A multi-form modelling approach to the dynamics and control of drum granulation processes

被引:14
作者
Wang, F. Y. [1 ]
Cameron, I. T. [1 ]
机构
[1] Univ Queensland, Sch Engn, Particle & Syst Design Ctr, Brisbane, Qld 4072, Australia
基金
澳大利亚研究理事会;
关键词
dynamic simulation; granulation; model-based control; multi-form models; population balance; systems engineering;
D O I
10.1016/j.powtec.2006.11.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Drum granulation processes are represented by a set of mass transfer, solid transport, as well as population balance equations. The population balance is mathematically described by partial differential-integral equations. The overall granulation model is highly non-linear, large-scale with multiple coordinates and uncertain parameters, leading to tremendous difficulties for optimisation and control. In our previous work, a two-level control strategy is proposed, which consists of an upper level optimal control for the determination of optimal set-points, and a lower level non-linear model predictive control (NMPC) for the simultaneous computations of uncertain parameters and control variables. However, long computing times and insufficient measurement data prevent industrial applications. In this paper, strategies are developed to improve the applicability of the multi-level, model predictive control scheme (ML-MPC) using the multi-form modelling approach. In the multi-form modelling approach, the granulation plants are represented by a variety of model forms for different end-uses. These include: (1) the distributed parameter population balance model (DP-PBM), (2) the lumped parameter population balance model (LP-PBM), (3) matrix representation with off-line computed matrix elements, (4) local linear models, (5) reduced order models using balanced truncating and methods of moment. It can be shown through dynamic simulations that significant computing time reductions can be achieved with properly selected model forms. Since both open-loop optimal control and closed loop MPC rely on iterative dynamic optimisation, overall computing time reduction makes on-line applications possible. Furthermore, the development of local linear models allows the applications of well-established linear system theory and techniques to process control, parameter identification and model order reduction. The demonstrated advantages of the proposed multi-form modelling approach imply a big step forward towards the industrial applications of model-based control for granulation processes. (C) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:2 / 11
页数:10
相关论文
共 15 条
[1]  
[Anonymous], 1996, MATLAB OPTIMIZATION
[2]   Process systems modelling and applications in granulation: A review [J].
Cameron, IT ;
Wang, FY ;
Immanuel, CD ;
Stepanek, F .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (14) :3723-3750
[3]  
Finlayson BA., 1972, Method of Weighted Residuals and Variational Principles
[4]   A DISCRETIZED POPULATION BALANCE FOR NUCLEATION, GROWTH, AND AGGREGATION [J].
HOUNSLOW, MJ ;
RYALL, RL ;
MARSHALL, VR .
AICHE JOURNAL, 1988, 34 (11) :1821-1832
[5]   Robust model-order reduction of complex biological processes [J].
Lee, TT ;
Wang, FY ;
Newell, RB .
JOURNAL OF PROCESS CONTROL, 2002, 12 (07) :807-821
[6]  
Lister J., 2004, The science and engineering of granulation processes
[7]  
Ljung L., 1986, SYSTEM IDENTIFICATIO
[8]  
Nielsen J., 2003, BIOREACTION ENG PRIN
[9]   SIMULTANEOUS NUCLEATION, CONDENSATION, AND COAGULATION IN AEROSOL REACTORS [J].
PRATSINIS, SE .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1988, 124 (02) :416-427
[10]  
Villadsen J., 1978, SOLUTION DIFFERENTIA