Embed Size (px)
Citation preview
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main
CONNECTIONS
Inlet Stream
STREAM NAME Stage FROM UNIT OPERATION
QReb249
Reboiler62__Main Tower P-100Pump
Outlet Stream
STREAM NAME Stage TO UNIT OPERATION
QCond277RC Bottoms2ProductoFUSEL
CondenserCondenserReboiler3__Main Tower80__Main Tower
E-102Cooler
MONITOR
Specifications Summary
Specified Value Current Value Wt. Error
Reflux Ratio 1.069e+010 * 2.794e+007 -0.9974
Reflux Rate 4.000e+004 kg/h * 4.000e+004 kg/h 4.981e-006
Btms Prod Rate 7000 kg/h * 1.632e+004 kg/h 1.331
Producto Rate 2.000e+004 kg/h * 2.000e+004 kg/h 5.574e-006
Fusel Rtae 9.200e-006 kg/h * 1.334e-005 kg/h -5.035e-007
77 Rate 1.060e-005 kg/h * 1.334e-005 kg/h 2.386e-008
Liquid Flow --- 1.776e+004 kg/h ---
Vapour Flow --- 3.796e+004 kg/h ---
Wt. Tol. Abs. Tol. Active Estimate Used
Reflux Ratio 1.000e-002 1.000e-002 Off On Off
Reflux Rate 1.000e-002 1.000 kg/h On On On
Btms Prod Rate 1.000e-002 1.000 kg/h Off On Off
Producto Rate 1.000e-002 1.000 kg/h On On On
Fusel Rtae 1.000e-002 1.000 kg/h On On On
77 Rate 1.000e-002 1.000 kg/h On On On
Liquid Flow 1.000e-002 1.000 kg/h Off On Off
Vapour Flow 1.000e-002 1.000 kg/h Off On Off
SPECS
Column Specification Parameters
Reflux Ratio
Fix/Rang: Fixed Prim/Alter: Primary Lower Bnd: --- Upper Bnd: ---
Stage: Condenser Flow Basis: Molar Liquid Spec: ---
Reflux Rate
Fix/Rang: Fixed Prim/Alter: Primary Lower Bnd: --- Upper Bnd: ---
Stage: Condenser Flow Basis: Mass Liquid Spec: ---
Btms Prod Rate
Fix/Rang: Fixed Prim/Alter: Primary Lower Bnd: --- Upper Bnd: ---
Stream: RC Bottoms2 Flow Basis: Mass
Producto Rate
Fix/Rang: Fixed Prim/Alter: Primary Lower Bnd: --- Upper Bnd: ---
Stream: Producto Flow Basis: Mass
Fusel Rtae
Fix/Rang: Fixed Prim/Alter: Primary Lower Bnd: --- Upper Bnd: ---
Stream: FUSEL Flow Basis: Mass
77 Rate
Fix/Rang: Fixed Prim/Alter: Primary Lower Bnd: --- Upper Bnd: ---
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 1 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Column Specification Parameters
77 Rate
Stream: 77 Flow Basis: Mass
Liquid Flow
Fix/Rang: Fixed Prim/Alter: Primary Lower Bnd: --- Upper Bnd: ---
Stage: 56__Main Tower Flow Basis: Mass Liquid Spec: Light
Vapour Flow
Fix/Rang: Fixed Prim/Alter: Primary Lower Bnd: --- Upper Bnd: ---
Stage: 56__Main Tower Flow Basis: Mass
SUBCOOLING
Degrees of Subcooling
Subcool to
Condenser
---
---
User Variables
PROFILES
General Parameters
Sub-Flow Sheet: 202-EA/EB (COL2) Number of Stages: 92 *
Profile Estimates
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
Temperature
(C)
71.11
71.11
71.24
71.38
71.52
71.66
71.80
71.94
72.08
72.22
72.36
72.50
72.64
72.78
72.92
73.05
73.19
73.33
73.47
73.61
73.75
73.89
74.04
74.18
74.32
74.46
74.61
74.75
74.90
75.05
75.20
75.35
75.50
75.65
Net Liquid
(Nm3/h(gas))
2.798e+004
2.798e+004
2.798e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.399e+004
1.399e+004
1.399e+004
1.399e+004
1.398e+004
1.398e+004
1.398e+004
1.397e+004
1.397e+004
1.396e+004
1.396e+004
Net Vapour
(Nm3/h(gas))
9.920e-004
2.798e+004
2.798e+004
2.798e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.798e+004
2.798e+004
2.798e+004
2.798e+004
2.797e+004
2.797e+004
2.797e+004
2.796e+004
2.796e+004
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 2 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Profile Estimates
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
Temperature
(C)
75.81
75.97
76.13
76.29
76.46
76.63
76.80
76.98
77.17
77.35
77.55
77.75
77.96
78.18
78.40
78.64
78.89
79.15
79.43
79.73
80.05
80.39
80.76
81.17
81.61
82.09
82.63
83.22
83.89
84.00
84.11
84.23
84.34
84.45
84.56
84.67
84.77
84.88
84.99
85.10
85.21
85.31
85.42
85.53
85.63
85.74
85.85
85.95
86.06
86.16
86.27
86.37
86.48
86.58
86.69
86.83
87.06
Net Liquid
(Nm3/h(gas))
1.395e+004
1.395e+004
1.394e+004
1.393e+004
1.393e+004
1.392e+004
1.391e+004
1.390e+004
1.389e+004
1.387e+004
1.386e+004
1.384e+004
1.383e+004
1.381e+004
1.379e+004
1.377e+004
1.374e+004
1.372e+004
1.369e+004
1.365e+004
1.362e+004
1.358e+004
1.353e+004
1.348e+004
1.342e+004
1.336e+004
1.329e+004
1.322e+004
4.304e+004
4.305e+004
4.306e+004
4.307e+004
4.309e+004
4.310e+004
4.311e+004
4.312e+004
4.313e+004
4.314e+004
4.315e+004
4.316e+004
4.317e+004
4.318e+004
4.319e+004
4.320e+004
4.321e+004
4.322e+004
4.323e+004
4.324e+004
4.325e+004
4.326e+004
4.327e+004
4.328e+004
4.329e+004
4.330e+004
4.330e+004
4.330e+004
4.327e+004
Net Vapour
(Nm3/h(gas))
2.795e+004
2.795e+004
2.794e+004
2.793e+004
2.793e+004
2.792e+004
2.791e+004
2.790e+004
2.789e+004
2.788e+004
2.786e+004
2.785e+004
2.784e+004
2.782e+004
2.780e+004
2.778e+004
2.776e+004
2.773e+004
2.771e+004
2.768e+004
2.764e+004
2.761e+004
2.757e+004
2.752e+004
2.747e+004
2.742e+004
2.735e+004
2.728e+004
2.721e+004
2.713e+004
2.714e+004
2.715e+004
2.716e+004
2.717e+004
2.718e+004
2.719e+004
2.720e+004
2.721e+004
2.722e+004
2.723e+004
2.724e+004
2.725e+004
2.726e+004
2.727e+004
2.728e+004
2.729e+004
2.730e+004
2.731e+004
2.732e+004
2.733e+004
2.734e+004
2.735e+004
2.736e+004
2.737e+004
2.738e+004
2.739e+004
2.738e+004
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 3 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Profile Estimates
91__Main Tower
92__Main Tower
Reboiler
Temperature
(C)
87.62
89.17
93.58
Net Liquid
(Nm3/h(gas))
4.324e+004
4.292e+004
1.591e+004
Net Vapour
(Nm3/h(gas))
2.736e+004
2.733e+004
2.701e+004
EFFICIENCIES
Stage EfficienciesStages
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Hydrogen
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
CO
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
CO2
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Nitrogen
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 4 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Stage EfficienciesStages
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Hydrogen
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
CO
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
CO2
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Nitrogen
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Stages
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Oxygen
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Methane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Ethane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Propane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 5 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Stage EfficienciesStages
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Oxygen
