Liquid-Liquid Equilibria for Ternary Systems of Water plus Methoxycyclopentane plus Alcohol (Methanol, Ethanol, 1-Propanol, or 2-Propanol)

被引:19
|
作者
Wales, Michael D. [1 ,2 ]
Huang, Chaoran [2 ]
Joos, Logan B. [2 ]
Probst, Kyle V. [1 ,3 ]
Vadlani, Praveen V. [3 ]
Anthony, Jennifer L. [2 ]
Rezac, Mary E. [2 ]
机构
[1] Kansas State Univ, IGERT Trainee Biorefining, Manhattan, KS 66506 USA
[2] Kansas State Univ, Dept Chem Engn, Durland Hall, Manhattan, KS 66506 USA
[3] Kansas State Univ, Dept Grain Sci & Ind, Bioproc & Renewable Energy Lab, Manhattan, KS 66506 USA
来源
JOURNAL OF CHEMICAL AND ENGINEERING DATA | 2016年 / 61卷 / 04期
基金
美国国家科学基金会; 美国食品与农业研究所;
关键词
CYCLOPENTYL METHYL-ETHER; TERT-BUTYL ETHER; 298.15; K; SOLVENT; EXTRACTION; BIODIESEL; TETRAHYDROFURAN; MICROALGAE; MIXTURES; PRODUCTS;
D O I
10.1021/acs.jced.5b00803
中图分类号
O414.1 [热力学];
学科分类号
摘要
Liquid-liquid equilibria data were determined for four ternary systems of water + alcohol + methoxycyclopentane (CPME); the alcohols used were methanol, ethanol, 1-propanol, and 2-propanol. All measurements were performed at 298.15 K and atmospheric pressure. Binodal curves were experimentally determined using both the cloud-point method and tie lines. The reliability of the tie-line data were verified by the Hand and Othmer-Tobias plots. Distribution coefficients and separation factors were determined from the tie-line data. The universal quasichemical activity coefficient model was used to correlate the experimental data. Additionally, these water-alcohol-CPME systems were compared to the water-methanol-chloroform system as a green alternative for Bligh and Dyer lipid extraction.
引用
收藏
页码:1479 / 1484
页数:6
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