...
首页> 外文期刊>Arabian Journal for Science and Engineering >Set-Point Supervisory Control Methodology for a Nonlinear Continuous Stirred Tank Reactor Process
【24h】

Set-Point Supervisory Control Methodology for a Nonlinear Continuous Stirred Tank Reactor Process

机译:非线性连续搅拌釜反应器过程的设定点监控方法

获取原文
获取原文并翻译 | 示例

摘要

In this paper, a set-point supervisory control methodology for switching and tuning is developed for nonlinear systems. This control strategy is evaluated in the simulation of highly nonlinear continuous stirred tank reactor process. In the first step, closed-loop adaptive control algorithm is used to estimate a bank of models and to calculate their corresponding controllers, each of these models and their associate controllers are tuning around a given operating points. Thereafter, an intelligent supervisor is implemented to orchestrate the switching between different models and to select at each instant the adequate and the best controller to the plant. The simulation results found for three scenarios that correspond to different scaling of the set-point show the effectiveness and superiority in terms of performances and robustness characteristics of this proposed control approach comparing with closed loop adaptive controller.
机译:在本文中,为非线性系统开发了一种用于切换和整定的设定点监督控制方法。在高度非线性的连续搅拌釜反应器过程的仿真中评估了该控制策略。第一步,使用闭环自适应控制算法来估计一组模型并计算其相应的控制器,这些模型中的每个模型及其关联控制器都围绕给定的工作点进行调整。此后,实施了智能管理器来协调不同模型之间的切换,并在每个时刻为工厂选择合适的最佳控制器。在与设定点的不同缩放比例相对应的三种情况下找到的仿真结果显示,与闭环自适应控制器相比,该控制方法在性能和鲁棒性方面表现出优势和优势。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号