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Methane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Ethane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Propane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 6 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Stage EfficienciesStages
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Oxygen
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Methane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Ethane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Propane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Stages
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
i-Butane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
n-Butane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
i-Pentane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
n-Pentane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 7 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Stage EfficienciesStages
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
i-Butane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
n-Butane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
i-Pentane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
n-Pentane
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 8 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Stage EfficienciesStages
92__Main Tower
Reboiler
Overall
1.000
1.000
i-Butane
1.000
1.000
n-Butane
1.000
1.000
i-Pentane
1.000
1.000
n-Pentane
1.000
1.000
Stages
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Methanol
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
H2O
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 9 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Stage EfficienciesStages
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Overall
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
Methanol
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
H2O
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
SOLVER
Column Solving Algorithm: Modified HYSIM Inside-Out
Solving OptionsMaximum Iterations: 10000
Equilibrium Error Tolerance: 1.000e-05
Heat/Spec Error Tolerance: 5.000e-004
Save Solutions as Initial Estimate: On
Super Critical Handling Model: Simple K
Trace Level: Low
Init from Ideal K's: Off
Initial Estimate Generator ParametersIterative IEG (Good for Chemicals): Off
Acceleration ParametersAccelerate K Value & H Model Parameters: Off
Damping ParametersAzeotrope Check: Off
Adaptive Initial Damping Factor: 0 *
Adaptive Damping Period: 10
Update Initial Damping Factor: Off
SIDE STRIPPERS
SIDE RECTIFIERS
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 10 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
PUMP AROUNDS
VAP BYPASSES
RATING
Tray Sections
Tray Section
Tray Diameter (m)
Weir Height (m)
Weir Length (m)
Tray Space (m)
Tray Volume (m3)
Disable Heat Loss Calculations
Heat Model
Rating Calculations
Tray Hold Up (m3)
Main Tower
1.500
5.000e-002 *
1.200 *
0.5500 *
0.9719
No
None
No
8.836e-002
Vessels
Vessel
Diameter (m)
Length (m)
Volume (m3)
Orientation
Vessel has a Boot
Boot Diameter (m)
Boot Length (m)
Hold Up (m3)
Reboiler
1.193
1.789
2.000 *
Horizontal
No
---
---
1.000
Condenser
1.193
1.789
2.000 *
Horizontal
No
---
---
1.000
Other Equipment In Column Flowsheet
Pressure Profile
Pressure (kg/cm2_g) Pressure Drop (kPa)
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
0.3000 kg/cm2_g *
0.3000 kg/cm2_g
0.3069 kg/cm2_g
0.3138 kg/cm2_g
0.3208 kg/cm2_g
0.3277 kg/cm2_g
0.3346 kg/cm2_g
0.3415 kg/cm2_g
0.3485 kg/cm2_g
0.3554 kg/cm2_g
0.3623 kg/cm2_g
0.3692 kg/cm2_g
0.3762 kg/cm2_g
0.3831 kg/cm2_g
0.3900 kg/cm2_g
0.3969 kg/cm2_g
0.4038 kg/cm2_g
0.4108 kg/cm2_g
0.4177 kg/cm2_g
0.4246 kg/cm2_g
0.4315 kg/cm2_g
0.4385 kg/cm2_g
0.4454 kg/cm2_g
0.4523 kg/cm2_g
0.4592 kg/cm2_g
0.0000 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 11 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
0.4662 kg/cm2_g
0.4731 kg/cm2_g
0.4800 kg/cm2_g
0.4869 kg/cm2_g
0.4938 kg/cm2_g
0.5008 kg/cm2_g
0.5077 kg/cm2_g
0.5146 kg/cm2_g
0.5215 kg/cm2_g
0.5285 kg/cm2_g
0.5354 kg/cm2_g
0.5423 kg/cm2_g
0.5492 kg/cm2_g
0.5562 kg/cm2_g
0.5631 kg/cm2_g
0.5700 kg/cm2_g
0.5769 kg/cm2_g
0.5838 kg/cm2_g
0.5908 kg/cm2_g
0.5977 kg/cm2_g
0.6046 kg/cm2_g
0.6115 kg/cm2_g
0.6185 kg/cm2_g
0.6254 kg/cm2_g
0.6323 kg/cm2_g
0.6392 kg/cm2_g
0.6462 kg/cm2_g
0.6531 kg/cm2_g
0.6600 kg/cm2_g
0.6669 kg/cm2_g
0.6738 kg/cm2_g
0.6808 kg/cm2_g
0.6877 kg/cm2_g
0.6946 kg/cm2_g
0.7015 kg/cm2_g
0.7085 kg/cm2_g
0.7154 kg/cm2_g
0.7223 kg/cm2_g
0.7292 kg/cm2_g
0.7362 kg/cm2_g
0.7431 kg/cm2_g
0.7500 kg/cm2_g
0.7569 kg/cm2_g
0.7638 kg/cm2_g
0.7708 kg/cm2_g
0.7777 kg/cm2_g
0.7846 kg/cm2_g
0.7915 kg/cm2_g
0.7985 kg/cm2_g
0.8054 kg/cm2_g
0.8123 kg/cm2_g
0.8192 kg/cm2_g
0.8262 kg/cm2_g
0.8331 kg/cm2_g
0.8400 kg/cm2_g
0.8469 kg/cm2_g
0.8538 kg/cm2_g
0.8608 kg/cm2_g
0.8677 kg/cm2_g
0.8746 kg/cm2_g
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 12 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
0.8815 kg/cm2_g
0.8885 kg/cm2_g
0.8954 kg/cm2_g
0.9023 kg/cm2_g
0.9092 kg/cm2_g
0.9162 kg/cm2_g
0.9231 kg/cm2_g
0.9300 kg/cm2_g
0.9300 kg/cm2_g *
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
0.6789 kPa
---
0.0000 kPa
Pressure Solving Options
Pressure Tolerance 1.000e-004 Pressure Drop Tolerance 1.000e-004
Damping Factor 1.000 Max Press Iterations 100
CONDITIONS
Name
Vapour
Temperature (C)
Pressure (kg/cm2_g)
Molar Flow (Nm3/h(gas))
Mass Flow (kg/h)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kcal/h)
49 @Main
0.0000
85.0000 *
2.0000 *
29905.9913
36317.3262
43.5416
-2.489e+005
76.72
-7.9388e+07
RC Bottoms2 @Main
0.0000
93.5835
0.9300
15914.0977
16317.2133
18.4077
-2.628e+005
55.24
-4.4595e+07
77 @Main
0.0000
71.1057
0.3000
0.0000
0.0000
0.0000
-2.340e+005
82.21
-2.3288e-02
Producto @Main
0.0000
71.3832
0.3138
13991.8926
20000.1115
25.1340
-2.340e+005
82.47
-3.4907e+07
Name
Vapour
Temperature (C)
Pressure (kg/cm2_g)
Molar Flow (Nm3/h(gas))
Mass Flow (kg/h)
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Heat Flow (kcal/h)
FUSEL @Main
0.0000
85.8467
0.8469
0.0000
0.0000
0.0000
-2.482e+005
75.36
-2.8883e-02
QReb2 @Main
---
---
---
---
---
---
---
---
1.0269e+07
QCond2 @Main
---
---
---
---
---
---
---
---
1.0384e+07
PROPERTIES
Name
Molecular Weight
Molar Density
Mass Density
Act. Volume Flow
Mass Enthalpy
Mass Entropy
Heat Capacity
Mass Heat Capacity
LHV Molar Basis (Std)
HHV Molar Basis (Std)
HHV Mass Basis (Std)
CO2 Loading
CO2 Apparent Mole Conc.
