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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Nonsquare multivariable non-minimal state space-proportional integral plus (NMSS-PIP) control for atmospheric crude oil distillation column
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Nonsquare multivariable non-minimal state space-proportional integral plus (NMSS-PIP) control for atmospheric crude oil distillation column

机译:Nonsquare多变量non-minimal状态space-proportional积分+ (NMSS-PIP)控制大气原油蒸馏列

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摘要

The goal of this paper is to show implementation of non-minimal state space (NMSS) representation with proportional-integral-plus (PIP) controller for industrial crude distillation column. The control structure was designed and developed for MIMO nonsquare configuration. Weighting matrices of LQ optimal PIP control structure were achieved based on ITAE criteria for the column. The control performance of PIP control was compared with conventional PI control with different scenarios. The results show that PIP control handles the process interactions truly in order to utilize all variables simultaneously. In feed composition change scenario, the PIP control was stable and behaved robustly while the PI control had some difficulties. Furthermore, the proposed control structure indicates efficient performance for both disturbance rejection and set point tracking. (C) 2016 Published by Elsevier B.V. on behalf of Institution of Chemical Engineers.
机译:本文的目标是展示的实现non-minimal状态空间(nms)表示与proportional-integral-plus (PIP)控制器为工业原油蒸馏塔。控制结构设计和开发米姆nonsquare配置。LQ最优脉冲控制结构基于ITAE准则列。脉冲控制的控制性能进行了比较与传统PI控制与不同场景。处理过程真正的交互同时利用所有变量。成分变化情况下,脉冲控制稳定和表现强劲,而PI控制有一些困难。控制结构表明高效性能抗干扰性和设定点跟踪。化学工程师的代表机构。

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