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Process parameters |
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Project |
Design parameters |
Performance parameters |
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Shell Side
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Tube Side
|
Shell Side
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Tube Side
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MEDIUM |
Fluid name |
Sulfuric Acid
96%
|
Cooling Water
|
Sulfuric Acid
96%
|
Cooling Water
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Temperature (Inlet) ℃ |
69.3
|
33
|
69.3
|
33
|
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Temperature (Outlet)℃ |
50
|
41
|
50
|
40.96
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Liquid Kg/h |
686811
|
|
686811
|
655000
|
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Density(inlet/outlet) Kg/m3 |
1801
|
1000
|
1801
|
1000
|
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Viscosity(inlet/outlet)(cp) |
7.35
|
0.76
|
7.35
|
0.76
|
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Inlet pressure Mpa |
0.54
|
0.3
|
0.54
|
0.3
|
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Pressure drop, Mpa |
≤0.1
|
≤0.1
|
0.049
|
0.032
|
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PERFORMANCE |
Heat exchanged quantity W |
|
~6034912.9
|
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Flow rate m/s |
|
0.514
|
1.717
|
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Heat transfer area affluent coefficient |
|
1.15
|
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Heat transfer coefficient W/m2 ℃ |
|
831.236
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Heat transfer area m2 |
|
399
|
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MATERIAL |
Type |
shell and tube
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The flow form
|
counter-current flow
|
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Sealing form |
welding connection in acid side, flange connection in water side
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Materials and specifications |
shell
|
304L δ= 10
|
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Heat transfer tube
|
316L Φ19×2.0×6000
|
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Tubesheet
|
304L δ= 55
|
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Baffle-crossing
|
304L δ= 10
|
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head
|
Q235-B δ= 12
|
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Flange standard |
Shell Side
|
Tube Side
|
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|
|
HG/T20592-2009(B) PN10 DN 350
|
HG/T20592-2009(B) PN10 DN 400
|
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Size |
Φ1000×7294×1470
|
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Operating weight |
14207 Kg
|
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The scope of supply |
●Complete set ●Control system
●Special cable ●Random accessories |
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