Circumventing the Black-Hole Problem in Design and Control of Dividing-Wall Distillation Columns

Owing to the great degree of mass integration and energy integration between the prefractionator and the main distillation column, it is usually infeasible to achieve a four-point composition contr...

[1]  Michael F. Malone,et al.  Approximate design and optimization of a thermally coupled distillation with prefractionation , 1988 .

[2]  G. Kaibel,et al.  Dividing wall columns: Fundamentals and recent advances , 2010 .

[3]  Jeffrey D. Ward,et al.  Quantifying Potential Energy Savings of Divided Wall Columns Based on Degree of Remixing , 2011 .

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

[5]  Ignacio E. Grossmann,et al.  Synthesis of complex thermally coupled distillation systems including divided wall columns , 2013 .

[6]  William L. Luyben,et al.  New Control Structure for Divided-Wall Columns , 2009 .

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

[8]  Costin Sorin Bildea,et al.  A control perspective on process intensification in dividing-wall columns , 2011 .

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

[10]  Eugeny Y. Kenig,et al.  Dividing wall columns in chemical process industry: A review on current activities , 2011 .

[11]  Hartmut Schoenmakers,et al.  Model predictive control of integrated unit operations: Control of a divided wall column , 2004 .

[12]  Anton A. Kiss,et al.  Energy efficient control of a BTX dividing-wall column , 2011, Comput. Chem. Eng..

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

[14]  Jan Harmsen,et al.  Process intensification in the petrochemicals industry: Drivers and hurdles for commercial implementation , 2010 .

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

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

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

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

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

[20]  Cristofer Bravo-Bravo,et al.  Extractive Dividing Wall Column: Design and Optimization , 2010 .

[21]  Peng Wang,et al.  A SIMPLE ALGORITHM FOR THE DESIGN OF FULLY THERMALLY COUPLED DISTILLATION COLUMNS (FTCDC) , 2012 .

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

[23]  Ignacio E. Grossmann,et al.  Strategies for the robust simulation of thermally coupled distillation sequences , 2012, Comput. Chem. Eng..

[24]  Anton A. Kiss,et al.  Comparison of Control Strategies for Dividing-Wall Columns , 2010 .

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

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

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

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

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

[30]  Georg Fieg,et al.  Decentralized temperature control of a pilot dividing wall column , 2011 .

[31]  Robin Smith,et al.  Operation and Control of Dividing Wall Distillation Columns: Part 2: Simulation and Pilot Plant Studies Using Temperature Control , 1998 .