Company Name Not Available Bedford, MA USA Case Name: 21Unit 232,223-Case High H2S-Bubble Cap.hsc Unit Set: Project
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Company Name Not Available Bedford, MA USA
Case Name:
21Unit 232,223-Case High H2S-Bubble Cap.hsc
Unit Set:
Project JTB1
Date/Time:
Fri Sep 06 10:09:27 2019
Heat Exchanger: 232-E9003 CONNECTIONS Tube Side
Shell Side
Inlet
Outlet
Name
585
From Op.
232-T9001
Op. Type
Tower
Temp
352.50 F
Inlet
Name To Op. Op. Type Temp
Outlet
ToSump
Name
Stage 21
From Op.
MP Steam @Main
Separator
Op. Type
Material Stream
368.72 F
MP Steam
Temp
Name
MP Steam Condensate
To Op.MP Steam Condensate @Main Op. Type
500.00 F
Material Stream
Temp
490.69 F
PARAMETERS Heat Exchanger Model:
Calculated By the Column
Tube Side DeltaP:
0.0000 psi
UA:
3.169e+004 Btu/F-hr
Shell Side DeltaP:
0.0000 psi
Tolerance:
Passes:
---
1.0000e-04
Tube Side Data
Shell Side Data
Heat Transfer Coeff
---
Heat Transfer Coeff
---
Tube Pressure Drop
0.00 psi
Shell Pressure Drop
0.00 psi
Fouling
0.00000 C-h-m2/kJ
Tube Length
19.69 ft
Tube O.D. Tube Thickness
1
20.00 mm
Shell Series
1
2.0000 mm
Shell Parallel
50.0000 mm
Orientation
Horizontal
Passes Per Shell
2 160
Layout Angle
Triangular (30 degrees)
TEMA Type
0.00000 C-h-m2/kJ
Shell Passes
Tube Pitch
Tubes Per Shell
Fouling
AE L
1
Baffle Type
Single
Baffle Cut(%Area)
20.00
Baffle Orientation
Horizontal
Spacing
800.0000 mm
Diameter
739.0488 mm
Area
649.26 ft2
SPECS Spec Value Reboiler Heat Balance
Active
Estimate
0.0000 MMBtu/hr
2.498e-004 MMBtu/hr
5.516e-005
On
Off
---
3.169e+004 Btu/F-hr
---
Off
Off
Reboiler UA
Curr Value
Rel Error
Detailed Specifications Reboiler Heat Balance Type:
Duty
Pass:
Error
Spec Value:
0.0000 MMBtu/hr
Spec Value:
---
Reboiler UA Type:
UA
Pass:
Overall
User Variables RATING Sizing Overall Data Configuration # of Shells in Series
1
Tube Passes per Shell
# of Shells in Parallel
1
Exchange Orientation
TEMA Type:
2 Horizontal
A
Elevation (Base)
0.0000 ft
First Tube Pass Flow Direction E
Counter L
Calculated Information Shell HT Coeff
---
Overall U
48.81 Btu/hr-ft2-F
Shell DP
0.0000 psi
Shell Vol per Shell
80.24 ft3
HT Area per Shell
649.3 ft2
Tube HT Coeff
---
Overall UA
3.169e+004 Btu/F-hr
Tube DP
0.0000 psi
Tube Vol per Shell
6.816 ft3
Shell Data Shell and Tube Bundle Shell Diameter (mm)
Aspen Technology Inc. Licensed to: Company Name Not Available
739.0
Tube Pitch (mm)
50.00
Aspen HYSYS Version 8.8 (34.0.0.8909)
