Inferential monitoring and optimization of crude separation units via hybrid models

被引:52
作者
Mahalec, Vladimir [1 ]
Sanchez, Yoel [1 ]
机构
[1] McMaster Univ, Dept Chem Engn, Hamilton, ON L8S 4L7, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Crude distillation; Hybrid model; Production planning; Process optimization; HYDROCARBON MIXTURES; DISTILLATION; VAPORIZATION; REGRESSION;
D O I
10.1016/j.compchemeng.2012.05.012
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
The hybrid model of a CDU introduced in this work can be used for both production planning and for RTO, since the model converges rapidly via SLP, it is small in size, its accuracy is comparable to rigorous models, and it can optimize the operating variables, including furnace duty and pumparound duties. This enables CDU part of the planning models to be as accurate as the RTO models, instead of using standard CDU modes of operation. The model includes mass and energy balances and statistical models relating crude distillation curve points, tower operating variables and tray temperatures to product distillation curves. Hybrid model of a sample CDU shows excellent agreement with property predictions from the rigorous model; RMSE of points on the product distillation curves is typically less than 0.5% of the rigorous model predictions. Optimization of the hybrid model via SLP converged to a better point than equation-oriented AspenPlus. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:15 / 26
页数:12
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