (m3/h)
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.8791
0.0012
0.0073
0.0009
0.0000
0.1116
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 15 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 12 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Liquid Phase (continued) Phase Fraction 1.000
Total 0.0067 1.0000 0.2232 1.0000 0.0003 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.9896
7.593
0.3383
2.695
0.2003
1.234
LIGHT
0.9896
7.593
0.3383
2.695
0.2003
1.234
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO PRODUCT FROM
Distillation: T-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 13Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
151.2
6.910
0.5235
0.2769
1.276e-002
-2.637e+005
78.05
-1.380e+005
1.259e-002 *
Aqueous Phase
1.0000
151.2
6.910
0.5235
0.2769
1.276e-002
-2.637e+005
78.05
-1.380e+005
1.259e-002
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1468
0.0000
0.3755
0.0000
0.0012
0.0000
MOLE FRACTION
0.2805
0.0000
0.7173
0.0000
0.0022
0.0000
MASS FLOW
(kg/h)
4.7045
0.0000
6.7654
0.0000
0.0693
0.0000
MASS FRACTION
0.4077
0.0000
0.5863
0.0000
0.0060
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4634
0.0000
0.5314
0.0000
0.0052
0.0000
Total 0.5235 1.0000 11.5392 1.0000 0.0128 1.0000
Aqueous Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
MOLAR FLOW
(kgmole/h)
0.1468
0.0000
0.3755
MOLE FRACTION
0.2805
0.0000
0.7173
MASS FLOW
(kg/h)
4.7045
0.0000
6.7654
MASS FRACTION
0.4077
0.0000
0.5863
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0068
LIQUID VOLUME
FRACTION
0.4634
0.0000
0.5314
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 16 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 13 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Aqueous Phase (continued) Phase Fraction 1.000
COMPONENTS
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0012
0.0000
MOLE FRACTION
0.0000
0.0022
0.0000
MASS FLOW
(kg/h)
0.0000
0.0693
0.0000
MASS FRACTION
0.0000
0.0060
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.0052
0.0000
Total 0.5235 1.0000 11.5392 1.0000 0.0128 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
---
---
---
---
---
---
HEAVY
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
UNIT OPERATIONS
FEED TO
Valve: VLV-103
PRODUCT FROM
Distillation: T-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 14Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.1555
93.61
1.090 *
0.5235
0.2769
1.276e-002
-2.637e+005
79.40
-1.380e+005
1.259e-002 *
Vapour Phase
0.1555
93.61
1.090
8.141e-002
4.827e-002
2.328e-003
-2.205e+005
169.1
-1.795e+004
2.308e-003
Aqueous Phase
0.8445
93.61
1.090
0.4421
0.2287
1.043e-002
-2.717e+005
62.88
-1.201e+005
1.029e-002
COMPOSITION
Overall Phase Vapour Fraction 0.1555
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1468
0.0000
0.3755
0.0000
0.0012
0.0000
MOLE FRACTION
0.2805
0.0000
0.7173
0.0000
0.0022
0.0000
MASS FLOW
(kg/h)
4.7045
0.0000
6.7654
0.0000
0.0693
0.0000
MASS FRACTION
0.4077
0.0000
0.5863
0.0000
0.0060
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4634
0.0000
0.5314
0.0000
0.0052
0.0000
Total 0.5235 1.0000 11.5392 1.0000 0.0128 1.0000
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 17 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 14 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Vapour Phase Phase Fraction 0.1555
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0384
0.0000
0.0429
0.0000
0.0002
0.0000
MOLE FRACTION
0.4714
0.0000
0.5267
0.0000
0.0019
0.0000
MASS FLOW
(kg/h)
1.2297
0.0000
0.7725
0.0000
0.0091
0.0000
MASS FRACTION
0.6114
0.0000
0.3841
0.0000
0.0045
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0015
0.0000
0.0008
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.6638
0.0000
0.3325
0.0000
0.0037
0.0000
Total 0.0814 1.0000 2.0113 1.0000 0.0023 1.0000
Aqueous Phase Phase Fraction 0.8445
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1084
0.0000
0.3327
0.0000
0.0010
0.0000
MOLE FRACTION
0.2453
0.0000
0.7524
0.0000
0.0023
0.0000
MASS FLOW
(kg/h)
3.4749
0.0000
5.9929
0.0000
0.0601
0.0000
MASS FRACTION
0.3647
0.0000
0.6290
0.0000
0.0063
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0044
0.0000
0.0060
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4187
0.0000
0.5758
0.0000
0.0055
0.0000
Total 0.4421 1.0000 9.5279 1.0000 0.0104 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.922
---
0.7000
264.6
0.8261
502.2
LIGHT
---
---
---
---
---
---
HEAVY
1.922
---
0.7000
264.6
0.8261
502.2
UNIT OPERATIONS
FEED TO
Distillation: T-102
PRODUCT FROM
Valve: VLV-103
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 15Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
118.8
1.900
0.3762
0.1641
6.856e-003
-2.792e+005
75.62
-1.050e+005
6.744e-003 *
Aqueous Phase
1.0000
118.8
1.900
0.3762
0.1641
6.856e-003
-2.792e+005
75.62
-1.050e+005
6.744e-003
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 18 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 15 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0010
0.0000
0.3741
0.0000
0.0011
0.0000
MOLE FRACTION
0.0025
0.0000
0.9944
0.0000
0.0030
0.0000
MASS FLOW
(kg/h)
0.0307
0.0000
6.7391
0.0000
0.0685
0.0000
MASS FRACTION
0.0045
0.0000
0.9855
0.0000
0.0100
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.0056
0.0000
0.9849
0.0000
0.0095
0.0000
Total 0.3762 1.0000 6.8383 1.0000 0.0069 1.0000
Aqueous Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0010
0.0000
0.3741
0.0000
0.0011
0.0000
MOLE FRACTION
0.0025
0.0000
0.9944
0.0000
0.0030
0.0000
MASS FLOW
(kg/h)
0.0307
0.0000
6.7391
0.0000
0.0685
0.0000
MASS FRACTION
0.0045
0.0000
0.9855
0.0000
0.0100
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.0056
0.0000
0.9849
0.0000
0.0095
0.0000
Total 0.3762 1.0000 6.8383 1.0000 0.0069 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
---
0.0000
---
0.0000
---
LIGHT
---
---
---
---
---
---
HEAVY
0.0000
---
0.0000
---
0.0000
---
UNIT OPERATIONS
FEED TO PRODUCT FROM
Distillation: T-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 16Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
70.18
1.080
0.1473
0.1128
5.901e-003
-2.405e+005
24.22
-3.543e+004
5.896e-003 *
Liquid Phase
1.0000
70.18
1.080
0.1473
0.1128
5.901e-003
-2.405e+005
24.22
-3.543e+004
5.896e-003
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 19 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 16 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1459
0.0000
0.0015
0.0000
0.0000
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
4.6739
0.0000
0.0263
0.0000
0.0007
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.1473 1.0000 4.7009 1.0000 0.0059 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1459
0.0000
0.0015
0.0000
0.0000
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
4.6739
0.0000
0.0263
0.0000
0.0007
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.1473 1.0000 4.7009 1.0000 0.0059 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Recycle: RCY-1
PRODUCT FROM
Distillation: T-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 17Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
70.18 *
1.080 *
0.1477 *
0.1131
5.917e-003
-2.405e+005
24.22
-3.552e+004
5.912e-003 *
Liquid Phase
1.0000
70.18
1.080
0.1477
0.1131
5.917e-003
-2.405e+005
24.22
-3.552e+004
5.912e-003
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 20 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 17 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1463 *
0.0000 *
0.0015 *
0.0000 *
0.0000 *
0.0000 *
MOLE FRACTION
0.9900 *
0.0000 *
0.0099 *
0.0000 *
0.0001 *
0.0000 *
MASS FLOW
(kg/h)
4.6864 *
0.0000 *
0.0264 *
0.0000 *
0.0007 *
0.0000 *
MASS FRACTION
0.9942 *
0.0000 *
0.0056 *
0.0000 *
0.0002 *
0.0000 *
LIQUID VOLUME
FLOW (m3/h)
0.0059 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
LIQUID VOLUME
FRACTION
0.9954 *
0.0000 *
0.0045 *
0.0000 *
0.0001 *
0.0000 *
Total 0.1477 1.0000 4.7135 1.0000 0.0059 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1463
0.0000
0.0015
0.0000
0.0000
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
4.6864
0.0000
0.0264
0.0000
0.0007
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.1477 1.0000 4.7135 1.0000 0.0059 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIGHT
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Mixer: V-104
PRODUCT FROM
Recycle: RCY-1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: Q-100Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: P-100
Duty SP: 64.99 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Pump: P-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 21 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Energy Stream: Q-100 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROCESS UTILITY
Energy Stream: Q-101Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: E-100
Duty SP: 4.994e+004 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Heater: E-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: Q-102Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: E-101
Duty SP: 2.802e+004 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO PRODUCT FROM
Cooler: E-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T101CONDFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Condenser @COL1
Duty SP: 1.948e+004 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO PRODUCT FROM
Distillation: T-100
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 22 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Energy Stream: T101COND (continued)Fluid Package: Basis-1
Property Package: PRSV
PROCESS UTILITY
Energy Stream: T101REBFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Reboiler @COL1
Duty SP: 6518 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Distillation: T-100
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T102CFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Condenser @COL2
Duty SP: 2407 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO PRODUCT FROM
Distillation: T-101
