共查询到17条相似文献,搜索用时 46 毫秒
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针对具有输入时滞的多阶段间歇过程,考虑执行器故障影响,提出了无穷时域优化混杂容错控制器设计方法。该方法首先将给定具有输入时滞的模型转化为新的无时滞的状态空间模型,接着再将此模型转换为包含状态变量误差和输出跟踪误差的扩展状态空间模型,并用切换系统模型表示,然后引入有限时域的二次目标函数,利用最优控制理论,设计出在无穷时域中容错控制器。为获得最小运行时间,针对不同阶段设计依赖于Lyapunov函数的驻留时间方法。创新之处在于,控制律设计简单,计算量小,且每一阶段时间求取不需要引用任何其他变量,简单易行。最后,以注塑成型过程为例,仿真结果证明所提出方法具有可行性和有效性。 相似文献
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基于T-S模糊模型的间歇过程的迭代学习容错控制 总被引:3,自引:1,他引:2
间歇过程不仅具有强非线性,同时还会受到诸如执行器等故障影响,研究非线性间歇过程在具有故障的情况下依然稳定运行至关重要。针对执行器增益故障及系统所具有的强非线性,提出一种新的基于间歇过程的T-S模糊模型的复合迭代学习容错控制方法。首先根据间歇过程的非线性模型,利用扇区非线性方法建立其T-S模糊故障模型,再利用间歇过程的二维特性与重复特性,在2D系统理论框架内,设计2D复合ILC容错控制器,进而构建此T-S模糊模型的等价二维Rosser模型,接着利用Lyapunov方法给出系统稳定充分条件并求解控制器增益。针对强非线性的连续搅拌釜进行仿真,结果表明所提出方法具有可行性与有效性。 相似文献
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首先指出间歇过程是一门独立的、有自身特点的、在化学工业中具有独特地位的学科。然后扼要回顾了计算机在间歇过程设计和生产调度中的应用,并介绍了几个典型的用于间歇过程的软件。最后简单介绍了由ISA颁布的间歇控制标准SP88,以便读者了解该领域的最新国际动态 相似文献
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间歇过程优化与先进控制综述 总被引:11,自引:3,他引:8
总结近年来间歇过程操作优化和设计优化中出现的各种新方法,以及在优化问题求解中使用的各种先进控制策略,反映间歇过程最优化和先进控制的最新研究方向。重点介绍间歇过程单元的操作优化和控制,兼顾在线稳态优化和动态优化。对新的研究方法提出展望。 相似文献
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针对间歇过程中因忽略数据在阶段划分中的非线性,导致故障监测精度低的问题,提出一种基于扩散距离的信息熵模糊C均值(DDEFCM)多阶段长短期记忆网络的自动编码器(LSTM-AE)间歇过程故障监测方法。首先为了自动识别聚类个数,利用信息熵描述批处理后的二维时间片矩阵。再采用扩散距离对模糊C均值聚类(FCM)算法进行改进,解决欧式距离不能表征数据非线性的问题,有效划分间歇过程的稳定阶段,然后利用轮廓系数划分过渡阶段。最后建立多阶段LSTM-AE监测模型。利用青霉素发酵数据和大肠杆菌实际生产数据对该方法进行验证,结果表明所提方法不仅可以提升阶段划分性能,还能更加准确地进行故障监测。 相似文献
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基于MPLS的间歇过程终点质量迭代优化控制 总被引:2,自引:0,他引:2
提出了多向偏最小二乘(MPLS)模型和迭代学习控制相结合的方法,实现间歇过程终点时刻产品质量指标的控制.利用间歇过程的重复特性,根据前一批次的终点质量偏差调整下-批次控制变量的轨迹,从而使质量指标逐步接近于理想指标.本文提出的方法可以有效地消除由于模型误差和未知扰动引起的质量偏差.在苯乙烯间歇聚合反应模型上进行了仿真分析,验证了该方法的有效性. 相似文献
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Siam Aumi Brandon Corbett Tracy Clarke‐Pringle Prashant Mhaskar 《American Institute of Chemical Engineers》2013,59(8):2852-2861
The problem of driving a batch process to a specified product quality using data‐driven model predictive control (MPC) is described. To address the problem of unavailability of online quality measurements, an inferential quality model, which relates the process conditions over the entire batch duration to the final quality, is required. The accuracy of this type of quality model, however, is sensitive to the prediction of the future batch behavior until batch termination. In this work, we handle this “missing data” problem by integrating a previously developed data‐driven modeling methodology, which combines multiple local linear models with an appropriate weighting function to describe nonlinearities, with the inferential model in a MPC framework. The key feature of this approach is that the causality and nonlinear relationships between the future inputs and outputs are accounted for in predicting the final quality and computing the manipulated input trajectory. The efficacy of the proposed predictive control design is illustrated via closed‐loop simulations of a nylon‐6,6 batch polymerization process with limited measurements. © 2013 American Institute of Chemical Engineers AIChE J, 59: 2852–2861, 2013 相似文献
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José Camacho Jesús Picó Alberto Ferrer 《American Institute of Chemical Engineers》2007,53(7):1789-1804
Unfold Partial-Least Squares (u-PLS) is a modeling method successfully applied to batch-process monitoring and end quality prediction. This method is integrated in a self-tuning optimization algorithm, based on extremum-seeking control. The optimization is driven by the gradient obtained by means of an adaptive u-PLS model. Since this is an empirical model, no first-principles based knowledge of the process is necessary. Heuristic rules are used to constrain the gradient taking into account nonlinearity and unknown causes of variability. Extensions to model the variability in initial conditions, to optimize several performance indices, and to handle inequality constraints are presented. The optimization algorithm is tested on a complex comprehensive simulated-process model for the fed-batch cultivation of Sacharomyces cerevisiae. Results show the performance and versatility of the proposed approach, as well as its robustness to process changes. © 2007 American Institute of Chemical Engineers AIChE J, 2007 相似文献
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论述了化学工业两化融合发展,趋向精细化、服务化和可持续化,对过程系统工程(PSE)提出挑战.研究了过程系统工程应从产品工程/纳米过程系统工程、间歇过程系统工程、供应链的优化与协同、多尺度过程集成及绿色过程系统工程5个方面提供技术支撑的前景. 相似文献
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Oswaldo Andrés-Martínez Luis A. Ricardez-Sandoval 《American Institute of Chemical Engineers》2022,68(5):e17665
In the pursuit of integrated scheduling and control frameworks for chemical processes, it is important to develop accurate integrated models and computational strategies such that optimal decisions can be made in a dynamic environment. In this study, a recently developed switched system formulation that integrates scheduling and control decisions is extended to closed-loop operation embedded with nonlinear model predictive control (NMPC). The resulting framework is a nested online scheduling and control loop that allows to obtain fast and accurate solutions as no model reduction is needed and no integer variables are involved in the formulations. In the outer loop, the integrated model is solved to calculate an optimal product switching sequence such that the process economics is optimized, whereas in the inner loop, an NMPC implements the scheduling decisions. The proposed scheme was tested on two multi-product continuous systems. Unexpected large disturbances and rush orders were handled effectively. 相似文献