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Application of Dynamic Matrix Control to Moderate and High Purity Distillation Towers.

dc.contributor.authorMcDonald, Karen A.en_US
dc.contributor.authorMcAvoy, Thomas J.en_US
dc.date.accessioned2007-05-23T09:37:23Z
dc.date.available2007-05-23T09:37:23Z
dc.date.issued1987en_US
dc.identifier.urihttp://hdl.handle.net/1903/4576
dc.description.abstractDynamic Matrix Control, a predictive computer control algorithm developed at Shell Oil Co. (Cutler, 1983) is applied to dual composition control of moderate and high purity, binary distillation towers. The composition control loops in these towers are highly interacting and, in addition, very nonlinear. The difficulty in obtaining a representative process model for nonlinear systems is demonstrated and methods to overcome this problem are suggested. Multivariable gain and time constant scheduling are evaluated using simple analytical models to update key process model parameters (process gains and time constants) on-line. This approach results in a significant improvement in regulatory control performance over the standard application of DMC.en_US
dc.format.extent1315441 bytes
dc.format.mimetypeapplication/pdf
dc.language.isoen_USen_US
dc.relation.ispartofseriesISR; TR 1987-68en_US
dc.titleApplication of Dynamic Matrix Control to Moderate and High Purity Distillation Towers.en_US
dc.typeTechnical Reporten_US
dc.contributor.departmentISRen_US


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