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Optimal temperature control in a batch polymerization reactor using nonlinear generalized predictive control

机译:使用非线性广义预测控制的间歇式聚合反应器中的最佳温度控制

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The application of Non-Linear Generalized predictive Control (NLGPC) to the free radical solution polymerization of styrene in a jacketed batch reactor has been realized.The dynamic behavior of polymerziation reactor is modelled and simulated for control purposes.The optimal temperature policies for mininmum time,desired conversion and molecular chain length were obtained at different initiator concentrations by applying the optimal control theory which is based on the Hamiltonian principle.The polynomial Nonlinear auto Regressive Integrated Moving Average with eXternal input (NARIMAX) model is used to relate the reactor temperature with heat input for nonlinear control algorithm.The linear (ARIMAX) and nonlinear (NARIMAX) models are utilized in the GPC algorithm for comparison.A Pseudo Random Binary Sequence (PRBS) signal was employed tooperate the system.The model paraters are evaluated by using Levenberg Marquart Method.The NLGPC,Linear Generalized Predictive Control (LGPC) and standard PID controllers are applied experimentally to the polymerziation reactor by using on-line computer control system.The performance of NLGPC control system was compared with LGPC and standard PID controller.It is concludied that the NLGPC control gives much better performance than the other.
机译:实现了非线性广义预测控制(NLGPC)在夹套间歇式反应器中苯乙烯自由基溶液聚合中的应用,对聚合反应器的动力学行为进行了建模和仿真以达到控制目的。最短时间的最佳温度策略通过基于汉密尔顿原理的最优控制理论,在不同的引发剂浓度下获得了理想的转化率和分子链长度。带有外部输入的多项式非线性自回归积分移动平均值(NARIMAX)模型用于将反应堆温度与非线性控制算法的热量输入.GPC算法中使用线性(ARIMAX)模型和非线性(NARIMAX)模型进行比较;使用伪随机二进制序列(PRBS)信号对系统进行操作。使用Levenberg评估模型参数Marquart方法。NLGPC,线性广义预测控制(LGPC)和标准dard PID控制器通过在线计算机控制系统在聚合反应器上进行了实验性应用。将NLGPC控制系统的性能与LGPC和标准PID控制器进行了比较,结论是NLGPC控制的性能要优于其他控制器。

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