Https Doc 00 8s Apps Viewer.googleusercontent
2
Company Name Not Available Calgary, Alberta CANADA Case Name: C:\Users\admin\Desktop\waseem.usc Unit Set: SI Date/Time: Tuesday May 27 2014, 13:13:18 Workbook: Case (Main) STATUS OK Material Streams Fluid Pkg: All Name Vapour Fraction Temperature Pressure Molar Flow Mass Flow Liquid Volume Flow Heat Flow (C) (kPa) (kgmole/h) (kg/h) (m3/h) (kJ/h) MA 0.0000 * 30.00 * 202.6 * 166.1 * 1.629e+004 12.31 -7.579e+007 Methanol 1.0000 130.0 * 202.6 * 498.3 * 1.597e+004 20.07 -9.780e+007 Me+H2O 1.0000 119.9 202.6 408.5 1.367e+004 16.75 -8.204e+007 DMM 0.0000 119.9 202.6 256.0 1.859e+004 15.63 -9.155e+007 Cold Me+H2O 0.6486 85.00 * 201.6 408.5 1.367e+004 16.75 -8.781e+007 Name Vapour Fraction Temperature Pressure Molar Flow Mass Flow Liquid Volume Flow Heat Flow (C) (kPa) (kgmole/h) (kg/h) (m3/h) (kJ/h) water 0.0000 * 30.00 * 101.3 * 2081 3.749e+004 * 37.57 -5.921e+008 steam 0.0000 66.47 96.30 2081 3.749e+004 37.57 -5.863e+008 me out 0.0000 64.48 101.3 390.0 1.250e+004 15.70 -9.157e+007 water out 0.0000 103.6 178.3 18.45 1173 1.041 -6.113e+006 Hot DMM 0.0000 * 119.8 201.6 256.0 1.859e+004 15.63 -9.156e+007 Name Vapour Fraction Temperature Pressure Molar Flow Mass Flow Liquid Volume Flow Heat Flow (C) (kPa) (kgmole/h) (kg/h) (m3/h) (kJ/h) COLD WATER 0.0000 66.52 91.28 2081 3.749e+004 37.57 -5.863e+008 Liq. 1.0000 -103.1 201.6 860.8 1735 24.84 -3.119e+006 BDO+ME 0.0000 -103.1 201.6 206.6 1.859e+004 17.53 -8.313e+007 Hydrogen 1.0000 239.9 * 202.6 * 860.8 * 1735 24.84 5.305e+006 Cold BDO+ME 0.0000 -38.25 200.6 206.6 1.859e+004 17.53 -8.118e+007 Name Vapour Fraction Temperature Pressure Molar Flow Mass Flow Liquid Volume Flow Heat Flow (C) (kPa) (kgmole/h) (kg/h) (m3/h) (kJ/h) H2 1.0000 60.00 * 202.6 * 860.8 * 1735 24.84 8.575e+005 H2out 1.0000 -20.00 * 197.6 860.8 1735 24.84 -1.099e+006 ME 0.0000 89.15 101.3 100.0 5899 4.737 -3.624e+007 BDO 0.0000 230.4 153.2 106.6 1.269e+004 12.79 -3.610e+007 Compositions Fluid Pkg: All Name Comp Mole Frac (Methanol) Comp Mole Frac (MaleicAnhydr) Comp Mole Frac (Hydrogen) Comp Mole Frac (DMM*) Comp Mole Frac (1,4Butanediol*) Comp Mole Frac (H2O) MA 0.000000 * 1.000000 * 0.000000 * 0.000000 * 0.000000 * 0.000000 * Methanol 1.000000 * 0.000000 * 0.000000 * 0.000000 * 0.000000 * 0.000000 * Me+H2O 0.978436 0.021564 0.000000 0.000000 0.000000 0.000000 DMM 0.385520 0.614480 0.000000 0.000000 0.000000 0.000000 Cold Me+H2O 0.978436 0.021564 0.000000 0.000000 0.000000 0.000000 Name Comp Mole Frac (Methanol) Comp Mole Frac (MaleicAnhydr) Comp Mole Frac (Hydrogen) Comp Mole Frac (DMM*) Comp Mole Frac (1,4Butanediol*) Comp Mole Frac (H2O) water 0.000000 * 0.000000 * 0.000000 * 0.000000 * 0.000000 * 1.000000 * steam 0.000000 0.000000 0.000000 0.000000 0.000000 1.000000 me out 1.000000 0.000000 0.000000 0.000000 0.000000 0.000000 water out 0.522523 0.477477 0.000000 0.000000 0.000000 0.000000 Hot DMM 0.385520 0.614480 0.000000 0.000000 0.000000 0.000000 Honeywell International Inc. UniSim Design (R410 Build 17061) Page 1 of 2 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 Licensed to: Company Name Not Available Printed by: admin * Specified by user.
