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Please use this identifier to cite or link to this item: http://hdl.handle.net/11375/12913
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dc.contributor.advisorCrowe, C. M.en_US
dc.contributor.authorSheel, John P.en_US
dc.date.accessioned2014-06-18T17:01:12Z-
dc.date.available2014-06-18T17:01:12Z-
dc.date.created2013-04-23en_US
dc.date.issued1996-12en_US
dc.identifier.otheropendissertations/7759en_US
dc.identifier.other8838en_US
dc.identifier.other4060360en_US
dc.identifier.urihttp://hdl.handle.net/11375/12913-
dc.description.abstract<p>The main purpose of this research was to find, from a simulation of an existing reactor under rather heavy constraints, how upon removal of these limitation the same reactor could be operated more economically and, efficiently. An accurate, simplified model of the process was developed and used in the design of single and double bed reactors with very consistent results. A better understanding of the process variables, reactions and constraints was obtained by extrapolation of the model within reasonable bounds.</p> <p>The usefulness of a multivariate search technique applied to a relatively complicated process was proven. Such techniques as Pontryagin's Maximum Principle l and dynamic programming2 become unwieldy for processes involving many state variables. An engineer can quickly grasp the ideas of multi-variable search methods whereas it is difficult to understand the above more elaborate techniques without much study. This report may be particularly useful to plant-process engineers who seek a practical optimum-seeking method.</p>en_US
dc.subjectChemical Engineeringen_US
dc.subjectChemical Engineeringen_US
dc.titleSimulation and Optimization of an Existing Ethylbenzene Dehydrogenation Reactor.en_US
dc.typethesisen_US
dc.contributor.departmentChemical Engineeringen_US
dc.description.degreeMaster of Engineering (MEngr)en_US
Appears in Collections:Open Access Dissertations and Theses

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