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Catalytic Dehydration of Ethanol into Ethylene in a Tubular Reactor of the Pilot Installation on Alumina Catalysts with Varied Grain Size Full article

Journal Russian Journal of Applied Chemistry
ISSN: 1070-4272 , E-ISSN: 1608-3296
Output data Year: 2017, Volume: 90, Number: 2, Pages: 169-178 Pages count : 10 DOI: 10.1134/S1070427217020021
Tags SIMULATION; SCALE
Authors Banzaraktsaeva S.P. 1 , Ovchinnikova E.V. 1 , Isupova L.A. 1 , Chumachenko V.A. 1
Affiliations
1 Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, pr. Akademika Lavrentʼeva, 5 Novosibirsk, 630090 Russia

Funding (1)

1 Federal Agency for Scientific Organizations 0303-2016-0017

Abstract: Synthesis of ethylene on trefoil and cylindrical experimental acid-modified aluminum oxide samples was studied under an ethanol (94%) gas load of 920–2200 h–1 and heat-carrier temperature of 400–440°C. In the conditions of a 98% ethanol conversion, the higher activity of the trefoil made it possible to reduce the height of the bed and its hydraulic resistance and, accordingly, raise the specific catalyst throughput for ethylene. Compared with industrial aluminum oxide, the throughput of 1 g of the catalyst for ethylene on experimental samples is higher by 2.5–6.5 kg yr–1, and the specific expenditure of ethanol is lower by 0.22–0.23 kg kg–1. The endothermic process in a tubular reactor is characterized by a high parametric sensitivity of the average integral temperature along the catalyst bed, with the average temperature being higher on the less active catalyst. Thus, the higher average temperature can compensate for the lower activity of the catalyst without additional increase in the contact duration and(or) heat-carrier temperature.
Cite: Banzaraktsaeva S.P. , Ovchinnikova E.V. , Isupova L.A. , Chumachenko V.A.
Catalytic Dehydration of Ethanol into Ethylene in a Tubular Reactor of the Pilot Installation on Alumina Catalysts with Varied Grain Size
Russian Journal of Applied Chemistry. 2017. V.90. N2. P.169-178. DOI: 10.1134/S1070427217020021 WOS Scopus РИНЦ OpenAlex AN
Original: Банзаракцаева С.П. , Овчинникова Е.В. , Исупова Л.А. , Чумаченко В.А.
Процесс каталитической дегидратации этанола в этилен в трубчатом реакторе пилотной установки на алюмооксидных катализаторах разного зернения
Журнал прикладной химии. 2017. Т.90. №2. С.146-155. РИНЦ
Dates:
Submitted: Nov 23, 2016
Published print: Feb 1, 2017
Published online: Jun 2, 2017
Identifiers:
≡ Web of science: WOS:000402833400002
≡ Scopus: 2-s2.0-85019997205
≡ Elibrary: 31027843
≡ OpenAlex: W2621399828
≡ Chemical Abstracts: 2017:914326
Citing:
≡ Web of science 10 Сбор данных от 20.02.2026
≡ Scopus 13 Сбор данных от 15.02.2026
≡ Elibrary 15 Сбор данных от 15.02.2026
≡ OpenAlex 15 Сбор данных от 15.02.2026
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