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Using a Microchannel Reactor to Optimize the Production of 1-Alkyl-3-Methylimidazolium Chlorides. / Klimenko, A. S.; Andreev, D. V.; Prikhod’ko, S. A. et al.

In: Catalysis in Industry, Vol. 12, No. 3, 01.07.2020, p. 207-215.

Research output: Contribution to journalArticlepeer-review

Harvard

Klimenko, AS, Andreev, DV, Prikhod’ko, SA, Gribovskii, AG, Makarshin, LL & Adonin, NY 2020, 'Using a Microchannel Reactor to Optimize the Production of 1-Alkyl-3-Methylimidazolium Chlorides', Catalysis in Industry, vol. 12, no. 3, pp. 207-215. https://doi.org/10.1134/S2070050420030071

APA

Klimenko, A. S., Andreev, D. V., Prikhod’ko, S. A., Gribovskii, A. G., Makarshin, L. L., & Adonin, N. Y. (2020). Using a Microchannel Reactor to Optimize the Production of 1-Alkyl-3-Methylimidazolium Chlorides. Catalysis in Industry, 12(3), 207-215. https://doi.org/10.1134/S2070050420030071

Vancouver

Klimenko AS, Andreev DV, Prikhod’ko SA, Gribovskii AG, Makarshin LL, Adonin NY. Using a Microchannel Reactor to Optimize the Production of 1-Alkyl-3-Methylimidazolium Chlorides. Catalysis in Industry. 2020 Jul 1;12(3):207-215. doi: 10.1134/S2070050420030071

Author

Klimenko, A. S. ; Andreev, D. V. ; Prikhod’ko, S. A. et al. / Using a Microchannel Reactor to Optimize the Production of 1-Alkyl-3-Methylimidazolium Chlorides. In: Catalysis in Industry. 2020 ; Vol. 12, No. 3. pp. 207-215.

BibTeX

@article{e36de60201b44901a76f68b442fb870a,
title = "Using a Microchannel Reactor to Optimize the Production of 1-Alkyl-3-Methylimidazolium Chlorides",
abstract = "The possibility of using microchannel flow reactors to obtain the kinetic and technological parameters of the synthesis of 1-butyl-3-methylimidazolium chloride (BMIMCl) ionic liquid is demonstrated for the reaction of 1-methylimidazole (MIm) with 1-chlorobutane with no solvents. BMIMCl is produced with high selectivity and specific output in a microchannel flow reactor at temperatures of 120–180°C a contact time of 2–45 min, and a pressure of 20 bar. A positive result is obtained, due to the laminar profile of the flow and a uniform distribution of the reagents concentration over the microchannel cross section. Studying the kinetics of the process in a microchannel flow reactor reveals a shift of the reaction to the mode of diffusive inhibition at temperatures above 150°C. The kinetic data obtained for BMIMCl synthesis are used to develop ways of producing 1-ethyl-3-methylimidazolium and 1-hexyl-3-methylimidazolium chlorides (EMIMCl and HMIMCl, respectively) under the conditions of a microchannel flow reactor. The approach proposed in this work is of interest in developing flow and periodic facilities for the low-tonnage production of dialkylimidazolium, ammonium, and pyridinium salts via quaternization of the corresponding alkyl chlorides and nitrogen-containing bases.",
keywords = "1-alkyl-3-methylimidazolium chloride, BMIMCl, ionic liquid, microchannel flow reactor, quaternization reaction, DESIGN, MICROREACTOR, FLOW, SOLVENT, PHASE, TEMPERATURE, KINETICS, CHEMISTRY, IONIC LIQUIDS",
author = "Klimenko, {A. S.} and Andreev, {D. V.} and Prikhod{\textquoteright}ko, {S. A.} and Gribovskii, {A. G.} and Makarshin, {L. L.} and Adonin, {N. Yu}",
year = "2020",
month = jul,
day = "1",
doi = "10.1134/S2070050420030071",
language = "English",
volume = "12",
pages = "207--215",
journal = "Catalysis in Industry",
issn = "2070-0504",
publisher = "Maik Nauka-Interperiodica Publishing",
number = "3",

}

RIS

TY - JOUR

T1 - Using a Microchannel Reactor to Optimize the Production of 1-Alkyl-3-Methylimidazolium Chlorides

AU - Klimenko, A. S.

