Simultaneous MINLP synthesis of heat exchanger networks comprising different exchanger types

Publisher Summary This chapter describes the simultaneous mixed-integer non linear programming (MINLP) synthesis of heat-integrated heat-exchanger networks (HEN) comprising different heat-exchanger types. The stage-wise superstructure of HEN is extended to alternative exchanger types. The selection of the types is modeled by disjunctions based on operating limitations and required heat-transfer area. Because different types of heat exchangers involve different design geometries that influence the inlet and outlet temperatures of heat exchangers, additional constraints are specified to provide feasible temperature distribution in HEN. To facilitate the synthesis of medium-size problems, the following synthesis/analysis scheme is proposed. The first step in the scheme is the prescreening procedure. It is applied to exclude all impossible matches between the hot and cold streams within the HEN superstructure due to the operating limitations of exchanger types. Therefore, the model size is reduced before the optimization takes place. The prescreening is followed by the MINLP optimization of the model.

[1]  Ignacio E. Grossmann,et al.  Preliminary screening procedure for the MINLP synthesis of process systems. II: Heat exchanger networks , 1994 .

[2]  Jaime Cerdá,et al.  Synthesis of structural-constrained heat exchanger networks—I. Series networks , 1998 .

[3]  Ignacio E. Grossmann,et al.  Simultaneous optimization models for heat integration—II. Heat exchanger network synthesis , 1990 .

[4]  Daniel R. Lewin,et al.  A generalized method for HEN synthesis using stochastic optimization. I. General framework and MER optimal synthesis , 1998 .

[5]  Ignacio E. Grossmann,et al.  A structural optimization approach in process synthesis—I: Utility systems , 1983 .

[6]  B. Linnhoff,et al.  The pinch design method for heat exchanger networks , 1983 .

[7]  Ignacio E. Grossmann,et al.  A modelling and decomposition strategy for the MINLP optimization of process flowsheets , 1989 .

[8]  Serge Domenech,et al.  Synthesis of heat‐exchanger network by simulated annealing and NLP procedures , 1997 .

[9]  I. Grossmann,et al.  A combined penalty function and outer-approximation method for MINLP optimization : applications to distillation column design , 1989 .

[10]  Zdravko Kravanja,et al.  Simultaneous MINLP synthesis of heat and power integrated heat exchanger networks , 1999 .

[11]  G. L. Shires,et al.  Process Heat Transfer , 1994 .

[12]  John J.J. Chen Comments on improvements on a replacement for the logarithmic mean , 1987 .

[13]  Zdravko Kravanja,et al.  Cost targeting for HEN through simultaneous optimization approach : a unified pinch technology and mathematical programming design of large HEN , 1997 .

[14]  Ignacio E. Grossmann,et al.  Disjunctive Programming Techniques for the Optimization of Process Systems with Discontinuous Investment Costs−Multiple Size Regions , 1996 .

[15]  Santanu Bandyopadhyay,et al.  Multiple utilities targeting for heat exchanger networks , 1998 .

[16]  Ignacio E. Grossmann,et al.  A structural optimization approach in process synthesis. II: Heat recovery networks , 1983 .

[17]  Ignacio E. Grossmann,et al.  Preliminary screening procedure for the MINLP synthesis of process systems—I. aggregation and decomposition techniques , 1994 .

[18]  G. Walker Industrial Heat Exchangers , 1990 .

[19]  Daniel R. Lewin,et al.  A generalized method for HEN synthesis using stochastic optimization. II. : The synthesis of cost-optimal networks , 1998 .

[20]  Ignacio E. Grossmann,et al.  Prosyn — An automated topology and parameter process synthesizer , 1994 .

[21]  Manfred Morari,et al.  Area and capital cost targets for heat exchanger network synthesis with constrained matches and unequal heat transfer coefficients , 1990 .

[22]  Karl T. Chuang,et al.  A New Method To Determine the Best Units for Breaking Heat Load Loops of Heat Exchanger Networks , 1999 .