Download - HMB for Preheat Train
-
7/23/2019 HMB for Preheat Train
1/8
LEGENDS
Burlington, MA
USA
Case Name: REFINERY ON PRESSURE SPECS.HSC
Unit Set: Refinery1
Date/Time: Tue Sep 08 10:25:24 2015
Workbook: PREHEAT TRAIN (TPL1)
Material Streams Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Std Ideal Liq Vol Flow
Heat Flow
Liquid Fraction
Light Liquid Fraction
Heavy Liquid Fraction
Vap Frac on a Mass Basis
Vap Frac on a Volume Basis
Molar Volume
Actual Volume Flow
Power
Actual Gas Flow
Actual Liquid Flow
Liq Vol Flow @Std Cond
Std Gas Flow
Molecular Weight
Mass Density
Std Ideal Liq Mass Density
Molar Density
Average Liquid Density
Liq Mass Density @Std Cond
Molar Heat CapacityMolar Enthalpy
Mass Enthalpy
Molar Entropy
Mass Entropy
Thermal Conductivity
Viscosity
Surface Tension
Specific Gravity rel Air
Watson K
Kinematic Viscosity
Cp/Cv
(C)
(psia)
(lbmole/hr)
(lb/hr)
(barrel/day)
(Btu/hr)
(ft3/lbmole)
(USGPM)
(kW)
(ACFM)
(USGPM)
(barrel/day)
(MMSCFD)
(lb/ft3)
(lb/ft3)
(lbmole/ft3)
(lbmole/ft3)
(API_60)
(Btu/lbmole-F)(Btu/lbmole)
(Btu/lb)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/hr-ft-F)
(cP)
(dyne/cm)
(rel_to_air)
(cSt)
FEED IN 6000 bpd
0.0000
45.00
49.31
489.1
6.777e+004
6000
-6.220e+007
1.000
1.000
3.471e-005
0.0000
0.0000
2.940
179.3
-1.823e+004
---
179.3
5958
4.446
138.6
47.12
48.28
0.3401
0.3485
49.79
67.07-1.272e+005
-917.7
47.95
0.3461
6.367e-002
0.9135
20.28
---
11.96
1.210
1.220
F Oil to EA-109
0.0000
232.7
19.50
33.76
1.149e+004
890.6
-8.217e+006
1.000
1.000
0.0000
0.0000
0.0000
7.501
31.58
-2408
---
31.58
897.2
0.3069
340.3
45.36
55.14
0.1333
0.1621
29.56
220.3-2.434e+005
-715.2
238.8
0.7017
5.985e-002
0.6997
16.33
---
12.03
0.9629
1.191
HSD to EA-108
0.0000
198.9
19.70
81.10
1.686e+004
1409
-1.272e+007
1.000
1.000
0.0000
0.0000
0.0000
4.884
49.39
-3727
---
49.39
1408
0.7372
207.9
42.56
51.13
0.2047
0.2460
40.77
131.0-1.568e+005
-754.2
123.2
0.5929
5.857e-002
0.3095
13.92
---
12.03
0.4540
1.167
From Con 2
1.0000
176.2
19.88
448.4
4.542e+004
3985
-4.314e+007
0.0000
0.0000
0.0000
1.0000
1.0000
421.5
2.357e+004
-1.264e+004
3150
---
3895
4.076
101.3
0.2403
48.73
2.372e-003
0.4810
45.33
53.40-9.621e+004
-949.8
76.96
0.7598
1.319e-002
9.070e-003
---
3.497
12.04
2.356
1.044
Cold KERO
0.0000
57.50*
16.88
116.3
1.627e+004
1446
-1.478e+007
1.000
0.9935
6.456e-003
0.0000
0.0000
3.033
43.99
-4331
---
43.99
1444
1.058
139.8
46.11
48.10
0.3297
0.3440
51.52
69.44-1.270e+005
-908.5
46.22
0.3306
6.470e-002
0.6209
---
---
12.04
0.8408
1.219
Aspen Technology Inc. Aspen HYSYS Version 7.3 (25.0.0.7336) Page 1 of 8
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
3738
