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Case Name: P&ID6_rev.hsc

2 Company Name Not Available
3 Bedford, MA Unit Set: SI10
4 USA
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Date/Time: Wed Mar 20 23:20:49 2024
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Heat Exchanger: E-107
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CONNECTIONS
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Tube Side Shell Side
13 Inlet Outlet Inlet Outlet
14 Name 9 Name 10 Name WAT3 Name WAT4
15 From Op. K-105 To Op. From Op. E-104 To Op.
16 Op. Type Compressor Op. Type Op. Type Heat Exchanger Op. Type
17 Temp 143.72 C Temp 130.00 C * Temp 60.00 C * Temp 104.72 C
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PARAMETERS
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Heat Exchanger Model: Simple End Point
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22 Tube Side DeltaP: 70.00 kPa * Shell Side DeltaP: 70.00 kPa * Passes: ---
23 UA: 1196 kJ/C-h Tolerance: 1.0000e-04
24 Tube Side Data Shell Side Data
25 Heat Transfer Coeff --- Heat Transfer Coeff ---
26 Tube Pressure Drop 70.00 kPa * Shell Pressure Drop 70.00 kPa *
27 Fouling 0.00000 C-h-m2/kJ Fouling 0.00000 C-h-m2/kJ
28 Tube Length 6.00 m Shell Passes 1
29 Tube O.D. 20.00 mm Shell Series 1
30 Tube Thickness 2.0000 mm Shell Parallel 1
31 Tube Pitch 50.0000 mm Baffle Type Single
32 Orientation Horizontal Baffle Cut(%Area) 20.00
33 Passes Per Shell 4* Baffle Orientation Horizontal
34 Tubes Per Shell 160 * Spacing 800.0000 mm
35 Layout Angle Triangular (30 degrees) Diameter 739.0488 mm
36 TEMA Type AE L Area 60.32 m2
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RATING
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Sizing
41 Overall Data
42 Configuration
43 # of Shells in Series 1 Tube Passes per Shell 4* Elevation (Base) 0.0000 m
44 # of Shells in Parallel 1 Exchange Orientation Horizontal First Tube Pass Flow Direction Counter
45 TEMA Type: A E L
46 Calculated Information
47 Shell HT Coeff --- Tube HT Coeff ---
48 Overall U 19.82 kJ/h-m2-C Overall UA 1196 kJ/C-h
49 Shell DP 70.00 kPa * Tube DP 70.00 kPa *
50 Shell Vol per Shell 2.272 m3 Tube Vol per Shell 0.1930 m3
51 HT Area per Shell 60.32 m2
52 Shell Data
53 Shell and Tube Bundle
54 Shell Diameter Tube Pitch Shell Fouling
739.0 50.00 0.0000
55 (mm) (mm) (C-h-m2/kJ)
56 # of Tubes per Shell 160 * Tube Layout Angle Triangular (30 degrees)
57 Shell Baffles
58 Shell Baffle Type Single Shell Baffle Orientation Horizontal
59 Baffle Cut (%Area) 20.00 Baffle Spacing 800.0 mm
60 Tube Data
61 Dimensions
62 OD ID Tube Thickness Tube Length
20.00 16.00 2.000 6.000
63 (mm) (mm) (mm) (m)
64 Tube Properties
65 Tube Fouling Thermal Cond. Wall Cp Wall Density
0.0000 45.00 --- ---
66 (C-h-m2/kJ) (W/m-K) (kJ/kg-C) (kg/m3)
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DETAILS
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Overall/Detailed Performance
71 Duty: 6.094e+04 kJ/h UA Curv. Error: 0.00e-01 kJ/C-h
72 Heat Leak: 0.000e-01 kJ/h Hot Pinch Temp: 143.7 C
73 Heat Loss: 0.000e-01 kJ/h Cold Pinch Temp: 104.7 C
74 UA: 1.196e+03 kJ/C-h Ft Factor: ---
75 Aspen Technology Inc. Aspen HYSYS Version 12.1 Page 1 of 2
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Case Name: P&ID6_rev.hsc
2 Company Name Not Available
3 Bedford, MA Unit Set: SI10
4 USA
5
Date/Time: Wed Mar 20 23:20:49 2024
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Heat Exchanger: E-107 (continued)
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Overall/Detailed Performance
11 Min. Approach: 39.00 C Uncorrected Lmtd: 53.00 C
12 Lmtd: 50.97 C
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75 Aspen Technology Inc. Aspen HYSYS Version 12.1 Page 2 of 2