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DC Field | Value | Language |
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dc.contributor.advisor | Marlin, T.E. | en_US |
dc.contributor.author | Forbes, Fraser J | en_US |
dc.date.accessioned | 2014-06-18T16:40:17Z | - |
dc.date.available | 2014-06-18T16:40:17Z | - |
dc.date.created | 2010-08-05 | en_US |
dc.date.issued | 1994-04 | en_US |
dc.identifier.other | opendissertations/2983 | en_US |
dc.identifier.other | 3996 | en_US |
dc.identifier.other | 1426911 | en_US |
dc.identifier.uri | http://hdl.handle.net/11375/7726 | - |
dc.description.abstract | <p>The value of model-based process optimization systems for competitive advantage in many industries, has been widely recognized. Such model-based optimization systems include Real-Time Optimization, On-Line Optimizing Control, off-line process scheduling, and any other economic process optimization scheme which uses a process model to predict optimal plant operation. The thesis investigates the design of these model-based optimization systems, particularly with respect to model structure and adjustable parameter selection.</p> <p>The main contribution of this work include design phase methods, based on fundamental principles of optimization and statistics theory, for determining whether a model-based optimization system can attain the plant optimum, as well as methods for discriminating between design alternatives. Three necessary conditions for zero-offset from the optimal plant operation are presented. These include Pont-Wise Model Adequacy, Augmented Model Adequacy and Point-Wise Stability. Recognizing that achieving zero-offset from the plant optimum may not always be possible, or may not be the only design objective, a Design Cost method is presented for selecting among design alternatives. This Design Cost method provides a natural "trade off" between offset elimination and variance of the predicted optimal manipulated variable values.</p> <p>Finally, the thesis is completed with a larger-scale case study involving the Williams-Otto Plant [1960]. In the case study selection of a process model and the adjustable parameter set for implementation in closed-loop Real-Time Optimization system is investigated.</p> | en_US |
dc.subject | Chemical Engineering | en_US |
dc.subject | Chemical Engineering | en_US |
dc.title | Model Structure and Adjustable Parameter Selection for Operations Optimization | en_US |
dc.type | thesis | en_US |
dc.contributor.department | Chemical Engineering | en_US |
dc.description.degree | Doctor of Philosophy (PhD) | en_US |
Appears in Collections: | Open Access Dissertations and Theses |
Files in This Item:
File | Size | Format | |
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fulltext.pdf | 4.84 MB | Adobe PDF | View/Open |
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