1997
DOI: 10.1002/aic.690430511
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Estimation of nonlinear systems using linear multiple models

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Cited by 111 publications
(63 citation statements)
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References 16 publications
(13 reference statements)
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“…These variables and their units are given in Table 1. Banerjee et al (1997) the solvent feed rate G s and the reactor feed temperature T rf are treated as measured disturbance variables, and are used along with the other simulation inputs for state estimation. The inhibitor flowrate is treated as an unmeasured disturbance, and is not used for estimation purposes.…”
Section: Solution Copolymerization Simulationmentioning
confidence: 99%
“…These variables and their units are given in Table 1. Banerjee et al (1997) the solvent feed rate G s and the reactor feed temperature T rf are treated as measured disturbance variables, and are used along with the other simulation inputs for state estimation. The inhibitor flowrate is treated as an unmeasured disturbance, and is not used for estimation purposes.…”
Section: Solution Copolymerization Simulationmentioning
confidence: 99%
“…This algorithm can be used in the same manner as the classical multiple model algorithms for other applications. Examples of such applications are, but not limited to, multiple model adaptive control (Athans et al, 2005), fault-tolerant control (Zhang and Jiang, 2001) and approximation of nonlinear systems with multiple models (Banerjee et al, 1997). This paper is organized as follows.…”
Section: Introductionmentioning
confidence: 99%
“…The index values are always a certain number within this interval, and there will be preference information, which may result in error in decision making [1]. In References [2][3], the expression of index numerical number using interval number is proposed. However, the interval value will be too big in such a case.…”
Section: Introductionmentioning
confidence: 99%