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Please use this identifier to cite or link to this item: http://hdl.handle.net/11375/14305
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dc.contributor.advisorHamielec, A.E.en_US
dc.contributor.authorBhattacharya, Dhruboen_US
dc.date.accessioned2014-06-18T17:07:02Z-
dc.date.available2014-06-18T17:07:02Z-
dc.date.created2009-08-13en_US
dc.date.issued1985-09en_US
dc.identifier.otheropendissertations/946en_US
dc.identifier.other1652en_US
dc.identifier.other939092en_US
dc.identifier.urihttp://hdl.handle.net/11375/14305-
dc.description.abstract<p>A general kinetic model which accounts for diffusion-controlled termination and propagation in free-radical copolymerization up to high conversions was developed. This model was tested on batch kinetic data for styrene/p-methyl styrene thermal copolymerization and data on the chemically-initiated bulk copolymerization of methyl methacrylate/p-methyl styrene. The model gave reasonable predictions of conversion, copolymer composition and molecular weights for these copolymer systems and thus should find use in the design, optimization and control of copolymer reactors.</p>en_US
dc.subjectChemical Engineeringen_US
dc.subjectChemical Engineeringen_US
dc.titleDiffusion-Controlled Copolymerization Kineticsen_US
dc.typethesisen_US
dc.contributor.departmentChemical Engineeringen_US
dc.description.degreeDoctor of Philosophy (PhD)en_US
Appears in Collections:Open Access Dissertations and Theses

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