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
-
7/23/2019 HMB for Preheat Train
2/8
LEGENDS
Burlington, MA
USA
Case Name: REFINERY ON PRESSURE SPECS.HSC
Unit Set: Refinery1
Date/Time: Tue Sep 08 10:25:24 2015
Workbook: PREHEAT TRAIN (TPL1) (continued)
Material Streams (continued) Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Std Ideal Liq Vol Flow
Heat Flow
Liquid Fraction
Light Liquid Fraction
Heavy Liquid Fraction
Vap Frac on a Mass Basis
Vap Frac on a Volume Basis
Molar Volume
Actual Volume Flow
Power
Actual Gas Flow
Actual Liquid Flow
Liq Vol Flow @Std Cond
Std Gas Flow
Molecular Weight
Mass Density
Std Ideal Liq Mass Density
Molar Density
Average Liquid Density
Liq Mass Density @Std Cond
Molar Heat CapacityMolar Enthalpy
Mass Enthalpy
Molar Entropy
Mass Entropy
Thermal Conductivity
Viscosity
Surface Tension
Specific Gravity rel Air
Watson K
Kinematic Viscosity
Cp/Cv
(C)
(psia)
(lbmole/hr)
(lb/hr)
(barrel/day)
(Btu/hr)
(ft3/lbmole)
(USGPM)
(kW)
(ACFM)
(USGPM)
(barrel/day)
(MMSCFD)
(lb/ft3)
(lb/ft3)
(lbmole/ft3)
(lbmole/ft3)
(API_60)
(Btu/lbmole-F)(Btu/lbmole)
(Btu/lb)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/hr-ft-F)
(cP)
(dyne/cm)
(rel_to_air)
(cSt)
Feed to EA-101
0.0000
42.00*
33.00
2685
4.837e+004
3319
-3.289e+008
1.000
0.0000
1.000
0.0000
0.0000
0.2902
97.15
-9.639e+004
---
97.15
3264
24.41
18.02
62.08
62.30
3.446
3.458
7.655
18.57-1.225e+005
-6799
13.86
0.7691
0.3663
0.6274
69.14
---
---
0.6309
1.157
Feed to EA-102
0.0000
56.46
47.31
489.1
6.777e+004
6000
-6.151e+007
1.000
1.000
0.0000
0.0000
0.0000
2.978
181.6
-1.803e+004
---
181.6
5958
4.446
138.6
46.53
48.28
0.3358
0.3485
49.79
68.87-1.258e+005
-907.6
50.36
0.3635
6.264e-002
0.7849
19.24
---
11.96
1.053
1.219
Feed to EA-104
0.1002
135.3
41.31
489.1
6.777e+004
6000
-5.583e+007
0.8998
0.8998
0.0000
0.0555
0.0645
21.11
1287
-1.636e+004
---
187.0
5958
4.446
138.6
6.565
48.28
4.738e-002
0.3485
49.79
80.23-1.141e+005
-823.8
67.76
0.4890
---
---
13.19
---
11.96
---
1.004
Feed to EA-105
0.1770
144.5
39.31
489.1
6.777e+004
6000
-5.477e+007
0.8230
0.8230
0.0000
0.1044
0.1185
37.16
2266
-1.605e+004
---
177.9
5958
4.446
138.6
3.729
48.28
2.691e-002
0.3485
49.79
80.78-1.120e+005
-808.1
70.70
0.5103
---
---
12.95
---
11.96
---
1.006
Cold HSD
0.0000
76.03
29.01*
81.10
1.686e+004
1409
-1.483e+007
1.000
0.9982
1.820e-003
0.0000
0.0000
4.289
43.37
-4347
---
43.37
1408
0.7372
207.9
48.47
51.13
0.2332
0.2460
40.77
104.6-1.829e+005
-879.8
87.85
0.4226
6.703e-002
1.278
---
---
12.03
1.647
1.183
Aspen Technology Inc. Aspen HYSYS Version 7.3 (25.0.0.7336) Page 2 of 8
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
3738
