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A Model for Catalytic Synthesis of Carbon Nanotubes in a Fluidized-Bed Reactor: Effect of Reaction Heat Научная публикация

Конференция XXII International Conference on Chemical Reactors
19-23 сент. 2016 , London
Журнал Chemical Engineering Journal
ISSN: 1385-8947 , E-ISSN: 1873-3212
Вых. Данные Год: 2017, Том: 329, Страницы: 305-311 Страниц : 7 DOI: 10.1016/j.cej.2017.06.001
Ключевые слова Catalysis kinetics, Catalytic synthesis, Fluidized-bed reactor, Heat of reaction, Multi-walled carbon nanotubes (MWCNT)
Авторы Rabinovich Oscar 1 , Tsytsenka (Blinova) Alla 1 , Kuznetsov Vladimir 2,3 , Moseenkov Sergei 2 , Krasnikov Dmitry 2,3
Организации
1 A.V. Luikov Heat and Mass Transfer Institute, NAS of Belarus, Minsk, Belarus
2 Boreskov Institute of Catalysis SB RAS, Novosibirsk, Russia
3 Novosibirsk State University, Novosibirsk, Russia

Информация о финансировании (2)

1 Российский фонд фундаментальных исследований 16-53-00146
2 Белорусский республиканский фонд фундаментальных исследований Т16Р-088

Реферат: In the present study, we have developed a mathematic model describing quasi-continuous catalytic synthesis of multi-walled carbon nanotubes (MWCNTs) in a fluidized bed (FB) reactor. The special attention has been paid to the effects related to heat release or absorption during MWCNT synthesis. The heat of the reaction for MWCNT growth has been shown to significantly affect the thermal field in the reactor with the diameter as low as 6 cm. We attribute this to the extremely low thermal conductivity of aerogel-like MWCNT agglomerates (0.5-0.7 W/(m⋅K)), the basic units of the fluidized bed. According to the proposed model, the overheating up to 60 degrees takes place in the reactor with the diameter of D = 18 cm, the wall temperature of 943 K, and blown by 1:1 C2H4/Ar mixture. We have observed major changes caused by overheating: the activity of the catalyst and morphological properties of the produced MWCNTs (outer diameter, the structure of the walls, and fraction of impurities). The role of these thermal effects rises dramatically with increasing the reactor size and should be taken into account when designing reactors for large-scale production of MWCNTs.
Библиографическая ссылка: Rabinovich O. , Tsytsenka (Blinova) A. , Kuznetsov V. , Moseenkov S. , Krasnikov D.
A Model for Catalytic Synthesis of Carbon Nanotubes in a Fluidized-Bed Reactor: Effect of Reaction Heat
Chemical Engineering Journal. 2017. V.329. P.305-311. DOI: 10.1016/j.cej.2017.06.001 WOS Scopus РИНЦ CAPlus OpenAlex
Даты:
Опубликована online: 2 июн. 2017 г.
Опубликована в печати: 1 дек. 2017 г.
Идентификаторы БД:
Web of science: WOS:000410765700030
Scopus: 2-s2.0-85021108635
РИНЦ: 31022453
Chemical Abstracts: 2017:1057825
OpenAlex: W2620617563
Цитирование в БД:
БД Цитирований
Web of science 16
Scopus 19
РИНЦ 18
OpenAlex 17
Альметрики: