![US6358908B1 - Azeotropic compositions of 1,3-dioxolane and hydrocarbons having 5 or 6 carbon atoms and the use thereof in the production of foams - Google Patents US6358908B1 - Azeotropic compositions of 1,3-dioxolane and hydrocarbons having 5 or 6 carbon atoms and the use thereof in the production of foams - Google Patents](https://patentimages.storage.googleapis.com/e8/1e/37/a2df84733db5ee/US6358908-drawings-page-3.png)
US6358908B1 - Azeotropic compositions of 1,3-dioxolane and hydrocarbons having 5 or 6 carbon atoms and the use thereof in the production of foams - Google Patents
![A review of extractive distillation from an azeotropic phenomenon for dynamic control - ScienceDirect A review of extractive distillation from an azeotropic phenomenon for dynamic control - ScienceDirect](https://ars.els-cdn.com/content/image/1-s2.0-S1004954118305871-ga1.jpg)
A review of extractive distillation from an azeotropic phenomenon for dynamic control - ScienceDirect
![Processes | Free Full-Text | Vapor–Liquid Equilibrium in Binary and Ternary Azeotropic Solutions Acetonitrile-Ethanol-Water with the Addition of Amino Esters of Boric Acid | HTML Processes | Free Full-Text | Vapor–Liquid Equilibrium in Binary and Ternary Azeotropic Solutions Acetonitrile-Ethanol-Water with the Addition of Amino Esters of Boric Acid | HTML](https://www.mdpi.com/processes/processes-10-02125/article_deploy/html/images/processes-10-02125-g004.png)
Processes | Free Full-Text | Vapor–Liquid Equilibrium in Binary and Ternary Azeotropic Solutions Acetonitrile-Ethanol-Water with the Addition of Amino Esters of Boric Acid | HTML
![Improved Design and Optimization for Separating Azeotropes with Heavy Component as Distillate through Energy-Saving Extractive Distillation by Varying Pressure | Industrial & Engineering Chemistry Research Improved Design and Optimization for Separating Azeotropes with Heavy Component as Distillate through Energy-Saving Extractive Distillation by Varying Pressure | Industrial & Engineering Chemistry Research](https://pubs.acs.org/cms/10.1021/acs.iecr.7b00687/asset/images/medium/ie-2017-00687f_0011.gif)
Improved Design and Optimization for Separating Azeotropes with Heavy Component as Distillate through Energy-Saving Extractive Distillation by Varying Pressure | Industrial & Engineering Chemistry Research
![Txy diagrams of different types of binary azeotropes: (a) homogeneous... | Download Scientific Diagram Txy diagrams of different types of binary azeotropes: (a) homogeneous... | Download Scientific Diagram](https://www.researchgate.net/publication/309895446/figure/fig2/AS:606787317276672@1521680778991/Txy-diagrams-of-different-types-of-binary-azeotropes-a-homogeneous-minimum-boiling.png)
Txy diagrams of different types of binary azeotropes: (a) homogeneous... | Download Scientific Diagram
![Txy diagrams of different types of binary azeotropes: (a) homogeneous... | Download Scientific Diagram Txy diagrams of different types of binary azeotropes: (a) homogeneous... | Download Scientific Diagram](https://www.researchgate.net/profile/Shisheng-Liang/publication/309895446/figure/fig2/AS:606787317276672@1521680778991/Txy-diagrams-of-different-types-of-binary-azeotropes-a-homogeneous-minimum-boiling_Q320.jpg)
Txy diagrams of different types of binary azeotropes: (a) homogeneous... | Download Scientific Diagram
![Separation of acetone–tetrahydrofuran azeotropic mixture by continuous extractive distillation - Yuan - 2013 - Journal of Chemical Technology & Biotechnology - Wiley Online Library Separation of acetone–tetrahydrofuran azeotropic mixture by continuous extractive distillation - Yuan - 2013 - Journal of Chemical Technology & Biotechnology - Wiley Online Library](https://onlinelibrary.wiley.com/cms/asset/7e9a274c-1281-4307-8650-0a0aad0ac64b/jctb3997-fig-0001-m.jpg)
Separation of acetone–tetrahydrofuran azeotropic mixture by continuous extractive distillation - Yuan - 2013 - Journal of Chemical Technology & Biotechnology - Wiley Online Library
![Processes | Free Full-Text | Zero-Discharge Process for Recycling of Tetrahydrofuran–Water Mixtures | HTML Processes | Free Full-Text | Zero-Discharge Process for Recycling of Tetrahydrofuran–Water Mixtures | HTML](https://www.mdpi.com/processes/processes-09-00729/article_deploy/html/images/processes-09-00729-g001.png)
Processes | Free Full-Text | Zero-Discharge Process for Recycling of Tetrahydrofuran–Water Mixtures | HTML
![Energy-efficient extractive pressure-swing distillation for separating binary minimum azeotropic mixture dimethyl carbonate and ethanol - ScienceDirect Energy-efficient extractive pressure-swing distillation for separating binary minimum azeotropic mixture dimethyl carbonate and ethanol - ScienceDirect](https://ars.els-cdn.com/content/image/1-s2.0-S1383586619321604-ga1.jpg)
Energy-efficient extractive pressure-swing distillation for separating binary minimum azeotropic mixture dimethyl carbonate and ethanol - ScienceDirect
![Separation of azeotropic mixtures (ethanol and water) enhanced by deep eutectic solvents - ScienceDirect Separation of azeotropic mixtures (ethanol and water) enhanced by deep eutectic solvents - ScienceDirect](https://ars.els-cdn.com/content/image/1-s2.0-S0378381217301024-fx1.jpg)
Separation of azeotropic mixtures (ethanol and water) enhanced by deep eutectic solvents - ScienceDirect
![Separation of dimethyl carbonate/methanol azeotropic mixture by pervaporation with dealcoholized room temperature-vulcanized silicone rubber/nanosilica hybrid active layer - ScienceDirect Separation of dimethyl carbonate/methanol azeotropic mixture by pervaporation with dealcoholized room temperature-vulcanized silicone rubber/nanosilica hybrid active layer - ScienceDirect](https://ars.els-cdn.com/content/image/1-s2.0-S1383586620314003-gr1.jpg)