Phase Equilibrium Study of the Separation of Ethanol–Water Solution with Supercritical CO2

JOURNAL OF CHEMICAL ENGINEERING OF JAPAN

Hiroshi Inomata¹  Akihiro Kondo¹  Shozaburo Saito¹  Kunio Arai¹ 

[1] Department of Molecular Chemistry & Engineering, Tohoku University

关键词: Supercritical Extraction;    Ethanol Solution;    Group Contribution Equation of State;    Vapor–Liquid Equilibrium;   

DOI  :  10.1252/jcej.23.199

来源: Maruzen Company Ltd

【 摘 要 】

References(20)Cited-By(23)To provide a better theoretical basis for obtaining higher concentration of ethanol from a fermentation broth using near- or super-critical CO2 extraction, the vapor–liquid equilibria for the quaternary system of CO2, ethanol, water and an entratner were measured at 35.0°C and 10 MPa for various entrainer concentrations. Experiments were carried out for four entrainers: glycerol, ethylene glycol, 1,3-propanediol and propylene glycol. The experimental results demonstrated that the upper limit of ethanol composition for the CO2–ethanol–water ternary system could be raised by the addition of the above entrainers other than propylene glycol. It was also found that this effect of the entrainer could be estimated qualitatively from its solubility parameter value. The group parameter values of the GC-EOS by Jorgensen were redetermined using binary vapor–liquid equilibrium (VLE) data in order to improve the accuracy of prediction of the VLE of the CO2–ethanol–water and the CO2–ethanol–water-entrainer mixtures.

【 授权许可】

Unknown