Model-free real-time optimization of process systems using safe Bayesian optimization

被引:8
|
作者
Krishnamoorthy, Dinesh [1 ,2 ]
Doyle, Francis J. [2 ]
机构
[1] Eindhoven Univ Technol, NL-5600 MB Eindhoven, Netherlands
[2] Harvard John A Paulson Sch Engn & Appl Sci, Allston, MA 02134 USA
关键词
Bayesian optimization; model-free optimization; real-time optimization; LOOP; STRATEGIES;
D O I
10.1002/aic.17993
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Conventional real-time optimization (RTO) requires detailed process models, which may be challenging or expensive to obtain. Model-free RTO methods are an attractive alternative to circumvent the challenge of developing accurate models. Most model-free RTO methods are based on estimating the steady-state cost gradient with respect to the decision variables and driving the estimated gradient to zero using integral action. However, accurate gradient estimation requires clear time scale separation from the plant dynamics, such that the dynamic plant can be assumed to be a static map. For processes with long settling times, this can lead to prohibitively slow convergence to the optimum. To avoid the need to estimate the cost gradients from the measurement, this article uses Bayesian optimization, which is a zeroth order black-box optimization framework. In particular, this article uses a safe Bayesian optimization based on interior point methods to ensure that the setpoints computed by the model-free steady-state RTO layer are guaranteed to be feasible with high probability (i.e., the safety-critical constraints will not be violated at steady-state). The proposed method can thus be seen as a model-free variant of the conventional two-step steady-state RTO framework (with steady-state detection), which is demonstrated on a benchmark Williams-Otto reactor example.
引用
收藏
页数:13
相关论文
共 50 条
  • [31] Guest Editorial: Optimization of real-time systems
    Anderson, James H.
    Rochange, Christine
    REAL-TIME SYSTEMS, 2014, 50 (03) : 315 - 316
  • [32] Model Parameterization Tailored to Real-time Optimization
    Chachuat, Benoit
    Srinivasan, Bala
    Bonvin, Dominique
    18TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, 2008, 25 : 1 - 13
  • [33] A Real-Time Model-Free Reconfiguration Mechanism for Fault-Tolerance: Application to a Hydraulic Process
    Yame, Joseph J.
    Sauter, Dominique
    2008 10TH INTERNATIONAL CONFERENCE ON CONTROL AUTOMATION ROBOTICS & VISION: ICARV 2008, VOLS 1-4, 2008, : 91 - +
  • [34] Model-free optimization in cement plants
    Holmes, DS
    IEEE-IAS/PCA 2003 CEMENT INDUSTRY TECHNICAL CONFERENCE, CONFERENCE RECORD, 2003, : 159 - 173
  • [35] Model-Free Nonlinear Feedback Optimization
    He, Zhiyu
    Bolognani, Saverio
    He, Jianping
    Dorfler, Florian
    Guan, Xinping
    IEEE TRANSACTIONS ON AUTOMATIC CONTROL, 2024, 69 (07) : 4554 - 4569
  • [36] Real-time optimization for gold cyanidation leaching process
    Zhang, Jun
    Mao, Zhi-Zhong
    Jia, Run-Da
    Kongzhi Lilun Yu Yingyong/Control Theory and Applications, 2014, 31 (09): : 1198 - 1205
  • [37] A Real-Time Process Optimization System for Injection Molding
    Li, Dequn
    Zhou, Huamin
    Zhao, Peng
    Li, Yang
    POLYMER ENGINEERING AND SCIENCE, 2009, 49 (10): : 2031 - 2040
  • [38] Results diagnosis for real-time process operations optimization
    Miletic, IP
    Marlin, TE
    COMPUTERS & CHEMICAL ENGINEERING, 1998, 22 : S475 - S482
  • [39] Distributed control and real-time optimization of a chemical process
    Ydstie, BE
    Coffey, DP
    DYNAMICS & CONTROL OF PROCESS SYSTEMS 1998, VOLUMES 1 AND 2, 1999, : 691 - 696
  • [40] Dynamic Real-time Optimization of a Batch Polymerization Process
    Bousbia-Salah, Ryad
    Lesage, Francois
    Hu, Guo-Hua
    Latifi, Abderrazak
    27TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, PT B, 2017, 40B : 1741 - 1746