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Mass transfer to packed beds

In packed beds, mass transfer coefficients are often correlated by means of a Chilton—Colburn factor, Ju, analogous to their Jh heat transfer (Sect. 4.4.4) [Pg.38]

The factor [B] im/[M], the logarithmic mean concentration of the inert component B divided by the total concentration, allows for the fact that the concentration of B may alter significantly. [Pg.38]

Other correlations for flow through packed beds involve the porosity, e, e.g. [Pg.39]

In all these expressions, Rep is the Reynolds number based on the particle diameter. [Pg.39]


Mass Transfer to Packed Bed and Driving Force. Pure water at 26.1°C is flowing at a rate of 0.0701 ft h through a packed bed of 0.251-in. benzoic acid spheres having a total surface area of 0.129 ft. The solubility of benzoic acid in water is 0.00184 lb mol benzoic acid/ft solution. The outlet concentration 1.80 x 10 lb mol/ft. Calculate the mass-transfer coefficient. ... [Pg.481]


See other pages where Mass transfer to packed beds is mentioned: [Pg.38]    [Pg.447]   


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