Internal Model Control: Robust Digital Controller Synthesis for Multivariable Open-Loop Stable or Unstable Processes
dc.contributor.author | Zafiriou, E. | en_US |
dc.contributor.author | Morari, M. | en_US |
dc.contributor.department | ISR | en_US |
dc.date.accessioned | 2007-05-23T09:46:03Z | |
dc.date.available | 2007-05-23T09:46:03Z | |
dc.date.issued | 1990 | en_US |
dc.description.abstract | The two-step Internal Model Control (IMC) procedure is presented for the synthesis of multivariable discrete controllers. This paper adds the following features to the IMC design methodology: (i) Extension to open-loop unstable plants. (ii) Design of the first-step (no model error) IMC controller so that the L2-error (sum of squared errors) is minimized for every setpoint or disturbance vector in a designer-specified set and their linear combinations. (iii) The second-step (model-plant mismatch) multivariable low-pass filter is designed for robust stability and performance by minimizing a non-conservative robustness measure, the Structured Singular Value. (iv) The potential problem in intersample rippling is avoided by introducing a modification in the first-step controller and formulating the robust performance objective for the continuous plant output. | en_US |
dc.format.extent | 1724992 bytes | |
dc.format.mimetype | application/pdf | |
dc.identifier.uri | http://hdl.handle.net/1903/4996 | |
dc.language.iso | en_US | en_US |
dc.relation.ispartofseries | ISR; TR 1990-48 | en_US |
dc.subject | chemical process control | en_US |
dc.subject | distillation control | en_US |
dc.subject | predictive control | en_US |
dc.subject | linear systems | en_US |
dc.subject | optimal control | en_US |
dc.subject | robust control | en_US |
dc.subject | Chemical Process Systems | en_US |
dc.title | Internal Model Control: Robust Digital Controller Synthesis for Multivariable Open-Loop Stable or Unstable Processes | en_US |
dc.type | Technical Report | en_US |
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