A Simple Criterion for Feasibility of Heat Integration between Distillation Streams Based on Relative Volatilities

[1]  Mohit Tawarmalani,et al.  Global optimization of multicomponent distillation configurations: 1. Need for a reliable global optimization algorithm , 2013 .

[2]  Rakesh Agrawal,et al.  Multicomponent Distillation Columns with Partitions and Multiple Reboilers and Condensers , 2001 .

[3]  Mohit Tawarmalani,et al.  Minimum energy of multicomponent distillation systems using minimum additional heat and mass integration sections , 2018 .

[4]  Mohit Tawarmalani,et al.  An MINLP formulation for the optimization of multicomponent distillation configurations , 2019, Comput. Chem. Eng..

[5]  110th Anniversary: Thermal Coupling via Heat Transfer: A Potential Route to Simple Distillation Configurations with Lower Heat Duty , 2019, Industrial & Engineering Chemistry Research.

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

[7]  Nikolaos V. Sahinidis,et al.  A polyhedral branch-and-cut approach to global optimization , 2005, Math. Program..

[8]  Mohit Tawarmalani,et al.  Short-Cut Methods versus Rigorous Methods for Performance-Evaluation of Distillation Configurations , 2018 .

[9]  Peter Mizsey,et al.  Rigorous Comparative Study of Energy-Integrated Distillation Schemes , 1996 .

[10]  Rakesh Agrawal,et al.  Optimal thermodynamic feed conditions for distillation of ideal binary mixtures , 1997 .

[11]  Sigurd Skogestad,et al.  Minimum energy diagrams for multieffect distillation arrangements , 2005 .

[12]  Christos T. Maravelias,et al.  Expanding the scope of distillation network synthesis using superstructure-based methods , 2020, Comput. Chem. Eng..

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

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

[15]  Mohit Tawarmalani,et al.  Thermal coupling links to liquid‐only transfer streams: An enumeration method for new FTC dividing wall columns , 2016 .

[16]  Mohit Tawarmalani,et al.  Thermal coupling links to liquid‐only transfer streams: A path for new dividing wall columns , 2014 .

[17]  Michael F. Malone,et al.  Net work consumption in distillation—short-cut evaluation and applications to synthesis , 1989 .

[18]  Christos T. Maravelias,et al.  Computationally efficient optimization models for preliminary distillation column design and separation energy targeting , 2020, Comput. Chem. Eng..

[19]  Improved direct and indirect systems of columns for ternary distillation , 1998 .

[20]  Ignacio E. Grossmann,et al.  Structural Considerations and Modeling in the Synthesis of Heat-Integrated-Thermally Coupled Distillation Sequences , 2006 .

[21]  D. Peng,et al.  A New Two-Constant Equation of State , 1976 .

[22]  Nikolaos V. Sahinidis,et al.  Exploiting integrality in the global optimization of mixed-integer nonlinear programming problems with BARON , 2018, Optim. Methods Softw..

[23]  Zbigniew Fidkowski,et al.  Energy requirements of nonconventional distillation systems , 1990 .

[24]  Michael F. Doherty,et al.  An approximate model for binary azeotropic distillation design , 1984 .

[25]  Ignacio E. Grossmann,et al.  Simultaneous optimization and heat integration of chemical processes , 1986 .

[26]  Xigang Yuan,et al.  Synthesis of simultaneously heat integrated and thermally coupled nonsharp distillation sequences based on stochastic optimization , 2019, Comput. Chem. Eng..

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

[28]  G. M. Wilson,et al.  Vapor-Liquid Equilibrium. XI. A New Expression for the Excess Free Energy of Mixing , 1964 .

[29]  Ignacio E. Grossmann,et al.  Simultaneous synthesis of distillation sequences in overall process schemes using an improved minlp approach , 1996 .

[30]  R. Agrawal,et al.  Process intensification in multicomponent distillation: A review of recent advancements , 2019, Chemical Engineering Research and Design.

[31]  Rakesh Agrawal,et al.  A matrix method for multicomponent distillation sequences , 2009 .

[32]  J. Prausnitz,et al.  LOCAL COMPOSITIONS IN THERMODYNAMIC EXCESS FUNCTIONS FOR LIQUID MIXTURES , 1968 .

[33]  Gary J. Powers,et al.  Synthesis strategies for multicomponent separation systems with energy integration , 1974 .

[34]  Rakesh Agrawal,et al.  A synthesis method for multicomponent distillation sequences with fewer columns , 2012 .

[35]  Z. Fidkowski,et al.  Minimum energy requirements of thermally coupled distillation systems , 1987 .

[36]  Rakesh Agrawal,et al.  Synthesis of distillation configurations. II: A search formulation for basic configurations , 2010, Comput. Chem. Eng..

[37]  R. Agrawal.  Multieffect distillation for thermally coupled configurations , 2000 .

[38]  Mohit Tawarmalani,et al.  A New Framework for Combining a Condenser and Reboiler in a Configuration To Consolidate Distillation Columns , 2015 .

[39]  Mark J. Andrecovich,et al.  An MILP formulation for heat‐integrated distillation sequence synthesis , 1985 .

[40]  Ignacio E. Grossmann,et al.  A rigorous disjunctive optimization model for simultaneous flowsheet optimization and heat integration , 1998 .

[41]  Rakesh Agrawal,et al.  More Operable Fully Thermally Coupled Distillation Column Configurations for Multicomponent Distillation , 1999 .

[42]  V. R. Dhole,et al.  Heat transfer across the wall of dividing wall columns , 1994 .

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

[44]  Mohit Tawarmalani,et al.  A systematic method to synthesize all dividing wall columns for n -component separation-Part I , 2018 .

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

[46]  R. Agrawal,et al.  Global optimization of multicomponent distillation configurations: 2. Enumeration based global minimization algorithm , 2016 .

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

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

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

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

[51]  Ivar J. Halvorsen.  Minimum Energy Requirements in Complex Distillation Arrangements , 2001 .

[52]  Mirko Skiborowski,et al.  Efficient optimization-based design of energy-integrated distillation processes , 2019, Comput. Chem. Eng..

[53]  Gary J. Powers,et al.  Synthesis of distillation systems with energy integration , 1974 .

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

[55]  C. Floudas,et al.  A mixed-integer nonlinear programming formulation for the synthesis of heat-integrated distillation sequences , 1988 .