Реферат: Presented is a study of hydrogen-rich generation by selective catalytic oxidation of gasoline in a nearly adiabatic monolith reactor. Experiments were conducted using a gasoline mixture containing 191 hydrocarbon species, while corresponding thermodynamic models employed a surrogate mixture of 29 organics with well-defined properties. Based on the data obtained, it was demonstrated that a nearly equilibrium synthesis could be produced using catalytic monoliths. Also discussed are problems encountered with a short contact time reactor operating at a pilot-scale, issues that are largely independent of the catalysts employed. It was found that this particular reactor design is prone to pre-reformation of the fuel prior to catalytic reaction. In addition, the breakthrough of the feed mixture was found to arise near the reactor wall under certain circumstances. Feed composition, superficial velocity, and various reactor design factors were all found to affect these phenomena.

Библиографическая ссылка: Bobrova L. , Zolotarsky I. , Sadykov V. , Sobyanin V.
Hydrogen-Rich Production from Gasoline in a Short Contact Time Catalytic Reactor
International Journal of Hydrogen Energy. 2007. V.32. N16. P.3698-3704. DOI: 10.1016/j.ijhydene.2006.08.051 WOS Scopus РИНЦ CAPlusCA OpenAlex

Даты:

Опубликована online:	10 окт. 2006 г.
Опубликована в печати:	1 нояб. 2007 г.

Идентификаторы БД:

Web of science:	WOS:000251463200012
Scopus:	2-s2.0-35648998503
РИНЦ:	13559474
Chemical Abstracts:	2007:1262106
Chemical Abstracts (print):	149:559551
OpenAlex:	W2006411895

Цитирование в БД:

БД	Цитирований
Web of science	23
Scopus	25
РИНЦ	24
OpenAlex	22

Альметрики: