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Please use this identifier to cite or link to this item: http://hdl.handle.net/11375/18750
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DC FieldValueLanguage
dc.contributor.advisorJohnson, A. I.-
dc.contributor.authorLozada, Alejandro-
dc.date.accessioned2016-01-19T20:00:48Z-
dc.date.available2016-01-19T20:00:48Z-
dc.date.issued1971-08-
dc.identifier.urihttp://hdl.handle.net/11375/18750-
dc.description.abstractThis report deals with the use of the "Modular Approach", in the simulation of change-over operations, for a continuous multiproduct chemical plant. A dynamic model of the continuous fat hydrolysis process was built, with the DYNSYS framework, with the purpose of evaluating the usefulness of this programme in simulating different change-over operation policies. Operator's activities were simulated making use of an interactive version of DYNSYS, demonstrating its value for studying alternate changeover policies and possible as a training device. Supervisory control was implemented in order to automate the change-over operations, simulating the functions of a small computer controlling the process. Improved operating policies for change-over are proposed and the validity of the simulation is discussed from both a practical and a theoretical point of view.en_US
dc.language.isoenen_US
dc.subjectModular Approachen_US
dc.subjectchange-over operationen_US
dc.subjectchemical planten_US
dc.subjectfat hydrolysis processen_US
dc.subjectDYNSYSen_US
dc.titleDynamic Simulation of a Multiproduct Chemical Planten_US
dc.typeThesisen_US
dc.contributor.departmentNoneen_US
dc.description.degreetypeThesisen_US
dc.description.degreeMaster of Engineering (ME)en_US
Appears in Collections:Open Access Dissertations and Theses

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