Anodic Protection Sulfuric Acid Cooler with Corrosion Resistant Shell-and-Tube Heat Exchanger for High Thermal Efficiency Dry Acid Cooler
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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
93%
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Cooling Water
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Sulfuric Acid
93%
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Cooling Water
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Temperature (Inlet) ℃ |
68
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33
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68
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33
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Temperature (Outlet)℃ |
40
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41
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40
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37.42
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Liquid Kg/h |
89928
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89928
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200000
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Density(inlet/outlet) Kg/m3 |
~1793
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1000
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~1793
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1000
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Viscosity(inlet/outlet)(cp) |
7.02
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0.76
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7.02
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0.76
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Inlet pressure Mpa |
0.45
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0.3
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0.45
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0.3
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Pressure drop, Mpa |
≤0.1
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≤0.1
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0.0043
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0.037
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PERFORMANCE |
Heat exchanged quantity W |
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~1023280.7
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Flow rate m/s |
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0.163
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0.737
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Heat transfer area affluent coefficient |
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1.15
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Heat transfer coefficient W/m2 ℃ |
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475.361
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Heat transfer area m2 |
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135
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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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Materials and specifications |
shell
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304L δ= 10
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Heat transfer tube
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316L Φ19×2.0×6000
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Tubesheet
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304L δ= 55
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Baffle-crossing
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304L δ= 10
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head
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Q235-B δ= 12
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Shell Side
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Tube Side
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HG/T20592-2009(B) PN10 DN 150
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HG/T20592-2009(B) PN10 DN 200
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Size |
Φ600×7214×1060
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Operating weight |
5979 Kg
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The scope of supply |
●Complete set ●Control system |
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