-
Upload
asrahaman9 -
Category
Documents
-
view
241 -
download
4
description
sdd
Transcript of Https Doc 00 8s Apps Viewer.googleusercontent
-
Company Name Not Available
Calgary, Alberta
CANADA
Case Name: C:\Users\admin\Desktop\waseem.usc
Unit Set: SI
Date/Time: Tuesday May 27 2014, 13:13:18
Workbook: Case (Main)
STATUS
OK
Material Streams Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Liquid Volume Flow
Heat Flow
(C)
(kPa)
(kgmole/h)
(kg/h)
(m3/h)
(kJ/h)
MA
0.0000 *
30.00 *
202.6 *
166.1 *
1.629e+004
12.31
-7.579e+007
Methanol
1.0000
130.0 *
202.6 *
498.3 *
1.597e+004
20.07
-9.780e+007
Me+H2O
1.0000
119.9
202.6
408.5
1.367e+004
16.75
-8.204e+007
DMM
0.0000
119.9
202.6
256.0
1.859e+004
15.63
-9.155e+007
Cold Me+H2O
0.6486
85.00 *
201.6
408.5
1.367e+004
16.75
-8.781e+007
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Liquid Volume Flow
Heat Flow
(C)
(kPa)
(kgmole/h)
(kg/h)
(m3/h)
(kJ/h)
water
0.0000 *
30.00 *
101.3 *
2081
3.749e+004 *
37.57
-5.921e+008
steam
0.0000
66.47
96.30
2081
3.749e+004
37.57
-5.863e+008
me out
0.0000
64.48
101.3
390.0
1.250e+004
15.70
-9.157e+007
water out
0.0000
103.6
178.3
18.45
1173
1.041
-6.113e+006
Hot DMM
0.0000 *
119.8
201.6
256.0
1.859e+004
15.63
-9.156e+007
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Liquid Volume Flow
Heat Flow
(C)
(kPa)
(kgmole/h)
(kg/h)
(m3/h)
(kJ/h)
COLD WATER
0.0000
66.52
91.28
2081
3.749e+004
37.57
-5.863e+008
Liq.
1.0000
-103.1
201.6
860.8
1735
24.84
-3.119e+006
BDO+ME
0.0000
-103.1
201.6
206.6
1.859e+004
17.53
-8.313e+007
Hydrogen
1.0000
239.9 *
202.6 *
860.8 *
1735
24.84
5.305e+006
Cold BDO+ME
0.0000
-38.25
200.6
206.6
1.859e+004
17.53
-8.118e+007
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Liquid Volume Flow
Heat Flow
(C)
(kPa)
(kgmole/h)
(kg/h)
(m3/h)
(kJ/h)
H2
1.0000
60.00 *
202.6 *
860.8 *
1735
24.84
8.575e+005
H2out
1.0000
-20.00 *
197.6
860.8
1735
24.84
-1.099e+006
ME
0.0000
89.15
101.3
100.0
5899
4.737
-3.624e+007
BDO
0.0000
230.4
153.2
106.6
1.269e+004
12.79
-3.610e+007
Compositions Fluid Pkg: All
Name
Comp Mole Frac (Methanol)
Comp Mole Frac (MaleicAnhydr)
Comp Mole Frac (Hydrogen)
Comp Mole Frac (DMM*)
Comp Mole Frac (1,4Butanediol*)
Comp Mole Frac (H2O)
MA
0.000000 *
1.000000 *
0.000000 *
0.000000 *
0.000000 *
0.000000 *
Methanol
1.000000 *
0.000000 *
0.000000 *
0.000000 *
0.000000 *
0.000000 *
Me+H2O
0.978436
0.021564
0.000000
0.000000
0.000000
0.000000
DMM
0.385520
0.614480
0.000000
0.000000
0.000000
0.000000
Cold Me+H2O
0.978436
0.021564
0.000000
0.000000
0.000000
0.000000
Name
Comp Mole Frac (Methanol)
Comp Mole Frac (MaleicAnhydr)