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T102RFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Reboiler @COL2
Duty SP: 1460 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Distillation: T-101
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 23 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Energy Stream: T102R (continued)Fluid Package: Basis-1
Property Package: PRSV
PROCESS UTILITY
Energy Stream: T103CONDFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Condenser @COL3
Duty SP: 3.594e+004 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO PRODUCT FROM
Distillation: T-102
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T103REBFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Reboiler @COL3
Duty SP: 3.355e+004 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Distillation: T-102
PRODUCT FROM LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: Reflux @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
45.29
10.00
0.7391
0.8146
5.056e-002
-2.018e+005
84.29
-1.492e+005
5.479e-002 *
Vapour Phase
0.0000
45.29
10.00
0.0000
0.0000
0.0000
-1.841e+005
138.8
0.0000
0.0000
Liquid Phase
1.0000
45.29
10.00
0.7391
0.8146
5.056e-002
-2.018e+005
84.29
-1.492e+005
5.479e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 24 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Reflux @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
45.92
12.50
573.9
5.914e-002
-4396
1.836
123.1
2.681
1.321e+006
2.876e+004
---
0.0000
0.0000
0.0000
---
14.62
123.1
17.48
671.3
1.643e-005
---
11.38
---
0.0000
1.072
1.072
1.757e+004
0.1307
619.5
5.479e-002
1.000
8.002e-002
382.7
0.0000
9.381
0.1217
7.502e-002
114.8
2.500
114.8
2.500
---
---
---
8.269
8.229
5.479e-002
---
Vapour Phase
46.02
0.4539
20.89
0.0000
-4000
3.015
76.20
1.656
1.326e+006
2.881e+004
---
0.0000
---
0.0000
---
14.57
76.20
0.0000
670.5
---
0.8431
11.38
---
---
1.122
1.247
---
0.4693
618.3
0.0000
0.0000
2.203
---
0.0000
---
1.877e-002
9.803e-003
67.89
1.475
61.09
1.327
---
---
---
8.297
8.285
0.0000
-9.862
Liquid Phase
45.92
12.50
573.9
5.914e-002
-4396
1.836
123.1
2.681
1.321e+006
2.876e+004
1.000
1.000
---
0.0000
---
14.62
123.1
17.48
671.3
1.643e-005
3.062e-002
11.38
---
---
1.072
1.072
---
0.1307
619.5
5.479e-002
1.000
8.002e-002
---
1.0000
9.381
0.1217
7.502e-002
114.8
2.500
114.8
2.500
---
---
---
8.269
8.229
5.479e-002
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
MOLAR FLOW
(kgmole/h)
0.0001
0.7317
0.0044
MOLE FRACTION
0.0001
0.9900
0.0060
MASS FLOW
(kg/h)
0.0019
33.7103
0.0794
MASS FRACTION
0.0001
0.9932
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0503
0.0001
LIQUID VOLUME
FRACTION
0.0000
0.9946
0.0016
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 25 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Reflux @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0015
0.0000
0.0014
MOLE FRACTION
0.0020
0.0000
0.0019
MASS FLOW
(kg/h)
0.0658
0.0000
0.0832
MASS FRACTION
0.0019
0.0000
0.0025
LIQUID VOLUME
FLOW (m3/h)
0.0001
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.0017
0.0000
0.0021
Total 0.7391 1.0000 33.9406 1.0000 0.0506 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.9974
0.0018
0.0006
0.0000
0.0002
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.9984
0.0007
0.0006
0.0000
0.0003
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.9988
0.0005
0.0005
0.0000
0.0002
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0001
0.7317
0.0044
0.0015
0.0000
0.0014
MOLE FRACTION
0.0001
0.9900
0.0060
0.0020
0.0000
0.0019
MASS FLOW
(kg/h)
0.0019
33.7103
0.0794
0.0658
0.0000
0.0832
MASS FRACTION
0.0001
0.9932
0.0023
0.0019
0.0000
0.0025
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0503
0.0001
0.0001
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.0000
0.9946
0.0016
0.0017
0.0000
0.0021
Total 0.7391 1.0000 33.9406 1.0000 0.0506 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.1034
1.007
0.2940
0.3171
1.976e-002
0.1059
LIGHT
0.1034
1.007
0.2940
0.3171
1.976e-002
0.1059
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL1
PRODUCT FROM
Total Condenser: Condenser @COL1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: To Condenser @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Overall
1.0000
46.65
10.00
Vapour Phase
1.0000
46.65
10.00
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 26 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Condenser @COL1 (contFluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
1.109
1.222
7.584e-002
-1.843e+005
139.4
-2.043e+005
8.218e-002 *
Vapour Phase
1.109
1.222
7.584e-002
-1.843e+005
139.4
-2.043e+005
8.218e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
45.92
0.4510
20.71
2.458
-4013
3.036
76.14
1.658
1.321e+006
2.876e+004
1.000
1.000
0.0000
0.0000
2.458
14.62
76.14
26.21
671.3
---
0.8449
11.38
---
0.0000
1.123
1.246
1.757e+004
0.4747
619.5
8.218e-002
0.0000
2.217
382.7
1.0000
---
1.889e-002
9.830e-003
67.82
1.477
61.13
1.331
---
---
---
8.269
8.229
8.218e-002
Vapour Phase
45.92
0.4510
20.71
2.458
-4013
3.036
76.14
1.658
1.321e+006
2.876e+004
1.000
1.000
---
0.0000
2.458
14.62
76.14
26.21
671.3
---
0.8449
11.38
---
---
1.123
1.246
---
0.4747
619.5
8.218e-002
0.0000
2.217
---
1.0000
---
1.889e-002
9.830e-003
67.82
1.477
61.13
1.331
---
---
---
8.269
8.229
8.218e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 27 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Condenser @COL1 (contFluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Viscosity Index
Overall
-9.607
Vapour Phase
-9.607
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0001
1.0976
0.0066
0.0022
0.0000
0.0021
MOLE FRACTION
0.0001
0.9900
0.0060
0.0020
0.0000
0.0019
MASS FLOW
(kg/h)
0.0028
50.5654
0.1191
0.0987
0.0000
0.1248
MASS FRACTION
0.0001
0.9932
0.0023
0.0019
0.0000
0.0025
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0754
0.0001
0.0001
0.0000
0.0002
LIQUID VOLUME
FRACTION
0.0000
0.9946
0.0016
0.0017
0.0000
0.0021
Total 1.1087 1.0000 50.9109 1.0000 0.0758 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0001
1.0976
0.0066
0.0022
0.0000
0.0021
MOLE FRACTION
0.0001
0.9900
0.0060
0.0020
0.0000
0.0019
MASS FLOW
(kg/h)
0.0028
50.5654
0.1191
0.0987
0.0000
0.1248
MASS FRACTION
0.0001
0.9932
0.0023
0.0019
0.0000
0.0025
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0754
0.0001
0.0001
0.0000
0.0002
LIQUID VOLUME
FRACTION
0.0000
0.9946
0.0016
0.0017
0.0000
0.0021
Total 1.1087 1.0000 50.9109 1.0000 0.0758 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Total Condenser: Condenser @COL1
PRODUCT FROM
Tray Section: Main TS @COL1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: Boilup @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Overall
1.0000
166.0
10.26
0.1785
0.1102
5.362e-003
-2.169e+005
Vapour Phase
1.0000
166.0
10.26
0.1785
0.1102
5.362e-003
-2.169e+005
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 28 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Boilup @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
156.9
-3.871e+004
5.313e-003 *
Vapour Phase
156.9
-3.871e+004
5.313e-003
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
25.72
0.3111
8.001
0.5737
-8434
6.099
50.40
1.960
3.455e+005
1.344e+004
1.000
1.000
0.0000
0.0000
0.5737
33.28
50.40
4.220
855.9
---
0.9152
10.62
---
0.0000
1.198
1.306
3.515e+004
1.302
863.9
5.313e-003
0.0000
3.214
1367
1.0000
---
2.801e-002
1.041e-002
42.08
1.636
38.60
1.501
---
---
---
0.2819
0.5725
5.313e-003
6.650
Vapour Phase
25.72
0.3111
8.001
0.5737
-8434
6.099
50.40
1.960
3.455e+005
1.344e+004
1.000
1.000
---
0.0000
0.5737
33.28
50.40
4.220
855.9
---
0.9152
10.62
---
---
1.198
1.306
---
1.302
863.9
5.313e-003
0.0000
3.214
---
1.0000
---
2.801e-002
1.041e-002
42.08
1.636
38.60
1.501
---
---
---
0.2819
0.5725
5.313e-003
6.650
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 29 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Boilup @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0857
0.0001
0.0884
0.0000
0.0002
0.0040
MOLE FRACTION
0.4801
0.0007
0.4955
0.0002
0.0011
0.0224
MASS FLOW
(kg/h)
2.7455
0.0057
1.5931
0.0017
0.0115
0.2323
MASS FRACTION
0.5982
0.0012
0.3471
0.0004
0.0025
0.0506
LIQUID VOLUME
FLOW (m3/h)
0.0035
0.0000
0.0016
0.0000
0.0000
0.0003
LIQUID VOLUME
FRACTION
0.6435
0.0016
0.2977
0.0004
0.0020
0.0548
Total 0.1785 1.0000 4.5896 1.0000 0.0054 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0857
0.0001
0.0884
0.0000
0.0002
0.0040
MOLE FRACTION
0.4801
0.0007
0.4955
0.0002
0.0011
0.0224
MASS FLOW
(kg/h)
2.7455
0.0057
1.5931
0.0017
0.0115
0.2323
MASS FRACTION
0.5982
0.0012
0.3471
0.0004
0.0025
0.0506
LIQUID VOLUME
FLOW (m3/h)
0.0035
0.0000
0.0016
0.0000
0.0000
0.0003
LIQUID VOLUME
FRACTION
0.6435
0.0016
0.2977
0.0004
0.0020
0.0548
Total 0.1785 1.0000 4.5896 1.0000 0.0054 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL1
PRODUCT FROM
Reboiler: Reboiler @COL1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: To Reboiler @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
158.8
10.26
0.7086
0.3924
1.840e-002
-2.595e+005
79.77
-1.839e+005
1.818e-002 *
Vapour Phase
0.0000
158.8
10.26
0.0000
0.0000
0.0000
-2.135e+005
155.1
0.0000
0.0000
Liquid Phase
1.0000
158.8
10.26
0.7086
0.3924
1.840e-002
-2.595e+005
79.77
-1.839e+005
1.818e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 30 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Reboiler @COL1 (continuFluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
23.07
32.83
757.7
2.158e-002
-1.124e+004
3.457
122.3
5.302
2.270e+005
9839
---
0.0000
0.0000
0.0000
---
38.51
122.3
16.76
888.7
5.995e-006
---
10.60
---
0.0000
1.073
1.184
3.612e+004
0.1268
899.6
1.818e-002
1.000
3.046e-002
1565
0.0000
33.96
0.4162
9.604e-002
114.0
4.941
103.3
4.477
---
---
---
0.2483
0.6017
1.818e-002
---
Vapour Phase
29.83
0.3200
9.546
0.0000
-7158
5.200
57.24
1.919
5.180e+005
1.736e+004
---
0.0000
---
0.0000
---
27.88
57.24
0.0000
831.6
---
0.9046
10.64
---
---
1.170
1.276
---
1.069
840.5
0.0000
0.0000
3.125
---
0.0000
---
2.668e-002
1.020e-002
