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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
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Shell Side
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Tube Side
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MEDIUM |
Fluid name |
Sulfuric Acid
98.28%
|
Cooling Water
|
Sulfuric Acid
98.28%
|
Cooling Water
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Temperature (Inlet) ℃ |
76.5
|
32
|
76.5
|
32
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Temperature (Outlet)℃ |
40
|
40
|
40
|
36.839
|
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Liquid Kg/h |
20770
|
|
20770
|
55000
|
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Density(inlet/outlet) Kg/m3 |
1783.0
|
1000
|
1783.0
|
1000
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Viscosity(inlet/outlet)(cp) |
6.65
|
0.768
|
6.65
|
0.768
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Inlet pressure Mpa |
0.48
|
0.3
|
0.48
|
0.3
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Pressure drop, Mpa |
≤0.06
|
≤0.06
|
0.00078
|
0.0019
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PERFORMANCE |
Heat exchanged quantity W |
|
~308085.4
|
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Flow rate m/s |
|
0.073
|
0.515
|
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Heat transfer area affluent coefficient |
|
1.15
|
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Heat transfer coefficient W/m2 ℃ |
|
332.687
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Heat transfer area m2 |
|
60
|
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Type |
shell and tube
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The flow form
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counter-current flow
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Sealing form |
welding connection in acid side, flange connection in water side
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shell
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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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Shell Side
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Tube Side
|
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|
HG20592-2009 PN10 DN 100
|
HG20592-2009 PN6 DN 100
|
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size |
Φ500×7174×960
|
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Operating weight |
3391 Kg
|
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The scope of supply |
●Complete set ●Control system
●Special cable ●Random accessories |
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