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• W3208884237 startingPage "58" @default.
• W3208884237 abstract "Abstract Wall mass and heat transfer rates in a square gas‐sparged, mechanically stirred reactor were measured by the electrochemical technique under the effect of various geometrical and hydrodynamic variables. For the 45° impeller, the mass transfer data fit the equation Sh = 0.7 Sc 0.33 Re 0.2 Re g 0.5 with an average deviation of ±6.9 %. For the 90° impeller, the data fit the equation Sh = 0.95 Sc 0.33 Re 0.14 Re g 0.53 with an average deviation of ±7.5 %. Gas sparging enhanced the wall mass transfer rates by factors of up to 2.61 and 3 for the 90° and 45° impellers, respectively, with a significant decrease in the total power consumption. The contribution of the present results to the operation of multiphase mechanically agitated vessels in different aspects is outlined." @default.
• W3208884237 created "2021-11-08" @default.
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• W3208884237 date "2021-11-19" @default.
• W3208884237 modified "2023-10-12" @default.
• W3208884237 title "Heat and Mass Transfer at the Wall of a Square Mechanically Stirred Gas‐Liquid‐Solid Catalytic Reactor" @default.
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• W3208884237 doi "https://doi.org/10.1002/ceat.202100142" @default.
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