Mathematical Modeling of Continuous Production of Carbon Nanofibers from Methane in a Reactor with a Moving Bed of a Nickel-Containing Catalyst Full article
| Journal |
Theoretical Foundations of Chemical Engineering
ISSN: 0040-5795 , E-ISSN: 1608-3431 |
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| Output data | Year: 2006, Volume: 40, Number: 5, Pages: 519-525 Pages count : 7 DOI: 10.1134/S0040579506050095 | ||||
| Tags | Nickel Catalyst; Methane Conversion; Continuous Production; Catalyst Deactivation; Reactor Outlet | ||||
| Authors |
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| Affiliations |
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Funding (4)
| 1 | Russian Foundation for Basic Research | 04-03-32618 |
| 2 | The Ministry of Education and Science of the Russian Federation | 60059 |
| 3 | The Ministry of Education and Science of the Russian Federation | 203.06.03.001 |
| 4 | Президиум РАН | 4.8.1 |
Abstract:
The continuous production of carbon nanofibers from methane on a Ni/Al2O3 catalyst (90 wt % Ni) in a plug-flow reactor with countercurrent or cocurrent flows of the phases is considered. The methane conversion, specific carbon content, and relative catalyst activity in the reactor are calculated as functions of the longitudinal coordinate, temperature, and specific gas and catalyst flow rates. It is shown that, at a fixed specific methane flow rate, there is an optimal specific catalyst flow rate at which the specific yield of carbon nanofibers is maximal, with this yield in the cocurrent reactor being higher than that the countercurrent reactor. At certain parameter values, the reactor may contain a region with a virtually deactivated catalyst, which is indicative of inefficiency of use of the reactor space.
Cite:
Zavarukhin S.G.
, Kuvshinov G.G.
Mathematical Modeling of Continuous Production of Carbon Nanofibers from Methane in a Reactor with a Moving Bed of a Nickel-Containing Catalyst
Theoretical Foundations of Chemical Engineering. 2006. V.40. N5. P.519-525. DOI: 10.1134/S0040579506050095 WOS Scopus РИНЦ ANCAN OpenAlex
Mathematical Modeling of Continuous Production of Carbon Nanofibers from Methane in a Reactor with a Moving Bed of a Nickel-Containing Catalyst
Theoretical Foundations of Chemical Engineering. 2006. V.40. N5. P.519-525. DOI: 10.1134/S0040579506050095 WOS Scopus РИНЦ ANCAN OpenAlex
Original:
Заварухин С.Г.
, Кувшинов Г.Г.
Математическое моделирование непрерывных процессов получения нановолокнистого углерода из метана в реакторе с движущимся слоем никельсодержащего катализатора
Теоретические основы химической технологии. 2006. Т.40. №5. С.556-562. RSCI РИНЦ
Математическое моделирование непрерывных процессов получения нановолокнистого углерода из метана в реакторе с движущимся слоем никельсодержащего катализатора
Теоретические основы химической технологии. 2006. Т.40. №5. С.556-562. RSCI РИНЦ
Dates:
| Submitted: | Aug 10, 2005 |
| Published print: | Sep 1, 2006 |
Identifiers:
| Web of science: | WOS:000241546300009 |
| Scopus: | 2-s2.0-33749983380 |
| Elibrary: | 13522127 |
| Chemical Abstracts: | 2006:1068615 |
| Chemical Abstracts (print): | 147:36603 |
| OpenAlex: | W2009776112 |