Techno-economic and energetic assessment of an innovative energy-saving separation process for electronic-grade acetone purification

[1]  S. Gu,et al.  4E analysis of the cryogenic CO2 separation process integrated with waste heat recovery , 2023, Energy.

[2]  Jose Adrian Chavez Velasco,et al.  Which separation scenarios are advantageous for membranes or distillations? , 2022, AIChE Journal.

[3]  P. Prajapati,et al.  Hand sanitizers as a preventive measure in COVID-19 pandemic, its characteristics, and harmful effects: a review , 2022, Journal of the Egyptian Public Health Association.

[4]  Boqiang Lin,et al.  The effects and reacts of COVID-19 pandemic and international oil price on energy, economy, and environment in China , 2021, Applied Energy.

[5]  Mohit Tawarmalani,et al.  Systematic Analysis Reveals Thermal Separations Are Not Necessarily Most Energy Intensive , 2021 .

[6]  J. Klemeš,et al.  Impacts of COVID-19 on energy demand and consumption: Challenges, lessons and emerging opportunities , 2021, Applied Energy.

[7]  Patricia Gorgojo,et al.  Adsorptive separation of C2H6/C2H4 on metal-organic frameworks (MOFs) with pillared-layer structures , 2020 .

[8]  Kaiyu Sun,et al.  Key issues and novel optimization approaches of industrial waste heat recovery in district heating systems , 2019, Energy.

[9]  Yang Su,et al.  Investigation of an energy-saving double-thermally coupled extractive distillation for separating ternary system benzene/toluene/cyclohexane , 2019, Energy.

[10]  Ting Ma,et al.  Design and optimization of a novel high temperature heat exchanger for waste heat cascade recovery from exhaust flue gases , 2018, Energy.

[11]  Galina S. Nyashina,et al.  Environmental, economic and energetic benefits of using coal and oil processing waste instead of coal to produce the same amount of energy , 2018, Energy Conversion and Management.

[12]  Fengyuan Zhang,et al.  Optimization of a novel cogeneration system including a gas turbine, a supercritical CO2 recompression cycle, a steam power cycle and an organic Rankine cycle , 2018, Energy Conversion and Management.

[13]  François Maréchal,et al.  A heat integration method with multiple heat exchange interfaces , 2018, Energy.

[14]  Wai Mun Chan,et al.  Synthesis of energy efficient chilled and cooling water network by integrating waste heat recovery refrigeration system , 2017 .

[15]  A. Malekpour,et al.  Pervaporation dehydration of binary and ternary mixtures of acetone, isopropanol and water using polyvinyl alcohol/zeolite membranes , 2017 .

[16]  D. Hone.  The Paris Agreement , 2017 .

[17]  M. F. Figueirêdo,et al.  Effect of Solvent Content and Heat Integration on the Controllability of Extractive Distillation Process for Anhydrous Ethanol Production , 2016 .

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

[19]  Luisa F. Cabeza,et al.  Industrial waste heat recovery technologies: An economic analysis of heat transformation technologies , 2015 .

[20]  I-Lung Chien,et al.  Critical Assessment of the Energy-Saving Potential of an Extractive Dividing-Wall Column , 2013 .

[21]  Chunjian Xu,et al.  Design and Control of Distillation System for Methylal/Methanol Separation. Part 2: Pressure Swing Distillation with Full Heat Integration , 2012 .

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

[23]  V. Senthil Kumar,et al.  Generalized model development for a cryo-adsorber and 1-D results for the isobaric refueling period , 2010 .

[24]  C. Shu,et al.  Thermal hazards evaluation of cumene hydroperoxide mixed with its derivatives , 2009 .

[25]  N. Kaistha,et al.  Internal Heat Integration and Controllability of Double Feed Reactive Distillation Columns, 2. Effect of Catalyst Redistribution , 2008 .

[26]  V. M. Zakoshansky,et al.  The cumene process for phenol-acetone production , 2007 .

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

[28]  F. Meunier,et al.  Adsorption of gas mixtures in TSA adsorbers under various heat removal conditions , 2004 .

[29]  Sigurd Skogestad,et al.  Selecting appropriate control variables for a heat-integrated distillation system with prefractionator , 2004, Comput. Chem. Eng..

[30]  Rakesh Agrawal,et al.  Optimal thermodynamic feed conditions for distillation of ideal binary mixtures , 1997 .

[31]  P. Andrigo,et al.  Phenol-acetone process: cumene oxidation kinetics and industrial plant simulation , 1992 .

[32]  D. Yang,et al.  Energy Saving Distillation Process for Mixed Trichlorobenzene Based on Orc Coupled Mvr Heat Pump Technology , 2022, SSRN Electronic Journal.

[33]  J. Nastaj,et al.  Experimental studies on 3A and 4A zeolite molecular sieves regeneration in TSA process: Aliphatic alcohols dewatering–water desorption , 2015 .

[34]  Jose A. Romagnoli,et al.  Chapter B4 – Process design and operation: Incorporating environmental, profitability, heat integration and controllability considerations , 2004 .

[35]  D. Bodansky.  The United Nations Framework Convention on Climate Change: A Commentary , 1993 .

[36]  T. Sakata,et al.  Separation of acetone/water mixture by thin acrylamide gel membrane prepared in pores of thin ceramic membrane. , 1990 .