Separating an azeotropic mixture of toluene and ethanol via heat integration pressure swing distillation
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Lili Wang | Yinglong Wang | Yixin Ma | Zhaoyou Zhu | Wanling Wang | Yixin Ma | Zhaoyou Zhu | Yinglong Wang | Lili Wang | Wanling Wang
[1] William L. Luyben,et al. Design and Control of a Fully Heat-Integrated Pressure-Swing Azeotropic Distillation System , 2008 .
[2] Weisong Li,et al. New Pressure-Swing Distillation for Separating Pressure-Insensitive Maximum Boiling Azeotrope via Introducing a Heavy Entrainer: Design and Control , 2013 .
[3] William L. Luyben,et al. Pressure-Swing Distillation for Minimum- and Maximum-Boiling Homogeneous Azeotropes , 2012 .
[4] William L. Luyben,et al. Plantwide control of an isopropyl alcohol dehydration process , 2006 .
[5] S. Xu,et al. Separation of tetrahydrofuran-water azeotropic mixture by batch extractive distillation process , 2006 .
[6] William L. Luyben. Control of the Maximum-Boiling Acetone/Chloroform Azeotropic Distillation System , 2008 .
[7] Jun Hong Liu,et al. Design and control of acetic acid dehydration system via heterogeneous azeotropic distillation , 2004 .
[8] William L. Luyben,et al. Design and Control of Distillation Systems for Separating Azeotropes , 2010 .
[9] Iván D. Gil,et al. Extractive Distillation of Acetone/Methanol Mixture Using Water as Entrainer , 2009 .
[10] Qunxiong Zhu,et al. Design and control of an ideal heat-integrated distillation column (ideal HIDIC) system separating a close-boiling ternary mixture , 2007 .
[11] William L. Luyben,et al. Comparison of the dynamic performances of three heat-integrated distillation configurations , 1988 .
[12] I-Lung Chien,et al. Design and Control of an Isopropyl Alcohol Dehydration Process via Extractive Distillation Using Dimethyl Sulfoxide as an Entrainer , 2008 .
[13] Peizhe Cui,et al. Heat-Integrated Pressure-Swing-Distillation Process for Separation of Tetrahydrofuran/Methanol with Different Feed Compositions , 2014 .
[14] Efstratios N. Pistikopoulos,et al. Optimal design and control of a high-purity industrial distillation system , 2001 .
[15] William L. Luyben,et al. Design and control of a two-column azeotropic distillation system , 1985 .
[16] Masaru Nakaiwa,et al. Internally Heat-Integrated Distillation Columns: A Review , 2003 .
[17] Weisong Li,et al. Comparison of Pressure-Swing Distillation and Extractive Distillation Methods for Isopropyl Alcohol/Diisopropyl Ether Separation , 2014 .
[18] A. Vicent Orchillés,et al. Using 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate as an Entrainer for the Extractive Distillation of Ethanol + Water Mixtures , 2010 .
[19] Devrim B. Kaymak,et al. Computers and Chemical Engineering , 2014 .
[20] Wei Wei,et al. Design and Control of Dimethyl Carbonate–Methanol Separation via Pressure-Swing Distillation , 2013 .
[21] Nidal Hilal,et al. Simulation and optimisation of extractive distillation with water as solvent , 2005 .
[22] Songlin Xu,et al. A new entrainer for separation of tetrahydrofuran–water azeotropic mixture by extractive distillation , 2006 .
[23] W. Luyben. Distillation Design and Control Using Aspen Simulation , 2006 .
[24] William L. Luyben,et al. New Control Structure for Divided-Wall Columns , 2009 .
[25] William L. Luyben,et al. Comparison of Extractive Distillation and Pressure-Swing Distillation for Acetone-Methanol Separation , 2008 .
[26] Michael F. Doherty,et al. A new pressure-swing-distillation process for separating homogeneous azeotropic mixtures , 1992 .
[27] Vishal Kaushik. Dynamics and Control of Distillation using Aspen , 2011 .
[29] Juan B. Montón,et al. Separation of isobutyl alcohol and isobutyl acetate by extractive distillation and pressure-swing distillation: Simulation and optimization , 2006 .
[30] James M. Douglas,et al. Conceptual Design of Chemical Processes , 1988 .
[31] B. Suphanit,et al. Optimal heat distribution in the internally heat-integrated distillation column (HIDiC) , 2011 .