Advanced control approaches for combined cooling/antisolvent crystallization in continuous mixed suspension mixed product removal cascade crystallizers

被引:57
|
作者
Yang, Yang [1 ]
Nagy, Zoltan K. [1 ]
机构
[1] Purdue Univ, Sch Chem Engn, W Lafayette, IN 47907 USA
关键词
Combined cooling/antisolvent crystallization; Mixed suspension mixed product removal crystallizer; Nonlinear model predictive control; Optimal control; Crystal size; Yield; MODEL-PREDICTIVE CONTROL; DIRECT NUCLEATION CONTROL; BATCH CRYSTALLIZATION; SIZE DISTRIBUTION; SYSTEMATIC DESIGN; FINES REMOVAL; SPECTROSCOPY; FRAMEWORK; REACTOR; RAMAN;
D O I
10.1016/j.ces.2015.01.060
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The control approaches for a continuous two stage mixed suspension mixed product removal (MSMPR) cascade crystallizer are studied in this work. Both cooling and antisolvent addition are applied at both stages to manipulate the process. Considering both crystal size and yield as controlled variables, the attainable region of crystal size and yield is obtained. Two advanced control schemes are discussed: (1) decentralized proportional-integral-derivative (PID) control; and (2) nonlinear model predictive control (NMPC). While decentralized PID control framework is proved to require change of control structure when a relatively large operating region is essential, nonlinear model predictive control scheme shows superior performance for fast target product property change over and disturbance rejection. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:362 / 373
页数:12
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