Comp Mole Frac (Hydrogen)
Comp Mole Frac (DMM*)
Comp Mole Frac (1,4Butanediol*)
Comp Mole Frac (H2O)
water
0.000000 *
0.000000 *
0.000000 *
0.000000 *
0.000000 *
1.000000 *
steam
0.000000
0.000000
0.000000
0.000000
0.000000
1.000000
me out
1.000000
0.000000
0.000000
0.000000
0.000000
0.000000
water out
0.522523
0.477477
0.000000
0.000000
0.000000
0.000000
Hot DMM
0.385520
0.614480
0.000000
0.000000
0.000000
0.000000
Honeywell International Inc. UniSim Design (R410 Build 17061) Page 1 of 2
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
Licensed to: Company Name Not Available Printed by: admin * Specified by user.
-
Company Name Not Available
Calgary, Alberta
CANADA
Case Name: C:\Users\admin\Desktop\waseem.usc
Unit Set: SI
Date/Time: Tuesday May 27 2014, 13:13:18
Workbook: Case (Main) (continued)
Compositions (continued) Fluid Pkg: All
Name
Comp Mole Frac (Methanol)
Comp Mole Frac (MaleicAnhydr)
Comp Mole Frac (Hydrogen)
Comp Mole Frac (DMM*)
Comp Mole Frac (1,4Butanediol*)
Comp Mole Frac (H2O)
COLD WATER
0.000000
0.000000
0.000000
0.000000
0.000000
1.000000
Liq.
0.000000
0.000000
1.000000
0.000000
0.000000
0.000000
BDO+ME
0.000000
0.522443
0.000003
0.238799
0.000000
0.238754
Hydrogen
0.000000 *
0.000000 *
1.000000 *
0.000000 *
0.000000 *
0.000000 *
Cold BDO+ME
0.000000
0.522443
0.000003
0.238799
0.000000
0.238754
Name
Comp Mole Frac (Methanol)
Comp Mole Frac (MaleicAnhydr)
Comp Mole Frac (Hydrogen)
Comp Mole Frac (DMM*)
Comp Mole Frac (1,4Butanediol*)
Comp Mole Frac (H2O)
H2
0.000000 *
0.000000 *
1.000000 *
0.000000 *
0.000000 *
0.000000 *
H2out
0.000000
0.000000
1.000000
0.000000
0.000000
0.000000
ME
0.000000
0.497655
0.000007
0.009011
0.000000
0.493328
BDO
0.000000
0.545691
0.000000
0.454309
0.000000
0.000000
Energy Streams Fluid Pkg: All
Name
Heat Flow (kJ/h)
qc
2.989e+007
qr
2.003e+007
Qr1
1.885e+007
Qc1
1.002e+007
Unit Ops
Operation Name Operation Type Feeds Products Ignored Calc Level
CRV-100 Conversion ReactorMA
Methanol
DMM
Me+H2ONo 500.0 *
CRV-101 Conversion ReactorHot DMM
Hydrogen
BDO+ME
Liq.No 500.0 *
E-100 Heat ExchangerMe+H2O
water
Cold Me+H2O
steamNo 500.0 *
E-101 Heat ExchangerDMM
steam
Hot DMM
COLD WATERNo 500.0 *
E-102 Heat ExchangerBDO+ME
H2
Cold BDO+ME
H2outNo 500.0 *
T-100 Distillation
Cold Me+H2O
qr
water out
me out
qc
No 2500 *
T-101 Distillation
Cold BDO+ME
Qr1
BDO
ME
Qc1
No 2500 *
Honeywell International Inc. UniSim Design (R410 Build 17061) Page 2 of 2
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
Licensed to: Company Name Not Available Printed by: admin * Specified by user.
