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solve 11-4. use just part a) of 11-3 11-3 Determine the cross-sectional area and diameter for a packed- tower design based on the conditions given

solve 11-4. use just part a) of 11-3 image text in transcribed
11-3 Determine the cross-sectional area and diameter for a packed- tower design based on the conditions given below (to be selected by instructor). Contaminant A chloroform 20 13 Water Flow Pressure Temp, Rate, Stripping Drop, C ML/d Factor N/m2. m Packing 3.5 50 5.1 cm Intalox saddles 10 4.3 3.5 50 5.8 cm LANPAC 20 2.5 4 400 5.1 cm Jaeger Tri-Packs 15 10 6 100 8.9 cm LANPAC-XL 10 3.5 200 8.9 cm Jaeger Tri-Packs B benzene C carbon tetrachloride D trichloroethylene E tetrachloroethylene 20 11-4 Determine the overall liquid-side mass transfer rate constant for the compound and tower design given in Problem 11-3 using the Onda correlations and a safety factor of 0.75. Determine the liquid-phase diffusion coefficient D, using the Hayduk-Laudie correlation (Eq. 4-121) and the gas-phase diffusion coefficient using the Wilke-Lee correlation (Eq. 4-123). The packing material is polyethylene. 11-3 Determine the cross-sectional area and diameter for a packed- tower design based on the conditions given below (to be selected by instructor). Contaminant A chloroform 20 13 Water Flow Pressure Temp, Rate, Stripping Drop, C ML/d Factor N/m2. m Packing 3.5 50 5.1 cm Intalox saddles 10 4.3 3.5 50 5.8 cm LANPAC 20 2.5 4 400 5.1 cm Jaeger Tri-Packs 15 10 6 100 8.9 cm LANPAC-XL 10 3.5 200 8.9 cm Jaeger Tri-Packs B benzene C carbon tetrachloride D trichloroethylene E tetrachloroethylene 20 11-4 Determine the overall liquid-side mass transfer rate constant for the compound and tower design given in Problem 11-3 using the Onda correlations and a safety factor of 0.75. Determine the liquid-phase diffusion coefficient D, using the Hayduk-Laudie correlation (Eq. 4-121) and the gas-phase diffusion coefficient using the Wilke-Lee correlation (Eq. 4-123). The packing material is polyethylene

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