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High-performance multi-scale control scheme for stable, integrating and unstable time-delay processes

•New control scheme for stable and integrating/unstable time-delay processes.•The design principle is to decompose a given plant into a sum of basic modes.•An individual sub-controller is specifically designed to control each mode.•The sub-controllers are combined to enhance cooperation among the pl...

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Bibliographic Details
Published in:Journal of process control 2013-11, Vol.23 (10), p.1333-1343
Main Authors: Nandong, Jobrun, Zang, Zhuquan
Format: Article
Language:English
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Summary:•New control scheme for stable and integrating/unstable time-delay processes.•The design principle is to decompose a given plant into a sum of basic modes.•An individual sub-controller is specifically designed to control each mode.•The sub-controllers are combined to enhance cooperation among the plant modes.•Numerical study demonstrates the applicability and effectiveness of the scheme. This paper presents a new multi-scale control scheme which is applicable to both stable and integrating/unstable time-delay processes. The salient feature of the proposed scheme is to decompose a given plant into a sum of basic modes, where an individual sub-controller is specifically designed to control each of these modes. An overall multi-scale controller is then synthesized by combining all the sub-controllers in such a way to achieve good cooperation among the different plant modes as to achieve good nominal performance and performance robustness. Extensive numerical study shows that the proposed multi-scale control scheme provides substantial improvement in control performance/robustness over the classical Smith predictor and some of its well-established variants.
ISSN:0959-1524
1873-2771
DOI:10.1016/j.jprocont.2013.08.007