Shell Fouling (C-h-m2/kJ)
0.0000
Page 1 of 6
Company Name Not Available Bedford, MA USA
Case Name:
21Unit 232,223-Case High H2S-Bubble Cap.hsc
Unit Set:
Project JTB1
Date/Time:
Fri Sep 06 10:09:27 2019
Heat Exchanger: 232-E9003 (continued) # of Tubes per Shell
160
Tube Layout Angle
Triangular (30 degrees) Shell Baffles
Shell Baffle Type
Single
Shell Baffle Orientation
Horizontal
Baffle Cut (%Area)
20.00
Baffle Spacing
800.0 mm
Tube Data Dimensions OD (mm)
ID (mm)
20.00
16.00
Tube Thickness (mm)
2.000
Tube Length (ft)
19.69
---
Wall Density (lb/ft3)
---
Tube Properties Tube Fouling (C-h-m2/kJ)
Thermal Cond. (Btu/hr-ft-F)
0.0000
26.00
Wall Cp (Btu/lb-F)
Nozzle Parameters Base Elevation Relative to Ground Level
0.0000 ft 585
MP Steam
ToSump
Diameter
(ft)
0.1640
0.1640
0.1640
Elevation (Base)
(ft)
0.0000
0.0000
0.0000
Elevation (Ground)
(ft)
0.0000
0.0000
0.0000
(%)
0.00
0.00
0.00
Elevation (% of Height)
MP Steam Condensate Diameter
(ft)
0.1640
Elevation (Base)
(ft)
0.0000
Elevation (Ground)
(ft)
0.0000
(%)
0.00
Elevation (% of Height)
CONDITIONS Name
585
MP Steam
ToSump
0.0000
1.0000
0.5639
0.2346
(F)
352.4960
500.0000
368.7211
490.6933 600.0000
Vapour Temperature Pressure
MP Steam Condensate
(psig)
92.4400
600.0000
92.4400
Molar Flow
(MMSCFD)
6.1439
4.0000
6.1439
4.0000
Mass Flow
(lb/hr)
64797.0778
7912.5703
64797.0778
7912.5703
Std Ideal Liq Vol Flow
(barrel/day)
5878.5401
542.8894
5878.5401
542.8894
Molar Enthalpy
(kJ/kgmole)
-9.189e+004
-2.357e+005
-7.627e+004
-2.597e+005
Molar Entropy
(Btu/lbmole-F)
25.38
38.24
33.67
27.40
(MMBtu/hr)
-2.6651e+01
-4.4503e+01
-2.2123e+01
-4.9031e+01
Heat Flow
PROPERTIES Name
585
Molecular Weight
MP Steam
ToSump
MP Steam Condensate
96.05
18.02
96.05
18.02
0.3852
7.019e-002
2.433e-002
0.2801
Molar Density
(lbmole/ft3)
Mass Density
(lb/ft3)
37.00
1.265
2.337
5.046
Act. Volume Flow
(ft3/s)
0.4864
1.738
7.702
0.4356
Mass Enthalpy
(Btu/lb)
-411.3
-5624
-341.4
-6197
Mass Entropy
(Btu/lb-F)
0.2643
2.123
0.3506
1.521
Heat Capacity
(Btu/lbmole-F)
63.03
10.38
56.04
20.82
(Btu/lb-F)
0.6562
0.5764
0.5834
1.156
LHV Molar Basis (Std)
(Btu/MMSCF)
4.711e+009
0.0000
4.711e+009
0.0000
HHV Molar Basis (Std)
(Btu/MMSCF)
5.003e+009
4.646e+007
5.003e+009
4.646e+007
HHV Mass Basis (Std)
(Btu/lb)
1.977e+004
978.7
1.977e+004
978.7
---
---
---
-----
Mass Heat Capacity
CO2 Loading CO2 Apparent Mole Conc.
(lbmole/ft3)
1.727e-013
---
---
CO2 Apparent Wt. Conc.