CO2 Apparent Wt. Conc.
LHV Mass Basis (Std)
Phase Fraction [Vol. Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act. Vol. Basis]
Mass Exergy
Partial Pressure of CO2
Cost Based on Flow
Act. Gas Flow
(kgmole/m3)
(kg/m3)
(m3/h)
(kJ/kg)
(kJ/kg-C)
(kJ/kgmole-C)
(kJ/kg-C)
(kJ/kgmole)
(kJ/kgmole)
(kJ/kg)
(kgmole/m3)
(kgmol/kg)
(kJ/kg)
(kJ/kg)
(kg/cm2_g)
(Cost/s)
(ACT_m3/h)
49 @Main
27.22
28.23
768.5
47.26
-9146
2.818
107.0
3.933
4.178e+005
4.856e+005
1.784e+004
---
2.771e-002
3.605e-005
1.535e+004
0.0000
0.0000
0.0000
-189.2
-1.033
0.0000
---
RC Bottoms2 @Main
22.98
35.94
826.0
19.75
-1.143e+004
2.404
93.01
4.047
2.241e+005
2.795e+005
1.216e+004
---
6.628e-002
8.024e-005
9753
0.0000
0.0000
0.0000
-99.42
-1.033
0.0000
---
77 @Main
32.04
22.96
735.6
1.814e-008
-7303
2.566
121.3
3.785
6.381e+005
7.201e+005
2.247e+004
---
4.722e-042
6.419e-045
1.991e+004
0.0000
0.0000
0.0000
-160.5
-1.033
0.0000
---
Producto @Main
32.04
22.95
735.3
27.20
-7303
2.574
121.3
3.786
6.380e+005
7.200e+005
2.247e+004
---
2.573e-040
3.500e-043
1.991e+004
0.0000
0.0000
0.0000
-161.9
-1.033
0.0000
---
FUSEL @Main
27.40
27.92
765.1
1.744e-008
-9057
2.750
107.8
3.935
4.264e+005
4.947e+005
1.805e+004
---
2.024e-002
2.645e-005
1.556e+004
0.0000
0.0000
0.0000
-164.2
-1.033
0.0000
---
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 13 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
PROPERTIES
Name
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)
(kJ/kgmole-C)
(STD_m3/h)
(kg/m3)
(m3/s)
(kg/cm2_g)
(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)
(kg/cm2_g)
(kg/cm2_g)
(m3/h)
49 @Main
30.64
107.0
3.155e+004
834.1
1.313e-002
3.538e-003
10.62
---
-1.033
1.084
1.230
3.571e+004
0.3737
838.4
43.32
1.000
3.542e-002
1312
0.0000
34.38
0.2785
0.2872
98.74
3.627
87.01
3.197
---
---
---
-0.7075
-0.7717
43.32
-15.65
RC Bottoms2 @Main
38.57
93.01
1.679e+004
886.4
5.487e-003
1.757e-003
10.62
---
-1.033
1.098
1.098
3.866e+004
0.3398
897.7
18.18
1.000
2.782e-002
1682
0.0000
45.33
0.4319
0.2807
84.70
3.685
84.70
3.685
---
---
---
-0.7091
-0.7989
18.18
-18.58
77 @Main
24.83
121.3
9.846e-006
795.7
5.039e-012
1.990e-003
10.63
---
-1.033
1.074
1.393
3.480e+004
0.4148
796.4
1.675e-008
1.000
4.356e-002
1086
0.0000
22.35
0.1601
0.3051
113.0
3.525
87.08
2.718
---
---
---
-0.7069
-0.7069
1.675e-008
-12.82
Producto @Main
24.84
121.3
1.476e+004
795.7
7.556e-003
2.009e-003
10.63
---
-1.033
1.074
1.393
3.479e+004
0.4137
796.4
25.11
1.000
4.357e-002
1086
0.0000
22.32
0.1600
0.3042
113.0
3.527
87.11
2.719
---
---
---
-0.7069
-0.7070
25.11
-12.89
FUSEL @Main
30.37
107.8
1.151e-005
832.3
4.844e-012
2.212e-003
10.62
---
-1.033
1.084
1.232
3.657e+004
0.3705
836.3
1.596e-008
1.000
3.581e-002
1335
0.0000
33.71
0.2726
0.2835
99.51
3.631
87.50
3.193
---
---
---
-0.7073
-0.7693
1.596e-008
-15.90
SUMMARY
Flow Basis: Molar The composition option is selected
Feed Composition
Flow Rate (Nm3/h(gas))
Hydrogen
CO
CO2
Nitrogen
Oxygen
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
Methanol
H2O
49
2.990599e+04
---
0.0000
0.0000
0.0010
0.0001
0.0000
0.0003
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.6544
0.3443
Flow Basis: Molar The composition option is selected
Feed Flows
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 14 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
SUMMARY
Flow Rate (Nm3/h(gas))
Hydrogen (Nm3/h(gas))
CO (Nm3/h(gas))
CO2 (Nm3/h(gas))
Nitrogen (Nm3/h(gas))
Oxygen (Nm3/h(gas))
Methane (Nm3/h(gas))
Ethane (Nm3/h(gas))
Propane (Nm3/h(gas))
i-Butane (Nm3/h(gas))
n-Butane (Nm3/h(gas))
i-Pentane (Nm3/h(gas))
n-Pentane (Nm3/h(gas))
Methanol (Nm3/h(gas))
H2O (Nm3/h(gas))
49
2.990599e+04
---
0.0000
0.0000
29.3456
1.7057
0.0000
7.7890
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
1.956915e+04
1.029800e+04
ProductsFlow Basis: Molar The composition option is selected
Product Compositions
Flow Rate (Nm3/h(gas))
Hydrogen
CO
CO2
Nitrogen
Oxygen
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
Methanol
H2O
77
0.0000
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
1.0000
0.0000
Producto
1.399189e+04
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.9998
0.0002
FUSEL
0.0000
---
0.0000
0.0000
0.0007
0.0000
0.0000
0.0002
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.6679
0.3311
Flow Rate (Nm3/h(gas))
Hydrogen
CO
CO2
Nitrogen
Oxygen
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
Methanol
H2O
RC Bottoms2
1.591410e+04
---
0.0000
0.0000
0.0018
0.0001
0.0000
0.0005
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.3507
0.6469
Flow Basis: Molar The composition option is selected
Product Flows
Flow Rate (Nm3/h(gas))
77
0.0000 *
Producto
1.399189e+04 *
FUSEL
0.0000 *
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 15 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
SUMMARY
Hydrogen (Nm3/h(gas))
CO (Nm3/h(gas))
CO2 (Nm3/h(gas))
Nitrogen (Nm3/h(gas))
Oxygen (Nm3/h(gas))
Methane (Nm3/h(gas))
Ethane (Nm3/h(gas))
Propane (Nm3/h(gas))
i-Butane (Nm3/h(gas))
n-Butane (Nm3/h(gas))
i-Pentane (Nm3/h(gas))
n-Pentane (Nm3/h(gas))
Methanol (Nm3/h(gas))
H2O (Nm3/h(gas))
77
---
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Producto
---
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
1.398873e+04 *
3.1607 *
FUSEL
---
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Flow Rate (Nm3/h(gas))
Hydrogen (Nm3/h(gas))
CO (Nm3/h(gas))
CO2 (Nm3/h(gas))
Nitrogen (Nm3/h(gas))
Oxygen (Nm3/h(gas))
Methane (Nm3/h(gas))
Ethane (Nm3/h(gas))
Propane (Nm3/h(gas))
i-Butane (Nm3/h(gas))
n-Butane (Nm3/h(gas))
i-Pentane (Nm3/h(gas))
n-Pentane (Nm3/h(gas))
Methanol (Nm3/h(gas))
H2O (Nm3/h(gas))
RC Bottoms2
1.591410e+04 *
---
0.0000 *
0.0000 *
29.3456 *
1.7057 *
0.0000 *
7.7890 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
5.580420e+03 *
1.029484e+04 *
Flow Basis: Molar The composition option is selected
