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- W2036187234 abstract "The rates of mass transfer at a vertical array of closely spaced horizontal tubes were measured by the limiting-current technique under single-phase flow, gas sparging and two-phase flow. The single-phase flow data were correlated by the equation: Sh = 0.75 Sc0.33 Re0.59. The gas sparging data with no net solution flow were correlated by the equation: J = 0.31(Reg.Fr)–0.22. For two-phase flow, the gas flow was found to enhance the rate of array mass transfer by a factor ranging from 1.25 to 5.25, depending on Reg and Re. The enhancement ratio increases with decreasing Re and increasing Reg. For Re ≥ 2500, the rate of mass transfer approaches the value of single-phase flow, regardless of the value of Reg, which ranged from 7 to 41. The importance of the present geometry in building electrochemical and catalytic reactors, where exothermic liquid-solid diffusion-controlled reactions take place, is highlighted. The present geometry offers the advantage that the outer surface acts as a turbulence promoter while the inner surface acts as a heat exchanger." @default.
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- W2036187234 date "2010-01-01" @default.
- W2036187234 modified "2023-10-12" @default.
- W2036187234 title "Liquid-Solid Mass Transfer Behavior of a Vertical Array of Closely Spaced Horizontal Tubes in Relation to Catalytic and Electrochemical Reactor Design" @default.
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- W2036187234 doi "https://doi.org/10.1002/ceat.200900311" @default.
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