Abstract
Mathematical modeling of catalytic steam reforming of methane in a reformer—an apparatus combining a heat exchanger and a reactor—is performed. On the basis of experimental data obtained on an operating reformer, the model is corrected and recommendations for redesigning the reformer are made.
Similar content being viewed by others
REFERENCES
Appl, M., Ammonia, Methanol, Hydrogen, Carbon Monoxide: Modern Production Technologies, London: CRU, 1997.
Sosna, M., Bondar, I., Gunko, B., and Grotz, B.J., History of Development of the TANDEM Reforming Process, Ammonia Safety Symp., Orlando, 1993.
Spravochnik azotchika(Nitrogen Industry Engineer’s Handbook), Moscow: Khimiya, 1986, p. 176.
Kalinin, E.K., Dreitser, G.A., and Yarkho, S.A., Intensi-fikatsiya teploobmena v kanalakh(Enhancement of Heat Transfer in Channels), Moscow: Mashinostroenie, 1972.
Sosna, M.Kh., Yagnyatinskii, B.V., Sokolinskii, Yu.A., et al., Channel Model of a Granular Bed, Teor. Osn. Khim. Tekhnol., 1989, vol. 23, no. 6, p. 785.
Aerov, M.E. and Todes, O.M., Gidravlicheskie i teplovye osnovy raboty apparatov so statsionarnym i kipyashchim zernistym sloem(Hydraulic and Thermal Principles of Operation of Apparatuses with Fixed and Fluidized Granular Bed), Leningrad: Khimiya, 1968.
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Sosna, M.K., Pogorelov, V.N., Buchek, V.I. et al. Modeling of a Methane Reformer Combined with a Recuperative Heat Exchanger. Theoretical Foundations of Chemical Engineering 38, 425–429 (2004). https://doi.org/10.1023/B:TFCE.0000036972.17117.45
Issue Date:
DOI: https://doi.org/10.1023/B:TFCE.0000036972.17117.45