Product Recoveries
Flow Rate (Nm3/h(gas))
Hydrogen (%)
CO (%)
CO2 (%)
Nitrogen (%)
Oxygen (%)
Methane (%)
Ethane (%)
Propane (%)
i-Butane (%)
n-Butane (%)
i-Pentane (%)
n-Pentane (%)
Methanol (%)
H2O (%)
77
0.0000
---
0.0001
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Producto
1.399189e+04
---
0.0696
46.6411
0.0000
0.0000
0.0000
0.0000
0.0000
46.7858
97.5565
0.0000
0.0000
0.0000
71.4836
0.0307
FUSEL
0.0000
---
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Flow Rate (Nm3/h(gas))
Hydrogen (%)
CO (%)
CO2 (%)
RC Bottoms2
1.591410e+04
---
48.3763
53.2142
100.0000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 16 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
SUMMARY
Nitrogen (%)
Oxygen (%)
Methane (%)
Ethane (%)
Propane (%)
i-Butane (%)
n-Butane (%)
i-Pentane (%)
n-Pentane (%)
Methanol (%)
H2O (%)
RC Bottoms2
100.0000
0.0000
100.0000
0.0000
53.2142
2.4081
0.0000
0.0000
0.0000
28.5164
99.9693
COLUMN PROFILES
Reflux Ratio: 2.794e+007 Reboil Ratio: 1.697 The Flows Option is Selected Flow Basis: Molar
Column Profiles Flows
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
Temp
(C)
71.1
71.1
71.2
71.4
71.5
71.7
71.8
71.9
72.1
72.2
72.4
72.5
72.6
72.8
72.9
73.1
73.2
73.3
73.5
73.6
73.8
73.9
74.0
74.2
74.3
74.5
74.6
74.8
74.9
75.0
75.2
75.3
75.5
75.7
75.8
76.0
76.1
76.3
76.5
76.6
Pres
(kg/cm2_g)
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
1
1
1
1
1
1
1
1
1
1
Net Liq
(Nm3/h(gas))
2.798e+004
2.798e+004
2.798e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.399e+004
1.399e+004
1.399e+004
1.399e+004
1.398e+004
1.398e+004
1.398e+004
1.397e+004
1.397e+004
1.396e+004
1.396e+004
1.395e+004
1.395e+004
1.394e+004
1.393e+004
1.393e+004
1.392e+004
Net Vap
(Nm3/h(gas))
---
2.798e+004
2.798e+004
2.798e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.798e+004
2.798e+004
2.798e+004
2.798e+004
2.797e+004
2.797e+004
2.797e+004
2.796e+004
2.796e+004
2.795e+004
2.795e+004
2.794e+004
2.793e+004
2.793e+004
2.792e+004
Net Feed
(Nm3/h(gas))
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Net Draws
(Nm3/h(gas))
9.334e-006
---
---
1.399e+004
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Duty
(kcal/h)
1.04e+007 *
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 17 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
COLUMN PROFILES
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Temp
(C)
76.8
77.0
77.2
77.4
77.5
77.7
78.0
78.2
78.4
78.6
78.9
79.2
79.4
79.7
80.0
80.4
80.8
81.2
81.6
82.1
82.6
83.2
83.9
84.0
84.1
84.2
84.3
84.4
84.6
84.7
84.8
84.9
85.0
85.1
85.2
85.3
85.4
85.5
85.6
85.7
85.8
86.0
86.1
86.2
86.3
86.4
86.5
86.6
86.7
86.8
87.1
87.6
89.2
93.6
Pres
(kg/cm2_g)
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
1
Net Liq
(Nm3/h(gas))
1.391e+004
1.390e+004
1.389e+004
1.387e+004
1.386e+004
1.384e+004
1.383e+004
1.381e+004
1.379e+004
1.377e+004
1.374e+004
1.372e+004
1.369e+004
1.365e+004
1.362e+004
1.358e+004
1.353e+004
1.348e+004
1.342e+004
1.336e+004
1.329e+004
1.322e+004
4.304e+004
4.305e+004
4.306e+004
4.307e+004
4.309e+004
4.310e+004
4.311e+004
4.312e+004
4.313e+004
4.314e+004
4.315e+004
4.316e+004
4.317e+004
4.318e+004
4.319e+004
4.320e+004
4.321e+004
4.322e+004
4.323e+004
4.324e+004
4.325e+004
4.326e+004
4.327e+004
4.328e+004
4.329e+004
4.330e+004
4.330e+004
4.330e+004
4.327e+004
4.324e+004
4.292e+004
---
Net Vap
(Nm3/h(gas))
2.791e+004
2.790e+004
2.789e+004
2.788e+004
2.786e+004
2.785e+004
2.784e+004
2.782e+004
2.780e+004
2.778e+004
2.776e+004
2.773e+004
2.771e+004
2.768e+004
2.764e+004
2.761e+004
2.757e+004
2.752e+004
2.747e+004
2.742e+004
2.735e+004
2.728e+004
2.721e+004
2.713e+004
2.714e+004
2.715e+004
2.716e+004
2.717e+004
2.718e+004
2.719e+004
2.720e+004
2.721e+004
2.722e+004
2.723e+004
2.724e+004
2.725e+004
2.726e+004
2.727e+004
2.728e+004
2.729e+004
2.730e+004
2.731e+004
2.732e+004
2.733e+004
2.734e+004
2.735e+004
2.736e+004
2.737e+004
2.738e+004
2.739e+004
2.738e+004
2.736e+004
2.733e+004
2.701e+004
Net Feed
(Nm3/h(gas))
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
2.991e+004
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Net Draws
(Nm3/h(gas))
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
1.091e-005
---
---
---
---
---
---
---
---
---
---
---
---
1.591e+004
Duty
(kcal/h)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
1.03e+007 *
Column Profiles Energy
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 18 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
COLUMN PROFILES
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
Temperature
(C)
71.11
71.11
71.24
71.38
71.52
71.66
71.80
71.94
72.08
72.22
72.36
72.50
72.64
72.78
72.92
73.05
73.19
73.33
73.47
73.61
73.75
73.89
74.04
74.18
74.32
74.46
74.61
74.75
74.90
75.05
75.20
75.35
75.50
75.65
75.81
75.97
76.13
76.29
76.46
76.63
76.80
76.98
77.17
77.35
77.55
77.75
77.96
78.18
78.40
78.64
78.89
79.15
79.43
79.73
80.05
80.39
Liq Enthalpy
(kJ/kgmole)
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.340e+005
-2.341e+005
-2.341e+005
-2.341e+005
-2.342e+005
-2.342e+005
-2.342e+005
-2.343e+005
-2.343e+005
-2.344e+005
-2.344e+005
-2.345e+005
-2.345e+005
-2.346e+005
-2.347e+005
-2.348e+005
-2.349e+005
-2.350e+005
-2.351e+005
-2.352e+005
-2.353e+005
-2.355e+005
-2.356e+005
-2.358e+005
-2.360e+005
-2.362e+005
-2.364e+005
-2.367e+005
-2.369e+005
-2.372e+005
-2.376e+005
-2.379e+005
-2.383e+005
-2.387e+005
-2.392e+005
-2.397e+005
-2.403e+005
-2.410e+005
Vap Enthalpy
(kJ/kgmole)
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.992e+005
-1.993e+005
-1.993e+005
-1.993e+005
-1.993e+005
-1.993e+005
-1.994e+005
-1.994e+005
-1.994e+005
-1.994e+005
-1.995e+005
-1.995e+005
-1.995e+005
-1.996e+005
-1.996e+005
-1.997e+005
-1.997e+005
-1.998e+005
-1.998e+005
-1.999e+005
-2.000e+005
-2.000e+005
-2.001e+005
-2.002e+005
-2.003e+005
-2.004e+005
