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Scrubber Design Calculation Excel Hot -

Designing a wet scrubber for high-temperature ("hot") gas streams requires balancing pollutant removal efficiency with heat recovery and structural integrity

Tower Diameter: Use the gas velocity and pressure drop to find the cross-sectional area. The diameter ( ) is typically calculated as Pressure Drop ( ΔPcap delta cap P scrubber design calculation excel hot

Overall Penetration ($Pt$): $$ Pt = \exp \left( - \left( \fracd_pd_pc \right)^B \right) $$ Efficiency $\eta = 1 - Pt$. Designing a wet scrubber for high-temperature ("hot") gas

Step 1: Input Section (The "Hot" Parameters)

Create these mandatory input cells:

  • Use the type of pollutant being removed and the efficiency of pollutant removal required to calculate the efficiency of pollutant removal.
  • Use a formula such as: η = (C_in - C_out) / C_in where η is the efficiency of pollutant removal, C_in is the inlet concentration, and C_out is the outlet concentration.

Qsat=Qin×Volume Correction Factorcap Q sub s a t end-sub equals cap Q sub i n end-sub cross Volume Correction Factor For example, a gas at 450∘F450 raised to the composed with power cap F might have a correction factor of 3. Determine Column Diameter Use the type of pollutant being removed and

Where:

  • Scrubber diameter: 1.53 m
  • Scrubber height: 3.15 m
  • Liquid flow rate: 10.2 L/s
  • Pressure drop: 250 Pa
  • Efficiency of pollutant removal: 92.5%

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