2016
DOI: 10.1002/cjce.22633
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A novel fast dynamic optimization approach for complex multivariable chemical process systems

Abstract: A novel fast dynamic optimization approach is proposed for complex multivariable chemical process systems, where the control variables are parameterized with different non‐uniform time grids and are treated as optimal decision variables to obtain the optimal switching structures for tackling the shortcoming caused by the conventional uniform parameterization method. Meanwhile, an adaptive fast calculation approach is proposed to calculate the differential equations so as to decrease the optimization time. The … Show more

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Cited by 9 publications
(5 citation statements)
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“…In other words, the zinc dust addition rate must remain constant during this period. This paper uses the control vector parameterization method to transform the optimal control problem into a parameter optimization problem, which can significantly reduce the computation complexity. Suppose the rolling optimization always starts at t 0 , the prediction horizon and the control horizon are all set as P steps.…”
Section: Time‐varying Icstr Model‐based Predictive Control For the Sementioning
confidence: 99%
“…In other words, the zinc dust addition rate must remain constant during this period. This paper uses the control vector parameterization method to transform the optimal control problem into a parameter optimization problem, which can significantly reduce the computation complexity. Suppose the rolling optimization always starts at t 0 , the prediction horizon and the control horizon are all set as P steps.…”
Section: Time‐varying Icstr Model‐based Predictive Control For the Sementioning
confidence: 99%
“…[45] . 硫化后纳 米零价铁性质的变化与其表面化学和晶相转化密切相 关. Su 等 [46] [44] Peaks are referred to magnetite Fe 3 O 4 (M) 图 9 纳米零价铁在水相反应中表面化学和晶相转化模型图 Figure 9 A concept model of nZVI surface chemistry and crystal phase evolution in aquatic medium…”
Section: 纳米零价铁表面化学和晶相结构mentioning
confidence: 99%
“…Figure 8 nZVI, nZVI APAM and nZVI CMC corroded aerobically for 2 h. (a) SEM; (b) XRD; (c) Ni(II) removal[44] …”
mentioning
confidence: 99%
“…The schematic of a typical fed‐batch reactor is presented in Fig. as illustration . The objective is to find the optimal temperature profile that maximizes the target product B at the final time of an operation in a batch reactor, where the reaction A → B → C takes place.…”
Section: Case Studiesmentioning
confidence: 99%