In a packed bed tower air is purified from methanol by using water. Tower has a cross sectional area of 0.2 m? and system operates at 313.1 K and 101.32 kPa. The inlet air contains 10 mol% methanol...


In a packed bed tower air is purified from methanol by using water. Tower has a cross<br>sectional area of 0.2 m? and system operates at 313.1 K and 101.32 kPa. The inlet air<br>contains 10 mol% methanol and at outlet the concentration of methanol drops to 2 mol%.<br>The gas flow is 20 kg mol inert air/h. The pure inlet flow is 50 kg mol water/h. Film<br>coefficients for the given flows in the tower are k',a= 0.07 kg mol/s.m³.mol frac and k',a=<br>0.04 kg mol/s.m³.mol frac. Equilibrium data is given below. Calculate the tower height.<br>Equilibrium data for methanol-water system at 313.1 K<br>Mole fraction Methanol Partial<br>pressure<br>of<br>in Liquid, xA<br>methanol in vapor pA<br>(mmHg)<br>0.05<br>25.0<br>0.10<br>46.0<br>0.15<br>66.5<br>

Extracted text: In a packed bed tower air is purified from methanol by using water. Tower has a cross sectional area of 0.2 m? and system operates at 313.1 K and 101.32 kPa. The inlet air contains 10 mol% methanol and at outlet the concentration of methanol drops to 2 mol%. The gas flow is 20 kg mol inert air/h. The pure inlet flow is 50 kg mol water/h. Film coefficients for the given flows in the tower are k',a= 0.07 kg mol/s.m³.mol frac and k',a= 0.04 kg mol/s.m³.mol frac. Equilibrium data is given below. Calculate the tower height. Equilibrium data for methanol-water system at 313.1 K Mole fraction Methanol Partial pressure of in Liquid, xA methanol in vapor pA (mmHg) 0.05 25.0 0.10 46.0 0.15 66.5

Jun 10, 2022
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