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甘油生物歧化为1,3-丙二醇过程的优化控制
引用本文:徐恭贤,邵诚,修志龙.甘油生物歧化为1,3-丙二醇过程的优化控制[J].中国化学工程学报,2008,16(1):128-134.
作者姓名:徐恭贤  邵诚  修志龙
作者单位:1. Institute of Advanced Control Technology, Dalian University of Technology, Dalian 116024, China;2. Department of Bioscience and Biotechnology, Dalian University of Technology, Dalian 116024, China
基金项目:Supported by the State Science and Technology Project of China (No.2001BA204B01 )
摘    要:An iterative optimization strategy is proposed and applied to the steady state optimizing control of the bio-dissimilation process of glycerol to 1,3-propanediol in the presence of model-plant mismatch and input constraints. The scheme is based on the Augmented Integrated System Optimization and Parameter Estimation (AI- SOPE) technique, but a linearization of some performance function in the modified model-based optimization problem of AISOPE is introduced to overcome the difficulty of determining an appropriate penalty parameter. When carrying out the iterative optimization, the penalty coefficient is set to a larger value at the current iteration than at the previous iteration, which can promote the evolution rate of the iterative optimization. Simulation studies illustrate the potential ofthe approach presented for the optimizing control of the bioTdissimilation process of glycerol to 1,3-propanediol. The effects of measurement noise, measured and unmeasured disturbances on the proposed algorithm are also investigated.

关 键 词:steady  state  optimizing  control  iterative  optimization  bio-dissimilation  process  1  3-propanediol  pen-alty  coefficient  model  mismatch  
收稿时间:2007-06-23
修稿时间:2007-09-11

Optimizing control of bio-dissimilation process of glycerol to 1,3-propanediol
XU Gongxian,SHAO Cheng,XIU Zhilong.Optimizing control of bio-dissimilation process of glycerol to 1,3-propanediol[J].Chinese Journal of Chemical Engineering,2008,16(1):128-134.
Authors:XU Gongxian  SHAO Cheng  XIU Zhilong
Affiliation:Institute of Advanced Control Technology, Dalian University of Technology, Dalian 116024, China;Department of Bioscience and Biotechnology, Dalian University of Technology, Dalian 116024, China
Abstract:An iterative optimization strategy is proposed and applied to the steady state optimizing control of the bio-dissimilation process of glycerol to 1,3-propanediol in the presence of model-plant mismatch and input con-straints. The scheme is based on the Augmented Integrated System Optimization and Parameter Estimation (AI-SOPE) technique, but a linearization of some performance function in the modified model-based optimization problem of AISOPE is introduced to overcome the difficulty of determining an appropriate penalty parameter.When carrying out the iterative optimization, the penalty coefficient is set to a larger value at the current iteration than at the previous iteration, which can promote the evolution rate of the iterative optimization. Simulation studies illustrate the potential of the approach presented for the optimizing control of the bio-dissimilation process of glyc-erol to 1,3-propanediol. The effects of measurement noise, measured and unmeasured disturbances on the proposed algorithm are also investigated.
Keywords:steady state optimizing control  iterative optimization  bio-dissimilation process  1  3-propanediol  penalty coefficient  model mismatch
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