(kgmol/kg)
4.668e-015
---
---
---
(Btu/lb)
1.861e+004
0.0000
1.861e+004
0.0000
LHV Mass Basis (Std) Phase Fraction [Vol. Basis]
---
1.000
0.5289
0.2346
Phase Fraction [Mass Basis]
0.0000
1.000
0.5245
0.2346
Phase Fraction [Act. Vol. Basis]
0.0000
1.000
0.9702
0.9216
(Btu/lb)
30.87
449.1
54.43
200.0
(psig)
-14.70
-14.70
-14.70
-14.70
0.0000
0.0000
0.0000
0.0000
Mass Exergy Partial Pressure of CO2 Cost Based on Flow
(Cost/s)
Aspen Technology Inc. Licensed to: Company Name Not Available
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 2 of 6
Company Name Not Available Bedford, MA USA
Case Name:
21Unit 232,223-Case High H2S-Bubble Cap.hsc
Unit Set:
Project JTB1
Date/Time:
Fri Sep 06 10:09:27 2019
Heat Exchanger: 232-E9003 (continued) PROPERTIES Name
585
Act. Gas Flow
MP Steam
ToSump
MP Steam Condensate
(ACT_m3/h)
---
177.2
761.7
40.92
(lbmole/ft3)
0.4906
3.458
0.4906
3.458
(Btu/lbmole-F)
63.03
10.38
56.04
20.82
(STD_m3/h)
7235
4711
7235
4711
(kg/m3)
754.8
998.0
754.8
998.0
(ft3/s)
0.4864
---
0.2295
3.417e-002
---
0.8503
---
---
11.60
---
11.60
---
---
---
---
---
-14.70
-14.70
-14.70
-14.70
Cp/(Cp - R)
1.033
1.236
1.037
1.105
Cp/Cv
1.033
1.540
1.039
1.048
(Btu/MSCF)
4.013e+004
3.517e+004
4.013e+004
3.517e+004
(cSt)
0.2212
0.8861
---
---
(kg/m3)
764.1
1015
764.1
1015
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
(psig)
Heat of Vap. Kinematic Viscosity
Liq. Mass Density (Std. Cond) Liq. Vol. Flow (Std. Cond)
5807
533.9
5807
533.9
1.000
0.0000
0.4361
0.7654
(ft3/lbmole)
2.596
14.25
41.10
3.570
(Btu/lb)
158.5
740.7
158.5
740.7
0.0000
1.0000
0.5639
0.2346
(barrel/day)
Liquid Fraction Molar Volume Mass Heat of Vap. Phase Fraction [Molar Basis] Surface Tension
(lbf/ft)
5.407e-004
---
5.610e-004
1.712e-003
(Btu/hr-ft-F)
4.236e-002
2.898e-002
---
---
(cP)
0.1311
1.795e-002
---
---
(Btu/lbmole-F)
61.05
8.399
54.05
18.84
Thermal Conductivity Viscosity Cv (Semi-Ideal) Mass Cv (Semi-Ideal) Cv
(Btu/lb-F)
0.6356
0.4662
0.5628
1.046
(Btu/lbmole-F)
61.05
6.742
53.92
19.87
(Btu/lb-F)
0.6356
0.3742
0.5613
1.103
(Btu/lbmole-F)
---
---
---
---
(Btu/lb-F)
---
---
---
---
---
---
---
-----
Mass Cv Cv (Ent. Method) Mass Cv (Ent. Method) Cp/Cv (Ent. Method) Reid VP at 37.8 C
(psig)
-8.349
---
-8.349
True VP at 37.8 C
(psig)
-8.083
---
-8.083
---
Liq. Vol. Flow - Sum(Std. Cond)
(ft3/s)
0.3773
3.469e-002
0.3775
3.469e-002
-45.22
---
-55.39
---
Viscosity Index
DETAILS Overall/Detailed Performance Duty:
4.529e+00 MMBtu/hr
UA Curv. Error:
0.00e-01 Btu/F-hr
Heat Leak:
---
Hot Pinch Temp:
500.0 F
Heat Loss:
---
Cold Pinch Temp:
368.7 F
UA:
3.169e+04 Btu/F-hr
Min. Approach:
131.3 F
Lmtd:
142.9 F
Ft Factor:
---
Uncorrected Lmtd:
143.3 F
