| Parameter | Input | Formula | Result | | --- | --- | --- | --- | | Gas Flow Rate (Q) | | | | | Velocity | | | | | Scrubber Diameter (D) | | =SQRT(4 Q/(PI() velocity)) | | | Scrubbing Liquid Flow Rate | | | | | L/G Ratio | | | | | Scrubber Height (H) | | =( scrubber volume /(PI() (D/2)^2)) | | | Pressure Drop (ΔP) | | =(f L* ρ)/(2*g) | |
Program this formula into Excel to find the diameter at 50%–70% of the flooding velocity. Equation: 4. Calculating Packing Height scrubber design calculation excel hot
For an industrial "hot" scrubber design calculation in Excel, you need to structure your spreadsheet to handle gas cooling (quenching) mass transfer simultaneously | Parameter | Input | Formula | Result
Excel: Calculate NTU using logarithmic mean concentration difference (LMTD) for the pollutants. C. Output/Results Section Tower Diameter (meters) Total Packed Height (meters) Required Water Flow Rate (m³/h) Pressure Drop (Pa or in. WC) 3. Key Considerations for Hot Gas Applications Key Considerations for Hot Gas Applications Pressure drop
Pressure drop is the primary driver for operating cost (fan energy). Your Excel sheet should calculate ΔP using two separate methods depending on the scrubber type:
Flv=LG⋅ρgρlcap F sub l v end-sub equals the fraction with numerator cap L and denominator cap G end-fraction center dot the square root of the fraction with numerator rho sub g and denominator rho sub l end-fraction end-root = Liquid mass flow rate ( = Gas mass flow rate ( = Gas and liquid densities ( Step 2: Determine Gas Capacity Factor ( Cscap C sub s ) at Flooding Using the packing factor ( Fpcap F sub p