Optimal batch distillation control based on specific measures

Two independent measures characterise a single batch distillation run: the degree of separation difficulty, which indicates the difficulty at the start and the degree of exhaustion, which indicates bottom exhaustion at the end of the run. If one of both measures remains within bounds, then constant quality control appears to be the best control policy. It has been proven in the literature that the application of slop recycling increases the production rate. One of the goals of this study is to derive simple scheduling models based on specific measures for the optimal operation of batch distillation with slop recycling. Simulation studies for a cyclic pseudo-steady state operation over a broad range of degrees of difficulty for binary and ternary distillations are performed. Also the influence of the tray hold-up has been studied. All simulations show that at maximum production rate the degree of separation difficulty balances the degree of exhaustion (dependent variable in the optimum). The slop recycling strategy keeps the degree of exhaustion during the production phase and the degree of difficulty during the slop phase within bounds. As a result, the improvement of slop recycling at constant quality control compared to constant reflux control is 15–20% for difficult separation and can amount to more than 35% for relatively easy separations. The resulting production time appears to have a linear relation with the average separation difficulty. This relation has been experimentally verified.

[1]  William L. Luyben,et al.  MULTICOMPONENT BATCH DISTILLATION: 1. TERNARY SYSTEMS WITH SLOP RECYCLE , 1988 .

[2]  Enrique Quintero-Marmol,et al.  Multicomponent batch distillation. 2. Comparison of alternative slop handling and operating strategies , 1990 .

[3]  Serge Domenech,et al.  Strategies for slop cut recycling in multicomponent batch distillation , 1994 .

[4]  L. Kerkhof,et al.  On the profit of optimum control in batch distillation , 1978 .

[5]  S. Jørgensen,et al.  Optimal control of binary batch distillation in tray or packed columns , 1986 .

[6]  Darrell Thomas Barnette Multicomponent batch distillation , 1983 .

[7]  Sandro Macchietto,et al.  An optimal recycle policy for multicomponent batch distillation , 1992 .

[8]  S. Farhat,et al.  Optimization of multiple‐fraction batch distillation by nonlinear programming , 1990 .

[9]  R. Jackson,et al.  Time-optimal problems in batch distillation for multicomponent mixtures and for columns with holdup , 1971 .

[10]  Urmila M. Diwekar,et al.  UNIFIED APPROACH TO SOLVING OPTIMAL DESIGN - CONTROL PROBLEMS IN BATCH DISTILLATION , 1992 .

[11]  Iqbal M. Mujtaba,et al.  Optimal operation of multicomponent batch distillation—multiperiod formulation and solution , 1993 .

[12]  Thomas F. Edgar,et al.  Application of Nonlinear Model Predictive Control to Optimal Batch Distillation , 1992 .

[13]  David W.T. Rippin,et al.  Simulation of single- and multiproduct batch chemical plants for optimal design and operation☆ , 1983 .

[14]  Sten Bay Jørgensen,et al.  Optimal control of binary batch distillation with recycled waste cut , 1987 .

[15]  R. K. Malik,et al.  Optimal reflux rate policy determination for multicomponent batch distillation columns , 1987 .

[16]  R. Jackson,et al.  The time-optimal problem in binary batch distillation with a recycled waste-cut , 1970 .

[17]  E. R. Robinson,et al.  The optimal control of an industrial batch distillation column , 1970 .