Optimization of multiple-fraction batch distillation with recycled waste cuts

被引:14
作者
Diehl, M
Schäfer, A
Bock, HG
Schlöder, JP
Leineweber, DB
机构
[1] Univ Heidelberg, Interdisciplinary Ctr Sci Comp, D-69120 Heidelberg, Germany
[2] Bayer AG, Proc Technol, D-51368 Leverkusen, Germany
关键词
D O I
10.1002/aic.690481214
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A strategy for the optimal operation of multiple-fraction batch distillation processes with waste cut recycling is presented. The processes are modeled by differential algebraic equations formulated in the gPROMS modeling language. A cost function based on economic criteria is developed. Recycling of the waste cuts is formulated as a cyclically repeated batch distillation process, where the waste cuts are recycled at intermediate points in time. The resulting multipoint boundary value optimization problem is efficiently solved by using the dynamic optimization package MUSCOD-II. A comparison of optimization results for the separation of a ternary mixture shows that considerable gains in profits can be obtained by a complete recycling of the waste cuts. Computation times are in the range of minutes on a standard workstation.
引用
收藏
页码:2869 / 2874
页数:6
相关论文
共 24 条
[1]  
Bauer I, 1999, THESIS U HEIDELBERG
[2]  
Bauer I., 1999, 359 IWR SFB U HEID
[3]  
BOCK H, 1984, P 9 IFAC WORLD C BUD
[4]   SENSITIVITY ANALYSIS OF INITIAL-VALUE PROBLEMS WITH MIXED ODES AND ALGEBRAIC EQUATIONS [J].
CARACOTSIOS, M ;
STEWART, WE .
COMPUTERS & CHEMICAL ENGINEERING, 1985, 9 (04) :359-365
[5]   OPTIMAL-CONTROL OF BINARY BATCH DISTILLATION WITH RECYCLED WASTE CUT [J].
CHRISTENSEN, FM ;
JORGENSEN, SB .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1987, 34 (02) :57-64
[6]  
Diehl M, 2001, ONLINE OPTIMIZATION OF LARGE SCALE SYSTEMS, P363
[7]   Real-time optimization and nonlinear model predictive control of processes governed by differential-algebraic equations [J].
Diehl, M ;
Bock, HG ;
Schlöder, JP ;
Findeisen, R ;
Nagy, Z ;
Allgöwer, F .
JOURNAL OF PROCESS CONTROL, 2002, 12 (04) :577-585
[8]  
Diehl M., 2002, REAL TIME OPTIMIZATI, V920
[9]  
Diehl M., 2001, 200125 IWR U HEID
[10]  
Diwekar U. M., 1995, BATCH DISTILLATION S