New rigorous one-step MILP formulation for heat exchanger network synthesis

In this paper, a rigorous MILP formulation for grass-root design of heat exchanger networks is developed. The methodology does not rely on traditional supertargeting followed by network design steps typical of the Pinch Design Method, nor is a non-linear model based on superstructures, but rather gives cost-optimal solutions in one step. Unlike most models, it considers splitting, non-isothermal mixing and it counts shells/units. The model relies on transportation/transshipment concepts that are complemented with constraints that allow keeping track of flow rate consistency when splitting takes place and with mechanisms to count heat exchanger shells and units. Several examples from the literature were tested, finding that the model usually obtains better solutions. In some cases, the model produced unknown solutions that were not found using superstructure optimization methods, even when the same pattern of matches is used.

[1]  Ignacio E. Grossmann,et al.  Improved optimization strategies for automated heat exchanger network synthesis through physical insights , 1990 .

[2]  Miguel J. Bagajewicz,et al.  Energy efficient water utilization systems in process plants , 2002 .

[3]  Warren D. Seider,et al.  Process design principles : synthesis, analysis, and evaluation , 1999 .

[4]  Miguel J. Bagajewicz,et al.  Design of Crude Distillation Plants with Vacuum Units. II. Heat Exchanger Network Design , 2002 .

[5]  Kevin C. Furman,et al.  Computational complexity of heat exchanger network synthesis , 2001 .

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

[7]  Robin Smith Chemical process design , 1994 .

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

[9]  Miguel J. Bagajewicz,et al.  Rigorous procedure for the design of conventional atmospheric crude fractionation units. Part III: Trade-off between complexity and energy savings , 2003 .

[10]  Kevin C. Furman,et al.  A Critical Review and Annotated Bibliography for Heat Exchanger Network Synthesis in the 20th Century , 2002 .

[11]  Jacek Jeżowski,et al.  Area target for heat exchanger networks using linear programming , 2003 .

[12]  J Jezowski HEAT EXCHANGER NETWORK GRASSROOT AND RETROFIT DESIGN, THE REVIEW OF THE STATE OF THE ART: PART II, HEAT EXCHANGER NETWORK SYNTHESIS BY MATHEMATICAL METHODS AND APPROACHES FOR RETROFIT DESIGN , 1994 .

[13]  Miguel J. Bagajewicz,et al.  Rigorous procedure for the design of conventional atmospheric crude fractionation units. Part II: Heat exchanger network , 2001 .

[14]  L. Naess,et al.  The synthesis of cost optimal heat exchanger networks. An industrial review of the state of the art , 1988 .

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

[16]  U. V. Shenoy,et al.  Heat Exchanger Network Synthesis:: Process Optimization by Energy and Resource Analysis , 1995 .

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