TABLES Shell Side - Overall Phase Temperature (F)
Pressure (psig)
Heat Flow (MMBtu/hr)
Enthalpy (kJ/kgmole)
490.69
600.00
0.00
500.00
600.00
4.53
UA (Btu/F-hr)
Molar Vap Frac
Mass Vap Frac
-259654.90 -235673.76 Heat of Vap. (Btu/MSCF)
0.00
0.2346
0.2346
---
0.00
1.0000
1.0000
---
Aspen Technology Inc. Licensed to: Company Name Not Available
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 3 of 6
Company Name Not Available Bedford, MA USA
Case Name:
21Unit 232,223-Case High H2S-Bubble Cap.hsc
Unit Set:
Project JTB1
Date/Time:
Fri Sep 06 10:09:27 2019
Heat Exchanger: 232-E9003 (continued) Shell Side - Vapour Phase Mass Flow (lb/hr)
Molecular Wt
Density (lb/ft3)
Mass Sp Heat (Btu/lb-F)
Viscosity (cP)
Thermal Cond (Btu/hr-ft-F)
1856.53
18.02
1.28
0.58
0.02
7912.57
18.02
1.26
0.58
0.02
Std Gas Flow (STD_m3/h)
Z Factor
Pseudo Pc (psig)
Pseudo Tc (F)
Pseudo Zc
0.03 0.03 Pseudo Omega
1105.26
0.85
3193.54
705.47
0.26
0.34
4710.64
0.85
3193.54
705.47
0.26
0.34
Shell Side - Light Liquid Phase Mass Flow (lb/hr)
Density (lb/ft3)
Mass Sp Heat (Btu/lb-F)
Viscosity (cP)
Thermal Cond (Btu/hr-ft-F)
Surface Tens (lbf/ft)
---
---
---
---
---
---
---
---
---
---
Molecular Wt
Sp Gravity
Pseudo Pc (psig)
Pseudo Tc (F)
Pseudo Zc
----Pseudo Omega
---
---
---
---
---
---
---
---
---
---
---
---
Shell Side - Heavy Liquid Phase Mass Flow (lb/hr)
Density (lb/ft3)
Mass Sp Heat (Btu/lb-F)
Viscosity (cP)
Thermal Cond (Btu/hr-ft-F)
Surface Tens (lbf/ft)
6056.04
49.23
1.33
0.11
0.35
---
---
---
---
---
Molecular Wt
Sp Gravity
Pseudo Pc (psig)
Pseudo Tc (F)
Pseudo Zc
0.00 --Pseudo Omega
18.02
0.79
3193.54
705.47
0.26
0.34
---
---
---
---
---
---
Shell Side - Mixed Liquid Mass Flow (lb/hr)
Density (lb/ft3)
Mass Sp Heat (Btu/lb-F)
Viscosity (cP)
Thermal Cond (Btu/hr-ft-F)
Surface Tens (lbf/ft)
6056.04
49.23
1.33
0.11
0.35
---
---
---
---
---
Molecular Wt
Sp Gravity
Pseudo Pc (psig)
Pseudo Tc (F)
Pseudo Zc
----Pseudo Omega
18.02
0.79
3193.54
705.47
0.26
0.34
---
---
---
---
---
---
Tube Side - Overall Phase Temperature (F)
Pressure (psig)
Heat Flow (MMBtu/hr)
Enthalpy (kJ/kgmole)
334.74
92.44
0.00
368.72
92.44
4.53
UA (Btu/F-hr)
Molar Vap Frac
-91886.83 -76274.66
Mass Vap Frac
Heat of Vap. (Btu/MSCF)
0.00
0.1160
0.0988
---
0.00
0.5638
0.5245
---
Tube Side - Vapour Phase Mass Flow (lb/hr)
Molecular Wt
Density (lb/ft3)
Mass Sp Heat (Btu/lb-F)
Viscosity (cP)
Thermal Cond (Btu/hr-ft-F)
6403.10
81.83
1.19
0.50
0.01
33984.42
89.34
1.26
0.52
0.01
Std Gas Flow (STD_m3/h)
Z Factor
Pseudo Pc (psig)
Pseudo Tc (F)
Pseudo Zc
839.16
0.86
536.12
475.76
0.27
0.85
519.09
518.39
0.27
Licensed to: Company Name Not Available
Aspen HYSYS Version 8.8 (34.0.0.8909)
0.02 Pseudo Omega
4079.47
Aspen Technology Inc.
