Optimization of the process for obtaining ethyl acetate by dehydrogenation of ethanol by achieving the stage of selective hydrogenation of acetaldehyde and feedstock replacing
https://doi.org/10.18412/1816-0387-2026-1-79-85
Abstract
The paper presents the results of real implementation of the acetaldehyde hydrogenation stage into the industrial process for ethyl acetate production by ethanol dehydrogenation. It has been shown for the first time with the selection of optimal conditions in parallel with acetaldehyde hydrogenation it is possible to obtain an increase in ethyl acetate, which is confirmed by the data from the pilot plant data and kinetic modeling data. The studies were carried out on a pilot plant with a production rate of 200 l/h, analytical control was carried out by the chromatographic method. The results obtained show that, in comparison with similar works, it is possible to simultaneously achieve acetaldehyde hydrogenation and an increase in ethyl acetate. The implementation of the selective hydrogenation stage of by-products will facilitate the isolation of commercial-quality ethyl acetate from the reaction mass, as well as increase the product yield due to the return of ethanol formed at the selective hydrogenation stage back into the reactor. Also, this paper provides practical recommendations on the operating modes of the catalyst.
About the Authors
I. P. SemenovRussian Federation
V. Yu. Chikalin
Russian Federation
S. E. Kievskaya
Russian Federation
O. I. Sycheva
Russian Federation
References
1. Чащин А.М., Глухарева М.И. Производство ацетатных растворителей в лесохимической промышленности. М.: Лесная промышленность, 1984. 240 с.
2. Šulgan B., Labovský J., Labovská Z. // Processes. 2020. V. 8. P. 1 – 32 https://doi.org/10.3390/pr8121618
3. Iwasa N., Takezawa N. // Bull. Chem. Soc. Jpn. 1991. V. 64. P. 2619 – 2623 https://doi.org/10.1246/bcsj.64.2619
4. Tu Y.-J., Li C., Chen Y.-W. // J. Chem. Tech. Biotechnol. 1994. V. 59. P. 141 – 147 https://doi.org/10.1002/jctb.280590205
5. Chung M.-J., Moon D.-J., Kim H.S. et al. // Journal of molecular catalysis. 1996. V. 113. P. 507 – 515 https://doi.org/10.1016/S1381-1169(96)00276-2
6. Sánchez B., Homs N., Fierro J. // Catalysis Today. 2005. V. 107. P. 431 – 435 http://dx.doi.org/10.1016/j.cattod.2005.07.057
7. Carotenuro G., Tesser R., Di Serio M. et al. // Catalysis today. 2013. V. 203. P. 202 – 210 https://doi.org/10.1016/j.cattod.2012.02.054
8. Andrade R., Hori C., Sato A. et al. // Biomass conf. bioref. 2016. V. 1. P. 1 – 9 https://doi.org/10.1007/s13399-016-0213-y
9. Sakun P., Chaowat A., Piyasan P. et al // Journal of Environmental Chemical Engineering. 2022. V. 10. P. 1-44 https://doi.org/10.1016/j.jece.2022.107542
10. Ruitao W., Kang S., Yifei C. et al // Surface Science. 2021. V. 703. P. 1-14 https://doi.org/10.1016/j.susc.2020.121742
11. Varad V., Praveen B. // Applied Catalysis A: General. 2025. V. 697. P. 1-26 https://doi.org/10.1016/j.apcata.2025.120228
12. Патент US 6809217B1, опубл. 26.10.2004
13. Меньщиков В.А., Семенов И.П. // Катализ в химической и нефтехимической промышленности. 2012. № 5. С 32 - 36
14. Семенов И.П. Разработка процесса дегидрирования этанола в этилацетат: дис. канд. техн. наук: 05.17.04 «Технология органических веществ». – М.: РТУ МИРЭА, 2013
15. Семенов И.П., Писаренко Ю.А., Меньщиков В.А. // Тонкие химические технологии. 2012. №7(5). С 52 - 56.
16. Цыганков П.С. Ректификационные установки спиртовой промышленности. М.: Лёгкая и пищевая пром-сть, 1984. 336 с.
17. Халаим А. Ф. Технология спирта. М.: Пищевая промышленность, 1972. 192 с
18. Патент RU 2650890 С1, опубл. 18.04.2018
Review
For citations:
Semenov I.P., Chikalin V.Yu., Kievskaya S.E., Sycheva O.I. Optimization of the process for obtaining ethyl acetate by dehydrogenation of ethanol by achieving the stage of selective hydrogenation of acetaldehyde and feedstock replacing. Kataliz v promyshlennosti. 2026;26(1):79-85. (In Russ.) https://doi.org/10.18412/1816-0387-2026-1-79-85
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