Within-batch and batch-to-batch inferential-adaptive control of semibatch reactors: A partial least squares approach

被引:82
作者
Flores-Cerrillo, J [1 ]
MacGregor, JF [1 ]
机构
[1] McMaster Univ, Dept Chem Engn, Hamilton, ON L8S 4L7, Canada
关键词
D O I
10.1021/ie020596u
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An inferential control strategy that combines within-batch information from process variable trajectories and information from prior batches to control multivariate product quality properties in semibatch reactors is presented. The approach extends mid-course correction (MCC) strategies by including batch-to-batch information in the controllers and an adaptive partial least squares (PLS) approach to update the models from batch to batch. As with other MCC approaches, the scheme retains the "no-control region" concept where control is taken at various stages during the batch only if the projected error in the final quality is deemed to be statistically significant. Only data on readily available process measurements (e.g., temperatures) throughout the batch, plus a measurement on a variable related to quality (e.g., particle size) at one or more discrete times during the batch, are required to achieve very precise control of the final product quality (e.g., particle-size distribution, PSD). Latent variable models based on PLS are a key element in the approach. They are able to extract information efficiently from the large number of highly correlated measurements on the process variable trajectories and relate it to high-dimensional output measurements on product quality (e.g., PSD) by projecting this information into low-dimensional latent variable spaces. The methodology is applied to the control of PSD in emulsion polymerization. The problem of regulation about a fixed set-point PSD in the face of disturbances and the problem of achieving new set-point PSDs are both illustrated.
引用
收藏
页码:3334 / 3345
页数:12
相关论文
共 57 条
[1]   PLS regression methods [J].
Höskuldsson, Agnar .
Journal of Chemometrics, 1988, 2 (03) :211-228
[2]  
BODE CA, 2002, 15 IFAC WORLD C BARC
[3]  
BONNE D, 2001, 6 IFAC S JUN 4 6, P449
[4]   Optimal operation of batch reactors - a personal view [J].
Bonvin, D .
JOURNAL OF PROCESS CONTROL, 1998, 8 (5-6) :355-368
[5]  
Bonvin D., 2002, AICHE S SER, P255
[6]  
BOX GEP, 1970, TIME SERIES ANAL FOR
[7]  
Box GEP., 1978, Statistics for experimenters
[8]   Integrated quality and tracking control of a batch PMMA reactor using a QBMPC technique [J].
Chae, DC ;
Chin, I ;
Lee, KS ;
Rho, H ;
Rhee, H ;
Lee, JH .
COMPUTERS & CHEMICAL ENGINEERING, 2000, 24 (2-7) :953-958
[9]   A technique for integrated quality control, profile control, and constraint handling for batch processes [J].
Chin, IS ;
Lee, KS ;
Lee, JH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (03) :693-705
[10]   Optimization of molecular-weight distribution using batch-to-batch adjustments [J].
Clarke-Pringle, TL ;
MacGregor, JF .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (09) :3660-3669