Результаты исследований: Научные публикации в периодических изданиях › статья › Рецензирование
Study of Deep Eutectic Solvent on the Base Choline Chloride as Entrainer for the Separation Alcohol−Ester Systems. / Samarov, Artemiy; Smirnov, Michael; Toikka, Alexander; Prikhodko, Igor.
в: Journal of Chemical & Engineering Data, Том 63, № 6, 14.06.2018, стр. 1877-1884.Результаты исследований: Научные публикации в периодических изданиях › статья › Рецензирование
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TY - JOUR
T1 - Study of Deep Eutectic Solvent on the Base Choline Chloride as Entrainer for the Separation Alcohol−Ester Systems
AU - Samarov, Artemiy
AU - Smirnov, Michael
AU - Toikka, Alexander
AU - Prikhodko, Igor
N1 - Publisher Copyright: © 2018 American Chemical Society.
PY - 2018/6/14
Y1 - 2018/6/14
N2 - Choline chloride-based deep eutectic solvent(DES) was tested for the separation of azeotropic mixtures ofethanol−ethyl acetate, n-propanol−n-propyl acetate and nbutanol−n-butyl acetate via liquid−liquid extraction. The mixtureof choline chloride with malonic acid with a molar ratio of 1:1was used. Extraction experiments were conducted with theternary mixture ethanol−ethyl acetate−DES at temperatures293.15, 303.15, and 313.15 K and with ternary mixtures npropanol−n-propyl acetate−DES and n-butanol−n-butyl acetate−DES at 293.15, 303.15, 313.15, and 323.15 K. Liquid−liquid tie-lines for studied systems were determined. Theextraction performance of DES was characterized with solutedistribution coefficients and values of selectively respectively toalcohol. The influence of the alkyl chain length of the alcohol and ester on the phase equilibria was investigated. Experimentaldata were fitted using the nonrandom two liquids model.
AB - Choline chloride-based deep eutectic solvent(DES) was tested for the separation of azeotropic mixtures ofethanol−ethyl acetate, n-propanol−n-propyl acetate and nbutanol−n-butyl acetate via liquid−liquid extraction. The mixtureof choline chloride with malonic acid with a molar ratio of 1:1was used. Extraction experiments were conducted with theternary mixture ethanol−ethyl acetate−DES at temperatures293.15, 303.15, and 313.15 K and with ternary mixtures npropanol−n-propyl acetate−DES and n-butanol−n-butyl acetate−DES at 293.15, 303.15, 313.15, and 323.15 K. Liquid−liquid tie-lines for studied systems were determined. Theextraction performance of DES was characterized with solutedistribution coefficients and values of selectively respectively toalcohol. The influence of the alkyl chain length of the alcohol and ester on the phase equilibria was investigated. Experimentaldata were fitted using the nonrandom two liquids model.
KW - LIQUID-LIQUID EQUILIBRIA
KW - TEMPERATURE IONIC LIQUIDS
KW - ETHYL-ACETATE
KW - ACETIC-ACID
KW - EXTRACTIVE DISTILLATION
KW - AZEOTROPIC MIXTURE
KW - DIMETHYL CARBONATE
KW - ETHANOL
KW - PLUS
KW - ANION
UR - http://www.scopus.com/inward/record.url?scp=85048532698&partnerID=8YFLogxK
UR - http://www.mendeley.com/research/study-deep-eutectic-solvent-base-choline-chloride-entrainer-separation-alcoholester-systems
U2 - 10.1021/acs.jced.7b00912
DO - 10.1021/acs.jced.7b00912
M3 - Article
VL - 63
SP - 1877
EP - 1884
JO - Journal of Chemical & Engineering Data
JF - Journal of Chemical & Engineering Data
SN - 0021-9568
IS - 6
ER -
ID: 25803178