Controllability measures for disturbance rejection

“Controllability measures for disturbance rejection”

Authors: Sigurd Skogestad and Erik A. Wolff,
Affiliation: NTNU, Department of Chemical Engineering
Reference: 1996, Vol 17, No 3, pp. 167-181.

Keywords: Input-output controllability, control structure design, relative gain array, relative disturbance gain

Abstract: Some plants have better built-in disturbance rejection capabilities than others, that is, their dynamic resilience (controllability) with respect to disturbance rejection is better. In the paper we consider controller independent disturbance measures for six classes of problems:.

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PDF (1632 Kb) DOI: 10.4173/mic.1996.3.1

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References:
[1] BRISTOL, E.H. (1966). On a new measure of interaction for multivariable process control, IEEE Trans. Autom. Control, AC-11,133-134 doi:10.1109/TAC.1966.1098266
[2] HOVD, M. SKOGESTAD, S. (1992). Simple frequency-dependent tools for control system analysis, structure selection and design, Automatica, 28,989-996 doi:10.1016/0005-1098(92)90152-6
[3] LUYBEN, W.L. (1988). The concept of 'Eigenstructure' in process control, Ind. Eng. Chem. Res., 27, 206-208 doi:10.1021/ie00073a038
[4] McAVOY, T. J. (1983). Interaction Analysis, ISA Monograph Series, Research Triangle Park, North Carolina, USA.
[5] McCUNE, L.C. GALLIER, P.W. (1973). Digital simulation: A tool for the analysis and design of distillation controls, ISA Trans., 12, 193-207.
[6] MORARI, M. (1983). Design of resilient process plants III, A general framework for the assessment of dynamic resilience. Chem. Eng. Sci., 38, 1881-1891 doi:10.1016/0009-2509(83)85044-1
[7] MORARI, M., GRIMM, W., OGLESBY, M.J. PROSSER, I.D. (1985). Design of resilient processing plants VII: Design of energy management system for unstable reactors - new insights, Chem. Eng. Sci., 40, 187-198 doi:10.1016/0009-2509(85)80058-0
[8] PERKINS, J.D. (1989). Interactions between process design and process control, Preprints IFAC-symposium DYCORD + ´89, Maastricht, Netherlands, Aug. 1989,349-357.
[9] SHIMIZU, K. MATSUBARA, M. (1985). Directions of disturbances and modeling errors on the control quality in distillation systems, Chem. Eng. Commun., 37, 67-91 doi:10.1080/00986448508911273
[10] SKOGESTAD, S. HOVD, M. (1990). Use of frequency-Dependent RGA for control structure selection, Proc. American Control Conference.ACC, 2133-2139, San Diego. May 1990.
[11] SKOGESTAD, S. MORARI, M. (1987). The effect of disturbance directions on closed-loop performance, Ind. Eng. Chem. Res., 26, 2029-2035 doi:10.1021/ie00070a017
[12] SKOGESTAD, S. MORARI, M. (1987). Control configuration selection for distillation columns, AIChE Journal, 33, 1620-1635 doi:10.1002/aic.690331006
[13] STANLEY, G., MARINO-GALARRAGA, M. McAVOY, T.J. (1985). Short-cut operability analysis I, The relative disturbance gain, Ind. Ind. Chem. Process Des. Dev., 24, 1181-1188 doi:10.1021/i200031a048
[14] WALLER, K.V., HÄGGBLOM, K.E., SANDELIN. P.M. FINNERMAN, D.H. (1988). Disturbance sensitivity of distillation control structures, AIChE Journal, 34, 853-858 doi:10.1002/aic.690340516

BibTeX:
@article{MIC-1996-3-1,
  title={{Controllability measures for disturbance rejection}},
  author={Skogestad, Sigurd and Wolff, Erik A.},
  journal={Modeling, Identification and Control},
  volume={17},
  number={3},
  pages={167--181},
  year={1996},
  doi={10.4173/mic.1996.3.1},
  publisher={Norwegian Society of Automatic Control}
};

Article

“Controllability measures for disturbance rejection”