-2.006e+005
-2.007e+005
-2.008e+005
-2.010e+005
-2.012e+005
-2.014e+005
-2.016e+005
-2.018e+005
Heat Loss
(kcal/h)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 19 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
COLUMN PROFILES
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Temperature
(C)
80.76
81.17
81.61
82.09
82.63
83.22
83.89
84.00
84.11
84.23
84.34
84.45
84.56
84.67
84.77
84.88
84.99
85.10
85.21
85.31
85.42
85.53
85.63
85.74
85.85
85.95
86.06
86.16
86.27
86.37
86.48
86.58
86.69
86.83
87.06
87.62
89.17
93.58
Liq Enthalpy
(kJ/kgmole)
-2.417e+005
-2.425e+005
-2.435e+005
-2.445e+005
-2.457e+005
-2.469e+005
-2.484e+005
-2.484e+005
-2.484e+005
-2.484e+005
-2.484e+005
-2.483e+005
-2.483e+005
-2.483e+005
-2.483e+005
-2.483e+005
-2.483e+005
-2.483e+005
-2.483e+005
-2.482e+005
-2.482e+005
-2.482e+005
-2.482e+005
-2.482e+005
-2.482e+005
-2.482e+005
-2.482e+005
-2.482e+005
-2.481e+005
-2.481e+005
-2.481e+005
-2.481e+005
-2.481e+005
-2.482e+005
-2.484e+005
-2.489e+005
-2.521e+005
-2.628e+005
Vap Enthalpy
(kJ/kgmole)
-2.021e+005
-2.024e+005
-2.027e+005
-2.031e+005
-2.035e+005
-2.040e+005
-2.045e+005
-2.045e+005
-2.045e+005
-2.045e+005
-2.045e+005
-2.045e+005
-2.045e+005
-2.045e+005
-2.045e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.044e+005
-2.045e+005
-2.048e+005
-2.056e+005
-2.101e+005
Heat Loss
(kcal/h)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
FEEDS / PRODUCTS
Flow Basis: Molar
Stream Type Duty State Flows Enthalpy Temp
(kcal/h) (Nm3/h(gas)) (kJ/kgmole) (C)
CondenserQCond2
77
Energy
Draw
1.0e+007 *
--- Liquid
---
9.33e-006 *
---
-2.3e+005 *
---
71.11*
1__Main Tower
2__Main Tower
3__Main Tower Producto Draw --- Liquid 1.40e+004 * -2.3e+005 * 71.38*
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 20 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
FEEDS / PRODUCTS
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower 49 Feed --- Mixed 2.99e+004 * -2.5e+005 * 105.60*
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 21 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
FEEDS / PRODUCTS
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower FUSEL Draw --- Liquid 1.09e-005 * -2.5e+005 * 85.85*
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
ReboilerQReb2
RC Bottoms2
Energy
Draw
1.0e+007 *
--- Liquid
---
1.59e+004 *
---
-2.6e+005 *
---
93.58*
SETUP
Sub-Flowsheet
Internal Feed Stream
QReb2
49
External Feed Stream
QReb2 @Main
49 @Main
Transfer Basis
None Req'd
P-H Flash
Internal Prod Stream
QCond2
77
RC Bottoms2
Producto
FUSEL
External Prod Stream
QCond2 @Main
77 @Main
RC Bottoms2 @Main
Producto @Main
FUSEL @Main
Transfer Basis
None Req'd
P-H Flash
P-H Flash
P-H Flash
P-H Flash
VARIABLES
Column Flowsheet Vars Available as ParametersData Source Variable Component Description
COMPONENT MAPS
Feed StreamsFeed Name
QReb2
49
In to SubFlowSheet Out of SubFlowSheet
Product StreamProduct Name
QCond2
77
RC Bottoms2
Producto
FUSEL
In to SubFlowSheet Out of SubFlowSheet
DYNAMICS
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 22 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
Vessel Dynamic Specifications
Vessel
Diameter (m)
Height.0 (m)
Volume.0 (m3)
Liquid Volume Percent (%)
Level Calculator
Fraction Calculator
Vessel Delta P (kPa)
Fixed Vessel P Spec (kg/cm2_g)
Fixed P Spec Active
Reboiler
1.193
1.789
2.000 *
50.00
Horizontal cylinder
Use levels and nozzles
0.0000
0.9300
Not Active
Condenser
1.193
1.789
2.000 *
50.00
Horizontal cylinder
Use levels and nozzles
0.0000
0.3000
Not Active
Other Equipment in Column Flowsheet
Holdup Details
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
Pressure
(kg/cm2_g)
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
Volume
(m3)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Bulk Liquid Volume
(m3)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 23 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Pressure
(kg/cm2_g)
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
-1.033
Volume
(m3)
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
0.0000 *
Bulk Liquid Volume
(m3)
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
COLUMN REFINERY ASSAY PLOTS
Single Tray : Single Tray :
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 24 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
0,00 2,00 4,00 6,00 8,00 10,00
Percent Composition
0,00
2,00
4,00
6,00
8,00
10,00
Tem
pera
ture
Boiling Point Properties
0,00 2,00 4,00 6,00 8,00 10,00
Percent Composition
0,00
2,00
4,00
6,00
8,00
10,00
Mol
ecul
ar W
eigh
t
Molecular Weight Properties
0,00 2,00 4,00 6,00 8,00 10,00
Percent Composition
0,00
2,00
4,00
6,00
8,00
10,00
Den
sity
Density Properties
Distillation: 202-EA/EB @Main (continued)
COLUMN REFINERY ASSAY PLOTS
Single Tray :
COLUMN REFINERY ASSAY TABLES
Boiling Point Assay
Single Tray : Assay Basis : Molar
Assay Percent
0.0 %
1.0 %
2.0 %
3.5 %
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 25 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
COLUMN REFINERY ASSAY TABLES
Boiling Point Assay
Assay Percent
5.0 %
7.5 %
10.0 %
12.5 %
15.0 %
17.5 %
20.0 %
25.0 %
30.0 %
35.0 %
40.0 %
45.0 %
50.0 %
55.0 %
60.0 %
65.0 %
70.0 %
75.0 %
80.0 %
85.0 %
90.0 %
92.5 %
95.0 %
96.5 %
98.0 %
99.0 %
100.0 %
Molecular Weight Assay
Single Tray : Assay Basis : Molar
Assay Percent
0.0 %
1.0 %
2.0 %
3.5 %
5.0 %
7.5 %
10.0 %
12.5 %
15.0 %
17.5 %
20.0 %
25.0 %
30.0 %
35.0 %
40.0 %
45.0 %
50.0 %
55.0 %
60.0 %
65.0 %
70.0 %
75.0 %
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 26 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
COLUMN REFINERY ASSAY TABLES
Molecular Weight Assay
Assay Percent
80.0 %
85.0 %
90.0 %
92.5 %
95.0 %
96.5 %
98.0 %
99.0 %
100.0 %
Density Assay
Single Tray : Assay Basis : Molar
Assay Percent
0.0 %
1.0 %
2.0 %
3.5 %
5.0 %
7.5 %
10.0 %
