When searching for , do not settle for a static PDF or a generic absorber sheet. You require a dynamic workbook that solves the adiabatic cooling curve, corrects gas density, and checks thermal survival of droplets.
This is the unique differentiator for high-temperature applications (e.g., kilns, incinerators, smelters). scrubber design calculation excel hot
equation to ensure the system operates within fan/blower limits. : For hot gases, calculate the energy balance ( When searching for , do not settle for
By building or purchasing an Excel tool that solves the adiabatic energy balance, corrects gas viscosity for temperature, and uses saturated gas volume for velocity calculations, you move from guessing to engineering. equation to ensure the system operates within fan/blower
The "Hot" headache: ΔP increases with temperature because gas viscosity rises. Use the : $$ΔP (mmH₂O/m) = C \times (G')^1.82 \times (μ_g)^0.2$$ Where $G'$ = gas mass velocity (kg/m²·s), $C$ = packing constant.
Before sizing the tower, you must calculate the saturated gas flow rate. Hot inlet gas will evaporate scrubbing liquid, increasing the gas volume and cooling it to its adiabatic saturation temperature.