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%