AU - Andreev, D. V.

AU - Prikhod’ko, S. A.

AU - Gribovskii, A. G.

AU - Makarshin, L. L.

AU - Adonin, N. Yu

PY - 2020/7/1

Y1 - 2020/7/1

N2 - The possibility of using microchannel flow reactors to obtain the kinetic and technological parameters of the synthesis of 1-butyl-3-methylimidazolium chloride (BMIMCl) ionic liquid is demonstrated for the reaction of 1-methylimidazole (MIm) with 1-chlorobutane with no solvents. BMIMCl is produced with high selectivity and specific output in a microchannel flow reactor at temperatures of 120–180°C a contact time of 2–45 min, and a pressure of 20 bar. A positive result is obtained, due to the laminar profile of the flow and a uniform distribution of the reagents concentration over the microchannel cross section. Studying the kinetics of the process in a microchannel flow reactor reveals a shift of the reaction to the mode of diffusive inhibition at temperatures above 150°C. The kinetic data obtained for BMIMCl synthesis are used to develop ways of producing 1-ethyl-3-methylimidazolium and 1-hexyl-3-methylimidazolium chlorides (EMIMCl and HMIMCl, respectively) under the conditions of a microchannel flow reactor. The approach proposed in this work is of interest in developing flow and periodic facilities for the low-tonnage production of dialkylimidazolium, ammonium, and pyridinium salts via quaternization of the corresponding alkyl chlorides and nitrogen-containing bases.

AB - The possibility of using microchannel flow reactors to obtain the kinetic and technological parameters of the synthesis of 1-butyl-3-methylimidazolium chloride (BMIMCl) ionic liquid is demonstrated for the reaction of 1-methylimidazole (MIm) with 1-chlorobutane with no solvents. BMIMCl is produced with high selectivity and specific output in a microchannel flow reactor at temperatures of 120–180°C a contact time of 2–45 min, and a pressure of 20 bar. A positive result is obtained, due to the laminar profile of the flow and a uniform distribution of the reagents concentration over the microchannel cross section. Studying the kinetics of the process in a microchannel flow reactor reveals a shift of the reaction to the mode of diffusive inhibition at temperatures above 150°C. The kinetic data obtained for BMIMCl synthesis are used to develop ways of producing 1-ethyl-3-methylimidazolium and 1-hexyl-3-methylimidazolium chlorides (EMIMCl and HMIMCl, respectively) under the conditions of a microchannel flow reactor. The approach proposed in this work is of interest in developing flow and periodic facilities for the low-tonnage production of dialkylimidazolium, ammonium, and pyridinium salts via quaternization of the corresponding alkyl chlorides and nitrogen-containing bases.

KW - 1-alkyl-3-methylimidazolium chloride

KW - BMIMCl

KW - ionic liquid

KW - microchannel flow reactor

KW - quaternization reaction

KW - DESIGN

KW - MICROREACTOR

KW - FLOW

KW - SOLVENT

KW - PHASE

KW - TEMPERATURE

KW - KINETICS

KW - CHEMISTRY

KW - IONIC LIQUIDS

UR - http://www.scopus.com/inward/record.url?scp=85091645802&partnerID=8YFLogxK

U2 - 10.1134/S2070050420030071

DO - 10.1134/S2070050420030071

M3 - Article

AN - SCOPUS:85091645802

VL - 12

SP - 207

EP - 215

JO - Catalysis in Industry

JF - Catalysis in Industry

SN - 2070-0504

IS - 3

ER -

ID: 25677099