56101A BAHX-A17342/5, BAHX-A 2629/4.4 Heat Exchanger
Tag No.：56101A
Model：BAHX-A17342/5, BAHX-A2629/4.4
Name：Heat Exchanger
1. Heat Exchanger 1, BAHX-A17342/5
|
Project number |
|
Project name |
|
Main heat exchanger |
||||||
|
Channel name |
|
Channel 1 Air |
Channel 2 Product Nitrogen |
Channel 3 Waste Nitrogen |
Channel 4 Oxygen |
|
|
|||
|
Total flow |
kg/h |
17342.1 |
7572.49 |
7292.51 |
2397.59 |
|
|
|||
|
Inlet gas phase molar ratio |
% |
100 |
100 |
100 |
100 |
|
|
|||
|
Outlet gas molar ratio |
% |
100 |
100 |
100 |
100 |
|
|
|||
|
Calculate outlet gas phase molar ratio |
% |
100 |
100 |
100 |
100 |
|
|
|||
|
Inlet temperature |
°C |
5 |
-180 |
-179 |
-180.3 |
|
|
|||
|
Output temperature |
°C |
- 116 /- 172 |
3 |
-7.58 |
3 |
|
|
|||
|
Outlet calculated temperature |
°C |
- 116.3 /- 172.3 |
3.2 |
-7.1 |
3.2 |
|
|
|||
|
Operating pressure |
MPa.G |
0.5 |
0.0142 |
0.0183 |
0.0318 |
|
|
|||
|
Resistance allowed |
Bar |
0.4 |
0.05 |
0.05 |
0.05 |
|
|
|||
|
Calculate the resistance (FRICTION) |
Bar |
0.10 |
0.033 |
0.039 |
0.034 |
|
|
|||
|
Log mean temperature difference |
°C |
7.5 |
||||||||
|
Fouling factor |
m2°C/W |
0 |
0 |
0 |
0 |
|
|
|||
|
Design temperature |
°C |
+50/-196 |
+50/-196 |
+50/-196 |
+50/-196 |
|
|
|||
|
Design pressure |
Bar.G |
6 |
6 |
6 |
6 |
|
|
|||
|
Number of units |
1 |
Length: 4000mm Width: 1200mm Height: 1150mm |
||||||||
|
|
|
|||||||||
|
Total heat exchange area |
m2 |
1460 |
1736 |
1426 |
482 |
|
|
|||
|
Inlet diameter |
mm |
DN300 |
DN300 |
DN200 |
DN200 |
|
|
|||
|
Outlet diameter |
mm |
DN150DN250 |
DN400 |
DN300 |
DN200 |
|
|
|||
2. Heat Exchanger 2, BAHX-A2629/4.4
|
Project number |
|
Project name |
|
Sub cooler |
|||||||
|
Channel name |
|
Channel 1 Air |
Channel 2 Dirty Phlegma |
Channel 3 Clean Phlegma |
Channel 4 Product Nitrogen |
Channel 5 Dirty Phlegma |
|
||||
|
Total flow |
Kg/h |
2629.15 |
5676.78 |
4819.66 |
7572.49 |
7292.51 |
|
||||
|
Inlet gas phase molar ratio |
% |
3 |
0 |
0 |
100 |
96 |
|
||||
|
Outlet gas molar ratio |
% |
0 |
0 |
0 |
100 |
100 |
|
||||
|
Calculate outlet gas phase molar ratio |
% |
0 |
0 |
0 |
100 |
100 |
|
||||
|
Inlet temperature |
°C |
-173.8 |
-174.7 |
-178.2 |
-194.1 |
- 189.9 |
|
||||
|
Output temperature |
°C |
-180 |
-185 |
-187 |
-180.1 |
-179 |
|
||||
|
Outlet calculated temperature |
°C |
|
|
|
|
|
|
||||
|
Operating pressure |
MPa.G |
0.4473 |
0.4449 |
0.4373 |
0.0192 |
0.0233 |
|
||||
|
|
|
|
|
|
|
|
|
||||
|
Resistance allowed |
Bar |
0.2 |
0.2 |
0.2 |
0.05 |
0.05 |
|
||||
|
Calculate the resistance (FRICTION) |
Bar |
0.02 |
0.02 |
0.02 |
0.022 |
0.022 |
|
||||
|
Log mean temperature difference |
°C |
6.77 |
|||||||||
|
Fouling factor |
m2 °C/W |
0 |
0 |
0 |
0 |
0 |
|
||||
|
Design temperature |
°C |
+50/-196 |
+50/-196 |
+50/-196 |
+50/-196 |
+50/-196 |
|
||||
|
Design pressure |
Bar.G |
6 |
6 |
6 |
6 |
|
|
||||
|
Number of units |
1 |
Length: 1200mm Width: 800mm Height: 626 mm
|
|||||||||
|
|
|
||||||||||
|
Total heat exchange area |
m2 |
|
|
|
|
|
|
||||
|
Inlet diameter |
mm |
DN50 |
DN50 |
DN50 |
DN300 |
DN250 |
|
||||
|
Outlet diameter |
mm |
DN50 |
DN50 |
DN50 |
DN300 |
DN200 |
|
||||
Product introduction:
Aluminum plate fin heat exchanger is a brazed heat exchanger with fixed aluminum fins in the middle of multi-layer aluminum plates. It has a large heat exchange area in a small volume. It can be widely used in the heat exchange needs of multi stream clean fluids such as cryogenic air separation equipment, chemical equipment and natural gas liquefaction equipment, as well as the heat radiators of automobiles and engineering vehicles.
For more information, please contact us by email sales@wintekgroup.com .
Key Words: Aluminum Plate Fin Heat Exchanger, Brazed Heat Exchanger, Multi Stream Heat Exchanger