48.93
1.640
44.86
1.504
---
---
---
0.5353
0.8487
0.0000
---
Liquid Phase
23.07
32.83
757.7
2.158e-002
-1.124e+004
3.457
122.3
5.302
2.270e+005
9839
1.000
1.000
---
0.0000
---
38.51
122.3
16.76
888.7
5.995e-006
8.816e-003
10.60
---
---
1.073
1.184
---
0.1268
899.6
1.818e-002
1.000
3.046e-002
---
1.0000
33.96
0.4162
9.604e-002
114.0
4.941
103.3
4.477
---
---
---
0.2483
0.6017
1.818e-002
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
MOLAR FLOW
(kgmole/h)
0.2386
0.0001
0.4641
MOLE FRACTION
0.3367
0.0002
0.6549
MASS FLOW
(kg/h)
7.6460
0.0059
8.3605
MASS FRACTION
0.4676
0.0004
0.5113
LIQUID VOLUME
FLOW (m3/h)
0.0096
0.0000
0.0084
LIQUID VOLUME
FRACTION
0.5222
0.0005
0.4553
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 31 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Reboiler @COL1 (continuFluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0013
0.0044
MOLE FRACTION
0.0001
0.0019
0.0062
MASS FLOW
(kg/h)
0.0019
0.0807
0.2570
MASS FRACTION
0.0001
0.0049
0.0157
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0001
0.0003
LIQUID VOLUME
FRACTION
0.0001
0.0042
0.0177
Total 0.7086 1.0000 16.3520 1.0000 0.0184 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.4826
0.0104
0.3879
0.0011
0.0008
0.1172
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.5184
0.0160
0.2343
0.0016
0.0016
0.2282
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.5418
0.0199
0.1952
0.0017
0.0012
0.2402
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.2386
0.0001
0.4641
0.0000
0.0013
0.0044
MOLE FRACTION
0.3367
0.0002
0.6549
0.0001
0.0019
0.0062
MASS FLOW
(kg/h)
7.6460
0.0059
8.3605
0.0019
0.0807
0.2570
MASS FRACTION
0.4676
0.0004
0.5113
0.0001
0.0049
0.0157
LIQUID VOLUME
FLOW (m3/h)
0.0096
0.0000
0.0084
0.0000
0.0001
0.0003
LIQUID VOLUME
FRACTION
0.5222
0.0005
0.4553
0.0001
0.0042
0.0177
Total 0.7086 1.0000 16.3520 1.0000 0.0184 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.433
57.47
0.5924
18.29
0.4108
18.77
LIGHT
1.433
57.47
0.5924
18.29
0.4108
18.77
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Reboiler: Reboiler @COL1
PRODUCT FROM
Tray Section: Main TS @COL1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 10 @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Overall
0.0000
166.0
10.26
Vapour Phase
0.0000
166.0
10.26
Liquid Phase
1.0000
166.0
10.26
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 32 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 10 @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.5302
0.2823
1.304e-002
-2.615e+005
81.98
-1.386e+005
1.287e-002 *
Vapour Phase
0.0000
0.0000
0.0000
-2.169e+005
156.9
0.0000
0.0000
Liquid Phase
0.5302
0.2823
1.304e-002
-2.615e+005
81.98
-1.386e+005
1.287e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
22.19
34.58
767.2
1.533e-002
-1.179e+004
3.695
117.9
5.314
1.871e+005
8435
---
0.0000
0.0000
0.0000
---
40.67
117.9
12.54
902.2
4.259e-006
---
10.59
---
0.0000
1.076
1.076
3.596e+004
0.1072
913.9
1.287e-002
1.000
2.892e-002
1621
0.0000
34.61
0.4485
8.222e-002
109.6
4.939
109.6
4.939
---
---
---
0.2267
0.4555
1.287e-002
Vapour Phase
25.72
0.3111
8.001
0.0000
-8434
6.099
50.40
1.960
3.455e+005
1.344e+004
---
0.0000
---
0.0000
---
33.28
50.40
0.0000
855.9
---
0.9152
10.62
---
---
1.198
1.306
---
1.302
863.9
0.0000
0.0000
3.214
---
0.0000
---
2.801e-002
1.041e-002
42.08
1.636
38.60
1.501
---
---
---
0.2819
0.5725
0.0000
Liquid Phase
22.19
34.58
767.2
1.533e-002
-1.179e+004
3.695
117.9
5.314
1.871e+005
8435
1.000
1.000
---
0.0000
---
40.67
117.9
12.54
902.2
4.259e-006
8.234e-003
10.59
---
---
1.076
1.076
---
0.1072
913.9
1.287e-002
1.000
2.892e-002
---
1.0000
34.61
0.4485
8.222e-002
109.6
4.939
109.6
4.939
---
---
---
0.2267
0.4555
1.287e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 33 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 10 @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Viscosity Index
Overall
---
Vapour Phase
---
Liquid Phase
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1529
0.0000
0.3757
0.0000
0.0012
0.0004
MOLE FRACTION
0.2885
0.0000
0.7085
0.0000
0.0022
0.0008
MASS FLOW
(kg/h)
4.9005
0.0002
6.7675
0.0002
0.0693
0.0247
MASS FRACTION
0.4166
0.0000
0.5753
0.0000
0.0059
0.0021
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4724
0.0000
0.5201
0.0000
0.0051
0.0024
Total 0.5302 1.0000 11.7624 1.0000 0.0130 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.4801
0.0007
0.4955
0.0002
0.0011
0.0224
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.5982
0.0012
0.3471
0.0004
0.0025
0.0506
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.6435
0.0016
0.2977
0.0004
0.0020
0.0548
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1529
0.0000
0.3757
0.0000
0.0012
0.0004
MOLE FRACTION
0.2885
0.0000
0.7085
0.0000
0.0022
0.0008
MASS FLOW
(kg/h)
4.9005
0.0002
6.7675
0.0002
0.0693
0.0247
MASS FRACTION
0.4166
0.0000
0.5753
0.0000
0.0059
0.0021
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4724
0.0000
0.5201
0.0000
0.0051
0.0024
Total 0.5302 1.0000 11.7624 1.0000 0.0130 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.664
77.67
0.6993
24.99
0.4928
27.93
LIGHT
1.664
77.67
0.6993
24.99
0.4928
27.93
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Material Stream: 10
PRODUCT FROM
Reboiler: Reboiler @COL1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 34 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 8 @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.6029
125.6
10.26
0.8997
0.6896
3.832e-002
-2.226e+005
125.9
-2.003e+005
3.847e-002 *
Vapour Phase
0.6029
125.6
10.26
0.5424
0.5068
3.002e-002
-1.921e+005
160.8
-1.042e+005
3.120e-002
Aqueous Phase
0.3971
125.6
10.26
0.3573
0.1827
8.300e-003
-2.689e+005
72.97
-9.609e+004
8.179e-003
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
Overall
31.93
0.5659
18.07
1.590
-6970
3.943
85.15
2.666
6.527e+005
2.044e+004
0.7834
0.7350
0.0000
0.0000
1.581
23.48
85.15
21.27
749.8
2.542e-006
---
11.27
---
0.0000
1.108
1.091
3.798e+004
---
746.9
3.847e-002
0.3971
1.767
1189
0.6029
44.68
---
---
76.83
2.406
78.02
2.443
---
---
---
Vapour Phase
38.93
0.3431
13.36
1.581
-4933
4.130
71.74
1.843
9.856e+005
2.531e+004
0.7834
0.7350
---
0.0000
1.581
18.07
71.74
12.83
703.5
---
0.9138
11.33
---
---
1.131
1.196
---
0.8503
676.8
3.120e-002
0.0000
2.914
---
0.6029
---
2.585e-002
1.136e-002
63.42
1.629
59.96
1.540
---
---
---
Aqueous Phase
21.31
39.05
832.1
9.151e-003
-1.262e+004
3.424
105.5
4.951
1.474e+005
6916
0.2166
0.2650
---
0.0000
---
43.05
105.5
8.449
917.3
2.542e-006
8.030e-003
10.61
---
---
1.086
1.168
---
0.1672
931.0
8.179e-003
1.000
2.561e-002
---
0.3971
44.68
0.5109
0.1391
97.18
4.561
90.31
4.238
86.42
4.055
1.221
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 35 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 8 @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(atm)
(atm)
(m3/h)
Overall
6.082
7.436
3.938e-002
---
Vapour Phase
6.871
7.323
3.120e-002
0.9266
Aqueous Phase
0.5241
7.417
8.179e-003
---
COMPOSITION
Overall Phase Vapour Fraction 0.6029
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1530
0.3659
0.3779
0.0008
0.0012
0.0011
MOLE FRACTION
0.1700
0.4066
0.4200
0.0008
0.0013
0.0013
MASS FLOW
(kg/h)
4.9015
16.8554
6.8072
0.0331
0.0693
0.0663
MASS FRACTION
0.1706
0.5866
0.2369
0.0012
0.0024
0.0023
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0251
0.0068
0.0000
0.0001
0.0001
LIQUID VOLUME
FRACTION
0.1608
0.6562
0.1780
0.0011
0.0017
0.0022
Total 0.8997 1.0000 28.7327 1.0000 0.0383 1.0000
Vapour Phase Phase Fraction 0.6029
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0748
0.3643
0.1012
0.0007
0.0003
0.0011
MOLE FRACTION
0.1378
0.6717
0.1865
0.0014
0.0005
0.0021
MASS FLOW
(kg/h)
2.3957
16.7842
1.8226
0.0325
0.0179
0.0656
MASS FRACTION
0.1134
0.7948
0.0863
0.0015
0.0008
0.0031
LIQUID VOLUME
FLOW (m3/h)
0.0030
0.0250
0.0018
0.0000
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.1003
0.8341
0.0608
0.0014
0.0006
0.0028
Total 0.5424 1.0000 21.1185 1.0000 0.0300 1.0000
Aqueous Phase Phase Fraction 0.3971
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0782
0.0015
0.2767
0.0000
0.0009
0.0000
MOLE FRACTION
0.2189
0.0043
0.7743
0.0000
0.0024
0.0000
MASS FLOW
(kg/h)
2.5058
0.0711
4.9845
0.0006
0.0514
0.0007
MASS FRACTION
0.3291
0.0093
0.6546
0.0001
0.0067
0.0001
LIQUID VOLUME
FLOW (m3/h)
0.0031
0.0001
0.0050
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.3794
0.0128
0.6017
0.0001
0.0059
0.0001
Total 0.3573 1.0000 7.6141 1.0000 0.0083 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.6298
155.4
0.2409
36.21
0.2291
60.34
LIGHT
---
---
---
---
---
---
HEAVY
0.6298
155.4
0.2409
36.21
0.2291
60.34
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL1
PRODUCT FROM
Material Stream: 8
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 36 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 8 @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROCESS UTILITY
Material Stream: 9 @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
45.29
10.00
0.3696
0.4073
2.528e-002
-2.018e+005
84.29
-7.459e+004
2.739e-002 *
Vapour Phase
0.0000
45.29
10.00
0.0000
0.0000
0.0000
-1.841e+005
138.8
0.0000
0.0000
Liquid Phase
1.0000
45.29
10.00
0.3696
0.4073
2.528e-002
-2.018e+005
84.29
-7.459e+004
2.739e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
Overall
45.92
12.50
573.9
2.957e-002
-4396
1.836
123.1
2.681
1.321e+006
2.876e+004
---
0.0000
0.0000
0.0000
---
14.62
123.1
8.738
671.3
8.214e-006
---
11.38
---
0.0000
1.072
1.072
1.757e+004
0.1307
619.5
2.739e-002
1.000
8.002e-002
382.7
0.0000
9.381
0.1217
7.502e-002
114.8
Vapour Phase
46.02
0.4539
20.89
0.0000
-4000
3.015
76.20
1.656
1.326e+006
2.881e+004
---
0.0000
---
0.0000
---
14.57
76.20
0.0000
670.5
---
0.8431
11.38
---
---
1.122
1.247
---
0.4693
618.3
0.0000
0.0000
2.203
---
0.0000
---
1.877e-002
9.803e-003
67.89
Liquid Phase
45.92
12.50
573.9
2.957e-002
-4396
1.836
123.1
2.681
1.321e+006
2.876e+004
1.000
1.000
---
0.0000
---
14.62
123.1
8.738
671.3
8.214e-006
3.062e-002
