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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
98.5%
|
Cooling Water
|
Sulfuric Acid
98.5%
|
Cooling Water
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Temperature (Inlet) ℃ |
96
|
33
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96
|
33
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Temperature (Outlet)℃ |
80
|
43
|
80
|
42.956
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Liquid Kg/h |
1412400
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1412400
|
865000
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Density(inlet/outlet) Kg/m3 |
1840
|
1000
|
1840
|
1000
|
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Viscosity(inlet/outlet)(cp) |
7.9
|
0.76
|
7.9
|
0.76
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Inlet pressure Mpa |
0.5
|
0.4
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0.5
|
0.4
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Pressure drop, Mpa |
≤0.07
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≤0.06
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0.062
|
0.008
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PERFORMANCE |
Heat exchanged quantity W |
|
~9968405.3
|
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Flow rate m/s |
|
0.574
|
1.245
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Heat transfer area affluent coefficient |
|
1.1
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Heat transfer coefficient W/m2 ℃ |
|
820.668
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Heat transfer area m2 |
|
260
|
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MATERIAL |
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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Materials and specifications |
shell
|
316L δ= 12
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Heat transfer tube
|
316L Φ19.05×1.65×4500
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Tubesheet
|
316L δ= 60
|
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Baffle-crossing
|
316L δ= 12
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head
|
316L δ= 60
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Flange standard |
Shell Side
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Tube Side
|
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HG/T20615-2009 class150 RF
|
HG/T20615-2009 class150 RF
|
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Size |
Φ1200×6794×1674
|
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Operating weight |
14409 Kg
|
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The scope of supply |
●Complete set ●Control system
●Special cable ●Random accessories |
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