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Application of a microchannel reactor to intensify the process of obtaining solketal from glycerol and acetone

https://doi.org/10.18412/1816-0387-2026-3-66-77

Abstract

The possibility of using a microchannel (MC) reactor for the synthesis of solketal from glycerol and acetone is demonstrated. The reaction proceeds efficiently in the presence of mordenite as a catalyst, which was fed as a suspension in a glycerol-methanol solution (glycerol/methanol = 2:1 v/v) at an acetone/glycerol molar ratio of 1.5. The main factors (MC reactor length, reactant feed rate, and reaction temperature) influencing the reaction rate and solketal selectivity were determined. The maximum glycerol conversion (64.8%) and solketal selectivity (94.3%) were obtained at 40 °C, a residence time of 18.85 min in a 3 m long MC reactor with a channel inner diameter of 2 mm. The efficiency of using the MC reactor in comparison with a batch reactor is demonstrated. The specific productivity of solketal in the MK reactor was 14 times higher than that of the batch reactor. These results indicate that microchannel technology can be considered a promising option for intensifying reactions for producing glycerol ketals and acetals.

About the Authors

D. V. Andreev
Boreskov Institute of Catalysis SB RAS, Novosibirsk
Russian Federation


N. A. Kaverov
Boreskov Institute of Catalysis SB RAS, Novosibirsk
Russian Federation


I. A. Lukoyanov
Boreskov Institute of Catalysis SB RAS, Novosibirsk
Russian Federation


V. N. Panchenko
Boreskov Institute of Catalysis SB RAS, Novosibirsk
Russian Federation


M. N. Timofeeva
Boreskov Institute of Catalysis SB RAS, Novosibirsk
Russian Federation


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Review

For citations:


Andreev D.V., Kaverov N.A., Lukoyanov I.A., Panchenko V.N., Timofeeva M.N. Application of a microchannel reactor to intensify the process of obtaining solketal from glycerol and acetone. Kataliz v promyshlennosti. 2026;26(3):66-77. (In Russ.) https://doi.org/10.18412/1816-0387-2026-3-66-77

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ISSN 1816-0387 (Print)
ISSN 2413-6476 (Online)