11.38
---
---
1.072
1.072
---
0.1307
619.5
2.739e-002
1.000
8.002e-002
---
1.0000
9.381
0.1217
7.502e-002
114.8
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 37 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 9 @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
2.500
114.8
2.500
---
---
---
8.269
8.229
2.739e-002
---
Vapour Phase
1.475
61.09
1.327
---
---
---
8.297
8.285
0.0000
-9.862
Liquid Phase
2.500
114.8
2.500
---
---
---
8.269
8.229
2.739e-002
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.3659
0.0022
0.0007
0.0000
0.0007
MOLE FRACTION
0.0001
0.9900
0.0060
0.0020
0.0000
0.0019
MASS FLOW
(kg/h)
0.0009
16.8551
0.0397
0.0329
0.0000
0.0416
MASS FRACTION
0.0001
0.9932
0.0023
0.0019
0.0000
0.0025
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0251
0.0000
0.0000
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.0000
0.9946
0.0016
0.0017
0.0000
0.0021
Total 0.3696 1.0000 16.9703 1.0000 0.0253 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0000
0.9974
0.0018
0.0006
0.0000
0.0002
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0000
0.9984
0.0007
0.0006
0.0000
0.0003
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.9988
0.0005
0.0005
0.0000
0.0002
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.3659
0.0022
0.0007
0.0000
0.0007
MOLE FRACTION
0.0001
0.9900
0.0060
0.0020
0.0000
0.0019
MASS FLOW
(kg/h)
0.0009
16.8551
0.0397
0.0329
0.0000
0.0416
MASS FRACTION
0.0001
0.9932
0.0023
0.0019
0.0000
0.0025
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0251
0.0000
0.0000
0.0000
0.0001
LIQUID VOLUME
FRACTION
0.0000
0.9946
0.0016
0.0017
0.0000
0.0021
Total 0.3696 1.0000 16.9703 1.0000 0.0253 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.1034
1.007
0.2940
0.3171
1.976e-002
0.1059
LIGHT
0.1034
1.007
0.2940
0.3171
1.976e-002
0.1059
HEAVY
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 38 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 9 @COL1 (continued)Fluid Package: Basis-1
Property Package: PRSV
UNIT OPERATIONS
FEED TO
Material Stream: DME Product
PRODUCT FROM
Total Condenser: Condenser @COL1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T101COND @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Condenser @COL1
Duty SP: 1.948e+004 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Energy Stream: T101COND
PRODUCT FROM
Total Condenser: Condenser @COL1
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T101REB @COL1Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Reboiler @COL1
Duty SP: 6518 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Reboiler: Reboiler @COL1
PRODUCT FROM
Energy Stream: T101REB
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: Reflux @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Overall
0.0000
122.5
6.800
6.664e-002
Vapour Phase
0.0000
122.5
6.800
0.0000
Liquid Phase
1.0000
122.5
6.800
6.664e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 39 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Reflux @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
5.356e-002
2.802e-003
-2.319e+005
52.76
-1.545e+004
2.794e-003 *
Vapour Phase
0.0000
0.0000
-1.987e+005
135.4
0.0000
0.0000
Liquid Phase
5.356e-002
2.802e-003
-2.319e+005
52.76
-1.545e+004
2.794e-003
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
33.48
20.10
673.1
3.315e-003
-6924
1.576
171.0
5.108
6.933e+005
2.070e+004
---
0.0000
0.0000
0.0000
---
23.78
171.0
1.576
796.4
9.209e-007
---
10.63
---
0.0000
1.051
1.300
3.283e+004
0.2548
798.8
2.794e-003
1.000
4.975e-002
980.5
0.0000
15.16
0.1397
0.1715
162.7
4.859
131.5
3.928
---
---
---
0.2871
0.2892
2.794e-003
-31.64
Vapour Phase
34.11
0.2305
7.863
0.0000
-5825
3.969
60.23
1.766
7.194e+005
2.109e+004
---
0.0000
---
0.0000
---
23.29
60.23
0.0000
794.3
---
0.9087
10.63
---
---
1.160
1.260
---
1.055
797.0
0.0000
0.0000
4.338
---
0.0000
---
2.132e-002
8.295e-003
51.92
1.522
47.79
1.401
---
---
---
0.3627
0.3721
0.0000
---
Liquid Phase
33.48
20.10
673.1
3.315e-003
-6924
1.576
171.0
5.108
6.933e+005
2.070e+004
1.000
1.000
---
0.0000
---
23.78
171.0
1.576
796.4
9.209e-007
1.042e-002
10.63
---
---
1.051
1.300
---
0.2548
798.8
2.794e-003
1.000
4.975e-002
---
1.0000
15.16
0.1397
0.1715
162.7
4.859
131.5
3.928
---
---
---
0.2871
0.2892
2.794e-003
-31.64
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 40 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Reflux @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0612
0.0000
0.0011
0.0000
0.0000
0.0043
MOLE FRACTION
0.9179
0.0007
0.0169
0.0007
0.0000
0.0638
MASS FLOW
(kg/h)
1.9601
0.0022
0.0203
0.0020
0.0000
0.2470
MASS FRACTION
0.8783
0.0010
0.0091
0.0009
0.0000
0.1107
LIQUID VOLUME
FLOW (m3/h)
0.0025
0.0000
0.0000
0.0000
0.0000
0.0003
LIQUID VOLUME
FRACTION
0.8791
0.0012
0.0073
0.0009
0.0000
0.1116
Total 0.0666 1.0000 2.2316 1.0000 0.0028 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.9084
0.0054
0.0057
0.0018
0.0000
0.0788
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.8533
0.0073
0.0030
0.0023
0.0000
0.1341
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.8518
0.0086
0.0024
0.0024
0.0000
0.1348
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0612
0.0000
0.0011
0.0000
0.0000
0.0043
MOLE FRACTION
0.9179
0.0007
0.0169
0.0007
0.0000
0.0638
MASS FLOW
(kg/h)
1.9601
0.0022
0.0203
0.0020
0.0000
0.2470
MASS FRACTION
0.8783
0.0010
0.0091
0.0009
0.0000
0.1107
LIQUID VOLUME
FLOW (m3/h)
0.0025
0.0000
0.0000
0.0000
0.0000
0.0003
LIQUID VOLUME
FRACTION
0.8791
0.0012
0.0073
0.0009
0.0000
0.1116
Total 0.0666 1.0000 2.2316 1.0000 0.0028 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.9896
7.593
0.3383
2.695
0.2003
1.234
LIGHT
0.9896
7.593
0.3383
2.695
0.2003
1.234
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL2
PRODUCT FROM
Total Condenser: Condenser @COL2
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 41 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Condenser @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
1.0000
123.7
6.800
7.331e-002
5.891e-002
3.082e-003
-1.990e+005
135.6
-1.459e+004
3.073e-003 *
Vapour Phase
1.0000
123.7
6.800
7.331e-002
5.891e-002
3.082e-003
-1.990e+005
135.6
-1.459e+004
3.073e-003
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
Overall
33.48
0.2294
7.683
0.3195
-5944
4.051
59.32
1.772
6.933e+005
2.070e+004
1.000
1.000
0.0000
0.0000
0.3195
23.78
59.32
1.733
796.4
---
0.9102
10.63
---
0.0000
1.163
1.263
3.283e+004
1.082
798.8
3.073e-003
0.0000
4.358
980.5
1.0000
---
2.146e-002
8.314e-003
51.01
1.523
46.95
1.402
---
---
---
Vapour Phase
33.48
0.2294
7.683
0.3195
-5944
4.051
59.32
1.772
6.933e+005
2.070e+004
1.000
1.000
---
0.0000
0.3195
23.78
59.32
1.733
796.4
---
0.9102
10.63
---
---
1.163
1.263
---
1.082
798.8
3.073e-003
0.0000
4.358
---
1.0000
---
2.146e-002
8.314e-003
51.01
1.523
46.95
1.402
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 42 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Condenser @COL2 (contFluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(atm)
(atm)
(m3/h)
Overall
0.2871
0.2892
3.073e-003
4.315
Vapour Phase
0.2871
0.2892
3.073e-003
4.315
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0673
0.0001
0.0012
0.0000
0.0000
0.0047
MOLE FRACTION
0.9179
0.0007
0.0169
0.0007
0.0000
0.0638
MASS FLOW
(kg/h)
2.1561
0.0024
0.0223
0.0022
0.0000
0.2717
MASS FRACTION
0.8783
0.0010
0.0091
0.0009
0.0000
0.1107
LIQUID VOLUME
FLOW (m3/h)
0.0027
0.0000
0.0000
0.0000
0.0000
0.0003
LIQUID VOLUME
FRACTION
0.8791
0.0012
0.0073
0.0009
0.0000
0.1116
Total 0.0733 1.0000 2.4547 1.0000 0.0031 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0673
0.0001
0.0012
0.0000
0.0000
0.0047
MOLE FRACTION
0.9179
0.0007
0.0169
0.0007
0.0000
0.0638
MASS FLOW
(kg/h)
2.1561
0.0024
0.0223
0.0022
0.0000
0.2717
MASS FRACTION
0.8783
0.0010
0.0091
0.0009
0.0000
0.1107
LIQUID VOLUME
FLOW (m3/h)
0.0027
0.0000
0.0000
0.0000
0.0000
0.0003
LIQUID VOLUME
FRACTION
0.8791
0.0012
0.0073
0.0009
0.0000
0.1116
Total 0.0733 1.0000 2.4547 1.0000 0.0031 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Total Condenser: Condenser @COL2
PRODUCT FROM
Tray Section: Main TS @COL2
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: Boilup @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Overall
1.0000
151.2
6.910
3.959e-002
Vapour Phase
1.0000
151.2
6.910
3.959e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 43 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Boilup @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
2.377e-002
1.152e-003
-2.174e+005
158.3
-8607
1.143e-003 *
Vapour Phase
2.377e-002
1.152e-003
-2.174e+005
158.3
-8607
1.143e-003
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
25.02
0.2115
5.291
0.1872
-8690
6.329
47.19
1.886
3.171e+005
1.268e+004
1.000
1.000
0.0000
0.0000
0.1872
34.36
47.19
0.9362
859.4
---
0.9383
10.62
---
0.0000
1.214
1.293
3.676e+004
1.870
866.3
1.143e-003
0.0000
4.728
1469
1.0000
---
2.628e-002
9.895e-003
38.87
1.554
36.50
1.459
---
---
---
0.2246
0.1218
1.143e-003
10.71
Vapour Phase
25.02
0.2115
5.291
0.1872
-8690
6.329
47.19
1.886
3.171e+005
1.268e+004
1.000
1.000
---
0.0000
0.1872
34.36
47.19
0.9362
859.4
---
0.9383
10.62
---
---
1.214
1.293
---
1.870
866.3
1.143e-003
0.0000
4.728
---
1.0000
---
2.628e-002
9.895e-003
38.87
1.554
36.50
1.459
---
---
---
0.2246
0.1218
1.143e-003
10.71
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 44 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Boilup @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0196
0.0000
0.0199
0.0000
0.0000
0.0000
MOLE FRACTION
0.4955
0.0000
0.5033
0.0000
0.0012
0.0000
MASS FLOW
(kg/h)
0.6287
0.0000
0.3590
0.0000
0.0028
0.0000
MASS FRACTION
0.6347
0.0000
0.3624
0.0000
0.0028
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0008
0.0000
0.0004
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.6856
0.0000
0.3121
0.0000
0.0023
0.0000
Total 0.0396 1.0000 0.9905 1.0000 0.0012 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0196
0.0000
0.0199
0.0000
0.0000
0.0000
MOLE FRACTION
0.4955
0.0000
