A Dimensionless Model for Predicting the Mass Transfer Area of Structured Packing

Tuesday, March 23, 2010: 4:00 PM
Lone Star Salon C (Grand Hyatt San Antonio)
Robert E. Tsai1, A. Frank Seibert2, R. Bruce Eldridge1 and Gary T. Rochelle1, (1)Chemical Engineering, The University of Texas at Austin, Austin, TX, (2)Separations Research Program, The University of Texas at Austin, Austin, TX

The mass transfer area of nine structured packings was measured in a 0.427 m ID column via absorption of CO2 from air into 0.1 kmol/m3 NaOH.  The area was most strongly related to packing size (125-500 m2/m3) and liquid load (2.5-75 m3/m2·h).  Surface tension (30-72 mN/m) had a weaker but significant effect.  Gas velocity (0.6-2.3 m/s), liquid viscosity (1-15 mPa·s), and flow channel configuration had essentially no impact on the mass transfer area.  Surface texture (embossing) increased the effective area by 10% at most.  The ratio of mass transfer area to specific area (ae/ap) was correlated within limits of ±13% for the entire experimental database:


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