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CONTROL STRATEGIES FOR BATCH CRYSTALLIZATION PROCESSES.

机译:批量结晶过程的控制策略。

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摘要

Batch crystallization is a key step in the production of pharmaceuticals, fine chemicals and food products. To date, only a few studies have been concerned with the question of open-loop strategies for control of the Crystal Size Distribution (CSD) and none, with feedback control strategies. To provide general guidelines for CSD control in batch systems, the author sought, in this study, to accomplish the following objectives: (1) the development of algorithms to calculate the operating condition sequence such that specific criteria or performance indices for the product CSD are satisfied (2) the identification of feedback control strategies to ensure attainment of a specified performance index (3) the design of estimators to overcome the limitations of currently-available on-line measurement instrumentation.The method developed in this study for identification of crystallizer control strategies may also be valuable for control of certain batch reactors such as emulsion polymerization or fermentation systems.Two approaches were adopted to achieve the first objective: the distributed system approach described in Chapter II and the lumped system approach in Chapter IV. The distributed approach involved solving the population balance equation by the method of characteristics. The algorithm derived from this approach permits calculation of the operating condition sequence such that a predetermined specific CSD will be obtained at the end of the crystallization process. The lumped approach is based on the transformed moment equations. Here, the Continuous Maximum Principle was applied to extremize various performance indices expressed in terms of the moments. A feedback control strategy has been developed (Chapter V) to maintain a specified performance index at its nominal value by a one-step iteration method. Finally, on-line measurement, estimation and identification studies, which can be considered a practical application of the distributed system approach, have been carried out in Chapter III.
机译:分批结晶是药品,精细化学品和食品生产中的关键步骤。迄今为止,只有很少的研究与控制晶体尺寸分布(CSD)的开环策略有关,而没有一个与反馈控制策略有关。为了为批处理系统中的CSD控制提供一般指导,作者在本研究中寻求实现以下目标:(1)开发算法以计算操作条件序列,从而使产品CSD的特定标准或性能指标得到满足满足(2)确定反馈控制策略以确保达到指定的性能指标(3)估算器的设计以克服当前可用的在线测量仪器的局限性。本研究中开发的用于确定结晶器控制的方法这些策略对于控制某些间歇式反应器(例如乳液聚合或发酵系统)可能也很有价值。为实现第一个目标,采用了两种方法:第二章所述的分布式系统方法和第四章所述的集总系统方法。分布式方法涉及通过特征方法求解人口平衡方程。从这种方法得出的算法允许计算操作条件序列,以便在结晶过程结束时获得预定的特定CSD。集总方法基于变换的矩方程。在这里,连续最大原理被应用到对各种表现指标进行极端化。已经开发出一种反馈控制策略(第V章),以通过一步迭代方法将指定的性能指标保持在其标称值。最后,第三章已经进行了在线测量,估计和识别研究,可以将其视为分布式系统方法的实际应用。

著录项

  • 作者

    CHANG, CHUEI-TIN.;

  • 作者单位

    Columbia University.;

  • 授予单位 Columbia University.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 1982
  • 页码 295 p.
  • 总页数 295
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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