0.5033
0.0000
0.0012
0.0000
MASS FLOW
(kg/h)
0.6287
0.0000
0.3590
0.0000
0.0028
0.0000
MASS FRACTION
0.6347
0.0000
0.3624
0.0000
0.0028
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0008
0.0000
0.0004
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.6856
0.0000
0.3121
0.0000
0.0023
0.0000
Total 0.0396 1.0000 0.9905 1.0000 0.0012 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL2
PRODUCT FROM
Reboiler: Reboiler @COL2
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: To Reboiler @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
150.5
6.910
0.5631
0.3007
1.391e-002
-2.630e+005
77.58
-1.481e+005
1.373e-002 *
Vapour Phase
0.0000
150.5
6.910
0.0000
0.0000
0.0000
-2.165e+005
157.6
0.0000
0.0000
Liquid Phase
1.0000
150.5
6.910
0.5631
0.3007
1.391e-002
-2.630e+005
77.58
-1.481e+005
1.373e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 45 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Reboiler @COL2 (continuFluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
22.25
35.20
783.1
1.600e-002
-1.182e+004
3.487
116.5
5.238
1.903e+005
8552
---
0.0000
0.0000
0.0000
---
40.48
116.5
13.31
900.8
4.444e-006
---
10.60
---
0.0000
1.077
1.077
3.734e+004
0.1292
912.2
1.373e-002
1.000
2.841e-002
1678
0.0000
37.31
0.4531
0.1012
108.2
4.864
108.2
4.864
---
---
---
0.2237
8.587e-002
1.373e-002
---
Vapour Phase
25.31
0.2121
5.366
0.0000
-8557
6.226
47.63
1.882
3.304e+005
1.306e+004
---
0.0000
---
0.0000
---
33.82
47.63
0.0000
855.9
---
0.9374
10.62
---
---
1.211
1.291
---
1.832
862.3
0.0000
0.0000
4.716
---
0.0000
---
2.610e-002
9.833e-003
39.31
1.554
36.89
1.458
---
---
---
0.2247
0.1269
0.0000
---
Liquid Phase
22.25
35.20
783.1
1.600e-002
-1.182e+004
3.487
116.5
5.238
1.903e+005
8552
1.000
1.000
---
0.0000
---
40.48
116.5
13.31
900.8
4.444e-006
5.648e-003
10.60
---
---
1.077
1.077
---
0.1292
912.2
1.373e-002
1.000
2.841e-002
---
1.0000
37.31
0.4531
0.1012
108.2
4.864
108.2
4.864
---
---
---
0.2237
8.587e-002
1.373e-002
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
MOLAR FLOW
(kgmole/h)
0.1664
0.0000
0.3955
MOLE FRACTION
0.2956
0.0000
0.7023
MASS FLOW
(kg/h)
5.3332
0.0000
7.1244
MASS FRACTION
0.4256
0.0000
0.5686
LIQUID VOLUME
FLOW (m3/h)
0.0067
0.0000
0.0071
LIQUID VOLUME
FRACTION
0.4818
0.0000
0.5132
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 46 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Reboiler @COL2 (continuFluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0012
0.0000
MOLE FRACTION
0.0000
0.0021
0.0000
MASS FLOW
(kg/h)
0.0000
0.0720
0.0000
MASS FRACTION
0.0000
0.0057
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.0049
0.0000
Total 0.5631 1.0000 12.5297 1.0000 0.0139 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.5163
0.0000
0.4825
0.0000
0.0011
0.0000
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.6538
0.0000
0.3435
0.0000
0.0026
0.0001
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.7032
0.0000
0.2946
0.0000
0.0021
0.0001
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1664
0.0000
0.3955
0.0000
0.0012
0.0000
MOLE FRACTION
0.2956
0.0000
0.7023
0.0000
0.0021
0.0000
MASS FLOW
(kg/h)
5.3332
0.0000
7.1244
0.0000
0.0720
0.0000
MASS FRACTION
0.4256
0.0000
0.5686
0.0000
0.0057
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0067
0.0000
0.0071
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4818
0.0000
0.5132
0.0000
0.0049
0.0000
Total 0.5631 1.0000 12.5297 1.0000 0.0139 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.747
120.1
0.6871
34.68
0.5198
40.91
LIGHT
1.747
120.1
0.6871
34.68
0.5198
40.91
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Reboiler: Reboiler @COL2
PRODUCT FROM
Tray Section: Main TS @COL2
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 13 @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Overall
0.0000
151.2
6.910
Vapour Phase
0.0000
151.2
6.910
Liquid Phase
1.0000
151.2
6.910
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 47 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 13 @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.5235
0.2769
1.276e-002
-2.637e+005
78.05
-1.380e+005
1.259e-002 *
Vapour Phase
0.0000
0.0000
0.0000
-2.174e+005
158.3
0.0000
0.0000
Liquid Phase
0.5235
0.2769
1.276e-002
-2.637e+005
78.05
-1.380e+005
1.259e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
22.04
35.72
787.2
1.466e-002
-1.196e+004
3.541
115.0
5.216
1.807e+005
8198
---
0.0000
0.0000
0.0000
---
41.04
115.0
12.38
904.5
4.072e-006
---
10.59
---
0.0000
1.078
1.078
3.737e+004
0.1264
916.3
1.259e-002
1.000
2.800e-002
1696
0.0000
37.74
0.4632
9.951e-002
106.7
4.839
106.7
4.839
---
---
---
0.2236
8.343e-002
1.259e-002
Vapour Phase
25.02
0.2115
5.291
0.0000
-8690
6.329
47.19
1.886
3.171e+005
1.268e+004
---
0.0000
---
0.0000
---
34.36
47.19
0.0000
859.4
---
0.9383
10.62
---
---
1.214
1.293
---
1.870
866.3
0.0000
0.0000
4.728
---
0.0000
---
2.628e-002
9.895e-003
38.87
1.554
36.50
1.459
---
---
---
0.2246
0.1218
0.0000
Liquid Phase
22.04
35.72
787.2
1.466e-002
-1.196e+004
3.541
115.0
5.216
1.807e+005
8198
1.000
1.000
---
0.0000
---
41.04
115.0
12.38
904.5
4.072e-006
5.556e-003
10.59
---
---
1.078
1.078
---
0.1264
916.3
1.259e-002
1.000
2.800e-002
---
1.0000
37.74
0.4632
9.951e-002
106.7
4.839
106.7
4.839
---
---
---
0.2236
8.343e-002
1.259e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 48 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 13 @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Viscosity Index
Overall
---
Vapour Phase
---
Liquid Phase
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1468
0.0000
0.3755
0.0000
0.0012
0.0000
MOLE FRACTION
0.2805
0.0000
0.7173
0.0000
0.0022
0.0000
MASS FLOW
(kg/h)
4.7045
0.0000
6.7654
0.0000
0.0693
0.0000
MASS FRACTION
0.4077
0.0000
0.5863
0.0000
0.0060
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4634
0.0000
0.5314
0.0000
0.0052
0.0000
Total 0.5235 1.0000 11.5392 1.0000 0.0128 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.4955
0.0000
0.5033
0.0000
0.0012
0.0000
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.6347
0.0000
0.3624
0.0000
0.0028
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.6856
0.0000
0.3121
0.0000
0.0023
0.0000
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1468
0.0000
0.3755
0.0000
0.0012
0.0000
MOLE FRACTION
0.2805
0.0000
0.7173
0.0000
0.0022
0.0000
MASS FLOW
(kg/h)
4.7045
0.0000
6.7654
0.0000
0.0693
0.0000
MASS FRACTION
0.4077
0.0000
0.5863
0.0000
0.0060
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4634
0.0000
0.5314
0.0000
0.0052
0.0000
Total 0.5235 1.0000 11.5392 1.0000 0.0128 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.767
130.9
0.7016
37.65
0.5312
45.78
LIGHT
1.767
130.9
0.7016
37.65
0.5312
45.78
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Material Stream: 13
PRODUCT FROM
Reboiler: Reboiler @COL2
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 49 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 11 @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0502
150.9
6.910
0.5302
0.2823
1.304e-002
-2.615e+005
82.08
-1.386e+005
1.287e-002 *
Vapour Phase
0.0502
150.9
6.910
2.663e-002
1.620e-002
7.868e-004
-2.174e+005
158.7
-5790
7.800e-004
Aqueous Phase
0.9498
150.9
6.910
0.5036
0.2661
1.225e-002
-2.638e+005
78.03
-1.329e+005
1.209e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
Overall
22.19
3.792
84.13
0.1398
-1.179e+004
3.700
111.3
5.017
1.871e+005
8435
6.035e-002
5.739e-002
0.0000
0.0000
0.1258
40.67
111.3
12.54
902.2
3.907e-006
---
10.59
---
0.0000
1.081
1.005
3.748e+004
---
913.9
1.287e-002
0.9498
0.2637
1689
0.0502
37.89
---
---
103.0
4.643
110.7
4.990
---
---
---
Vapour Phase
25.35
0.2117
5.368
0.1258
-8576
6.261
47.72
1.882
3.306e+005
1.304e+004
6.035e-002
5.739e-002
---
0.0000
0.1258
33.84
47.72
0.6296
858.0
---
0.9379
10.62
---
---
1.211
1.289
---
1.845
865.4
7.800e-004
0.0000
4.723
---
0.0502
---
2.622e-002
9.903e-003
39.40
1.554
37.02
1.460
---
---
---
Aqueous Phase
22.02
35.80
788.3
1.406e-002
-1.198e+004
3.544
114.7
5.208
1.796e+005
8155
0.9396
0.9426
---
0.0000
---
41.10
114.7
11.91
905.0
3.907e-006
5.547e-003
10.59
---
---
1.078
1.078
---
0.1267
916.9
1.209e-002
1.000
2.793e-002
---
0.9498
37.89
0.4649
9.984e-002
106.4
4.831
106.4
4.831
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 50 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 11 @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(atm)
(atm)
(m3/h)
Overall
0.2267
0.4555
1.287e-002
---
Vapour Phase
0.2495
0.4987
7.800e-004
10.57
Aqueous Phase
0.2244
0.2113
1.209e-002
---
COMPOSITION
Overall Phase Vapour Fraction 0.0502
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1529
0.0000
0.3757
0.0000
0.0012
0.0004
MOLE FRACTION
0.2885
0.0000
0.7085
0.0000
0.0022
0.0008
MASS FLOW
(kg/h)
4.9005
0.0002
6.7675
0.0002
0.0693
0.0247
MASS FRACTION
0.4166
0.0000
0.5753
0.0000
0.0059
0.0021
LIQUID VOLUME
FLOW (m3/h)
0.0062
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4724
0.0000
0.5201
0.0000
0.0051
0.0024
Total 0.5302 1.0000 11.7624 1.0000 0.0130 1.0000
Vapour Phase Phase Fraction 5.022e-002
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0130
0.0000
0.0133
0.0000
0.0000
0.0003
MOLE FRACTION
0.4865
0.0002
0.5007
0.0001
0.0012
0.0114
MASS FLOW
(kg/h)
0.4151
0.0002
0.2402
0.0001
0.0019
0.0176
MASS FRACTION
0.6149
0.0003
0.3558
0.0002
0.0028
0.0260
LIQUID VOLUME
FLOW (m3/h)
0.0005
0.0000
0.0002
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.6630
0.0004
0.3059
0.0002
0.0023
0.0283
Total 0.0266 1.0000 0.6751 1.0000 0.0008 1.0000
Aqueous Phase Phase Fraction 0.9498
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1400
0.0000
0.3623
0.0000
0.0011
0.0001
MOLE FRACTION
0.2780
0.0000
0.7195
0.0000
0.0022
0.0002
MASS FLOW
(kg/h)
4.4854
0.0000
6.5273
0.0001
0.0674
0.0071
MASS FRACTION
0.4046
0.0000
0.5887
0.0000
0.0061
0.0006
LIQUID VOLUME
FLOW (m3/h)
0.0056
0.0000
0.0065
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4601
0.0000
0.5339
0.0000
0.0052
0.0007