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
-
7/23/2019 HMB for Preheat Train
3/8
LEGENDS
Burlington, MA
USA
Case Name: REFINERY ON PRESSURE SPECS.HSC
Unit Set: Refinery1
Date/Time: Tue Sep 08 10:25:24 2015
Workbook: PREHEAT TRAIN (TPL1) (continued)
Material Streams (continued) Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Std Ideal Liq Vol Flow
Heat Flow
Liquid Fraction
Light Liquid Fraction
Heavy Liquid Fraction
Vap Frac on a Mass Basis
Vap Frac on a Volume Basis
Molar Volume
Actual Volume Flow
Power
Actual Gas Flow
Actual Liquid Flow
Liq Vol Flow @Std Cond
Std Gas Flow
Molecular Weight
Mass Density
Std Ideal Liq Mass Density
Molar Density
Average Liquid Density
Liq Mass Density @Std Cond
Molar Heat CapacityMolar Enthalpy
Mass Enthalpy
Molar Entropy
Mass Entropy
Thermal Conductivity
Viscosity
Surface Tension
Specific Gravity rel Air
Watson K
Kinematic Viscosity
Cp/Cv
(C)
(psia)
(lbmole/hr)
(lb/hr)
(barrel/day)
(Btu/hr)
(ft3/lbmole)
(USGPM)
(kW)
(ACFM)
(USGPM)
(barrel/day)
(MMSCFD)
(lb/ft3)
(lb/ft3)
(lbmole/ft3)
(lbmole/ft3)
(API_60)
(Btu/lbmole-F)(Btu/lbmole)
(Btu/lb)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/hr-ft-F)
(cP)
(dyne/cm)
(rel_to_air)
(cSt)
11
0.0000
92.68
43.31
489.1
6.777e+004
6000
-5.923e+007
1.000
1.000
0.0000
0.0000
0.0000
3.108
189.5
-1.736e+004
---
189.5
5958
4.446
138.6
44.59
48.28
0.3218
0.3485
49.79
74.56-1.211e+005
-873.9
57.83
0.4174
5.920e-002
0.5124
16.05
---
11.96
0.7175
1.213
Feed to EA-109
0.2346
149.6
37.31
489.1
6.777e+004
6000
-5.408e+007
0.7654
0.7654
0.0000
0.1435
0.1609
51.22
3123
-1.585e+004
---
170.2
5958
4.446
138.6
2.705
48.28
1.952e-002
0.3485
49.79
80.88-1.106e+005
-798.0
72.58
0.5238
---
---
12.91
---
11.96
---
1.008
Feed to PreFlash
0.3049
155.6
35.31
489.1
6.777e+004
6000
-5.323e+007
0.6951
0.6951
0.0000
0.1939
0.2148
70.17
4279
-1.560e+004
---
160.2
5958
4.446
138.6
1.975
48.28
1.425e-002
0.3485
49.79
80.95-1.088e+005
-785.4
74.88
0.5404
---
---
12.88
---
11.96
---
1.010
22
0.0000
166.0*
17.50
33.76
1.149e+004
890.6
-9.068e+006
1.000
1.000
0.0000
0.0000
0.0000
7.038
29.63
-2658
---
29.63
897.2
0.3069
340.3
48.34
55.14
0.1421
0.1621
29.56
199.4-2.686e+005
-789.3
209.1
0.6146
6.496e-002
1.527
20.57
---
12.03
1.972
1.202
23
0.0000
166.0*
17.50*
33.76*
1.149e+004
890.6
-9.068e+006
1.000
1.000
0.0000
0.0000
0.0000
7.038
29.63
-2658
---
29.63
897.2
0.3069
340.3
48.34
55.14
0.1421
0.1621
29.56
199.4-2.686e+005
-789.3
209.1
0.6146
6.496e-002
1.527
20.57
---
12.03
1.972
1.202
Aspen Technology Inc. Aspen HYSYS Version 7.3 (25.0.0.7336) Page 3 of 8
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
3738
