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基于样条插值模型的间歇精馏模拟与预测控制

吴微 师佳 周华 曹志凯 江青茵

化工学报2012,Vol.63Issue(4):1124-1131,8.
化工学报2012,Vol.63Issue(4):1124-1131,8.DOI:10.3969/j.issn.0438-1157.2012.04.020

基于样条插值模型的间歇精馏模拟与预测控制

Simulation and predictive control based on spline interpolation model of batch distillation

吴微 1师佳 1周华 1曹志凯 1江青茵1

作者信息

  • 1. 厦门大学化学化工学院化学工程与生物工程系,福建厦门361005
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摘要

Abstract

Batch distillation is a widely used separation process in chemical engineering. Due to the comparatively small investment and flexibility in production, batch distillation has found various industrial applications in biopharmaceuticals, fine chemicals production and foods processing. To guarantee high product quality, modeling and advanced process control for batch distillation have received significant attention. As an unsteady state dynamic process with strong nonlinearity, however, it is still not easy for engineers to design a control system on the basis of a simple model to guarantee good control performance for batch distillation. In this paper, by using the batch distillation model in Aspen Batch Distillation? (ABD) as prototype, the process data of tower residual liquid and distillate compositions under different reflux ratios were obtained firstly. Based on the process data, then, the distillate volume and concentration of the process were formulated by the steady-state spline interpolation models (SIM). To compensate the dynamic error caused by variation of reflux ratios, a simple dynamic model was identified and combined with the steady-state SIM, resulting in a simple dynamic SIM for batch distillation. The comparison of the responses of the proposed SIM and ABD model to the time-varying reflux ratio indicated the applicability and precision of the proposed SIM. By using the SIM as the prediction model, a model predictive control (MPC) algorithm was further proposed for the concentration control of batch distillation. Numericalsimulations demonstrated the applicability and robustness of the proposed control scheme for batch distillation with different feed compositions. The proposed control scheme lays a solid foundation for the further studies on online optimization of batch distillation.

关键词

间歇精馏/样条插值模型/模型预测控制

Key words

batch distillation/ spline interpolation model/ model predictive control

分类

信息技术与安全科学

引用本文复制引用

吴微,师佳,周华,曹志凯,江青茵..基于样条插值模型的间歇精馏模拟与预测控制[J].化工学报,2012,63(4):1124-1131,8.

基金项目

中央高校基本科研业务费专项(2010121047). (2010121047)

化工学报

OA北大核心CSCDCSTPCD

0438-1157

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