On-line parameter estimation in a high-pressure low-density polyethylene tubular reactor

被引:23
作者
Kiparissides, C
Verros, G
Pertsinidis, A
Goossens, I
机构
[1] ARISTOTELIAN UNIV THESSALONIKI,CHEM PROC ENGN RES INST,GR-54006 THESSALONIKI,GREECE
[2] EXXON CHEM BELGIUM,ANTWERP POLYMER PLANT,B-2070 ZWIJNDRECHT,BELGIUM
关键词
D O I
10.1002/aic.690420214
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The high throughput and operating cost of the reactor provide the economic incentive in considering the on-line optimization of the LDPE tubular reactor. For an on-line optimization procedure it is crucial to develop a flexible and adaptive on-line parameter estimator, which based on the appropriate measurements from the reactor will adjust certain key model parameters so that the model can capture the actual reactor operation and reliably be used for the real-time optimization of the reactor performance. Various issues involved in developing the on-fine estimator for such applications as the mathematical modeling of the reactor, the selection of the adjustable model parameters and reactor measurements, the decomposition of the problem according to the characteristic time constants of various disturbances, and the efficient and robust solution of the mathematical problem are discussed. The tools developed were successfully used on an EXXON high-pressure LDPE tubular reactor. Results from the numerical experiments that are compared with scaled data from a real reactor show that the estimated temperature profiles agree remarkably with those observed at various phases of the reactor operation.
引用
收藏
页码:440 / 454
页数:15
相关论文
共 31 条
[11]   ONLINE OPTIMIZATION OF CONSTRAINED MULTIVARIABLE CHEMICAL PROCESSES [J].
JANG, SS ;
JOSEPH, B ;
MUKAI, H .
AICHE JOURNAL, 1987, 33 (01) :26-35
[12]   COMPARISON OF 2 APPROACHES TO ONLINE PARAMETER AND STATE ESTIMATION OF NONLINEAR-SYSTEMS [J].
JANG, SS ;
JOSEPH, B ;
MUKAL, H .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (03) :809-814
[13]   MATHEMATICAL-MODELING, OPTIMIZATION, AND QUALITY-CONTROL OF HIGH-PRESSURE ETHYLENE POLYMERIZATION REACTORS [J].
KIPARISSIDES, C ;
VERROS, G ;
MACGREGOR, JF .
JOURNAL OF MACROMOLECULAR SCIENCE-REVIEWS IN MACROMOLECULAR CHEMISTRY AND PHYSICS, 1993, C33 (04) :437-527
[14]   HIERARCHICAL CONTROL OF A TRAIN OF CONTINUOUS POLYMERIZATION REACTORS [J].
KIPARISSIDES, C ;
PONNUSWAMY, SR .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1981, 59 (06) :752-759
[15]   ROBUST PARAMETER-ESTIMATION IN ONLINE OPTIMIZATION .1. METHODOLOGY AND SIMULATED CASE-STUDY [J].
KRISHNAN, S ;
BARTON, GW ;
PERKINS, JD .
COMPUTERS & CHEMICAL ENGINEERING, 1992, 16 (06) :545-562
[16]   ROBUST PARAMETER-ESTIMATION IN ONLINE OPTIMIZATION .2. APPLICATION TO AN INDUSTRIAL-PROCESS [J].
KRISHNAN, S ;
BARTON, GW ;
PERKINS, JD .
COMPUTERS & CHEMICAL ENGINEERING, 1993, 17 (07) :663-669
[17]  
MAVRIDIS H, 1985, POLYM P ENG, V3, P263
[18]   ONLINE INFERENCE OF POLYMER PROPERTIES IN AN INDUSTRIAL POLYETHYLENE REACTOR [J].
MCAULEY, KB ;
MACGREGOR, JF .
AICHE JOURNAL, 1991, 37 (06) :825-835
[19]   STUDIES IN THE SYNTHESIS OF CONTROL-STRUCTURES FOR CHEMICAL PROCESSES .2. STRUCTURAL ASPECTS AND THE SYNTHESIS OF ALTERNATIVE FEASIBLE CONTROL SCHEMES [J].
MORARI, M ;
STEPHANOPOULOS, G .
AICHE JOURNAL, 1980, 26 (02) :232-246
[20]   THE MATHEMATICAL-MODELING OF TRANSIENT SYSTEMS USING DIFFERENTIAL ALGEBRAIC EQUATIONS [J].
PANTELIDES, CC ;
GRITSIS, D ;
MORISON, KR ;
SARGENT, RWH .
COMPUTERS & CHEMICAL ENGINEERING, 1988, 12 (05) :449-454