Gurumurthy, CV and Govindarao, VMH (1974) Rate Model and Mechanism of Liquid-Phase Oxidation of Propionaldehyde. In: Industrial and Engineering Chemistry Fundamentals, 13 (1). pp. 9-17.
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Abstract
A rate equation is developed for the liquid-phase oxidation of propionaldehyde with oxygen in the presence of manganese propionate catalyst in a sparged reactor. The equation takes into account diffusional limitations based on Brian's solution for mass transfer accompanied by a pseudo m-. nth-order reaction. Sauter-mean bubble diameter, gas holdup, interfacial area, and bubble rise velocity are measured, and rates of mass transfer within the gas phase and across the gas-liquid interface are computed. Statistically designed experiments show the adequacy of the equation. The oxidation reaction is zero order with respect to oxygen concentration, 3/2 order with respect to aldehyde concentration, and order with respect to catalyst concentration. The activation energy is 12.1 kcal/g mole.
Item Type: | Journal Article |
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Publication: | Industrial and Engineering Chemistry Fundamentals |
Publisher: | American Chemical Society |
Additional Information: | Copyright of this article belongs to American Chemical Society. |
Department/Centre: | Division of Mechanical Sciences > Chemical Engineering |
Date Deposited: | 17 Dec 2009 04:31 |
Last Modified: | 19 Sep 2010 05:50 |
URI: | http://eprints.iisc.ac.in/id/eprint/24491 |
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