Scrubber Design Calculation Excel Hot [upd] Site

Calculate tower cross-sectional area and round up to standard industrial pipe or vessel diameters. Section 4: Outputs and Performance Summary

🔥 Because it’s fully editable – no black-box VBA, just transparent formulas and lookup tables. Change packing type, gas flow, or removal efficiency – results update instantly.

where R is the gas constant (8.314 J/mol·K). scrubber design calculation excel hot

$$F_p = X = \fracLG \times \sqrt\fracρ_gρ_l$$ Excel: =(L_G_ratio)*(SQRT(gas_density/1000)) (assuming liquid density ~1000 kg/m³)

$$Q_actual = Q_std \times \fracT_op + 273273 \times \frac1.013P_op$$ Calculate tower cross-sectional area and round up to

) to determine the cooling load or potential for heat recovery. www.mchip.net Excel Implementation Resources

Represents the difficulty of the separation. For dilute systems with a clean scrubbing liquid, it simplifies to: where R is the gas constant (8

For hot gases, packing material must be high-temperature resistant (e.g., metal, ceramic, or specialized plastics). Input the provided by manufacturers in your Excel sheet. Calculate pressure drop ( ) using the Ergun equation or manufacturer correlations. Step 4: Mass Transfer (Height of Packing) The removal efficiency ( ) is determined by the number of transfer units ( NTUcap N cap T cap U ) and the height of a transfer unit ( HTUcap H cap T cap U (Assuming linear equilibrium) For hot scrubbing, NTUcap N cap T cap U