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
-
7/23/2019 HMB for Preheat Train
4/8
LEGENDS
Burlington, MA
USA
Case Name: REFINERY ON PRESSURE SPECS.HSC
Unit Set: Refinery1
Date/Time: Tue Sep 08 10:25:24 2015
Workbook: PREHEAT TRAIN (TPL1) (continued)
Material Streams (continued) Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Std Ideal Liq Vol Flow
Heat Flow
Liquid Fraction
Light Liquid Fraction
Heavy Liquid Fraction
Vap Frac on a Mass Basis
Vap Frac on a Volume Basis
Molar Volume
Actual Volume Flow
Power
Actual Gas Flow
Actual Liquid Flow
Liq Vol Flow @Std Cond
Std Gas Flow
Molecular Weight
Mass Density
Std Ideal Liq Mass Density
Molar Density
Average Liquid Density
Liq Mass Density @Std Cond
Molar Heat CapacityMolar Enthalpy
Mass Enthalpy
Molar Entropy
Mass Entropy
Thermal Conductivity
Viscosity
Surface Tension
Specific Gravity rel Air
Watson K
Kinematic Viscosity
Cp/Cv
(C)
(psia)
(lbmole/hr)
(lb/hr)
(barrel/day)
(Btu/hr)
(ft3/lbmole)
(USGPM)
(kW)
(ACFM)
(USGPM)
(barrel/day)
(MMSCFD)
(lb/ft3)
(lb/ft3)
(lbmole/ft3)
(lbmole/ft3)
(API_60)
(Btu/lbmole-F)(Btu/lbmole)
(Btu/lb)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/hr-ft-F)
(cP)
(dyne/cm)
(rel_to_air)
(cSt)
HSD to EA-103
0.0000
162.0*
17.70*
81.10*
1.686e+004
1409
-1.340e+007
1.000
1.000
0.0000
0.0000
0.0000
4.680
47.32
-3927
---
47.32
1408
0.7372
207.9
44.42
51.13
0.2137
0.2460
40.77
123.2-1.652e+005
-794.9
112.9
0.5431
6.121e-002
0.4384
16.57
---
12.03
0.6162
1.172
HSD Rundown
0.0000
48.00*
27.56*
81.10
1.686e+004
1409
-1.525e+007
1.000
0.9958
4.177e-003
0.0000
0.0000
4.181
42.27
-4469
---
42.27
1408
0.7372
207.9
49.72
51.13
0.2392
0.2460
40.77
98.45-1.880e+005
-904.6
79.30
0.3815
6.865e-002
2.094
---
---
12.03
2.630
1.179
diesel minors to EA-1
0.9087
168.0*
17.88
448.4
4.542e+004
3985
-4.421e+007
9.128e-002
9.128e-002
0.0000
0.8656
0.8651
420.5
2.351e+004
-1.296e+004
---
18.62
3895
4.076
101.3
0.2409
48.73
2.378e-003
0.4810
45.33
53.89-9.859e+004
-973.2
74.19
0.7324
---
---
12.72
---
12.04
---
1.039
35
0.0000
76.00*
15.70
81.10
1.686e+004
1409
-1.483e+007
1.000
0.9982
1.820e-003
0.0000
0.0000
4.289
43.37
-4347
---
43.37
1408
0.7372
207.9
48.46
51.13
0.2331
0.2460
40.77
104.6-1.829e+005
-879.9
87.85
0.4226
6.703e-002
1.279
---
---
12.03
1.648
1.183
Feed to EA-103
0.0000
79.49
45.31
489.1
6.777e+004
6000
-6.008e+007
1.000
1.000
0.0000
0.0000
0.0000
3.058
186.5
-1.761e+004
---
186.5
5958
4.446
138.6
45.31
48.28
0.3270
0.3485
49.79
72.48-1.228e+005
-886.5
55.13
0.3979
6.049e-002
0.5934
17.20
---
11.96
0.8177
1.215
Aspen Technology Inc. Aspen HYSYS Version 7.3 (25.0.0.7336) Page 4 of 8
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