Total 0.5036 1.0000 11.0873 1.0000 0.0123 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.750
132.6
0.6958
38.01
0.5273
46.50
LIGHT
---
---
---
---
---
---
HEAVY
1.750
132.6
0.6958
38.01
0.5273
46.50
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL2
PRODUCT FROM
Material Stream: 11
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 51 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 11 @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROCESS UTILITY
Material Stream: 12 @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
122.5
6.800
6.664e-003
5.356e-003
2.802e-004
-2.319e+005
52.76
-1545
2.794e-004 *
Vapour Phase
0.0000
122.5
6.800
0.0000
0.0000
0.0000
-1.987e+005
135.4
0.0000
0.0000
Liquid Phase
1.0000
122.5
6.800
6.664e-003
5.356e-003
2.802e-004
-2.319e+005
52.76
-1545
2.794e-004
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
Overall
33.48
20.10
673.1
3.315e-004
-6924
1.576
171.0
5.108
6.933e+005
2.070e+004
---
0.0000
0.0000
0.0000
---
23.78
171.0
0.1576
796.4
9.209e-008
---
10.63
---
0.0000
1.051
1.300
3.283e+004
0.2548
798.8
2.794e-004
1.000
4.975e-002
980.5
0.0000
15.16
0.1397
0.1715
162.7
Vapour Phase
34.11
0.2305
7.863
0.0000
-5825
3.969
60.23
1.766
7.194e+005
2.109e+004
---
0.0000
---
0.0000
---
23.29
60.23
0.0000
794.3
---
0.9087
10.63
---
---
1.160
1.260
---
1.055
797.0
0.0000
0.0000
4.338
---
0.0000
---
2.132e-002
8.295e-003
51.92
Liquid Phase
33.48
20.10
673.1
3.315e-004
-6924
1.576
171.0
5.108
6.933e+005
2.070e+004
1.000
1.000
---
0.0000
---
23.78
171.0
0.1576
796.4
9.209e-008
1.042e-002
10.63
---
---
1.051
1.300
---
0.2548
798.8
2.794e-004
1.000
4.975e-002
---
1.0000
15.16
0.1397
0.1715
162.7
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 52 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 12 @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
4.859
131.5
3.928
---
---
---
0.2871
0.2892
2.794e-004
-31.64
Vapour Phase
1.522
47.79
1.401
---
---
---
0.3627
0.3721
0.0000
---
Liquid Phase
4.859
131.5
3.928
---
---
---
0.2871
0.2892
2.794e-004
-31.64
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0061
0.0000
0.0001
0.0000
0.0000
0.0004
MOLE FRACTION
0.9179
0.0007
0.0169
0.0007
0.0000
0.0638
MASS FLOW
(kg/h)
0.1960
0.0002
0.0020
0.0002
0.0000
0.0247
MASS FRACTION
0.8783
0.0010
0.0091
0.0009
0.0000
0.1107
LIQUID VOLUME
FLOW (m3/h)
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.8791
0.0012
0.0073
0.0009
0.0000
0.1116
Total 0.0067 1.0000 0.2232 1.0000 0.0003 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.9084
0.0054
0.0057
0.0018
0.0000
0.0788
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.8533
0.0073
0.0030
0.0023
0.0000
0.1341
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.8518
0.0086
0.0024
0.0024
0.0000
0.1348
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0061
0.0000
0.0001
0.0000
0.0000
0.0004
MOLE FRACTION
0.9179
0.0007
0.0169
0.0007
0.0000
0.0638
MASS FLOW
(kg/h)
0.1960
0.0002
0.0020
0.0002
0.0000
0.0247
MASS FRACTION
0.8783
0.0010
0.0091
0.0009
0.0000
0.1107
LIQUID VOLUME
FLOW (m3/h)
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.8791
0.0012
0.0073
0.0009
0.0000
0.1116
Total 0.0067 1.0000 0.2232 1.0000 0.0003 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
0.9896
7.593
0.3383
2.695
0.2003
1.234
LIGHT
0.9896
7.593
0.3383
2.695
0.2003
1.234
HEAVY
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 53 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 12 @COL2 (continued)Fluid Package: Basis-1
Property Package: PRSV
UNIT OPERATIONS
FEED TO
Material Stream: 12
PRODUCT FROM
Total Condenser: Condenser @COL2
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T102C @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Condenser @COL2
Duty SP: 2407 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Energy Stream: T102C
PRODUCT FROM
Total Condenser: Condenser @COL2
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T102R @COL2Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Reboiler @COL2
Duty SP: 1460 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Reboiler: Reboiler @COL2
PRODUCT FROM
Energy Stream: T102R
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: Reflux @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Overall
0.0000
70.18
1.080
0.7367
Vapour Phase
0.0000
70.18
1.080
0.0000
Liquid Phase
1.0000
70.18
1.080
0.7367
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 54 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Reflux @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.5641
2.950e-002
-2.405e+005
24.22
-1.771e+005
2.948e-002 *
Vapour Phase
0.0000
0.0000
-1.995e+005
141.8
0.0000
0.0000
Liquid Phase
0.5641
2.950e-002
-2.405e+005
24.22
-1.771e+005
2.948e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
31.91
23.12
737.8
3.186e-002
-7537
0.7592
166.4
5.215
6.318e+005
1.980e+004
---
0.0000
0.0000
0.0000
---
24.97
166.4
17.42
796.7
8.850e-006
---
10.62
---
0.0000
1.053
1.053
4.066e+004
0.4182
797.3
2.948e-002
1.000
4.325e-002
1274
0.0000
22.91
0.1634
0.3085
158.1
4.954
158.1
4.954
---
---
---
0.2250
0.2231
2.948e-002
-12.61
Vapour Phase
32.02
3.916e-002
1.254
0.0000
-6231
4.430
48.42
1.512
6.369e+005
1.989e+004
---
0.0000
---
0.0000
---
24.86
48.42
0.0000
795.9
---
0.9791
10.63
---
---
1.207
1.231
---
5.379
796.6
0.0000
0.0000
25.54
---
0.0000
---
1.638e-002
6.743e-003
40.10
1.253
39.34
1.229
---
---
---
0.2250
0.2246
0.0000
---
Liquid Phase
31.91
23.12
737.8
3.186e-002
-7537
0.7592
166.4
5.215
6.318e+005
1.980e+004
1.000
1.000
---
0.0000
---
24.97
166.4
17.42
796.7
8.850e-006
1.658e-003
10.62
---
---
1.053
1.053
---
0.4182
797.3
2.948e-002
1.000
4.325e-002
---
1.0000
22.91
0.1634
0.3085
158.1
4.954
158.1
4.954
---
---
---
0.2250
0.2231
2.948e-002
-12.61
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 55 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Reflux @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.7293
0.0000
0.0073
0.0000
0.0001
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
23.3693
0.0000
0.1316
0.0000
0.0036
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0294
0.0000
0.0001
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.7367 1.0000 23.5046 1.0000 0.0295 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.9980
0.0000
0.0019
0.0000
0.0000
0.0000
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.9989
0.0000
0.0011
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9991
0.0000
0.0009
0.0000
0.0000
0.0000
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.7293
0.0000
0.0073
0.0000
0.0001
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
23.3693
0.0000
0.1316
0.0000
0.0036
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0294
0.0000
0.0001
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.7367 1.0000 23.5046 1.0000 0.0295 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.008
28.24
0.1961
6.433
0.1855
2.623
LIGHT
1.008
28.24
0.1961
6.433
0.1855
2.623
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL3
PRODUCT FROM
Total Condenser: Condenser @COL3
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 56 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Condenser @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
1.0000
70.95
1.080
0.8840
0.6769
3.540e-002
-1.998e+005
142.6
-1.766e+005
3.537e-002 *
Vapour Phase
1.0000
70.95
1.080
0.8840
0.6769
3.540e-002
-1.998e+005
142.6
-1.766e+005
3.537e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
Overall
31.91
3.906e-002
1.246
22.63
-6262
4.469
48.36
1.516
6.318e+005
1.980e+004
1.000
1.000
0.0000
0.0000
22.63
24.97
48.36
20.90
796.7
---
0.9793
10.62
---
0.0000
1.208
1.231
4.066e+004
5.436
797.3
3.537e-002
0.0000
25.60
1274
1.0000
---
1.646e-002
6.774e-003
40.05
1.255
39.29
1.231
---
---
---
Vapour Phase
31.91
3.906e-002
1.246
22.63
-6262
4.469
48.36
1.516
6.318e+005
1.980e+004
1.000
1.000
---
0.0000
22.63
24.97
48.36
20.90
796.7
---
0.9793
10.62
---
---
1.208
1.231
---
5.436
797.3
3.537e-002
0.0000
25.60
---
1.0000
---
1.646e-002
6.774e-003
40.05
1.255
39.29
1.231
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 57 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Condenser @COL3 (contFluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(atm)
(atm)
(m3/h)
Overall
0.2250
0.2231
3.537e-002
19.76
Vapour Phase
0.2250
0.2231
3.537e-002
19.76
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.8752
0.0000
0.0088
0.0000
0.0001
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
28.0432
0.0000
0.1580
0.0000
0.0043
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0352
0.0000
0.0002
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.8840 1.0000 28.2055 1.0000 0.0354 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.8752
0.0000
0.0088
0.0000
0.0001
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
28.0432
0.0000
0.1580
0.0000
0.0043
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0352
0.0000
0.0002
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.8840 1.0000 28.2055 1.0000 0.0354 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Total Condenser: Condenser @COL3
PRODUCT FROM
Tray Section: Main TS @COL3
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: Boilup @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Overall
1.0000
118.8
1.900
0.8398
Vapour Phase
1.0000
118.8
1.900
0.8398
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 58 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Boilup @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.3672
1.536e-002
-2.392e+005
177.5
-2.008e+005
1.511e-002 *
Vapour Phase
0.3672
1.536e-002
-2.392e+005
177.5
-2.008e+005
1.511e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
18.22
5.996e-002
1.092
14.01
-1.313e+004
9.743
34.95
1.918
5761
316.1
1.000
1.000
0.0000
0.0000
14.01
54.68
34.95
19.86
996.3
---
0.9854
9.420
---
0.0000
1.312
1.333
3.995e+004
8.881
1013
1.511e-002
0.0000
16.68
2192
1.0000
---
2.576e-002
9.702e-003
26.63
1.461
26.22
1.439
---
---
---
0.1557
6.616e-002
1.511e-002
22.89
Vapour Phase
18.22
5.996e-002
1.092
14.01
-1.313e+004
