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When hot gas enters a wet scrubber, the liquid rapidly cools the gas via adiabatic evaporation. The gas temperature drops down to its wet-bulb temperature. Your Excel sheet must calculate this thermal equilibrium to account for significant water loss.
), dry gas composition, and target pollutant removal efficiency (e.g., 99%). Liquid-to-gas ratio ( minimum target), inlet water temperature ( ∘Craised to the composed with power C ), and chemical reagent concentration (e.g., % scrubber design calculation excel hot
mg⋅Cpg⋅(Tin−Tsat)=mevap⋅ΔHvapm sub g center dot cap C p sub g center dot open paren cap T sub i n end-sub minus cap T sub s a t end-sub close paren equals m sub e v a p end-sub center dot cap delta cap H sub v a p end-sub Cpgcap C p sub g = Specific heat of the inlet gas (kJ/kg·°C) Tsatcap T sub s a t end-sub = Adiabatic saturation temperature (°C) mevapm sub e v a p end-sub = Mass of water evaporated (kg/hr) = Latent heat of vaporization of water (kJ/kg) Excel Tip: Because Tsatcap T sub s a t end-sub
The diameter of a vertical packed scrubber is determined by the gas velocity relative to the flooding point. This public link is valid for 7 days
): Calculate the flow ratio to position your operating line safely away from the equilibrium curve.
): Divide the heat duty by the latent heat of vaporization of water ( Tsatcap T sub s a t end-sub Can’t copy the link right now
The first step is establishing the "source" data. In an Excel sheet, these are typically grouped in a dedicated "Inputs" tab. Gas Stream Properties : Include the inlet volumetric flow rate (e.g., in ), inlet temperature, and pressure. Saturation Calculations
: Calculate the saturated gas flow rate. For example, a gas at 400°F may have a saturation temperature around 127°F, which changes the volumetric flow rate ( Qsatcap Q sub s a t end-sub ) used for sizing.
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