hysys print
DESCRIPTION
Planta de obtención de dimetil éterTRANSCRIPT
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
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* 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
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* 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
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* 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
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* 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
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* 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
---
---
---
---
---
---
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LEGENDS
Burlington, MA
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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
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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
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* 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
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* 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
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* 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
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LEGENDS
Burlington, MA
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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
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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
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* 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
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* 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
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* 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
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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
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* 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
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* 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
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* 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
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* 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 )
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* 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 )
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Burlington, MA
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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 )
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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
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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
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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
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* 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
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* 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
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LEGENDS
Burlington, MA
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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
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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
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* 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
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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
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* 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
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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
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* 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
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* 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 )
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* 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
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LEGENDS
Burlington, MA
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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
---
---
---
---
---
---
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LEGENDS
Burlington, MA
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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
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LEGENDS
Burlington, MA
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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
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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
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* 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
---
---
---
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* 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
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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
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* 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
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* 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
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* 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
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* 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
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* 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
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* 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
---
---
---
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* 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 )
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* 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
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LEGENDS
Burlington, MA
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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
---
---
---
---
---
---
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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
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LEGENDS
Burlington, MA
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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
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* 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
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* 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
---
---
---
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LEGENDS
Burlington, MA
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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
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* 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
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* Specified by user.Licensed to: LEGENDS
LEGENDS
Burlington, MA
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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
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* 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
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* 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
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LEGENDS
Burlington, MA
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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
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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
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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
---
---
---
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* 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 )
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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
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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
---
---
---
---
---
---
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* 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
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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
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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
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