12.5 %
15.0 %
17.5 %
20.0 %
25.0 %
30.0 %
35.0 %
40.0 %
45.0 %
50.0 %
55.0 %
60.0 %
65.0 %
70.0 %
75.0 %
80.0 %
85.0 %
90.0 %
92.5 %
95.0 %
96.5 %
98.0 %
99.0 %
100.0 %
User Properties
Assay Percent
0.0 %
1.0 %
2.0 %
3.5 %
5.0 %
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 27 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
0 10 20 30 40 50 60 70 80 90 10070,0
75,0
80,0
85,0
90,0
95,0
Tem
pera
ture
(C
)
Temperature vs. Tray Position from Top
Distillation: 202-EA/EB @Main (continued)
COLUMN REFINERY ASSAY TABLES
User Properties
Assay Percent
7.5 %
10.0 %
12.5 %
15.0 %
17.5 %
20.0 %
25.0 %
30.0 %
35.0 %
40.0 %
45.0 %
50.0 %
55.0 %
60.0 %
65.0 %
70.0 %
75.0 %
80.0 %
85.0 %
90.0 %
92.5 %
95.0 %
96.5 %
98.0 %
99.0 %
100.0 %
TRAY by TRAY PROPERTIES PLOTS
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 28 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
0 10 20 30 40 50 60 70 80 90 1000,200
0,300
0,400
0,500
0,600
0,700
0,800
0,900
1,00
Pre
ssur
e (k
g/cm
2_g)
Pressure vs. Tray Position from Top
0 10 20 30 40 50 60 70 80 90 1000,000
5,00e+003
1,00e+004
1,50e+004
2,00e+004
2,50e+004
3,00e+004
3,50e+004
4,00e+004
4,50e+004
Net
Mol
ar F
low
(N
m3/
h(ga
s))
Vapour
Liquid
Flow vs. Tray Position from Top
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES PLOTS
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 29 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
0 10 20 30 40 50 60 70 80 90 100730
740
750
760
770
780
790
800
810
820
830
Den
sity
(kg
/m3)
22,0
24,0
26,0
28,0
30,0
32,0
34,0Density(Light)
Mol Weight(Light)
Column Properties vs. Tray Position from Top
0 10 20 30 40 50 60 70 80 90 1000,000
1,00e-003
2,00e-003
3,00e-003
4,00e-003
5,00e-003
6,00e-003
Mol
e F
ract
ion
Hydrogen (Light)
CO (Light)
CO2 (Light)
Nitrogen (Light)
Composition vs. Tray Position from Top
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES PLOTS
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 30 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
0 10 20 30 40 50 60 70 80 90 1000,000
500
1,00e+003
1,50e+003
2,00e+003
2,50e+003
3,00e+003
3,50e+003
4,00e+003
K V
alue
Hydrogen
CO
CO2
Nitrogen
K-Value vs. Tray Position from Top
0 10 20 30 40 50 60 70 80 90 1000,000
1,00e+015
2,00e+015
3,00e+015
4,00e+015
5,00e+015
6,00e+015
7,00e+015
Mol
e F
ract
ion
Rat
io
Light
Component Ratio vs. Tray Position from Top
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES PLOTS
TRAY by TRAY PROPERTIES TABLES
Column Temperature / Pressure Profile
Column Stage
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
Temperature
(C)
71.11
71.11
71.24
71.38
71.52
71.66
Pressure
(kg/cm2_g)
0.3000
0.3000
0.3069
0.3138
0.3208
0.3277
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 31 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Column Temperature / Pressure Profile
Column Stage
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
Temperature
(C)
71.80
71.94
72.08
72.22
72.36
72.50
72.64
72.78
72.92
73.05
73.19
73.33
73.47
73.61
73.75
73.89
74.04
74.18
74.32
74.46
74.61
74.75
74.90
75.05
75.20
75.35
75.50
75.65
75.81
75.97
76.13
76.29
76.46
76.63
76.80
76.98
77.17
77.35
77.55
77.75
77.96
78.18
78.40
78.64
78.89
79.15
79.43
79.73
80.05
80.39
80.76
81.17
81.61
82.09
Pressure
(kg/cm2_g)
0.3346
0.3415
0.3485
0.3554
0.3623
0.3692
0.3762
0.3831
0.3900
0.3969
0.4038
0.4108
0.4177
0.4246
0.4315
0.4385
0.4454
0.4523
0.4592
0.4662
0.4731
0.4800
0.4869
0.4938
0.5008
0.5077
0.5146
0.5215
0.5285
0.5354
0.5423
0.5492
0.5562
0.5631
0.5700
0.5769
0.5838
0.5908
0.5977
0.6046
0.6115
0.6185
0.6254
0.6323
0.6392
0.6462
0.6531
0.6600
0.6669
0.6738
0.6808
0.6877
0.6946
0.7015
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 32 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Column Temperature / Pressure Profile
Column Stage
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Temperature
(C)
82.63
83.22
83.89
84.00
84.11
84.23
84.34
84.45
84.56
84.67
84.77
84.88
84.99
85.10
85.21
85.31
85.42
85.53
85.63
85.74
85.85
85.95
86.06
86.16
86.27
86.37
86.48
86.58
86.69
86.83
87.06
87.62
89.17
93.58
Pressure
(kg/cm2_g)
0.7085
0.7154
0.7223
0.7292
0.7362
0.7431
0.7500
0.7569
0.7638
0.7708
0.7777
0.7846
0.7915
0.7985
0.8054
0.8123
0.8192
0.8262
0.8331
0.8400
0.8469
0.8538
0.8608
0.8677
0.8746
0.8815
0.8885
0.8954
0.9023
0.9092
0.9162
0.9231
0.9300
0.9300
Column Flow Profile
Options Selected
Molar flow is selected Net is selected as flow basis
Tray Number
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
Vapour
(Nm3/h(gas))
9.920e-004
2.798e+004
2.798e+004
2.798e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
Bulk Liquid
(Nm3/h(gas))
2.798e+004
2.798e+004
2.798e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 33 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Tray Number
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
Vapour
(Nm3/h(gas))
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.799e+004
2.798e+004
2.798e+004
2.798e+004
2.798e+004
2.797e+004
2.797e+004
2.797e+004
2.796e+004
2.796e+004
2.795e+004
2.795e+004
2.794e+004
2.793e+004
2.793e+004
2.792e+004
2.791e+004
2.790e+004
2.789e+004
2.788e+004
2.786e+004
2.785e+004
2.784e+004
2.782e+004
2.780e+004
2.778e+004
2.776e+004
2.773e+004
2.771e+004
2.768e+004
2.764e+004
2.761e+004
2.757e+004
2.752e+004
2.747e+004
2.742e+004
2.735e+004
2.728e+004
2.721e+004
2.713e+004
2.714e+004
2.715e+004
2.716e+004
2.717e+004
2.718e+004
2.719e+004
Bulk Liquid
(Nm3/h(gas))
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.400e+004
1.399e+004
1.399e+004
1.399e+004
1.399e+004
1.398e+004
1.398e+004
1.398e+004
1.397e+004
1.397e+004
1.396e+004
1.396e+004
1.395e+004
1.395e+004
1.394e+004
1.393e+004
1.393e+004
1.392e+004
1.391e+004
1.390e+004
1.389e+004
1.387e+004
1.386e+004
1.384e+004
1.383e+004
1.381e+004
1.379e+004
1.377e+004
1.374e+004
