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Please use this identifier to cite or link to this item: http://hdl.handle.net/11375/19952
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DC FieldValueLanguage
dc.contributor.advisorJohnson, A. I.-
dc.contributor.advisorHamielec, A. E.-
dc.contributor.authorPang, Kwok-Hing-
dc.date.accessioned2016-07-27T14:26:15Z-
dc.date.available2016-07-27T14:26:15Z-
dc.date.issued1965-03-
dc.identifier.urihttp://hdl.handle.net/11375/19952-
dc.description.abstractThe present apparatus was used to obtain rate data for the absorption of oxygen in a catalysed liquid phase reaction with acetaldehyde. The effects of several system parameters, namely, acetaldehyde concentration, catalyst concentration, partial pressure of oxygen and temperature on the rate of absorption were studied. An attempt was made to correlate absorption rates and product distribution with mathematical models based on the film theory and existing kinetic models proposed by Bolland and Bawn. Absorption rates predicted by these semi-empirical correlations are compared with experimental values. The differential equations involving diffusion with chemical reaction were solved on the digital computer IBM 7040 and the analog computer PACE TRlO.en_US
dc.language.isoenen_US
dc.subjectGas Absorptionen_US
dc.subjectLiquid Phaseen_US
dc.subjectChemical Reactionen_US
dc.subjectacetaldehydeen_US
dc.titleSimultaneous Gas Absorption and Liquid Phase Chemical Reactionen_US
dc.contributor.departmentChemical Engineeringen_US
dc.description.degreetypeThesisen_US
dc.description.degreeMaster of Engineering (MEngr)en_US
Appears in Collections:Open Access Dissertations and Theses

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