​​

Scrubber Design Calculation Excel Hot Jun 2026

Double-check that your Packing Factor ( Fpcap F sub p

The template can then be used to calculate the following outputs:

When hot gas hits the liquid scrubbing media, water evaporates instantly. This cools the gas to its ( Tsatcap T sub s a t end-sub

Standard scrubber design assumes isothermal conditions. But when your inlet gas is at 400°C (752°F) or higher, three critical physics problems emerge: scrubber design calculation excel hot

Store constant parameters and empirical formulas here. Use Excel formulas linked to temperature to ensure properties update automatically during iterations. Latent heat of vaporization ( ), density ( ρLrho sub cap L ), and viscosity ( μLmu sub cap L Gas Properties: Specific heat capacities ( ) as a function of temperature ( Constants: Gas constant ( ), atmospheric pressure ( Patmcap P sub a t m end-sub Tab 3: Calculation Engine

). Your blower CFM must be sized for the actual temperature, not just standard conditions.

Before chemical scrubbing happens, hot gas must be "quenched" to its adiabatic saturation temperature. Double-check that your Packing Factor ( Fpcap F

[ Q_actual = Q_normal \times \left( \fracP_normalP_actual \right) \times \left( \fracT_actualT_normal \right) ]

Designing a Wet Scrubber for Hot Gas Streams: Engineering Principles & Excel Guide

D=4⋅Aπcap D equals the square root of the fraction with numerator 4 center dot cap A and denominator pi end-fraction end-root = Column cross-sectional area ( m2m squared Vgcap V sub g = Operational gas velocity ( , typically for packed towers) = Column internal diameter ( Step 4: Packing Height and Liquid Hydraulics The height of the packing zone ( ) is calculated using the Number of Transfer Units ( ) and the Height of a Transfer Unit ( Z=NTU⋅HTUcap Z equals NTU center dot HTU Use Excel formulas linked to temperature to ensure

) or empirical flooding constants to add directly to your formulas. Share public link

Based on the Number of Transfer Units (NTU) and Height of a Transfer Unit (HTU).

Designing a wet scrubber for hot gas streams—such as incinerator exhaust, boiler flue gas, or thermal oxidizer discharges—presents unique thermodynamic challenges that standard design spreadsheets fail to capture. Evaporative Cooling and Water Makeup

-->