1.372e+004
1.369e+004
1.365e+004
1.362e+004
1.358e+004
1.353e+004
1.348e+004
1.342e+004
1.336e+004
1.329e+004
1.322e+004
4.304e+004
4.305e+004
4.306e+004
4.307e+004
4.309e+004
4.310e+004
4.311e+004
4.312e+004
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 34 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Tray Number
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Vapour
(Nm3/h(gas))
2.720e+004
2.721e+004
2.722e+004
2.723e+004
2.724e+004
2.725e+004
2.726e+004
2.727e+004
2.728e+004
2.729e+004
2.730e+004
2.731e+004
2.732e+004
2.733e+004
2.734e+004
2.735e+004
2.736e+004
2.737e+004
2.738e+004
2.739e+004
2.738e+004
2.736e+004
2.733e+004
2.701e+004
Bulk Liquid
(Nm3/h(gas))
4.313e+004
4.314e+004
4.315e+004
4.316e+004
4.317e+004
4.318e+004
4.319e+004
4.320e+004
4.321e+004
4.322e+004
4.323e+004
4.324e+004
4.325e+004
4.326e+004
4.327e+004
4.328e+004
4.329e+004
4.330e+004
4.330e+004
4.330e+004
4.327e+004
4.324e+004
4.292e+004
1.591e+004
Column Properties Profile
Options Selected
Mass basis is selected
Stage
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
Surf Tens
(dyne/cm)
22.4
22.4
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.3
22.4
22.4
22.4
Mol Wt
L-Liq
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
32.0
31.9
31.9
31.9
31.9
31.9
31.9
31.9
Dens
L-Liq
(kg/m3)
736
736
735
735
735
735
735
735
735
735
734
734
734
734
734
734
734
734
734
734
734
733
733
733
733
Visc
L-Liq
(cP)
0.305
0.305
0.305
0.304
0.304
0.303
0.303
0.302
0.302
0.301
0.301
0.301
0.300
0.300
0.299
0.299
0.298
0.298
0.298
0.297
0.297
0.296
0.296
0.296
0.295
Therm Con
L-Liq
(W/m-K)
0.160
0.160
0.160
0.160
0.160
0.160
0.160
0.160
0.160
0.160
0.160
0.160
0.160
0.160
0.161
0.161
0.161
0.161
0.161
0.161
0.162
0.162
0.162
0.162
0.163
Heat Cap
L-Liq
(kJ/kg-C)
3.78
3.78
3.79
3.79
3.79
3.79
3.79
3.79
3.79
3.79
3.79
3.79
3.79
3.79
3.80
3.80
3.80
3.80
3.80
3.80
3.80
3.80
3.80
3.80
3.80
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 35 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Stage
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
Surf Tens
(dyne/cm)
22.4
22.5
22.5
22.5
22.6
22.6
22.7
22.8
22.8
22.9
23.0
23.1
23.2
23.3
23.4
23.5
23.7
23.8
24.0
24.2
24.4
24.6
24.8
25.1
25.4
25.7
26.1
26.5
26.9
27.4
28.0
28.6
29.3
30.0
30.9
31.8
32.9
34.0
34.0
34.0
34.0
34.0
33.9
33.9
33.9
33.9
33.9
33.9
33.8
33.8
33.8
33.8
33.8
33.7
33.7
Mol Wt
L-Liq
31.8
31.8
31.8
31.8
31.8
31.7
31.7
31.7
31.6
31.6
31.6
31.5
31.5
31.5
31.4
31.4
31.3
31.2
31.2
31.1
31.0
30.9
30.8
30.7
30.6
30.5
30.4
30.2
30.0
29.9
29.7
29.4
29.2
28.9
28.6
28.2
27.8
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
Dens
L-Liq
(kg/m3)
733
733
733
733
733
733
733
733
734
734
734
734
734
734
734
735
735
735
736
736
736
737
738
738
739
740
741
742
743
744
746
748
750
753
756
759
763
767
767
767
767
767
767
767
766
766
766
766
766
766
766
766
765
765
765
Visc
L-Liq
(cP)
0.295
0.295
0.294
0.294
0.294
0.293
0.293
0.293
0.292
0.292
0.292
0.291
0.291
0.291
0.290
0.290
0.290
0.290
0.289
0.289
0.289
0.289
0.289
0.289
0.289
0.288
0.288
0.288
0.288
0.288
0.289
0.289
0.289
0.289
0.289
0.290
0.290
0.290
0.290
0.289
0.289
0.288
0.288
0.288
0.287
0.287
0.287
0.286
0.286
0.286
0.285
0.285
0.284
0.284
0.284
Therm Con
L-Liq
(W/m-K)
0.163
0.163
0.163
0.164
0.164
0.165
0.165
0.166
0.166
0.167
0.168
0.169
0.169
0.170
0.171
0.172
0.174
0.175
0.176
0.178
0.180
0.181
0.183
0.186
0.188
0.191
0.194
0.198
0.202
0.206
0.211
0.217
0.224
0.231
0.240
0.250
0.261
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
0.273
Heat Cap
L-Liq
(kJ/kg-C)
3.81
3.81
3.81
3.81
3.81
3.81
3.81
3.81
3.81
3.82
3.82
3.82
3.82
3.82
3.82
3.83
3.83
3.83
3.83
3.83
3.84
3.84
3.84
3.84
3.85
3.85
3.85
3.86
3.86
3.87
3.87
3.88
3.88
3.89
3.90
3.91
3.92
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
3.93
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 36 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Stage
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Surf Tens
(dyne/cm)
33.7
33.7
33.7
33.7
33.6
33.6
33.6
33.6
33.6
33.6
33.8
34.5
36.9
45.3
Mol Wt
L-Liq
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.4
27.3
27.0
26.0
23.0
Dens
L-Liq
(kg/m3)
765
765
765
765
765
765
764
764
764
764
765
766
776
826
Visc
L-Liq
(cP)
0.283
0.283
0.283
0.282
0.282
0.282
0.281
0.281
0.281
0.280
0.280
0.277
0.272
0.281
Therm Con
L-Liq
(W/m-K)
0.273
0.273
0.273
0.272
0.272
0.272
0.272
0.272
0.273
0.273
0.276
0.283
0.313
0.432
Heat Cap
L-Liq
(kJ/kg-C)
3.93
3.94
3.94
3.94
3.94
3.94
3.94
3.94
3.94
3.94
3.94
3.94
3.95
4.05
Column Composition Profile
Options Selected
Fraction is selected as the composition basis Net is selected as flow basis
Molar basis is selected
Stage
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
Hydrogen
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO2
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Nitrogen
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 37 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Stage
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
Hydrogen
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO2
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0002
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
0.0007
Nitrogen
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 38 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Stage
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Hydrogen
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO
L-Liq
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
CO2
L-Liq
0.0007
0.0007
0.0007
0.0007
0.0008
0.0018
0.0059
0.0018
Nitrogen
L-Liq
0.0000
0.0000
0.0000
0.0001
0.0002
0.0009
0.0017
0.0001
Heavy/Light Key Component Ratios
Options Selected
Molar basis is selected
Key Components
Light Key
Hydrogen
CO
CO2
Nitrogen
Oxygen
