Exergy, economic and environmental analysis of an integrated pressure-swing reactive distillation process for the isobutyl acetate production via methyl acetate transesterification

[1]  C. Bîldea,et al.  Novel eco-efficient reactive distillation process for dimethyl carbonate production by indirect alcoholysis of urea , 2021, Frontiers of Chemical Science and Engineering.

[2]  H. Sharon.  Energy, exergy, environmental benefits and economic aspects of novel hybrid solar still for sustainable water distillation , 2021 .

[3]  A. Zeng,et al.  Separation of n-heptane/isobutanol via eco-efficient vapor recompression-assisted distillation: process optimization and control strategy , 2021, Frontiers of Chemical Science and Engineering.

[4]  Lei Wang,et al.  Energy-saving investigation of organic material recovery from wastewater via thermal coupling extractive distillation combined with heat pump based on thermoeconomic and environmental analysis , 2021 .

[5]  Álvaro Orjuela,et al.  Isobutyl acetate by reactive distillation. Part II. Kinetic study , 2020 .

[6]  Álvaro Orjuela,et al.  Isobutyl acetate by reactive distillation. Part III. Conceptual design, simulation and optimization , 2020 .

[7]  Álvaro Orjuela,et al.  Isobutyl acetate by reactive distillation. Non-reactive phase equilibrium and topological analysis , 2020 .

[8]  Pengfei Xu,et al.  Rigorous design and control of thermally integrated pressure‐swing reactive distillation process for isobutyl acetate production considering the effect of column pressures , 2020 .

[9]  A. Zeng,et al.  Eco-efficient vapor recompression-assisted pressure-swing distillation process for the separation of a maximum-boiling azeotrope , 2020 .

[10]  Zhishan Zhang,et al.  Energy-saving investigation of hybrid reactive distillation for n-butyl acetate production from two blending feedstocks , 2020 .

[11]  Nguyen Van Duc Long,et al.  Electrical-driven self-heat recuperative pressure-swing azeotropic distillation to minimize process cost and CO2 emission: Process electrification and simultaneous optimization , 2020 .

[12]  D. Wong,et al.  Reactive vapor-recompression distillation for green hexamethylene-1,6-dicarbamate synthesis , 2020 .

[13]  Yiqing Luo,et al.  A novel method for generating distillation configurations , 2019, Frontiers of Chemical Science and Engineering.

[14]  H. Cen,et al.  Novel Process Design Combined with Reactive Distillation and Pressure-Swing Distillation for Propylene Glycol Monomethyl Ether Acetate Synthesis , 2019, Industrial & Engineering Chemistry Research.

[15]  Jun Gao,et al.  Energy-saving hybrid processes combining pressure-swing reactive distillation and pervaporation membrane for n-propyl acetate production , 2019, Separation and Purification Technology.

[16]  Jun Gao,et al.  Separation of ternary mixture with double azeotropic system by a pressure-swing batch distillation integrated with quasi-continuous process , 2019, Process Safety and Environmental Protection.

[17]  Ojasvi,et al.  Design and control of an energy-efficient alternative process for separation of Dichloromethane-Methanol binary azeotropic mixture , 2019, Separation and Purification Technology.

[18]  Ashish Singh,et al.  Heat-pump assisted distillation versus double-effect distillation for bioethanol recovery followed by pressure swing adsorption for bioethanol dehydration , 2019, Separation and Purification Technology.

[19]  Xiaojing Shi,et al.  Comparison of pressure-swing distillation and heterogeneous azeotropic distillation for recovering benzene and isopropanol from wastewater , 2019, Process Safety and Environmental Protection.

[20]  Lichun Dong,et al.  Design and control of pressure-swing distillation for separating ternary systems with three binary minimum azeotropes , 2019, AIChE Journal.

[21]  W. Shen,et al.  Process Development, Assessment, and Control of Reactive Dividing-Wall Column with Vapor Recompression for Producing n-Propyl Acetate , 2018, Industrial & Engineering Chemistry Research.

[22]  A. A. Kiss,et al.  Reactive Distillation: Stepping Up to the Next Level of Process Intensification , 2018, Industrial & Engineering Chemistry Research.

[23]  Kang Ma,et al.  Energy-saving thermally coupled ternary extractive distillation process by combining with mixed entrainer for separating ternary mixture containing bioethanol , 2018 .

[24]  Weerawat Runguphan,et al.  Metabolic engineering of Pichia pastoris for production of isobutanol and isobutyl acetate , 2018, Biotechnology for Biofuels.

[25]  J. Posada,et al.  Comparative early stage assessment of multiproduct biorefinery systems: An application to the isobutanol platform. , 2017, Bioresource technology.

[26]  Gregorius Rionugroho Harvianto,et al.  A thermally coupled reactive distillation and pervaporation hybrid process for n-butyl acetate production with enhanced energy efficiency , 2017 .

[27]  Rui Li,et al.  Investigation about Energy Saving for Synthesis of Isobutyl Acetate in the Reactive Dividing-Wall Column , 2017 .

[28]  J. Degrève,et al.  Retrofitting of extractive distillation columns with high flux, low separation factor membranes: A way to reduce the energy demand? , 2016 .

[29]  Li Xu,et al.  Transesterification of Methyl Acetate with Isobutanol in a Reactive and Extractive Distillation Column with Ionic Liquid as Catalyst and Molecular Liquid as Entrainer , 2016 .

[30]  Chao Yu,et al.  Design and control of different pressure thermally coupled reactive distillation for amyl acetate synthesis , 2015 .

[31]  S. B. Adejuyigbe,et al.  Performance enhancement of vapor recompression heat pump , 2014 .

[32]  Amiya K. Jana,et al.  A novel intensified heat integration in multicomponent distillation , 2012 .

[33]  Hong Li,et al.  Hydrolysis of methyl acetate via catalytic distillation: Simulation and design of new technological process , 2010 .

[34]  Amiya K. Jana,et al.  Heat integrated distillation operation , 2010 .

[35]  Alime Izci,et al.  Liquid-phase esterification of acetic acid with isobutanol catalyzed by ion-exchange resins , 2007 .

[36]  Ž. Olujić,et al.  Estimation and reduction of CO2 emissions from crude oil distillation units , 2006 .

[37]  Robin Smith,et al.  Reducing CO2 emissions and energy consumption of heat-integrated distillation systems. , 2005, Environmental science & technology.

[38]  Laureano Jiménez,et al.  The Production of Butyl Acetate and Methanol via Reactive and Extractive Distillation. I. Chemical Equilibrium, Kinetics, and Mass-Transfer Issues , 2002 .

[39]  S. Bandyopadhyay.  Effect of feed on optimal thermodynamic performance of a distillation column , 2002 .

[40]  Rajamani Krishna,et al.  Modelling reactive distillation , 2000 .

[41]  J. Resa,et al.  (vapour + liquid) equilibria for (methanol + butyl acetate), (vinyl acetate + butyl acetate), (methanol + isobutyl acetate), and (vinyl acetate + isobutyl acetate) , 1998 .

[42]  J. Llorens,et al.  Pressure selection for non-reactive and reactive pressure-swing distillation , 2019, Chemical Engineering and Processing - Process Intensification.

[43]  A METHOD OF GEOMETRICAL REPRESENTATION OF THE THERMODYNAMIC PROPERTIES OF SUBSTANCES BY MEANS OF SURFACES , 2010 .

[44]  Shyan-Shu Shieh,et al.  Plant-wide design and control of acetic acid dehydration system via heterogeneous azeotropic distillation and divided wall distillation , 2008 .