A SIMPLE ALGORITHM FOR THE DESIGN OF FULLY THERMALLY COUPLED DISTILLATION COLUMNS (FTCDC)

Although material and thermal coupling between the prefractionator and main distillation column renders the fully thermally coupled distillation column (FTCDC) a frequently favorable design option, it also complicates considerably process synthesis and design. In this contribution, a simple algorithm for the synthesis and design of the FTCDC is derived with the optimization of an economical objective function. In terms of an initial process design chosen arbitrarily to meet the given product specification, the algorithm allows the treatment of the continuous operating variables (e.g., the vapor and liquid split ratios) and discontinuous structural variables (e.g., the number of stages in each column section) in a unified manner and permits searches of their optimum values sequentially in each iteration step. The proposed algorithm is characterized by great simplicity in principle and high robustness to the guess of initial process design and the thermodynamic properties of the mixtures separated. Five example problems dealing with the separation of various ternary mixtures with ideal and nonideal thermodynamic properties are employed to evaluate the proposed procedure, and the obtained results demonstrate its applicability and robustness to the synthesis and design of the FTCDC.

[1]  Juan Gabriel Segovia-Hernández,et al.  Control behaviour of thermally coupled distillation sequences , 2002 .

[2]  R. Agrawal,et al.  Are Thermally Coupled Distillation Columns Always Thermodynamically More Efficient for Ternary Distillations , 1998 .

[3]  Sigurd Skogestad,et al.  Optimal operation of Petlyuk distillation: Steady-state behavior , 2001 .

[4]  Arthur W. Westerberg,et al.  Temperature-heat diagrams for complex columns. 3. Underwood's method for the Petlyuk configuration , 1989 .

[5]  Zbigniew T. Fidkowski,et al.  Thermally coupled system of distillation columns: Optimization procedure , 1986 .

[6]  David Shan-Hill Wong,et al.  Controllability and energy efficiency of a high-purity divided wall column , 2007 .

[7]  C. Pantelides,et al.  Optimal design of thermally coupled distillation columns , 1999 .

[8]  Arturo Jiménez-Gutiérrez,et al.  Optimization of Petlyuk sequences using a multi objective genetic algorithm with constraints , 2011, Comput. Chem. Eng..

[9]  J. R. Flower,et al.  Synthesising heat-integrated distillation sequences using mixed integer programming , 1988 .

[10]  Arturo Jiménez,et al.  Controllability Analysis of Thermally Coupled Distillation Systems , 1999 .

[11]  Sigurd Skogestad,et al.  Operation of Integrated Three-Product (Petlyuk) Distillation Columns , 1995 .

[12]  William L. Luyben,et al.  Distillation Design and Control Using AspenTM Simulation: Luyben/Distillation Design and Control Using Aspen Simulation , 2006 .

[13]  K. A. Amminudin,et al.  Design and Optimization of Fully Thermally Coupled Distillation Columns: Part 1: Preliminary Design and Optimization Methodology , 2001 .

[14]  Dale F. Rudd,et al.  Parametric studies in industrial distillation: Part I. Design comparisons , 1978 .

[15]  Young Han Kim Structural Design of Extended Fully Thermally Coupled Distillation Columns , 2001 .

[16]  C. Triantafyllou,et al.  The design and optimisation of fully thermally coupled distillation columns : Process design , 1992 .

[17]  F. B. Petlyuk,et al.  Distillation Theory and Its Application to Optimal Design of Separation Units: Index , 2004 .

[18]  Arturo Jiménez,et al.  Design of energy-efficient Petlyuk systems , 1999 .

[19]  Juha Tanskanen,et al.  A rigorous minimum energy calculation method for a fully thermally coupled distillation system , 2007 .

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

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

[22]  Young Han Kim Rigorous Design of Fully Thermally Coupled Distillation Column , 2001 .

[23]  Kyu Suk Hwang,et al.  Application of a fully thermally coupled distillation column for fractionation process in naphtha reforming plant , 2004 .

[24]  W. Luyben Distillation Design and Control Using Aspen Simulation , 2006 .

[25]  Young Han Kim Structural design and operation of a fully thermally coupled distillation column , 2002 .

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

[27]  Claudia Gutiérrez-Antonio,et al.  Pareto front of ideal Petlyuk sequences using a multiobjective genetic algorithm with constraints , 2009, Comput. Chem. Eng..

[28]  F. B. Petlyuk Distillation Theory and Its Application to Optimal Design of Separation Units: Preface , 2004 .

[29]  Michael F. Malone Optimality Regions for Complex Column Alternatives in Distillation Systems , 1988 .