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Diesel Fuel Pre-Reforming into Methane-Hydrogen Mixtures Full article

Journal Theoretical Foundations of Chemical Engineering
ISSN: 0040-5795 , E-ISSN: 1608-3431
Output data Year: 2015, Volume: 49, Number: 1, Pages: 30-40 Pages count : 11 DOI: 10.1134/S0040579515010030
Tags adiabatic reactor, catalyst, diesel fuel, kinetics, methane-hydrogen mixture, pre-reforming
Authors Kirillov V.A. 1,2,3 , Shigarov A.B. 1,2,3 , Amosov Yu.I. 1,2,3 , Belyaev V.D. 1,2,3 , Urusov A.R. 4
Affiliations
1 Boreskov Institute of Catalysis, Siberian Branch, Russian Academy of Sciences, pr. Lavrent’eva 5, Novosibirsk, 630090 Russia
2 OOO UNIKAT, pr. Lavrent’eva 5, Novosibirsk, 630090 Russia
3 Novosibirsk State University, ul. Pirogova 2, Novosibirsk, 630090 Russia
4 Krylov State Research Centre, Moskovskoe sh. 44, St. Petersburg, 196158 Russia

Funding (2)

1 Russian Foundation for Basic Research 13-03-12404
2 The Ministry of Education and Science of the Russian Federation

Abstract: The pre-reforming of diesel fuel combined with subsequent steam reforming of pre-reforming products integrated with membrane separation of hydrogen is the most promising way of obtaining pure hydrogen for fuel cells. Here, we consider the first part of this problem-diesel fuel pre-reforming. The following commercial nickel-containing catalysts have been tested in the pre-reforming reaction: NIAP-18 (Ni, 15 wt %; CaO, 8 wt %; Al2O3, 74.4 wt %), NIAP-12-05 (Ni, 48 wt %; Cr2O3, 27 wt %), NIAP-07-01 (NiO, 36 wt %), NIAP-07-05 (NiO, 38 wt %; Cr2O3, 12 wt %). A number of new pre-reforming catalysts based on manganese and cobalt compounds have also been examined. The tests have been carried out at pressures of 1, 6, and 15 atm, temperatures of 470–560°C, and gas hourly space velocities of 6000–12000 h−1. The experiments have demonstrated that the nickel-containing catalysts afford a near-equilibrium product composition, while the reaction over the catalysts based on manganese and cobalt compounds yields a nonequilibrium product composition. A mathematical model has been developed for diesel fuel pre-reforming in an adiabatic reactor with a fixed catalytic bed. Model parameters ranging from process kinetics to heat and mass transfer coefficients have been estimated. The results of modeling have been compared to experimental data available from the literature. The potential of the mathematical model has been illustrated by performing calculations for adiabatic reactors with various output capacities.
Cite: Kirillov V.A. , Shigarov A.B. , Amosov Y.I. , Belyaev V.D. , Urusov A.R.
Diesel Fuel Pre-Reforming into Methane-Hydrogen Mixtures
Theoretical Foundations of Chemical Engineering. 2015. V.49. N1. P.30-40. DOI: 10.1134/S0040579515010030 WOS Scopus РИНЦ ANCAN OpenAlex
Original: Кириллов В.А. , Шигаров А.Б. , Амосов Ю.И. , Беляев В.Д. , Урусов А.Р.
Предриформинг дизельного топлива в метановодородные смеси
Теоретические основы химической технологии. 2015. Т.49. №1. С.32-43. DOI: 10.7868/S0040357115010030 РИНЦ OpenAlex
Dates:
Submitted: Aug 11, 2014
Published print: Jan 1, 2015
Published online: Feb 16, 2015
Identifiers:
Web of science: WOS:000349372400004
Scopus: 2-s2.0-84923037977
Elibrary: 24008630
Chemical Abstracts: 2015:280452
Chemical Abstracts (print): 164:24519
OpenAlex: W2006976510
Citing:
DB Citing
Web of science 10
Scopus 11
Elibrary 9
OpenAlex 10
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