On-line optimization of constrained mult
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Shi-Shang Jang; Babu Joseph; Hiro Mukai
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Article
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1987
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American Institute of Chemical Engineers
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English
β 721 KB
A two-phase approach to the control and operation of complex chemical processes at their optimum operating conditions is presented. The first phase consists of on-line parameter identification and state estimation of approximate nonlinear dynamic process models using on-line and off-line measurement