Abstract
Kinetics of methane conversion in a fluidized bed of microspherically grained nickel-alumina catalyst has been studied at pressures from 0.3 to 3.1 MPa. The rate equation shows that the reaction is inhibited by H2O.
Abstract
Иаучена кинетика конверсии метана с водяным паром в кипящем слое микросферического алюмоникелевого катализатора при давлении от 0,3 до 3,1 МПа. Предложено уравнение скорости реакции, по которому конверсия тормозится водяным паром.
Article PDF
Similar content being viewed by others
Avoid common mistakes on your manuscript.
References
A. R. Brun-Tsekhovoi, A. N. Zadorin, S. S. Kurdyumov, Ya. R. Katsobashvili: Proc. 7th World Hydrogen Energy Conference. 1988, vol. 2, p. 885.
Brun-Tsekhovoi, Ya. R. Katsobashvili, S. S. Kurdyumov, N. V. Sidorova: Khim. Tekhnol. Topliv i Masel,2, 11 (1976).
A. A. Vvedenskii: Thermodynamic Calculations of Fuel Industry Processes, Gostoptekhizdat, Moskva 1969.
M. I. Temkin, F. S. Schub, A. A. Khomenko, L. O. Apelbaum: in Scientific Fundamentals for Catalytic Conversion of Hydrocarbons. Naukova Dumka, Kiev 1977.
V. A. Sobyanin, I. I. Bobrova, E. Yu. Titova, O. V. Bazhan, V. D. Belyaev, N. N. Bobrov: React. Kinet. Catal. Lett.,39, 443 (1989).
V. I. Atroshchenko, G. L. Zvyagintsev: Khim. Prom.,1, 36 (1970).
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Brun-Tsekhovoi, A.R., Kurdyumov, S.S. & Rozental, A.L. Kinetics of methane conversion over microspherically grained nickel-alumina catalysts. React Kinet Catal Lett 47, 37–42 (1992). https://doi.org/10.1007/BF02063557
Received:
Accepted:
Issue Date:
DOI: https://doi.org/10.1007/BF02063557