1

Case Name: NoName.hsc

2 Company Name Not Available
3 Bedford, MA Unit Set: SI
4 USA
Date/Time: Mon Mar 11 00:02:21 2019
5
6
7 Heat Exchanger: E-3711
8
9
10
CONNECTIONS
11
12
Tube Side Shell Side
13 Inlet Outlet Inlet Outlet
14 Name CWS Name CWR Name Inlet Process Name Outlet Process
15 From Op. To Op. From Op. To Op.
16 Op. Type Op. Type Op. Type Op. Type
17 Temp 31.00 C * Temp 36.00 C * Temp 77.00 C * Temp 39.87 C
18
19
PARAMETERS
20
Heat Exchanger Model: Simple End Point
21
22 Tube Side DeltaP: 40.00 kPa Shell Side DeltaP: 20.00 kPa * Passes: ---
23 UA: 1.570e+006 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 40.00 kPa Shell Pressure Drop 20.00 kPa *
27 Fouling 0.00000 C-h-m2/kJ Fouling 0.00000 C-h-m2/kJ
28 Tube Length 9.74 m * Shell Passes 1
29 Tube O.D. 19.05 mm * Shell Series 1
30 Tube Thickness 1.5250 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 2 Baffle Orientation Horizontal
34 Tubes Per Shell 3200 * Spacing 800.0000 mm
35 Layout Angle Triangular (30 degrees) Diameter 1650.0000 mm *
36 TEMA Type AE L Area 1865.32 m2
37
38
CONDITIONS
39 Name CWS Inlet Process CWR Outlet Process
40 Vapour 0.0000 1.0000 0.0000 0.0000
41 Temperature (C) 31.0000 * 77.0000 * 36.0000 * 39.8688
42 Pressure (kPa) 600.0000 * 1700.0000 * 560.0000 * 1680.0000
43 Molar Flow (kgmole/h) 77712.5835 1895.1726 77712.5835 1895.1726
44 Mass Flow (kg/h) 1400000.0000 * 79750.0000 * 1400000.0000 79750.0000
45 Std Ideal Liq Vol Flow (m3/h) 1402.8253 153.0842 1402.8253 153.0842
46 Molar Enthalpy (kJ/kgmole) -2.857e+005 2.246e+004 -2.854e+005 6561
47 Molar Entropy (kJ/kgmole-C) 55.24 74.33 56.51 24.26
48 Heat Flow (kJ/h) -2.2206e+10 4.2574e+07 -2.2176e+10 1.2433e+07
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69 Aspen Technology Inc. Aspen HYSYS Version 10 Page 1 of 1
Licensed to: Company Name Not Available * Specified by user.