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Measurement System Design for Chemical ProcessesLiba, Michael Joseph 16 June 2011 (has links)
The problem of measurement system design for stochastic linear systems, a popular modeling strategy for chemical processes, is addressed. A multi-objective optimization approach is used. The design metrics are the capital cost of measurement equipment and a weighted uncertainty in terms of the Kalman filter state estimation error covariance matrix. The Pareto optimal set of measurement systems is identified by any of the following applicable techniques: an exhaustive combinatorial search, sequential sensor addition/removal, and branch-and-bound with semi-definite programs (BnB/SDP) solved at each node. The decision-making process involves the use of simulation experiments as a means to map Pareto optimal measurement systems to a dollar cost of operation. The closed-loop performance of Pareto optimal measurement systems are then simulated under a joint Kalman filter and robust profit-maximizing model predictive control strategy.
The design methodology is applied to two example problems. The first involves a low dimensionality fluid handling network where a number of stream flow rates, a tank level, and a leak stream describe the dynamics. The design variables are the process outputs and the precision with which they are measured. It is observed that the sequential and
BnB/SDP techniques are able to approximate the true Pareto optimal set very well, with improved performance in the latter case attainable through trial and error. The second example problem involves a high-dimensionality thermal network model of a one-floor office building. The impact of zero and nonzero state noise covariance structures on the results of the proposed design procedure is investigated. It is shown that measurement importance is placed on the disturbance variables in the deterministic case, whereas importance is placed on the controlled variables when model uncertainty is assumed. Closed-loop simulations incorporating MPC and Kalman filtering are then performed to generate expected operational cost data. The measurement system that minimizes the overall cost of capital investment and operation over the expected lifespan of the measurement is chosen as the final design. It is shown that the combination of measured variables which minimizes the overall cost is those of the three largest bodies of air that are to be controlled. / Thesis (Master, Chemical Engineering) -- Queen's University, 2011-06-15 22:17:06.903
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The design of a hybrid microprocessor/binary decision programmable controller /Hudson, Robert Douglas. January 1984 (has links)
No description available.
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Estimation and control of sheet forming processesRigopoulos, Apostolos 12 1900 (has links)
No description available.
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A micromechanics study of transverse matrix cracking in cross-ply compositesHøiseth, Kjell 05 1900 (has links)
No description available.
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Prediction of workpiece location as a function of fixture-induced errorsRaghu, Anand 05 1900 (has links)
No description available.
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Variables affecting supercalenderingAinsley, J. A. January 1976 (has links)
No description available.
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Highly parallel methods for eigenvalue problemsMckeown, H. G. January 1983 (has links)
No description available.
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Developing a macrocyclic sensor to probe interactions in biologyWhite, Rebecca January 2009 (has links)
This thesis describes the development of a small molecule sensor for the detection of specific protein-protein interactions. The responsive sensor has been designed to produce a measurable signal upon a bivalent interaction with a dimeric protein target, and has the potential to probe the biological significance of specific binding events.
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A study of methods to overcome manufacturing lead time instabilityJohns, Stuart Lionel January 1992 (has links)
No description available.
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A Moessbauer study of relaxation and phase transitions in some magnetic systemsChadwick, J. January 1988 (has links)
No description available.
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