首页> 外文OA文献 >Control strategies for exothermic batch and fed-batch processes A sub-optimal strategy is developed which combines fast response with a chosen control signal safety margin. Design procedures are described and results compared with conventional control.
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Control strategies for exothermic batch and fed-batch processes A sub-optimal strategy is developed which combines fast response with a chosen control signal safety margin. Design procedures are described and results compared with conventional control.

机译:放热分批和补料分批过程的控制策略开发了次优策略,该策略将快速响应与选定的控制信号安全裕度相结合。描述了设计程序,并将结果与​​常规控件进行了比较。

摘要

There is a considerable scope for improving the temperature control ofudexothermic processes. In this thesis, a sub-optimal control strategyudis developed through utilizing the dynamic, simulation tool. Thisudscheme is built around easily obtained knowledge of the system andudstill retains flexibility. It can be applied to both exothermic batchudand fed-batch processes. It consists of servo and regulatory modes,udwhere a Generalized Predictive Controller (GPC) was used to provideudself-tuning facilities.udThe methods outlined allow for limited thermal runaway whilst keepingudsome spare cooling capacity to ensure that operation at constraintsudare not violated. A special feature of the method proposed is thatudswitching temperatures and temperature profiles can be readily foundudfrom plant trials whilst the addition rate profile Is capable ofudfairly straightforward computation. The work shows that It isudunnecessary to demand stability for the whole of the exothermicudreaction cycle, permitting a small runaway has resulted in a fastudtemperature response within the given safety margin.udThe Idea was employed for an exothermic single Irreversible reactionudand also to a set of complex reactions. Both are carried out in audvessel with a heating/cooling coil. Two constraints are Imposed; (1)udlimited heat transfer area, and (11) a maximum allowable reactionudtemperature Tmax.udThe non-minimum phase problem can be considered as one of theuddifficulties in managing exothermic fed-batch process when coldudreactant Is added to vessel at the maximum operating temperature. Theudcontrol system coped with this within limits, a not unexpected result.udIn all cases, the new strategy out-performed the conventionaludcontroller and produced smoother variations in the manipulatedudvariable. The simulation results showed that batch to batch variationsudand disturbances In cooling were successfully handled. GPC worked welludbut can be susceptible to measurement noise.
机译:在改善放热过程的温度控制方面存在很大的范围。本文利用动态仿真工具开发了次优控制策略。该 udscheme围绕容易获得的系统知识而建立,并且 udest保留了灵活性。它可以应用于放热分批处理和补料分批处理。它由伺服和调节模式组成,其中使用了通用预测控制器(GPC)来提供自调整功能。 ud概述的方法允许有限的热失控,同时保持过大的备用冷却能力,以确保在限制条件下运行不敢违反。所提出的方法的一个特殊之处在于,可以很容易地从工厂试验中找到切换温度和温度曲线,而添加速率曲线可以非常简单地进行计算。这项工作表明,在整个放热/放气循环中都没有必要要求稳定性,允许小的失控导致在给定的安全范围内快速/耐高温响应。 ud该想法用于放热的单个不可逆反应 udand也会引起一系列复杂的反应。两者都在带有加热/冷却盘管的容器中进行。施加了两个约束: (1)有限的传热面积,(11)最大允许的反应高温Tmax。 ud非最小相问题可以被认为是添加冷过反应剂时处理放热分批进料过程的难点之一。在最高工作温度下运输到容器。 udcontrol系统在有限的范围内解决了这个问题,这并不是一个意外的结果。 ud在所有情况下,新策略的性能均优于常规 udcontroller,并且在受控 udvariable中产生了更平滑的变化。仿真结果表明,成功地处理了冷却过程中批次间的变化 udand扰动。 GPC运作良好 ud,但是容易受到测量噪声的影响。

著录项

  • 作者

    Kaymaz I. Ali;

  • 作者单位
  • 年度 1989
  • 总页数
  • 原文格式 PDF
  • 正文语种 en
  • 中图分类

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