3738
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
-
7/23/2019 HMB for Preheat Train
5/8
LEGENDS
Burlington, MA
USA
Case Name: REFINERY ON PRESSURE SPECS.HSC
Unit Set: Refinery1
Date/Time: Tue Sep 08 10:25:24 2015
Workbook: PREHEAT TRAIN (TPL1) (continued)
Material Streams (continued) Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Std Ideal Liq Vol Flow
Heat Flow
Liquid Fraction
Light Liquid Fraction
Heavy Liquid Fraction
Vap Frac on a Mass Basis
Vap Frac on a Volume Basis
Molar Volume
Actual Volume Flow
Power
Actual Gas Flow
Actual Liquid Flow
Liq Vol Flow @Std Cond
Std Gas Flow
Molecular Weight
Mass Density
Std Ideal Liq Mass Density
Molar Density
Average Liquid Density
Liq Mass Density @Std Cond
Molar Heat CapacityMolar Enthalpy
Mass Enthalpy
Molar Entropy
Mass Entropy
Thermal Conductivity
Viscosity
Surface Tension
Specific Gravity rel Air
Watson K
Kinematic Viscosity
Cp/Cv
(C)
(psia)
(lbmole/hr)
(lb/hr)
(barrel/day)
(Btu/hr)
(ft3/lbmole)
(USGPM)
(kW)
(ACFM)
(USGPM)
(barrel/day)
(MMSCFD)
(lb/ft3)
(lb/ft3)
(lbmole/ft3)
(lbmole/ft3)
(API_60)
(Btu/lbmole-F)(Btu/lbmole)
(Btu/lb)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/hr-ft-F)
(cP)
(dyne/cm)
(rel_to_air)
(cSt)
1
0.0000
98.00*
17.00*
448.4
4.542e+004
3985
-5.440e+007
1.000
0.6831
0.3169
0.0000
0.0000
2.265
126.7
-1.594e+004
---
126.7
3895
4.076
101.3
44.72
48.73
0.4414
0.4810
45.33
57.81-1.213e+005
-1198
42.77
0.4223
6.711e-002
0.4654
---
---
12.04
0.6497
1.196
4
1.0000
98.00
17.00
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
0.0000
1.0000
1.0000
416.8
0.0000
0.0000
0.0000
---
0.0000
0.0000
32.19
7.724e-002
53.75
2.399e-003
1.670
21.19
14.58-1.020e+005
-3170
47.21
1.467
1.271e-002
1.007e-002
---
1.111
12.05
8.139
1.165
5
0.0000
98.00
17.00
306.3
4.287e+004
3809
-3.727e+007
1.000
1.000
0.0000
0.0000
0.0000
3.175
121.3
-1.092e+004
---
121.3
3804
2.784
139.9
44.07
48.10
0.3149
0.3438
51.53
75.86-1.217e+005
-869.4
54.77
0.3914
6.281e-002
0.3994
17.94
---
12.04
0.5657
1.209
7
0.0000
98.00
17.00
142.1
2560
175.6
-1.714e+007
1.000
0.0000
1.000
0.0000
0.0000
0.3039
5.384
-5022
---
5.384
172.7
1.292
18.02
59.28
62.30
3.291
3.458
7.655
18.90-1.206e+005
-6694
16.91
0.9389
0.3928
0.2849
58.98
---
12.05
0.3001
1.175
Kerosene
0.0000
101.7
17.88
116.3
1.627e+004
1446
-1.409e+007
1.000
1.000
0.0000
0.0000
0.0000
3.186
46.22
-4130
---
46.22
1444
1.058
139.8
43.88
48.10
0.3138
0.3440
51.52
76.39-1.211e+005
-866.3
55.51
0.3970
6.271e-002
0.3853
17.67
---
12.04
0.5481
1.208
Aspen Technology Inc. Aspen HYSYS Version 7.3 (25.0.0.7336) Page 5 of 8
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
3738