9.743
34.95
1.918
5761
316.1
1.000
1.000
---
0.0000
14.01
54.68
34.95
19.86
996.3
---
0.9854
9.420
---
---
1.312
1.333
---
8.881
1013
1.511e-002
0.0000
16.68
---
1.0000
---
2.576e-002
9.702e-003
26.63
1.461
26.22
1.439
---
---
---
0.1557
6.616e-002
1.511e-002
22.89
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 59 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: Boilup @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase Vapour Fraction 1.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0042
0.0000
0.8328
0.0000
0.0027
0.0000
MOLE FRACTION
0.0051
0.0000
0.9917
0.0000
0.0032
0.0000
MASS FLOW
(kg/h)
0.1360
0.0000
15.0031
0.0000
0.1625
0.0000
MASS FRACTION
0.0089
0.0000
0.9805
0.0000
0.0106
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0002
0.0000
0.0150
0.0000
0.0002
0.0000
LIQUID VOLUME
FRACTION
0.0111
0.0000
0.9788
0.0000
0.0101
0.0000
Total 0.8398 1.0000 15.3017 1.0000 0.0154 1.0000
Vapour Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0042
0.0000
0.8328
0.0000
0.0027
0.0000
MOLE FRACTION
0.0051
0.0000
0.9917
0.0000
0.0032
0.0000
MASS FLOW
(kg/h)
0.1360
0.0000
15.0031
0.0000
0.1625
0.0000
MASS FRACTION
0.0089
0.0000
0.9805
0.0000
0.0106
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0002
0.0000
0.0150
0.0000
0.0002
0.0000
LIQUID VOLUME
FRACTION
0.0111
0.0000
0.9788
0.0000
0.0101
0.0000
Total 0.8398 1.0000 15.3017 1.0000 0.0154 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
---
---
---
---
---
---
LIGHT
---
---
---
---
---
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL3
PRODUCT FROM
Reboiler: Reboiler @COL3
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: To Reboiler @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
118.7
1.900
1.216
0.5314
2.222e-002
-2.791e+005
75.61
-3.394e+005
2.185e-002 *
Vapour Phase
0.0000
118.7
1.900
0.0000
0.0000
0.0000
-2.390e+005
177.6
0.0000
0.0000
Liquid Phase
1.0000
118.7
1.900
1.216
0.5314
2.222e-002
-2.791e+005
75.61
-3.394e+005
2.185e-002
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 60 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Reboiler @COL3 (continuFluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
18.21
51.07
929.9
2.381e-002
-1.533e+004
4.152
75.87
4.167
5219
286.6
---
0.0000
0.0000
0.0000
---
54.73
75.87
28.75
996.6
6.614e-006
---
9.341
---
0.0000
1.123
1.194
3.995e+004
0.1573
1013
2.185e-002
1.000
1.958e-002
2194
0.0000
54.71
0.6830
0.1462
67.55
3.710
63.54
3.490
---
---
---
0.1493
6.616e-002
2.185e-002
---
Vapour Phase
18.28
5.997e-002
1.096
0.0000
-1.308e+004
9.716
35.01
1.916
8066
441.3
---
0.0000
---
0.0000
---
54.43
35.01
0.0000
994.8
---
0.9853
9.683
---
---
1.311
1.332
---
8.850
1011
0.0000
0.0000
16.68
---
0.0000
---
2.573e-002
9.699e-003
26.70
1.461
26.28
1.438
---
---
---
0.1748
6.614e-002
0.0000
---
Liquid Phase
18.21
51.07
929.9
2.381e-002
-1.533e+004
4.152
75.87
4.167
5219
286.6
1.000
1.000
---
0.0000
---
54.73
75.87
28.75
996.6
6.614e-006
1.157e-003
9.341
---
---
1.123
1.194
---
0.1573
1013
2.185e-002
1.000
1.958e-002
---
1.0000
54.71
0.6830
0.1462
67.55
3.710
63.54
3.490
---
---
---
0.1493
6.616e-002
2.185e-002
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
MOLAR FLOW
(kgmole/h)
0.0052
0.0000
1.2069
MOLE FRACTION
0.0043
0.0000
0.9926
MASS FLOW
(kg/h)
0.1667
0.0000
21.7422
MASS FRACTION
0.0075
0.0000
0.9820
LIQUID VOLUME
FLOW (m3/h)
0.0002
0.0000
0.0218
LIQUID VOLUME
FRACTION
0.0094
0.0000
0.9807
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 61 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: To Reboiler @COL3 (continuFluid Package: Basis-1
Property Package: PRSV
COMPOSITION
Overall Phase (continued) Vapour Fraction 0.0000
COMPONENTS
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0038
0.0000
MOLE FRACTION
0.0000
0.0032
0.0000
MASS FLOW
(kg/h)
0.0000
0.2311
0.0000
MASS FRACTION
0.0000
0.0104
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0002
0.0000
LIQUID VOLUME
FRACTION
0.0000
0.0099
0.0000
Total 1.2159 1.0000 22.1400 1.0000 0.0222 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0085
0.0000
0.9881
0.0000
0.0034
0.0000
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0149
0.0000
0.9741
0.0000
0.0110
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0187
0.0000
0.9709
0.0000
0.0104
0.0000
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0052
0.0000
1.2069
0.0000
0.0038
0.0000
MOLE FRACTION
0.0043
0.0000
0.9926
0.0000
0.0032
0.0000
MASS FLOW
(kg/h)
0.1667
0.0000
21.7422
0.0000
0.2311
0.0000
MASS FRACTION
0.0075
0.0000
0.9820
0.0000
0.0104
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0002
0.0000
0.0218
0.0000
0.0002
0.0000
LIQUID VOLUME
FRACTION
0.0094
0.0000
0.9807
0.0000
0.0099
0.0000
Total 1.2159 1.0000 22.1400 1.0000 0.0222 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.989
---
0.9955
---
1.059
---
LIGHT
1.989
---
0.9955
---
1.059
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Reboiler: Reboiler @COL3
PRODUCT FROM
Tray Section: Main TS @COL3
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Material Stream: 15 @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Overall
0.0000
118.8
1.900
Vapour Phase
0.0000
118.8
1.900
Liquid Phase
1.0000
118.8
1.900
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 62 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 15 @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.3762
0.1641
6.856e-003
-2.792e+005
75.62
-1.050e+005
6.744e-003 *
Vapour Phase
0.0000
0.0000
0.0000
-2.392e+005
177.5
0.0000
0.0000
Liquid Phase
0.3762
0.1641
6.856e-003
-2.792e+005
75.62
-1.050e+005
6.744e-003
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
18.18
51.20
930.7
7.348e-003
-1.536e+004
4.160
75.59
4.158
4009
220.6
---
0.0000
0.0000
0.0000
---
54.87
75.59
8.895
997.4
2.041e-006
---
9.102
---
0.0000
1.124
1.194
3.994e+004
0.1561
1014
6.744e-003
1.000
1.953e-002
2197
0.0000
54.78
0.6847
0.1452
67.28
3.701
63.29
3.481
---
---
---
0.1278
6.617e-002
6.744e-003
Vapour Phase
18.22
5.996e-002
1.092
0.0000
-1.313e+004
9.743
34.95
1.918
5761
316.1
---
0.0000
---
0.0000
---
54.68
34.95
0.0000
996.3
---
0.9854
9.420
---
---
1.312
1.333
---
8.881
1013
0.0000
0.0000
16.68
---
0.0000
---
2.576e-002
9.702e-003
26.63
1.461
26.22
1.439
---
---
---
0.1557
6.616e-002
0.0000
Liquid Phase
18.18
51.20
930.7
7.348e-003
-1.536e+004
4.160
75.59
4.158
4009
220.6
1.000
1.000
---
0.0000
---
54.87
75.59
8.895
997.4
2.041e-006
1.154e-003
9.102
---
---
1.124
1.194
---
0.1561
1014
6.744e-003
1.000
1.953e-002
---
1.0000
54.78
0.6847
0.1452
67.28
3.701
63.29
3.481
---
---
---
0.1278
6.617e-002
6.744e-003
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 63 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 15 @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Viscosity Index
Overall
---
Vapour Phase
---
Liquid Phase
---
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0010
0.0000
0.3741
0.0000
0.0011
0.0000
MOLE FRACTION
0.0025
0.0000
0.9944
0.0000
0.0030
0.0000
MASS FLOW
(kg/h)
0.0307
0.0000
6.7391
0.0000
0.0685
0.0000
MASS FRACTION
0.0045
0.0000
0.9855
0.0000
0.0100
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.0056
0.0000
0.9849
0.0000
0.0095
0.0000
Total 0.3762 1.0000 6.8383 1.0000 0.0069 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.0051
0.0000
0.9917
0.0000
0.0032
0.0000
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.0089
0.0000
0.9805
0.0000
0.0106
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.0111
0.0000
0.9788
0.0000
0.0101
0.0000
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0010
0.0000
0.3741
0.0000
0.0011
0.0000
MOLE FRACTION
0.0025
0.0000
0.9944
0.0000
0.0030
0.0000
MASS FLOW
(kg/h)
0.0307
0.0000
6.7391
0.0000
0.0685
0.0000
MASS FRACTION
0.0045
0.0000
0.9855
0.0000
0.0100
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.0056
0.0000
0.9849
0.0000
0.0095
0.0000
Total 0.3762 1.0000 6.8383 1.0000 0.0069 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.987
---
0.9973
---
1.062
---
LIGHT
1.987
---
0.9973
---
1.062
---
HEAVY
---
---
---
---
---
---
UNIT OPERATIONS
FEED TO
Material Stream: 15
PRODUCT FROM
Reboiler: Reboiler @COL3
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 64 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 14 @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.1555
93.61
1.090
0.5235
0.2769
1.276e-002
-2.637e+005
79.40
-1.380e+005
1.259e-002 *
Vapour Phase
0.1555
93.61
1.090
8.141e-002
4.827e-002
2.328e-003
-2.205e+005
169.1
-1.795e+004
2.308e-003
Aqueous Phase
0.8445
93.61
1.090
0.4421
0.2287
1.043e-002
-2.717e+005
62.88
-1.201e+005
1.029e-002
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
Overall
22.04
0.2351
5.182
2.227
-1.196e+004
3.602
96.12
4.361
1.807e+005
8198
0.1825
0.1743
0.0000
0.0000
2.216
41.04
96.12
12.38
904.5
3.087e-006
---
10.59
---
0.0000
1.095
1.014
4.207e+004
---
916.3
1.259e-002
0.8445
4.253
1909
0.1555
49.70
---
---
87.81
3.984
94.75
4.299
---
---
---
Vapour Phase
24.71
3.674e-002
0.9078
2.216
-8923
6.844
41.88
1.695
3.023e+005
1.223e+004
0.1825
0.1743
---
0.0000
2.216
34.97
41.88
1.925
863.9
---
0.9857
10.61
---
---
1.248
1.265
---
9.112
871.3
2.308e-003
0.0000
27.22
---
0.1555
---
2.068e-002
8.272e-003
33.56
1.358
33.10
1.340
---
---
---
Aqueous Phase
21.55
39.79
857.5
1.111e-002
-1.261e+004
2.918
106.1
4.924
1.583e+005
7346
0.8175
0.8257
---
0.0000
---
42.39
106.1
10.45
913.6
3.087e-006
9.103e-004
10.59
---
---
1.085
1.085
---
0.2673
926.2
1.029e-002
1.000
2.513e-002
---
0.8445
49.70
0.4988
0.2292
97.80
4.538
97.80
4.538
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 65 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 14 @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(atm)
(atm)
(m3/h)
Overall
0.2236
8.343e-002
1.260e-002
---
Vapour Phase
0.2243
0.1166
2.308e-003
23.04
Aqueous Phase
0.2233
7.877e-002
1.029e-002
-28.73
COMPOSITION
Overall Phase Vapour Fraction 0.1555
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1468
0.0000
0.3755
0.0000
0.0012
0.0000
MOLE FRACTION
0.2805
0.0000
0.7173
