КФУ. Карточка публикации. Numerical investigation of the ethylbenzene dehydrogenation reaction in a fixed bed reactor with catalyst granules of various sizes

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NUMERICAL INVESTIGATION OF THE ETHYLBENZENE DEHYDROGENATION REACTION IN A FIXED BED REACTOR WITH CATALYST GRANULES OF VARIOUS SIZES

Форма представления

Статьи в зарубежных журналах и сборниках

Год публикации

2019

Авторы, сотрудники КФУ

Гилмурахманов Булат Шайхуллович, автор

Ламберов Александр Адольфович, автор

Другие авторы

С.А. Соловьев, О.В. Соловьева

Авторы, аспиранты КФУ

Гилмурахманов Булат Шайхуллович, автор

Библиографическое описание на языке оригинала

In this work, we get a numerical simulation analyzes the effect of catalyst granule size on the operation efficiency of the fixed bed reactor for the dehydrogenation of ethylbenzene to styrene. For the laboratory reactor, we built a detailed model of cylindrical catalyst granules with a length of 3 mm, 6 mm and 9 mm. We carried out an analysis of the granule size effect on the bed characteristics, such as porosity and the catalyst total surface area. We obtained results for a wide range of feed gas rates. The ranges and rates of the catalyst efficiency decrease for different feed gas rates are determined.

Ключевые слова

numerical simulation analyzes, dehydrogenation, ethylbenzene, catalyst

Название журнала

Journal of Physics: Conference Series

Издательство

IOP Publishing

URL

doi:10.1088/1742-6596/1399/5/055022

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https://repository.kpfu.ru/?p_id=234251

Полная запись метаданных

Поле DC	Значение	Язык
dc.contributor.author	Гилмурахманов Булат Шайхуллович	ru_RU
dc.contributor.author	Ламберов Александр Адольфович	ru_RU
dc.contributor.author	Гилмурахманов Булат Шайхуллович	ru_RU
dc.date.accessioned	2019-01-01T00:00:00Z	ru_RU
dc.date.available	2019-01-01T00:00:00Z	ru_RU
dc.date.issued	2019	ru_RU
dc.identifier.citation	In this work, we get a numerical simulation analyzes the effect of catalyst granule size on the operation efficiency of the fixed bed reactor for the dehydrogenation of ethylbenzene to styrene. For the laboratory reactor, we built a detailed model of cylindrical catalyst granules with a length of 3 mm, 6 mm and 9 mm. We carried out an analysis of the granule size effect on the bed characteristics, such as porosity and the catalyst total surface area. We obtained results for a wide range of feed gas rates. The ranges and rates of the catalyst efficiency decrease for different feed gas rates are determined.	ru_RU
dc.identifier.uri	https://repository.kpfu.ru/?p_id=234251	ru_RU
dc.description.abstract	Journal of Physics: Conference Series	ru_RU
dc.language.iso	ru	ru_RU
dc.publisher	IOP Publishing	ru_RU
dc.subject	numerical simulation analyzes	ru_RU
dc.subject	dehydrogenation	ru_RU
dc.subject	ethylbenzene	ru_RU
dc.subject	catalyst	ru_RU
dc.title	Numerical investigation of the ethylbenzene dehydrogenation reaction in a fixed bed reactor with catalyst granules of various sizes	ru_RU
dc.type	Статьи в зарубежных журналах и сборниках	ru_RU