Reaction profile control of the continuous pulp digester

被引：19

作者：

Doyle, FJ ^{[1
]}

Kayihan, F

机构：

[1] Univ Delaware, Dept Chem Engn, Newark, DE 19716 USA

[2] IETeK, Integrated Engn Technol, Tacoma, WA 98422 USA

来源：

CHEMICAL ENGINEERING SCIENCE | 1999年 / 54卷 / 13-14期

关键词：

continuous digester; process control; profile control; model predictive control; subspace identification;

D O I：

10.1016/S0009-2509(98)00363-7

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

In this work, a model-based control strategy is presented for the Kappa number profile control of a continuous pulp digester. The strategy employs an empirically derived process model using subspace identification techniques. A state-space model predictive control algorithm is used to adjust five manipulated inputs in order to regulate five process outputs, in response to five randomly varying process disturbances (of which three are measurable:). Profile sensitivity to closed-loop response is also explored. (C) 1999 Elsevier Science Ltd. All rights reserved.

引用

页码：2679 / 2688

页数：10

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[2]

[Anonymous], 1965, DYNAMIC PROGRAMMING

[3]

CHRISTENSEN T, 1982, 129 POLAIC PURD U

[4]

CUTLER CR, 1979, AICHE 86 ANN NAT M