Design Calculation Excel Hot — Scrubber

where R = 8.314 J/(mol·K) .

A=Qsat3600⋅Vgcap A equals the fraction with numerator cap Q sub s a t end-sub and denominator 3600 center dot cap V sub g end-fraction scrubber design calculation excel hot

Account for the high moisture content of quenched gas by sizing a chevron or mesh mist eliminator at the top of the tower to prevent liquid carryover. where R = 8

Before any mass transfer (absorption) can be calculated, you must determine the quenched gas properties. The hot gas enters at temperature Tincap T sub i n end-sub and is cooled to the adiabatic saturation temperature Tsatcap T sub s a t end-sub by evaporating water. Heat Duty ( The hot gas enters at temperature Tincap T

Designing a scrubber for hot gases introduces unique thermodynamics. The gas must be cooled down to its adiabatic saturation temperature before efficient mass transfer or particulate collection can occur.

A=QsatVgcap A equals the fraction with numerator cap Q sub s a t end-sub and denominator cap V sub g end-fraction