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
Methanol
H2O
Chosen
On
On
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Off
Off
Heavy Key
Hydrogen
CO
CO2
Nitrogen
Oxygen
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
Methanol
H2O
Chosen
Off
Off
Off
Off
On
On
Off
Off
Off
Off
Off
Off
Off
Off
Stage
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
Light Liq
6.759e+015
5.683e+011
1.779e+010
4.510e+007
1.117e+007
4.671e+006
2.222e+006
1.114e+006
5.723e+005
2.976e+005
1.557e+005
8.169e+004
9.447e+006
9.788e+006
6.458e+006
3.711e+006
2.026e+006
1.082e+006
5.731e+005
3.024e+005
1.594e+005
8.407e+004
4.437e+004
2.345e+004
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 39 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Heavy/Light Key Component Ratios
Stage
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
Light Liq
1.241e+004
6584
3500
1866
997.4
535.2
288.5
156.3
85.37
47.11
26.40
15.14
8.989
5.614
3.753
2.721
2.147
1.826
0.6898
0.6582
0.6454
0.6323
0.6188
0.6050
0.5911
0.5774
0.5642
0.5522
0.5424
0.5362
0.5362
0.5463
0.5736
0.6302
0.7393
0.9453
1.340
2.121
3.749
3.750
3.751
3.752
3.753
3.754
3.755
3.756
3.757
3.758
3.759
3.760
3.760
3.761
3.762
3.763
3.764
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 40 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Heavy/Light Key Component Ratios
Stage
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
92__Main Tower
Reboiler
Light Liq
3.765
3.766
3.767
3.768
3.769
3.769
3.770
3.769
3.756
3.659
3.059
1.608
0.9580
1.268
3.987
Column K-Values Profile
Tray Number
Condenser
1__Main Tower
2__Main Tower
3__Main Tower
4__Main Tower
5__Main Tower
6__Main Tower
7__Main Tower
8__Main Tower
9__Main Tower
10__Main Tower
11__Main Tower
12__Main Tower
13__Main Tower
14__Main Tower
15__Main Tower
16__Main Tower
17__Main Tower
18__Main Tower
19__Main Tower
20__Main Tower
21__Main Tower
22__Main Tower
23__Main Tower
24__Main Tower
25__Main Tower
26__Main Tower
27__Main Tower
28__Main Tower
29__Main Tower
30__Main Tower
31__Main Tower
32__Main Tower
33__Main Tower
34__Main Tower
35__Main Tower
36__Main Tower
Hydrogen
3797
3141
11.99
474.1
394.3
392.7
391.1
389.6
388.1
386.6
385.2
383.7
1.737
1.131
1.095
1.093
1.093
1.093
1.093
1.093
1.093
1.093
1.094
1.094
1.094
1.094
1.094
1.094
1.094
1.094
1.094
1.094
1.095
1.095
1.095
1.095
1.095
CO
243.8
180.1
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
CO2
0.2640
0.2641
0.2637
0.2634
0.2632
0.2630
0.2628
0.2626
0.2624
0.2623
0.2622
0.2620
0.2620
0.2619
0.2618
0.2618
0.2618
0.2619
0.2619
0.2620
0.2622
0.2623
0.2625
0.2628
0.2631
0.2634
0.2638
0.2643
0.2648
0.2654
0.2661
0.2668
0.2677
0.2686
0.2696
0.2707
0.2720
Nitrogen
0.2641
0.2641
0.2637
0.2634
0.2633
0.2631
0.2629
0.2628
0.2627
0.2626
0.2625
0.2625
0.2625
0.2625
0.2625
0.2626
0.2627
0.2628
0.2630
0.2632
0.2635
0.2638
0.2641
0.2645
0.2650
0.2655
0.2661
0.2668
0.2676
0.2684
0.2693
0.2704
0.2715
0.2728
0.2742
0.2758
0.2775
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 41 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Column K-Values Profile
Tray Number
37__Main Tower
38__Main Tower
39__Main Tower
40__Main Tower
41__Main Tower
42__Main Tower
43__Main Tower
44__Main Tower
45__Main Tower
46__Main Tower
47__Main Tower
48__Main Tower
49__Main Tower
50__Main Tower
51__Main Tower
52__Main Tower
53__Main Tower
54__Main Tower
55__Main Tower
56__Main Tower
57__Main Tower
58__Main Tower
59__Main Tower
60__Main Tower
61__Main Tower
62__Main Tower
63__Main Tower
64__Main Tower
65__Main Tower
66__Main Tower
67__Main Tower
68__Main Tower
69__Main Tower
70__Main Tower
71__Main Tower
72__Main Tower
73__Main Tower
74__Main Tower
75__Main Tower
76__Main Tower
77__Main Tower
78__Main Tower
79__Main Tower
80__Main Tower
81__Main Tower
82__Main Tower
83__Main Tower
84__Main Tower
85__Main Tower
86__Main Tower
87__Main Tower
88__Main Tower
89__Main Tower
90__Main Tower
91__Main Tower
Hydrogen
1.095
1.096
1.096
1.096
1.096
1.097
1.097
1.097
1.098
1.098
1.098
1.099
1.099
1.100
1.100
1.101
1.101
1.102
1.103
1.104
1.105
1.106
1.107
1.108
1.109
1.111
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
CO
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
1.000
CO2
0.2734
0.2750
0.2767
0.2786
0.2807
0.2818
1.810e-002
1.059e-002
1.103e-002
1.154e-002
1.214e-002
1.283e-002
1.365e-002
1.462e-002
1.580e-002
1.722e-002
1.897e-002
2.116e-002
2.394e-002
2.754e-002
3.230e-002
3.874e-002
4.769e-002
6.048e-002
7.933e-002
0.1079
0.1075
0.1071
0.1067
0.1063
0.1059
0.1055
0.1051
0.1047
0.1043
0.1039
0.1035
0.1031
0.1027
0.1023
0.1019
0.1016
0.1012
0.1008
0.1004
0.1001
9.972e-002
9.936e-002
9.901e-002
9.869e-002
9.848e-002
9.863e-002
0.1000
0.1061
0.1319
Nitrogen
0.2794
0.2815
0.2838
0.2863
0.2892
1.654e-002
1.159e-002
1.216e-002
1.282e-002
1.359e-002
1.449e-002
1.556e-002
1.684e-002
1.839e-002
2.028e-002
2.263e-002
2.559e-002
2.940e-002
3.437e-002
4.103e-002
5.018e-002
6.312e-002
8.203e-002
0.1106
0.1557
0.2292
0.2282
0.2273
0.2264
0.2254
0.2245
0.2236
0.2227
0.2218
0.2209
0.2200
0.2192
0.2183
0.2174
0.2166
0.2157
0.2149
0.2140
0.2132
0.2124
0.2115
0.2107
0.2099
0.2091
0.2085
0.2080
0.2086
0.2124
0.2289
0.3005
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 42 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
METHANEX CORPBurlington, MAUSA
Case Name: Loop Sintesis + destilacion converge(agregue temp a la salida de IQ)converge completo.hsc
Unit Set: Methanex3b1
Date/Time: Fri Feb 19 09:13:12 2016
Distillation: 202-EA/EB @Main (continued)
TRAY by TRAY PROPERTIES TABLES
Column K-Values Profile
Tray Number
92__Main Tower
Reboiler
Hydrogen
0.9999
0.9997
CO
0.9999
0.9997
CO2
0.2906
4.484
Nitrogen
0.8071
24.46
NOTES
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628) Page 43 of 43
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: METHANEX CORP
