Real-time optimization of a tubular reactor with distributed feed

被引:13
作者
Cougnon, P [1 ]
Dochain, D
Guay, M
Perrier, M
机构
[1] Univ Catholique Louvain, IMAP, B-1348 Louvain, Belgium
[2] Queens Univ, Dept Chem Engn, Kingston, ON K7L 3N6, Canada
[3] Ecole Polytech, Dept Genie Chim, Montreal, PQ H3C 3A7, Canada
关键词
extremum seeking; adaptive learning; tubular reactor; distributed feed; persistence of excitation;
D O I
10.1002/aic.10799
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An adaptive extremum seeking control scheme for a class of nonlinear distributed parameter systems is presented. It addresses the real-time optimization of a parallel chemical reaction system in an isothermal tubular reactor with uniform distributed feed described by a set of hyperbolic partial differential equations. Only limited knowledge of the kinetics is assumed. An adaptive learning technique is introduced to design an extremum seeking algorithm that drives the system states to a set point that maximizes the value of an objective function. Lyapunov's stability theorem is used in the design of the extremum seeking controller structure and the development of the parameter learning laws.(c) 2006 American Institute of Chemical Engineers.
引用
收藏
页码:2120 / 2128
页数:9
相关论文
共 21 条
[1]   Ethylene epoxidation in a catalytic packed-bed membrane reactor: experiments and model [J].
Al-Juaied, MA ;
Lafarga, D ;
Varma, A .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (02) :395-402
[2]  
ANDERSON BDO, 1986, STABILITY ADAPTIVE S
[3]   An experimental and theoretical investigation of a catalytic membrane reactor for the oxidative dehydrogenation of methanol [J].
Brinkmann, T ;
Perera, SP ;
Thomas, WJ .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (06) :2047-2061
[4]   Optimal feed distribution in a packed-bed membrane reactor: The case of methanol oxidative dehydrogenation [J].
Diakov, V ;
Varma, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (02) :309-314
[5]  
ELVENSPIEL O, 1999, CHEM REACTION ENG
[6]   Adaptive extremum seeking control of nonlinear dynamic systems with parametric uncertainties [J].
Guay, M ;
Zhang, T .
AUTOMATICA, 2003, 39 (07) :1283-1293
[7]   Theoretical analysis of reactant dosing concepts to perform parallel-series reactions [J].
Hamel, C ;
Thomas, S ;
Schädlich, K ;
Seidel-Morgenstern, A .
CHEMICAL ENGINEERING SCIENCE, 2003, 58 (19) :4483-4492
[8]   Adaptive extremum seeking control of a non-isothermal tubular reactor with unknown kinetics [J].
Hudon, N ;
Perrier, M ;
Guay, M ;
Dochain, D .
COMPUTERS & CHEMICAL ENGINEERING, 2005, 29 (04) :839-849
[9]   Selective oxidation of ethane over a VOx/γ-Al2O3 catalyst -: investigation of the reaction network [J].
Klose, F ;
Joshi, M ;
Hamel, C ;
Seidel-Morgenstern, A .
APPLIED CATALYSIS A-GENERAL, 2004, 260 (01) :101-110
[10]   Ethylene epoxidation on Ag-Cs/α-Al2O3 catalyst:: Experimental results and strategy for kinetic parameter determination [J].
Lafarga, D ;
Al-Juaied, MA ;
Bondy, CM ;
Varma, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (07) :2148-2156