0.01
0.25 0.28
Page 4 of 6
Company Name Not Available Bedford, MA USA
Case Name:
21Unit 232,223-Case High H2S-Bubble Cap.hsc
Unit Set:
Project JTB1
Date/Time:
Fri Sep 06 10:09:27 2019
Heat Exchanger: 232-E9003 (continued) Tube Side - Light Liquid Phase Mass Flow (lb/hr)
Density (lb/ft3)
Mass Sp Heat (Btu/lb-F)
Viscosity (cP)
Thermal Cond (Btu/hr-ft-F)
Surface Tens (lbf/ft)
58394.90
38.13
0.63
0.15
0.05
30813.58
37.29
0.66
0.14
0.05
Molecular Wt
Sp Gravity
Pseudo Pc (psig)
Pseudo Tc (F)
0.00 0.00
Pseudo Zc
Pseudo Omega
97.92
0.61
489.07
552.79
0.27
0.31
104.72
0.60
462.77
576.77
0.26
0.33
Tube Side - Heavy Liquid Phase Mass Flow (lb/hr)
Density (lb/ft3)
Mass Sp Heat (Btu/lb-F)
Viscosity (cP)
Thermal Cond (Btu/hr-ft-F)
Surface Tens (lbf/ft)
---
---
---
---
---
---
---
---
---
---
Molecular Wt
Sp Gravity
Pseudo Pc (psig)
Pseudo Tc (F)
-----
Pseudo Zc
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
---
---
Tube Side - Mixed Liquid Mass Flow (lb/hr)
Density (lb/ft3)
Mass Sp Heat (Btu/lb-F)
Viscosity (cP)
Thermal Cond (Btu/hr-ft-F)
Surface Tens (lbf/ft)
58394.90
38.13
0.63
0.15
0.05
30813.58
37.29
0.66
0.14
0.05
Molecular Wt
Sp Gravity
Pseudo Pc (psig)
Pseudo Tc (F)
-----
Pseudo Zc
Pseudo Omega
97.92
0.61
489.07
552.79
0.27
0.31
104.72
0.60
462.77
576.77
0.26
0.33
---
600.0 Tube Side
Pressure (psig)
500.0
Shell Side
400.0
300.0
200.0
100.0
0.0 320.0
340.0
360.0
380.0
400.0
420.0
440.0
460.0
480.0
500.0
Temperature (F) DYNAMICS Basic Model Model Parameters Aspen Technology Inc. Licensed to: Company Name Not Available
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 5 of 6
Company Name Not Available Bedford, MA USA
Case Name:
21Unit 232,223-Case High H2S-Bubble Cap.hsc
Unit Set:
Project JTB1
Date/Time:
Fri Sep 06 10:09:27 2019
Heat Exchanger: 232-E9003 (continued) Model Parameters Tube Volume
(ft3)
3.531
Shell UA
(lb/hr)
Shell Volume
(ft3)
3.531
Tube UA
(lb/hr)
Elevation
(ft)
0.0000
Minimum Flow Scale Factor
(Btu/F-hr)
3.169e+004
Overall UA
----0.0000
Summary Shell Duty:
---
Tube Duty:
---
Pressure Flow Specifications Shell Side Specification Delta P
(psi)
0.0000
Active
k
lb/s/sqrt(psia-lb/ft3)
---
Not Active
lb/s/sqrt(psia-lb/ft3)
---
Not Active
Tube Side Specifications Delta P
(psi)
0.0000
Active
k
Holdup Shell Holdup Phase
Accumulation (MMSCFD)
Moles (kgmole)
Volume (ft3)
Vapour
0.0000
0.0000
0.0000
Liquid
0.0000
0.0000
0.0000
Aqueous
0.0000
0.0000
0.0000
Total
0.0000
0.0000
0.0000
Tube Holdup Phase
Accumulation (MMSCFD)
Moles (kgmole)
Volume (ft3)
Vapour
0.0000
0.0000
0.0000
Liquid
0.0000
0.0000
0.0000
Aqueous
0.0000
0.0000
0.0000
Total
0.0000
0.0000
0.0000
NOTES
HTFS
Exchanger Design and Rating
Aspen Technology Inc. Licensed to: Company Name Not Available
Aspen HYSYS Version 8.8 (34.0.0.8909)
Page 6 of 6