A New Method for Synthesis of Thermodynamically Equivalent Structures for Petlyuk Arrangements
暂无分享,去创建一个
[1] Salvador Hernández,et al. Analysis of Control Properties of Thermally Coupled Distillation Sequences for Four-Component Mixtures , 2005 .
[2] Ilkka Turunen,et al. Synthesis and Optimal Design of Thermodynamically Equivalent Thermally Coupled Distillation Systems , 2004 .
[3] Rakesh Agrawal,et al. More Operable Fully Thermally Coupled Distillation Column Configurations for Multicomponent Distillation , 1999 .
[4] Hans Becker,et al. Partitioned Distillation Columns -- Why, When & How , 2001 .
[5] Sigurd Skogestad,et al. Minimum Energy Consumption in Multicomponent Distillation. 2. Three-Product Petlyuk Arrangements , 2003 .
[6] Sigurd Skogestad,et al. Optimizing control of Petlyuk distillation : Understanding the steady-state behavior , 1997 .
[7] Michael F. Malone. Optimality Regions for Complex Column Alternatives in Distillation Systems , 1988 .
[8] Z. Fidkowski,et al. Minimum energy requirements of thermally coupled distillation systems , 1987 .
[9] Andrzej Kraslawski,et al. Partially thermally coupled distillation systems for multicomponent separations , 2003 .
[10] Cathy H. Wu. Artificial Neural Networks for Molecular Sequence Analysis , 1997, Comput. Chem..
[11] K. A. Amminudin,et al. Design and Optimization of Fully Thermally Coupled Distillation Columns: Part 1: Preliminary Design and Optimization Methodology , 2001 .
[12] C. Pantelides,et al. Optimal design of thermally coupled distillation columns , 1999 .
[13] G. Kaibel. Distillation columns with vertical partitions , 1987 .
[14] Ignacio E. Grossmann,et al. Thermodynamically equivalent configurations for thermally coupled distillation , 2003 .
[15] R. Agrawal,et al. Are Thermally Coupled Distillation Columns Always Thermodynamically More Efficient for Ternary Distillations , 1998 .
[16] P. Mizsey,et al. Energy savings of integrated and coupled distillation systems , 1999 .
[17] M. Powell. Optimization in action: 7th–9th January 1975. University of Bristol, UK. Organized by the Institute of Mathematics and its Applications, Essex, UK , 1975 .
[18] Sigurd Skogestad,et al. Minimum Energy Consumption in Multicomponent Distillation. 3. More Than Three Products and Generalized Petlyuk Arrangements , 2003 .
[19] Rakesh Agrawal,et al. Multicomponent thermally coupled systems of distillation columns at minimum reflux , 2001 .
[20] R. Agrawal,et al. More operable arrangements of fully thermally coupled distillation columns , 1998 .
[21] Juan Gabriel Segovia-Hernández,et al. Control behaviour of thermally coupled distillation sequences , 2002 .
[22] Sascha Wenzel,et al. Design of Complex Distillation Columns by Overall‐Cost Optimization , 2004 .
[23] Kyu Suk Hwang,et al. Application of a fully thermally coupled distillation column for fractionation process in naphtha reforming plant , 2004 .
[24] Michael A. Schultz,et al. Reduce Costs with Dividing-Wall Columns , 2002 .
[25] Robin Smith,et al. Operation and Control of Dividing Wall Distillation Columns: Part 1: Degrees of Freedom and Dynamic Simulation , 1998 .
[26] Analysis of Ternary Distillation Column Sequences , 1987 .
[27] V. R. Dhole,et al. Heat transfer across the wall of dividing wall columns , 1994 .
[28] F. Petlyuk. Thermodynamically Optimal Method for Separating Multicomponent Mixtures , 1965 .
[29] Andrzej Kraslawski,et al. Optimal Design of Distillation Flowsheets with a Lower Number of Thermal Couplings for Multicomponent Separations , 2002 .
[30] Gerd Kaibel,et al. Process Synthesis and Design in Industrial Practice , 2002 .
[31] Arturo Jiménez,et al. Controllability Analysis of Thermally Coupled Distillation Systems , 1999 .
[32] Ilkka Turunen,et al. Synthesis of Functionally Distinct Thermally Coupled Configurations for Quaternary Distillations , 2003 .
[33] Ernest J. Henley,et al. Equilibrium-Stage Separation Operations in Chemical Engineering , 1981 .
[34] Arthur W. Westerberg,et al. Temperature-heat diagrams for complex columns. 3. Underwood's method for the Petlyuk configuration , 1989 .
[35] Zbigniew T. Fidkowski,et al. Thermally coupled system of distillation columns: Optimization procedure , 1986 .
[36] Rakesh Agrawal,et al. Synthesis of Distillation Column Configurations for a Multicomponent Separation , 1996 .
[37] Sigurd Skogestad,et al. Operation of Integrated Three-Product (Petlyuk) Distillation Columns , 1995 .
[38] Sigurd Skogestad,et al. Complex distillation arrangements: Extending the petlyuk ideas , 1997 .
[39] Arturo Jiménez,et al. Design of energy-efficient Petlyuk systems , 1999 .
[40] Young Han Kim. Structural design and operation of a fully thermally coupled distillation column , 2002 .
[41] L. Puigjaner,et al. Controllability of different multicomponent distillation arrangements , 2003 .
[42] Rakesh Agrawal,et al. A Method to Draw Fully Thermally Coupled Distillation Column Configurations for Multicomponent Distillation , 2000 .
[43] Hartmut Schoenmakers,et al. Model predictive control of integrated unit operations: Control of a divided wall column , 2004 .
[44] Sigurd Skogestad,et al. Shortcut Analysis of Optimal Operation of Petlyuk Distillation , 2004 .