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Nonlinear process-model-based control and optimization of batch polymerization reactor.

机译:基于非线性过程模型的间歇聚合反应器控制和优化。

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A batch polymerization reactor simulator which generates dynamics of state variables including temperature and molecular weight distribution (MWD). The "method of moments" and a novel technique, "class method" are used to calculate the leading distribution parameters and the approximate entire MWD respectively.; The dynamic simulator is used to test Nonlinear Model-Based Control (NMBC) strategy for the temperature control of batch polymerization reactor described by the nonlinear and nonstationary process behavior. The simulator is also used for optimization studies which is to find optimum operation recipes which give the specified MWD and minimum reaction time. A direct searching method, the "complex method," is used as an optimizer.; The simulation studies show a very promising results. Both the "method of moments" and "class method" are effective to generate the distribution parameters and entire distribution. A single control strategy, NMBC, effectively controls the reactor temperature from the initial heat-up to the end of reaction. The optimizer searches the optimum of operation recipes with choices of product and operation target.
机译:间歇聚合反应器模拟器,可生成状态变量的动力学信息,包括温度和分子量分布(MWD)。 “矩量法”和一种新颖的技术“分类法”分别用于计算领先的分布参数和近似的整个MWD。动态仿真器用于测试基于非线性模型和非平稳过程行为描述的间歇式聚合反应器温度控制的基于非线性模型的控制(NMBC)策略。该模拟器还用于优化研究,以找到给出指定的MWD和最短反应时间的最佳操作配方。直接搜索方法“复杂方法”用作优化程序。仿真研究显示了非常有希望的结果。 “矩量方法”和“分类方法”都可以有效地生成分布参数和整个分布。单一控制策略NMBC有效地控制了从初始加热到反应结束的反应器温度。优化器根据产品和操作目标的选择来搜索最佳的操作配方。

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