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
-
7/23/2019 HMB for Preheat Train
6/8
LEGENDS
Burlington, MA
USA
Case Name: REFINERY ON PRESSURE SPECS.HSC
Unit Set: Refinery1
Date/Time: Tue Sep 08 10:25:24 2015
Workbook: PREHEAT TRAIN (TPL1) (continued)
Material Streams (continued) Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Std Ideal Liq Vol Flow
Heat Flow
Liquid Fraction
Light Liquid Fraction
Heavy Liquid Fraction
Vap Frac on a Mass Basis
Vap Frac on a Volume Basis
Molar Volume
Actual Volume Flow
Power
Actual Gas Flow
Actual Liquid Flow
Liq Vol Flow @Std Cond
Std Gas Flow
Molecular Weight
Mass Density
Std Ideal Liq Mass Density
Molar Density
Average Liquid Density
Liq Mass Density @Std Cond
Molar Heat CapacityMolar Enthalpy
Mass Enthalpy
Molar Entropy
Mass Entropy
Thermal Conductivity
Viscosity
Surface Tension
Specific Gravity rel Air
Watson K
Kinematic Viscosity
Cp/Cv
(C)
(psia)
(lbmole/hr)
(lb/hr)
(barrel/day)
(Btu/hr)
(ft3/lbmole)
(USGPM)
(kW)
(ACFM)
(USGPM)
(barrel/day)
(MMSCFD)
(lb/ft3)
(lb/ft3)
(lbmole/ft3)
(lbmole/ft3)
(API_60)
(Btu/lbmole-F)(Btu/lbmole)
(Btu/lb)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/hr-ft-F)
(cP)
(dyne/cm)
(rel_to_air)
(cSt)
Naptha
0.0122
71.71
19.20
231.4
2.143e+004
2058
-1.942e+007
0.9878
0.9878
0.0000
0.0093
0.0100
6.296
181.6
-5692
---
63.86
2050
2.104
92.63
14.71
44.52
0.1588
0.4806
65.75
49.93-8.393e+004
-906.1
26.94
0.2909
---
---
14.98
---
12.12
---
1.001
3
0.0000
42.00*
17.20
231.4
2.143e+004
2058
-2.005e+007
1.000
0.9994
6.000e-004
0.0000
0.0000
2.145
61.89
-5876
---
61.89
2050
2.104
92.63
43.18
44.52
0.4662
0.4806
65.75
46.48-8.664e+004
-935.4
22.39
0.2417
6.156e-002
0.3470
---
---
12.12
0.5017
1.287
8
0.9088
168.0*
17.88*
448.4*
4.542e+004
3985
-4.421e+007
9.123e-002
9.123e-002
0.0000
0.8657
0.8652
420.5
2.351e+004
-1.296e+004
---
18.61
3895
4.076
101.3
0.2409
48.73
2.378e-003
0.4810
45.33
53.89-9.858e+004
-973.2
74.20
0.7324
---
---
12.72
---
12.04
---
1.039
Cold Fractionater Ovh
0.6017
145.0*
15.88
448.4
4.542e+004
3985
-4.760e+007
0.3983
0.3983
0.0000
0.4326
0.4277
301.6
1.686e+004
-1.395e+004
---
76.84
3895
4.076
101.3
0.3359
48.73
3.316e-003
0.4810
45.33
55.78-1.062e+005
-1048
64.59
0.6376
---
---
14.22
---
12.04
---
1.024
12
0.0000
162.0*
17.70
81.10
1.686e+004
1409
-1.340e+007
1.000
1.000
0.0000
0.0000
0.0000
4.680
47.32
-3927
---
47.32
1408
0.7372
207.9
44.42
51.13
0.2137
0.2460
40.77
123.2-1.652e+005
-794.9
112.9
0.5431
6.121e-002
0.4384
16.57
---
12.03
0.6162
1.172
Aspen Technology Inc. Aspen HYSYS Version 7.3 (25.0.0.7336) Page 6 of 8
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
3738
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
