首页> 外文OA文献 >DESIGN OF OPTIMAL PROCEDURAL CONTROLLERS FOR CHEMICAL PROCESSES MODELLED AS STOCHASTIC DISCRETE EVENT SYSTEMS
【2h】

DESIGN OF OPTIMAL PROCEDURAL CONTROLLERS FOR CHEMICAL PROCESSES MODELLED AS STOCHASTIC DISCRETE EVENT SYSTEMS

机译:用作随机离散事件系统的化学过程最优程序控制器的设计

摘要

This thesis presents a formal method for the the design of optimal and provably correctudprocedural controllers for chemical processes modelled as Stochastic Discrete Event Systemsud(SDESs). The thesis extends previous work on Procedural Control Theory (PCT) [1],udwhich used formal techniques for the design of automation Discrete Event Systems (DESs).udMany dynamic processes for example, batch operations and the start-up and shut down ofudcontinuous plants, can be modelled as DESs. Controllers for these systems are typicallyudof the sequential type.udMost prior work on characterizing the behaviour of DESs has been restricted to deterministicudsystems. However, DESs consisting of concurrent interacting processes presentuda broad spectrum of uncertainty such as uncertainty in the occurrence of events. Theudformalism of weighted probabilistic Finite State Machine (wp-FSM) is introduced forudmodelling SDESs and pre-de ned failure models are embedded in wp-FSM to describeudand control the abnormal behaviour of systems. The thesis presents e cient algorithmsudand procedures for synthesising optimal procedural controllers for such SDESs.udThe synthesised optimal controllers for such stochastic systems will take into considerationudprobabilities of events occurrence, operation costs and failure costs of events inudmaking optimal choices in the design of control sequences. The controllers will force theudsystem from an initial state to one or more goal states with an optimal expected cost andudwhen feasible drive the system from any state reached after a failure to goal states.udOn the practical side, recognising the importance of the needs of the target enduduser, the design of a suitable software implementation is completed. The potential of bothudthe approach and the supporting software are demonstrated by two industry case studies.udFurthermore, the simulation environment gPROMS was used to test whether the operatingudspeci cations thus designed were met in a combined discrete/continuous environment.
机译:本文提出了一种形式化的方法,用于设计建模为随机离散事件系统 ud(SDES)的化学过程的最优且证明正确的过程控制器。论文扩展了以前关于过程控制理论(PCT)[1]的工作,该过程使用形式化技术来设计自动化离散事件系统(DES)。 ud许多动态过程,例如批处理操作以及启动和关闭不连续的植物,可以建模为DES。这些系统的控制器通常是顺序类型的。ud表征DES行为的大多数先前工作仅限于确定性的系统。但是,由并发交互过程组成的DES呈现出广泛的不确定性,例如事件发生中的不确定性。引入了概率概率有限状态机(wp-FSM)的形式主义来对SDES进行建模,并在wp-FSM中嵌入了预定的故障模型来描述/控制系统的异常行为。本文提出了用于合成此类SDES最优过程控制器的高效算法 udc程序。 ud此类随机系统的综合最优控制器将考虑事件发生的概率,事件发生的操作成本和失败成本在进行最优选择时控制序列的设计。控制器将以最佳的预期成本将系统从初始状态强制转换为一个或多个目标状态,并且在可行的情况下,将系统从故障后达到的任何状态驱动至目标状态。根据目标最终用户的需求,完成了合适的软件实现的设计。该方法和支持软件的潜力已通过两个行业案例研究得到了证明。 ud此外,仿真环境gPROMS用于测试在离散/连续的组合环境中是否满足了如此设计的操作规范。

著录项

  • 作者

    Feng Zhangpeng;

  • 作者单位
  • 年度 2008
  • 总页数
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类

相似文献

  • 外文文献
  • 中文文献
  • 专利

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