Superstructure optimization for the synthesis of chemical process flowsheets: Application to optimal hybrid membrane systems

The superstructure has proved an effective tool for the synthesis of chemical-engineering process flowsheets. The superstructure is assumed to contain all possible alternatives of a potential treatment network, including the optimal solution that is hidden. A common approach for formulating superstructures for process-synthesis problems involving heat and mass exchange has been to use the state-space framework. In this way, unit operations, utility units, and utility streams can be embedded in such a way that all the process synthesis alternatives can be realized. Such a framework has been applied to water and wastewater synthesis problems. This article reviews the optimization studies that have been carried out on membrane and hybrid membrane process-synthesis problems for wastewater treatment. Comparison is made between different representations and their mathematical programs to highlight the relationship between the superstructure representation and their mathematical programming formulations. From this analysis, possible improvement of these superstructures is suggested. Also, a generic representation is provided for a systematic and clear description for assembling hybrid membrane system superstructures via the state space approach. Several case studies are given in order to illustrate the proposed approach.

[1]  Takeshi Matsuura,et al.  Membrane‐Based Hybrid Processes: A Review , 2006 .

[2]  R. Field,et al.  Hydrophobic pervaporation for environmental applications : Process optimization and integration , 2002 .

[3]  I. Grossmann,et al.  Logic-based MINLP algorithms for the optimal synthesis of process networks , 1996 .

[4]  Mahmoud M. El-Halwagi,et al.  Synthesis of reverse‐osmosis networks for waste reduction , 1992 .

[5]  Amy R. Ciric,et al.  Synthesis of nonequilibrium reactive distillation processes by MINLP optimization , 1994 .

[6]  C. Floudas Nonlinear and Mixed-Integer Optimization: Fundamentals and Applications , 1995 .

[7]  Miguel J. Bagajewicz,et al.  On the state space approach to mass/heat exchanger network design* , 1998 .

[8]  R. Billet,et al.  Prediction of Mass Transfer Columns with Dumped and Arranged Packings , 1999 .

[9]  Reinhard Billet,et al.  Predicting mass transfer in packed columns , 1993 .

[10]  Ignacio E. Grossmann Challenges in the new millennium: Product discovery and design, enterprise and supply chain optimization, global life cycle assessment , 2003 .

[11]  Efstratios N. Pistikopoulos,et al.  Modular synthesis framework for combined separation/reaction systems , 2001 .

[12]  Ignacio E. Grossmann,et al.  New trends in optimization-based approaches to process synthesis , 1996 .

[13]  Efstratios N. Pistikopoulos,et al.  Hybrid generalized modular/collocation framework for distillation column synthesis , 2006 .

[14]  Ali Elkamel,et al.  Optimal design of reverse-osmosis networks for wastewater treatment , 2008 .

[15]  Patrick Linke,et al.  Advanced process systems design technology for pollution prevention and waste treatment , 2004 .

[16]  I. Kookos Optimal Design of Membrane/Distillation Column Hybrid Processes , 2003 .

[17]  Mahmoud M. El-Halwagi Optimal Design of Membrane-Hybrid Systems for Waste Reduction , 1993 .

[18]  Ignacio E. Grossmann,et al.  Systematic Methods of Chemical Process Design , 1997 .

[19]  Miguel J. Bagajewicz,et al.  Mass/heat‐exchange network representation of distillation networks , 1992 .

[20]  Xiao-Ning Li,et al.  Conceptual process synthesis: past and current trends , 2004 .

[21]  Efstratios N. Pistikopoulos,et al.  Generalized modular representation framework for process synthesis , 1996 .

[22]  R. Billet,et al.  Modelling of pressure drop in packed columns , 1991 .

[23]  Mahmoud M. El-Halwagi,et al.  Synthesis of mass exchange networks , 1989 .

[24]  A. Elkamel,et al.  Global Optimization of Reverse Osmosis Network for Wastewater Treatment and Minimization , 2008 .

[25]  Patrick Linke,et al.  Attainable reaction and separation processes from a superstructure‐based method , 2003 .

[26]  James M. Douglas,et al.  Conceptual Design of Chemical Processes , 1988 .

[27]  I. Grossmann,et al.  A systematic modeling framework of superstructure optimization in process synthesis , 1999 .

[28]  Arthur Westerberg,et al.  A retrospective on design and process synthesis , 2004, Comput. Chem. Eng..

[29]  Efstratios N. Pistikopoulos,et al.  Modular representation synthesis framework for homogeneous azeotropic separation , 1999 .

[30]  Jeffrey J. Siirola,et al.  Process synthesis prospective , 2004, Comput. Chem. Eng..

[31]  Franco Evangelista A short cut method for the design of reverse osmosis desalination plants , 1985 .

[32]  Efstratios N. Pistikopoulos,et al.  Generalized modular framework for the synthesis of heat integrated distillation column sequences , 2005 .

[33]  Charles H. Gooding,et al.  Modeling spiral wound membrane modules for the pervaporative removal of volatile organic compounds from water , 1994 .

[34]  Ignacio E. Grossmann,et al.  Optimal feed locations and number of trays for distillation columns with multiple feeds , 1993 .

[35]  Ignacio E. Grossmann,et al.  Integration of hierarchical decomposition and mathematical programming for the synthesis of process flowsheets , 1998 .

[36]  Mahmoud M. El-Halwagi,et al.  Optimal design of pervaporation systems for waste reduction , 1993 .

[37]  Charles H. Gooding,et al.  MASS TRANSFER IN SPIRAL WOUND PERVAPORATION MODULES , 1994 .

[38]  Antonis C. Kokossis,et al.  Nonisothermal synthesis of homogeneous and multiphase reactor networks , 2000 .