-
7/23/2019 HMB for Preheat Train
7/8
LEGENDS
Burlington, MA
USA
Case Name: REFINERY ON PRESSURE SPECS.HSC
Unit Set: Refinery1
Date/Time: Tue Sep 08 10:25:24 2015
Workbook: PREHEAT TRAIN (TPL1) (continued)
Material Streams (continued) Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Std Ideal Liq Vol Flow
Heat Flow
Liquid Fraction
Light Liquid Fraction
Heavy Liquid Fraction
Vap Frac on a Mass Basis
Vap Frac on a Volume Basis
Molar Volume
Actual Volume Flow
Power
Actual Gas Flow
Actual Liquid Flow
Liq Vol Flow @Std Cond
Std Gas Flow
Molecular Weight
Mass Density
Std Ideal Liq Mass Density
Molar Density
Average Liquid Density
Liq Mass Density @Std Cond
Molar Heat CapacityMolar Enthalpy
Mass Enthalpy
Molar Entropy
Mass Entropy
Thermal Conductivity
Viscosity
Surface Tension
Specific Gravity rel Air
Watson K
Kinematic Viscosity
Cp/Cv
(C)
(psia)
(lbmole/hr)
(lb/hr)
(barrel/day)
(Btu/hr)
(ft3/lbmole)
(USGPM)
(kW)
(ACFM)
(USGPM)
(barrel/day)
(MMSCFD)
(lb/ft3)
(lb/ft3)
(lbmole/ft3)
(lbmole/ft3)
(API_60)
(Btu/lbmole-F)(Btu/lbmole)
(Btu/lb)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/hr-ft-F)
(cP)
(dyne/cm)
(rel_to_air)
(cSt)
Cold FO
0.0000
91.00*
16.50
33.76
1.149e+004
890.6
-9.921e+006
1.000
0.9997
2.651e-004
0.0000
0.0000
6.598
27.78
-2908
---
27.78
897.2
0.3069
340.3
51.57
55.14
0.1516
0.1621
29.56
174.7-2.938e+005
-863.6
174.1
0.5117
7.058e-002
5.364
---
---
12.03
6.494
1.194
2
0.0000
42.00*
16.88
116.3
1.627e+004
1446
-1.500e+007
1.000
0.9927
7.323e-003
0.0000
0.0000
2.984
43.28
-4397
---
43.28
1444
1.058
139.8
46.86
48.10
0.3351
0.3440
51.52
67.00-1.290e+005
-922.2
42.93
0.3070
6.561e-002
0.7553
---
---
12.04
1.006
1.221
Kero Water
0.0000
35.00*
35.00*
857.7
1.545e+004
1060
-1.053e+008
1.000
0.0000
1.000
0.0000
0.0000
0.2886
30.86
-3.085e+004
---
30.86
1043
7.797
18.02
62.42
62.30
3.465
3.458
7.655
18.56-1.227e+005
-6812
13.44
0.7460
0.3612
0.7185
70.36
---
---
0.7186
1.153
14
0.0000
42.78*
35.00
857.7
1.545e+004
1060
-1.050e+008
1.000
0.0000
1.000
0.0000
0.0000
0.2904
31.05
-3.078e+004
---
31.05
1043
7.797
18.02
62.05
62.30
3.444
3.458
7.655
18.57-1.225e+005
-6798
13.90
0.7717
0.3668
0.6184
69.01
---
---
0.6222
1.157
HSD Water
0.0000
35.00*
35.00*
1252
2.255e+004
1547
-1.536e+008
1.000
0.0000
1.000
0.0000
0.0000
0.2886
45.04
-4.501e+004
---
45.04
1521
11.38
18.02
62.42
62.30
3.465
3.458
7.655
18.56-1.227e+005
-6812
13.44
0.7460
0.3612
0.7185
70.36
---
---
0.7186
1.153
Aspen Technology Inc. Aspen HYSYS Version 7.3 (25.0.0.7336) Page 7 of 8
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
3738
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS
-