0.0000
0.0022
0.0000
MASS FLOW
(kg/h)
4.7045
0.0000
6.7654
0.0000
0.0693
0.0000
MASS FRACTION
0.4077
0.0000
0.5863
0.0000
0.0060
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0068
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4634
0.0000
0.5314
0.0000
0.0052
0.0000
Total 0.5235 1.0000 11.5392 1.0000 0.0128 1.0000
Vapour Phase Phase Fraction 0.1555
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0384
0.0000
0.0429
0.0000
0.0002
0.0000
MOLE FRACTION
0.4714
0.0000
0.5267
0.0000
0.0019
0.0000
MASS FLOW
(kg/h)
1.2297
0.0000
0.7725
0.0000
0.0091
0.0000
MASS FRACTION
0.6114
0.0000
0.3841
0.0000
0.0045
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0015
0.0000
0.0008
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.6638
0.0000
0.3325
0.0000
0.0037
0.0000
Total 0.0814 1.0000 2.0113 1.0000 0.0023 1.0000
Aqueous Phase Phase Fraction 0.8445
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1084
0.0000
0.3327
0.0000
0.0010
0.0000
MOLE FRACTION
0.2453
0.0000
0.7524
0.0000
0.0023
0.0000
MASS FLOW
(kg/h)
3.4749
0.0000
5.9929
0.0000
0.0601
0.0000
MASS FRACTION
0.3647
0.0000
0.6290
0.0000
0.0063
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0044
0.0000
0.0060
0.0000
0.0001
0.0000
LIQUID VOLUME
FRACTION
0.4187
0.0000
0.5758
0.0000
0.0055
0.0000
Total 0.4421 1.0000 9.5279 1.0000 0.0104 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.922
---
0.7000
264.6
0.8261
502.2
LIGHT
---
---
---
---
---
---
HEAVY
1.922
---
0.7000
264.6
0.8261
502.2
UNIT OPERATIONS
FEED TO
Tray Section: Main TS @COL3
PRODUCT FROM
Material Stream: 14
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 66 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 14 @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROCESS UTILITY
Material Stream: 16 @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Vapour / Phase Fraction
Temperature: (C)
Pressure: (atm)
Molar Flow (kgmole/h)
Mass Flow (tonne/d)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kJ/h)
Liq Vol Flow @Std Cond (m3/h)
Overall
0.0000
70.18
1.080
0.1473
0.1128
5.901e-003
-2.405e+005
24.22
-3.543e+004
5.896e-003 *
Vapour Phase
0.0000
70.18
1.080
0.0000
0.0000
0.0000
-1.995e+005
141.8
0.0000
0.0000
Liquid Phase
1.0000
70.18
1.080
0.1473
0.1128
5.901e-003
-2.405e+005
24.22
-3.543e+004
5.896e-003
PROPERTIES
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
Overall
31.91
23.12
737.8
6.372e-003
-7537
0.7592
166.4
5.215
6.318e+005
1.980e+004
---
0.0000
0.0000
0.0000
---
24.97
166.4
3.484
796.7
1.770e-006
---
10.62
---
0.0000
1.053
1.053
4.066e+004
0.4182
797.3
5.896e-003
1.000
4.325e-002
1274
0.0000
22.91
0.1634
0.3085
158.1
Vapour Phase
32.02
3.916e-002
1.254
0.0000
-6231
4.430
48.42
1.512
6.369e+005
1.989e+004
---
0.0000
---
0.0000
---
24.86
48.42
0.0000
795.9
---
0.9791
10.63
---
---
1.207
1.231
---
5.379
796.6
0.0000
0.0000
25.54
---
0.0000
---
1.638e-002
6.743e-003
40.10
Liquid Phase
31.91
23.12
737.8
6.372e-003
-7537
0.7592
166.4
5.215
6.318e+005
1.980e+004
1.000
1.000
---
0.0000
---
24.97
166.4
3.484
796.7
1.770e-006
1.658e-003
10.62
---
---
1.053
1.053
---
0.4182
797.3
5.896e-003
1.000
4.325e-002
---
1.0000
22.91
0.1634
0.3085
158.1
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 67 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 16 @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
PROPERTIES
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
Overall
4.954
158.1
4.954
---
---
---
0.2250
0.2231
5.896e-003
-12.61
Vapour Phase
1.253
39.34
1.229
---
---
---
0.2250
0.2246
0.0000
---
Liquid Phase
4.954
158.1
4.954
---
---
---
0.2250
0.2231
5.896e-003
-12.61
COMPOSITION
Overall Phase Vapour Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1459
0.0000
0.0015
0.0000
0.0000
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
4.6739
0.0000
0.0263
0.0000
0.0007
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.1473 1.0000 4.7009 1.0000 0.0059 1.0000
Vapour Phase Phase Fraction 0.0000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MOLE FRACTION
0.9980
0.0000
0.0019
0.0000
0.0000
0.0000
MASS FLOW
(kg/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
MASS FRACTION
0.9989
0.0000
0.0011
0.0000
0.0000
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9991
0.0000
0.0009
0.0000
0.0000
0.0000
Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000
Liquid Phase Phase Fraction 1.000
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MOLAR FLOW
(kgmole/h)
0.1459
0.0000
0.0015
0.0000
0.0000
0.0000
MOLE FRACTION
0.9900
0.0000
0.0099
0.0000
0.0001
0.0000
MASS FLOW
(kg/h)
4.6739
0.0000
0.0263
0.0000
0.0007
0.0000
MASS FRACTION
0.9942
0.0000
0.0056
0.0000
0.0002
0.0000
LIQUID VOLUME
FLOW (m3/h)
0.0059
0.0000
0.0000
0.0000
0.0000
0.0000
LIQUID VOLUME
FRACTION
0.9954
0.0000
0.0045
0.0000
0.0001
0.0000
Total 0.1473 1.0000 4.7009 1.0000 0.0059 1.0000
K VALUE
COMPONENTS
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
MIXED
1.008
28.24
0.1961
6.433
0.1855
2.623
LIGHT
1.008
28.24
0.1961
6.433
0.1855
2.623
HEAVY
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 68 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Material Stream: 16 @COL3 (continued)Fluid Package: Basis-1
Property Package: PRSV
UNIT OPERATIONS
FEED TO
Material Stream: 16
PRODUCT FROM
Total Condenser: Condenser @COL3
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T103COND @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Condenser @COL3
Duty SP: 3.594e+004 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Energy Stream: T103COND
PRODUCT FROM
Total Condenser: Condenser @COL3
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Energy Stream: T103REB @COL3Fluid Package: Basis-1
Property Package: PRSV
CONDITIONS
Duty Type: Direct Q Duty Calculation Operation: Reboiler @COL3
Duty SP: 3.355e+004 kJ/h Minimum Available Duty: --- Maximum Available Duty: ---
COMPOSITION
( Not a material stream - No compositions exist )
UNIT OPERATIONS
FEED TO
Reboiler: Reboiler @COL3
PRODUCT FROM
Energy Stream: T103REB
LOGICAL CONNECTION
UTILITIES
( No utilities reference this stream )
PROCESS UTILITY
Equilibrium Reactor: ERV-100
CONNECTIONS
Inlet Stream Connections
Stream Name From Unit Operation5 E-100Heater
Outlet Stream ConnectionsAspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 69 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Equilibrium Reactor: ERV-100 (continued)
CONNECTIONS
Outlet Stream ConnectionsStream Name To Unit Operation
6A Mixer: MIX-100
6B Mixer: MIX-100
Energy Stream Connections
Stream Name From Unit Operation
PARAMETERS
Physical Parameters Optional Heat Transfer
Delta P Vessel Volume Duty Energy Stream0.0000 kPa --- 0.0000 kJ/h
User Variables
REACTION DETAILS
Component
Methanol
diM-Ether
H2O
Molecular Weight
32.04
46.07
18.02
Stoichiometric Coefficient
-2 *
1 *
1 *
REACTION RESULTS FOR : Global Rxn Set
Extents
Rxn-1
Act. % Conv.
82.68
Base Comp.
Methanol
Eqm Constant
5.908
Rxn Extent
1.014e-004
Balance
Methanol
diM-Ether
H2O
AcetAldehyde
AceticAcid
Acetone
Total Inflow
2.453e-004
2.088e-007
3.539e-006
2.088e-007
3.204e-007
3.171e-007
Total Rxn
-2.028e-004
1.014e-004
1.014e-004
2.647e-023
0.0000
5.294e-023
Total Outflow
4.249e-005
1.016e-004
1.050e-004
2.088e-007
3.204e-007
3.171e-007
RATING
Sizing
Cylinder Vertical Reactor has a Boot: No
Volume --- Diameter --- Height ---
Nozzles
Base Elevation Relative to Ground Level 0.0000 m * Diameter --- Height ---
Diameter (m)
Elevation (Base) (m)
Elevation (Ground) (m)
Elevation (% of Height) (%)
5
5.000e-002
0.0000
0.0000
---
6A
5.000e-002
0.0000
0.0000
---
6B
5.000e-002
0.0000
0.0000
---
PROPERTIES
Name
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
(kgmole/m3)
(kg/m3)
(m3/h)
5
31.93
0.3778
12.06
2.382
6B
31.93
0.2937
9.380
0.0000
6A
31.93
0.2937
9.380
3.063
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 70 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
USA
Case Name: DMEPLANT.HSC
Unit Set: NewUser1
Date/Time: Wed May 23 23:14:35 2012
Equilibrium Reactor: ERV-100 (continued)
PROPERTIES
Name
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Vol Basis (Std)
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
Avg. Liq. Density
Specific Heat
Std. Gas Flow
Std. Ideal Liq. Mass Density
Act. Liq. Flow
Z Factor
Watson K
User Property
Partial Pressure of H2S
Cp/(Cp - R)
Cp/Cv
Heat of Vap.
Kinematic Viscosity
Liq. Mass Density (Std. Cond)
Liq. Vol. Flow (Std. Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap.
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
Cv (Semi-Ideal)
Mass Cv (Semi-Ideal)
Cv
Mass Cv
Cv (Ent. Method)
Mass Cv (Ent. Method)
Cp/Cv (Ent. Method)
Reid VP at 37.8 C
True VP at 37.8 C
Liq. Vol. Flow - Sum(Std. Cond)
Viscosity Index
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kg)
(atm)
(Cost/s)
(ACT_m3/h)
(kgmole/m3)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(atm)
(kJ/kgmole)
(cSt)
(kg/m3)
(m3/h)
(m3/kgmole)
(kJ/kg)
(dyne/cm)
(W/m-K)
(cP)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(atm)
(atm)
(m3/h)
5
-5995
4.466
65.36
2.047
6.315e+005
1.978e+004
1.000
1.000
0.0000
0.0000
2.382
24.97
65.36
21.27
797.3
---
0.9243
10.62
---
0.0000
1.146
1.223
2.873e+004
0.9821
798.0
3.601e-002
0.0000
2.647
899.6
1.0000
---
3.321e-002
1.185e-002
57.04
1.786
53.46
1.674
---
---
---
0.2419
0.2417
3.601e-002
3.001
6B
-5995
5.972
73.93
2.315
6.527e+005
2.044e+004
---
0.0000
0.0000
0.0000
---
---
73.93
0.0000
749.8
0.0000
---
11.27
---
0.0000
1.127
1.150
3.625e+004
0.3148
746.9
0.0000
1.000
3.404
1135
0.0000
0.4232
9.584e-002
2.953e-003
65.61
2.055
64.29
2.013
---
---
---
6.082
7.436
0.0000
11.30
6A
-5995
5.972
73.93
2.315
6.527e+005
2.044e+004
1.000
1.000
0.0000
0.0000
3.063
23.48
73.93
21.27
749.8
---
---
11.27
---
0.0000
1.127
1.150
3.625e+004
1.980
746.9
3.847e-002
0.0000
3.404
1135
1.0000
---
5.088e-002
1.857e-002
65.61
2.055
64.29
2.013
---
---
---
6.082
7.436
3.847e-002
11.30
Aspen Technology Inc. Aspen HYSYS Version 7.2 (24.0.0.7263) Page 71 of 71
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS