Thermally Coupled Catalytic Reactor for Steam Reforming of Methane and Liquid Hydrocarbons: Experiment and Mathematical Modeling Full article
Journal |
Theoretical Foundations of Chemical Engineering
ISSN: 0040-5795 , E-ISSN: 1608-3431 |
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Output data | Year: 2003, Volume: 37, Number: 3, Pages: 276-284 Pages count : 9 DOI: 10.1023/A:1024039823317 | ||||
Tags | Methane; Steam; Catalytic Reactor; Reaction Zone; Thermal Condition | ||||
Authors |
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Affiliations |
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Funding (1)
1 | International Science and Technology Center | 2291 |
Abstract:
An energy-efficient catalytic reactor for producing synthesis gas from methane and liquid hydrocarbons is proposed that is based on the coupling of an endothermic reaction (steam reforming of methane, hexane, or isooctane) and an exothermic reaction (hydrogen oxidation by atmospheric oxygen) in a single cocurrent apparatus. To describe the processes in such an apparatus, a two-dimensional two-temperature mathematical model is developed. It was revealed experimentally and by mathematical modeling that the heat- and mass-transfer coefficients of the gas flow in contact with the catalytically active wall in the exothermic reaction zone considerably affect the thermal conditions in the reactor.
Cite:
Kirillov V.A.
, Kuzin N.A.
, Kulikov A.V.
, Fadeev S.I.
, Shigarov A.B.
, Sobyanin V.A.
Thermally Coupled Catalytic Reactor for Steam Reforming of Methane and Liquid Hydrocarbons: Experiment and Mathematical Modeling
Theoretical Foundations of Chemical Engineering. 2003. V.37. N3. P.276-284. DOI: 10.1023/A:1024039823317 WOS Scopus РИНЦ ANCAN OpenAlex
Thermally Coupled Catalytic Reactor for Steam Reforming of Methane and Liquid Hydrocarbons: Experiment and Mathematical Modeling
Theoretical Foundations of Chemical Engineering. 2003. V.37. N3. P.276-284. DOI: 10.1023/A:1024039823317 WOS Scopus РИНЦ ANCAN OpenAlex
Original:
Кириллов В.А.
, Кузин Н.А.
, Куликов А.В.
, Фадеев С.И.
, Шигаров А.Б.
, Собянин В.А.
Сопряженный по тепловым потокам каталитический реактор паровой конверсии метана и жидких углеводородов. Эксперимент и математическое моделирование.
Теоретические основы химической технологии. 2003. Т.37. №3. С.300-308. Scopus РИНЦ
Сопряженный по тепловым потокам каталитический реактор паровой конверсии метана и жидких углеводородов. Эксперимент и математическое моделирование.
Теоретические основы химической технологии. 2003. Т.37. №3. С.300-308. Scopus РИНЦ
Dates:
Submitted: | Aug 30, 2002 |
Published print: | May 1, 2003 |
Identifiers:
Web of science: | WOS:000183780100011 |
Scopus: | 2-s2.0-0038542090 |
Elibrary: | 13440048 |
Chemical Abstracts: | 2003:432519 |
Chemical Abstracts (print): | 139:232720 |
OpenAlex: | W251007168 |