Structural Considerations and Modeling in the Synthesis of Heat-Integrated-Thermally Coupled Distillation Sequences

This paper examines the design of mixed thermally coupled−heat-integrated distillation sequences. The approach considers a variety of methodologies, from conventional columns (each distillation column with a condenser and a reboiler) to fully thermally coupled systems (only one reboiler and one condenser in the entire system). A discussion about superstructure generation and the convenience of using a representation based on separation tasks instead of equipment is presented, as well as a set of logical rules in terms of boolean variables that allow all of the feasible structures to be generated systematically. Based on the logical rules, an algorithm is developed for generating valid sequences (even by hand) without explicitly solving the logical equations. All the specific aspects were related to intercolumn heat integration when partially thermally coupled systems are considered. A disjunctive programming formulation for extracting the optimal solution is presented. The model is based on the Fenske−Und...

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

[2]  James R. Fair,et al.  Distillation: Principles and Practices , 1998 .

[3]  Nikolaos V. Sahinidis,et al.  BARON: A general purpose global optimization software package , 1996, J. Glob. Optim..

[4]  R. Raman,et al.  RELATION BETWEEN MILP MODELLING AND LOGICAL INFERENCE FOR CHEMICAL PROCESS SYNTHESIS , 1991 .

[5]  C. Triantafyllou The Design and Optimisation of Fully Thermally Coupled Distillation Columns , 1992 .

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

[7]  Sigurd Skogestad,et al.  Minimum Energy Consumption in Multicomponent Distillation. 3. More Than Three Products and Generalized Petlyuk Arrangements , 2003 .

[8]  K. Kobe The properties of gases and liquids , 1959 .

[9]  Rakesh Agrawal,et al.  A Method to Draw Fully Thermally Coupled Distillation Column Configurations for Multicomponent Distillation , 2000 .

[10]  Rakesh Agrawal,et al.  Multicomponent thermally coupled systems of distillation columns at minimum reflux , 2001 .

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

[12]  Andrzej Kraslawski,et al.  Optimal Design of Distillation Flowsheets with a Lower Number of Thermal Couplings for Multicomponent Separations , 2002 .

[13]  Ilkka Turunen,et al.  Synthesis of Functionally Distinct Thermally Coupled Configurations for Quaternary Distillations , 2003 .

[14]  R. Agrawal,et al.  More operable arrangements of fully thermally coupled distillation columns , 1998 .

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

[16]  I. Grossmann,et al.  Aggregated Models for Integrated Distillation Systems , 1999 .

[17]  Ignacio E. Grossmann,et al.  Thermodynamically equivalent configurations for thermally coupled distillation , 2003 .

[18]  F. Petlyuk Thermodynamically Optimal Method for Separating Multicomponent Mixtures , 1965 .

[19]  Rakesh Agrawal,et al.  New thermally coupled schemes for ternary distillation , 1999 .

[20]  Ignacio E. Grossmann,et al.  A decomposition method for synthesizing complex column configurations using tray-by-tray GDP models , 2004, Comput. Chem. Eng..

[21]  G. Kaibel Distillation columns with vertical partitions , 1987 .

[22]  Rakesh Agrawal,et al.  Synthesis of Distillation Column Configurations for a Multicomponent Separation , 1996 .

[23]  P. Mizsey,et al.  Energy savings of integrated and coupled distillation systems , 1999 .

[24]  Rakesh Agrawal,et al.  Thermally coupled distillation with reduced number of intercolumn vapor transfers , 2000 .

[25]  Andrzej Kraslawski,et al.  Systematic Synthesis of Functionally Distinct New Distillation Systems for Five-Component Separations , 2005 .

[26]  R. Reid,et al.  The Properties of Gases and Liquids , 1977 .

[27]  Ignacio E. Grossmann,et al.  Generalized Disjunctive Programming Model for the Optimal Synthesis of Thermally Linked Distillation Columns , 2001 .

[28]  B. Linnhoff,et al.  The design of separators in the context of overall processes , 1988 .

[29]  Ignacio E. Grossmann,et al.  Design of distillation sequences: from conventional to fully thermally coupled distillation systems , 2004, Comput. Chem. Eng..

[30]  Sigurd Skogestad,et al.  Minimum Energy Consumption in Multicomponent Distillation. 2. Three-Product Petlyuk Arrangements , 2003 .

[31]  Ignacio E. Grossmann,et al.  An outer-approximation algorithm for a class of mixed-integer nonlinear programs , 1986, Math. Program..

[32]  S. Skogestad,et al.  Minimum Energy Consumption in Multicomponent Distillation. 1. Vmin Diagram for a Two-Product Column , 2003 .

[33]  E. Balas,et al.  Canonical Cuts on the Unit Hypercube , 1972 .

[34]  Ignacio E. Grossmann,et al.  Optimal synthesis of complex distillation columns using rigorous models , 2005, Comput. Chem. Eng..

[35]  Sigurd Skogestad,et al.  Minimum Energy Consumption in Multicomponent Distillation Part II: Three-product Petlyuk Arrangements , 2002 .

[36]  Peter Mizsey,et al.  A predictor-based bounding strategy for synthesizing energy integrated total flowsheets , 1990 .