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Multivariable adaptive nonlinear predictive control: Development and application to a distillation column.

机译:多变量自适应非线性预测控制:蒸馏塔的开发和应用。

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Model-based predictive control (MPC) strategies have enabled a revolutionary leap in process control in the past twenty years. Even so, despite many commercial successes, conventional MPC applications can show significant performance deterioration when the controlled process exhibits significant time-varying and nonlinear characteristics. In addition, the computer resources required to rigorously address such characteristics can be prohibitive.; This research presents a novel, computationally efficient formulation of MPC that can mitigate such control performance deterioration. The new control strategy incorporates elements from the research areas of adaptive and nonlinear control, as well as MPC.; The controller is evaluated experimentally for the dual composition control of a multi-component distillation column. The controller is shown to perform well over a wide range of process conditions. The controller is easy to tune by specifying a single tuning parameter value for each controlled variable to achieve performance/robustness tradeoffs. A novel design for processes with general time-delay structures is presented. In addition, the controller is found to be applicable to non-square multivariable processes that include integrators and non-minimum phase characteristics through extensions reported by other researchers.
机译:在过去的20年中,基于模型的预测控制(MPC)策略在过程控制方面实现了革命性的飞跃。即使如此,尽管在商业上取得了许多成功,但是当受控过程显示出明显的时变和非线性特征时,常规的MPC应用程序仍会表现出明显的性能下降。另外,严格解决这些特征所需的计算机资源可能是禁止的。这项研究提出了一种新颖的,计算效率高的MPC配方,可以减轻这种控制性能的恶化。新的控制策略结合了自适应和非线性控制以及MPC研究领域的要素。通过实验对控制器进行了评估,以控制多组分蒸馏塔的双重成分。该控制器在各种工艺条件下均表现良好。通过为每个受控变量指定单个调整参数值以实现性能/鲁棒性的折衷,控制器易于调整。提出了一种具有一般时间延迟结构的过程的新颖设计。另外,发现该控制器适用于非平方多变量过程,该过程包括积分器和通过其他研究人员报告的扩展的非最小相位特性。

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