April 7, 2026
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Process parameters |
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Project |
Design parameters |
Performance parameters |
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Shell Side |
Tube Side |
Shell Side |
Tube Side |
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MEDIUM |
Fluid Name |
Sulfuric Acid 98% |
Cooling Water |
Sulfuric Acid 98% |
Cooling Water |
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Temperature (Inlet) ℃ |
60 |
33 |
60 |
33 |
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Temperature (Outlet)℃ |
40 |
43 |
40 |
37.993 |
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Liquid Kg/h |
128000 |
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128000 |
180000 |
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Density(inlet/outlet) Kg/m3 |
1791 |
1000 |
1791 |
1000 |
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Viscosity(inlet/outlet)(cp) |
7.45/10.82 |
0.76 |
7.45/10.82 |
0.76 |
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Inlet pressure Mpa |
0.3 |
0.25 |
0.3 |
0.25 |
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Pressure drop, Mpa |
≤0.1 |
≤0.1 |
0.008 |
0.002 |
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PERFORMANCE |
Heat exchanged quantity W |
~1040355.6 |
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Flow rate m/s |
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0.222 |
0.518 |
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Heat transfer area affluent coefficient |
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1.1 |
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Heat transfer coefficient W/m2 ℃ |
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486.36 |
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Heat transfer area m2 |
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175 |
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MATERIAL |
Type |
Shell and Tube |
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) PN16 DN 150 |
HG/T20592-2009(B) PN10 DN 200 |
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Size |
Φ700×7574×1162 |
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Operating weight |
7631 Kg |
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The scope of supply |
●Complete set ●Control system ●Special cable ●Random accessories |
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