Semicontinuous Thermal Separation Systems

Since the year 2000, semicontinuous separation processes have been studied as a unique process intensification technique for the thermal separation of chemical mixtures. Typically, a single separation unit is used for multiple purposes with the aid of an auxiliary storage tank called a middle vessel. The system is operated cyclically but without startup or shutdown phases. As a result, multiple separation steps can be carried out with fewer capital expenses. In several cases, a significant profitability advantage over continuous or batch process alternatives has been shown, particularly for intermediate production capacities. The progress in semicontinuous systems is reviewed, including the development of semicontinuous ternary distillation, liquid-liquid extraction, azeotrope distillation, reactive distillation, and semicontinuous systems with integrated reaction and distillation or extraction. Control and operational strategies for semicontinuous systems are reviewed, as well as heuristics for modeling and simulation.

[1]  Wojciech Kujawski,et al.  Semi-continuous ethanol production in bioreactor from whey with co-immobilized enzyme and yeast cells followed by pervaporative recovery of product – Kinetic model predictions considering glucose repression , 2009 .

[2]  Thomas A. Adams,et al.  Design heuristics for semicontinuous separation processes with chemical reactions , 2009 .

[3]  Warren D. Seider,et al.  Semicontinuous, middle-vessel distillation of ternary mixtures , 2000 .

[4]  Ljubica Matijašević,et al.  Dividing wall column—A breakthrough towards sustainable distilling , 2010 .

[5]  Warren D. Seider,et al.  Distillate−Bottoms Control of Middle-Vessel Distillation Columns , 2000 .

[6]  Rafiqul Gani,et al.  Process intensification: A perspective on process synthesis , 2010 .

[7]  Hongjuan Liu,et al.  Downstream processing of 1,3‐propanediol fermentation broth , 2006 .

[8]  Warren D. Seider,et al.  Semicontinuous, middle-vessel, extractive distillation , 2000 .

[9]  N. P. Padhy,et al.  Application of particle swarm optimization technique and its variants to generation expansion planning problem , 2004 .

[10]  Sigurd Skogestad,et al.  Control configuration selection for distillation columns , 1987 .

[11]  Thomas A. Adams,et al.  Semicontinuous Distillation with Chemical Reaction in a Middle Vessel , 2006 .

[12]  Thomas A. Adams,et al.  Semicontinuous reactive extraction and reactive distillation , 2009 .

[13]  Victor M. Zavala,et al.  Large-scale nonlinear programming using IPOPT: An integrating framework for enterprise-wide dynamic optimization , 2009, Comput. Chem. Eng..

[14]  Thomas A. Adams,et al.  Practical optimization of complex chemical processes with tight constraints , 2008, Comput. Chem. Eng..

[15]  Warren D. Seider,et al.  Semicontinuous, pressure-swing distillation , 2000 .

[16]  W. Luyben Distillation Design and Control Using Aspen Simulation , 2006 .

[17]  Efstratios N. Pistikopoulos,et al.  New algorithms for mixed-integer dynamic optimization , 2003, Comput. Chem. Eng..

[18]  Paul I. Barton,et al.  Optimization of hybrid systems , 2006, Comput. Chem. Eng..

[19]  J. Álvarez-Ramírez,et al.  SOME ASPECTS OF THE OPERATION OF SEMI-CONTINUOUS, MIDDLE-VESSEL DISTILLATION COLUMNS , 2004 .

[20]  P. I. Barton,et al.  Global Mixed-Integer Dynamic Optimization , 2005 .

[21]  F. Maréchal,et al.  Thermochemical production of liquid fuels from biomass: Thermo-economic modeling, process design and process integration analysis , 2010 .

[22]  Thomas A. Adams,et al.  Semicontinuous distillation for ethyl lactate production , 2008 .