Scrubber Design Calculation Excel Best Today

NTU = LN( (y_in - y_eq_in) / (y_out - y_eq_out) ) Create a solver loop that adjusts packing height until outlet composition meets environmental limits. 5. Liquid Distribution and Wetting Rate A hidden killer. Even with 100 stages, if liquid doesn’t wet the packing, mass transfer fails.

ΔP (in H2O/ft packing) = C * (G² / ρg) * (10^(L*D)) Where C and D are packing constants. Or use the generalized method: ΔP = 0.115 * (G^1.85) * (Fp^0.85) for dry packing, plus liquid correction. scrubber design calculation excel best

=EXP( -2.5 * LN(X) - 1.2 ) [Approximate; use published tables for accuracy] Then back-calculate area: A = Gas_flow_rate / G_flood . Diameter = SQRT(4*A/π) . Using the Leva correlation (simplest for Excel): NTU = LN( (y_in - y_eq_in) / (y_out

Use Goal Seek on pressure drop vs. gas rate to avoid flooding. 4. Packing Height (Mass Transfer) This is where Excel shines. For gas absorption (e.g., HCl in water), the Height of Transfer Unit (HTU) method is standard. Even with 100 stages, if liquid doesn’t wet

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