多级蒸发器系统分数阶控制器的设计与优化整定

IF 3 Q2 ENGINEERING, CHEMICAL Digital Chemical Engineering Pub Date : 2023-09-26 DOI:10.1016/j.dche.2023.100125
Smitarani Pati , Nikhil Pachori , Gaurav Manik , Om Prakash Verma
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引用次数: 0

摘要

通过适当调节控制器来严格控制工艺参数是一门迫切应用于各种工艺工业的技术。这些行业中的大多数都受到由于输入参数变化和扰动存在而产生的非线性的影响。本工作的目的是研究基于造纸工业的多段蒸发器(MSE)能源密集型装置在不同节能方案下的非线性动力学。MSE用于浓缩弱黑液(BL),这是一种基于生物质的副产品。因此,为了从BL中提取生物能,需要适当控制产品液的质量。BL的质量通过两个工艺参数来测量,即产品浓度和温度。因此,在本工作中,研究并采用了一种智能控制器分数阶比例积分微分控制器来解决伺服和调节过程中出现的问题。本文提出了一种最先进的元启发式方法——黑寡妇优化算法来调整控制器参数,并与另一种优化方法——水循环算法进行了比较。仿真结果证明了所提出的策略的有效性,并证实了工艺参数的性能改进。为了说明所提出的控制方案的优点,还与传统PID、2-DOF-PID和FOPID控制器进行了比较分析。
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Design and optimal tuning of fraction order controller for multiple stage evaporator system

The tight control of the process parameters through appropriate tuning of controllers is an art that imperatively employed to various process industries. Most of these industries are influenced by the nonlinearity that occurred due to the input parameter variation and presence of disturbances. The aim of this work is to investigate the nonlinear dynamics of a paper industry based energy intensive unit named Multiple Stage Evaporator (MSE) in presence of different Energy Reduction Schemes. MSE is used to concentrate the weak Black Liquor (BL), a biomass based byproduct. Hence, to extract the bioenergy from the BL, the quality of the product liquor needs to be appropriately controlled. The quality of BL is measured by two process parameters, product concentration and temperature. Hence, in this work, an intelligent controller Fraction Order Proportional-Integral-Derivative controller has been studied and employed to resolve the servo and the regulatory problem occurred during the process. A state-of-art metaheuristic approach, Black Widow Optimization Algorithm has been proposed here to tune the controller parameters and compared with another optimization approaches named Water Cycle Algorithm. The simulated result demonstrates the usefulness of the proposed strategy and confirm the performance improvement for the process parameters. To enlighten the advantages of the proposed control scheme, a comparative analysis have also been performed with conventional PID, 2-DOF-PID and FOPID controllers.

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