7/23/2019 HMB for Preheat Train
8/8
LEGENDS
Burlington, MA
USA
Case Name: REFINERY ON PRESSURE SPECS.HSC
Unit Set: Refinery1
Date/Time: Tue Sep 08 10:25:24 2015
Workbook: PREHEAT TRAIN (TPL1) (continued)
Material Streams (continued) Fluid Pkg: All
Name
Vapour Fraction
Temperature
Pressure
Molar Flow
Mass Flow
Std Ideal Liq Vol Flow
Heat Flow
Liquid Fraction
Light Liquid Fraction
Heavy Liquid Fraction
Vap Frac on a Mass Basis
Vap Frac on a Volume Basis
Molar Volume
Actual Volume Flow
Power
Actual Gas Flow
Actual Liquid Flow
Liq Vol Flow @Std Cond
Std Gas Flow
Molecular Weight
Mass Density
Std Ideal Liq Mass Density
Molar Density
Average Liquid Density
Liq Mass Density @Std Cond
Molar Heat CapacityMolar Enthalpy
Mass Enthalpy
Molar Entropy
Mass Entropy
Thermal Conductivity
Viscosity
Surface Tension
Specific Gravity rel Air
Watson K
Kinematic Viscosity
Cp/Cv
(C)
(psia)
(lbmole/hr)
(lb/hr)
(barrel/day)
(Btu/hr)
(ft3/lbmole)
(USGPM)
(kW)
(ACFM)
(USGPM)
(barrel/day)
(MMSCFD)
(lb/ft3)
(lb/ft3)
(lbmole/ft3)
(lbmole/ft3)
(API_60)
(Btu/lbmole-F)(Btu/lbmole)
(Btu/lb)
(Btu/lbmole-F)
(Btu/lb-F)
(Btu/hr-ft-F)
(cP)
(dyne/cm)
(rel_to_air)
(cSt)
16
0.0000
45.00*
35.00
1252
2.255e+004
1547
-1.532e+008
1.000
0.0000
1.000
0.0000
0.0000
0.2909
45.39
-4.489e+004
---
45.39
1521
11.38
18.02
61.94
62.30
3.438
3.458
7.655
18.58-1.224e+005
-6793
14.03
0.7789
0.3684
0.5939
68.62
---
---
0.5986
1.158
Nap Water
0.0000
35.00*
35.00*
2685
4.837e+004
3319
-3.295e+008
1.000
0.0000
1.000
0.0000
0.0000
0.2886
96.63
-9.657e+004
---
96.63
3264
24.41
18.02
62.42
62.30
3.465
3.458
7.655
18.56-1.227e+005
-6812
13.44
0.7460
0.3612
0.7185
70.36
---
---
0.7186
1.153
19
0.0000
50.00*
16.50
33.76
1.149e+004
890.6
-1.034e+007
1.000
0.9952
4.803e-003
0.0000
0.0000
6.383
26.87
-3031
---
26.87
897.2
0.3069
340.3
53.30
55.14
0.1567
0.1621
29.56
160.7-3.063e+005
-900.2
154.0
0.4526
7.295e-002
11.07
---
---
12.03
12.97
1.170
FO Water
0.0000
35.00*
35.00*
1048
1.887e+004
1295
-1.286e+008
1.000
0.0000
1.000
0.0000
0.0000
0.2886
37.70
-3.768e+004
---
37.70
1273
9.523
18.02
62.42
62.30
3.465
3.458
7.655
18.56-1.227e+005
-6812
13.44
0.7460
0.3612
0.7185
70.36
---
---
0.7186
1.153
21
0.0000
47.00*
35.00
1048
1.887e+004
1295
-1.281e+008
1.000
0.0000
1.000
0.0000
0.0000
0.2913
38.05
-3.755e+004
---
38.05
1273
9.523
18.02
61.84
62.30
3.433
3.458
7.655
18.58-1.223e+005
-6790
14.15
0.7854
0.3697
0.5731
68.26
---
---
0.5786
1.159
Aspen Technology Inc. Aspen HYSYS Version 7.3 (25.0.0.7336) Page 8 of 8
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
3738
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
* Specified by user.Licensed to: LEGENDS