Formalin Production

Page 63

5.2

Absorption Column Design

W = 861.752 Kg-mol/hr Equilibrium relationship = y = x(solute free) y = mx At bottom of tower

y1  0.2305 so 0.2305 SMF solute.mole. fraction   0.299  1  0.2305 SFG mole. fraction.solute. free.gas A  461.591Kgmol / hr  0.128Kgmol / sec y1 

5.2.1 Number Of Plates  y2  0.00105 0.00105  0.00105 1  0.00105 y1  y2  N 1    (Souders and Brown equation) y1 mx2  N 1  1

y2 

  Absorption.Factor 

W  1.86 mA

 N 1   0.9964  N 1  1 N  7.83 Assuming Tray spacing 24” from graph Kv = 0.30ft  L  62.4lb / ft 3 M g  0.0332(32)  0.0138(32)  0.2305(30)  0.2317(18)  0.4876(28)  26.3lb / lbmol

g 

PM g RT

1.35atm * 26.3  0.044lb / ft 3 0.7302*1108

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