首页> 外文会议>Control Systems Conference; 20040614-18; Quebec City(CA) >DISTRIBUTED PARAMETER PREDICTIVE CONTROL OF BLEACHING TOWERS
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DISTRIBUTED PARAMETER PREDICTIVE CONTROL OF BLEACHING TOWERS

机译:漂白塔的分布参数预测控制

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In bleaching towers the process variables, such as lignin and chemical concentrations, vary spatially within the reactor. Processes in which the variables of interest vary spatially are termed distributed parameter systems (DPS) and represent a substantial challenge for developing high performance control systems. This control challenge in DPS stems from the requirement that process dynamics must be represented in terms of partial differential equations (PDE) and/or integral equations; whereas, almost all of control theory assumes that the process dynamics can be represented by ordinary differential equations (ODE). In this paper, we present the key ideas in the development of a distributed parameter approach to model predictive control (MPC) of chemical bleaching towers. The proposed control approach is based on the method of characteristics and uses finite difference approximations of the second-order (diffusion) terms in bleaching tower models. This approach allows the underlying PDE model to be converted to a set of ODEs, which are amenable to the rich array of advanced control techniques currently available. The efficacy of the proposed method is illustrated using a chlorine dioxide bleaching case study. It should be noted that although the method is illustrated with a ClO_2 simulation study, our technique applies to any convection-diffusion-reaction system at high Peclet numbers. The performance of our approach is compared to a more standard, finite-difference MPC approach with respect to control accuracy, robustness to plant-model mismatch and computational expense.
机译:在漂白塔中,工艺变量(例如木质素和化学浓度)在反应器内空间变化。感兴趣的变量在空间上变化的过程称为分布式参数系统(DPS),对开发高性能控制系统提出了重大挑战。 DPS中的控制挑战源于要求过程动力学必须以偏微分方程(PDE)和/或积分方程表示的要求;然而,几乎所有的控制理论都假设过程动力学可以用常微分方程(ODE)表示。在本文中,我们提出了在化学漂白塔的模型预测控制(MPC)模型的分布式参数方法开发中的关键思想。所提出的控制方法基于特性方法,并在漂白塔模型中使用了二阶(扩散)项的有限差分近似。这种方法允许将基础PDE模型转换为一组ODE,这些ODE可以适应当前可用的丰富的高级控制技术。通过二氧化氯漂白案例研究说明了所提出方法的有效性。应该注意的是,尽管该方法通过ClO_2模拟研究进行了说明,但我们的技术适用于任何高Peclet数的对流-扩散-反应系统。在控制精度,对工厂模型不匹配的鲁棒性和计算费用方面,我们的方法的性能与更标准的有限差分MPC方法进行了比较。

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