Abstract
The unsteady-state solution is obtained by an operator theory in functional analysis setting for a general finite catalytic packed-bed tubular reactor model with axial dispersion in the bed, mass transfer between the catalyst particles and the flowing phase, and intraparticle diffusion and surface reaction in the catalyst particles.
Article PDF
Similar content being viewed by others
Avoid common mistakes on your manuscript.
References
Kubin, M.:Collect. Czech. Chem. Commun. 30, 1104(1965).
Kubin, M.:Collect. Czech. Chem. Commun. 30, 2900 (1965).
Kucera, E.:J. of Chrmatogmphy 19, 237 (1965).
Schneider, P. and Smith, J.M.:AIChE J.,14, 762 (1968).
Schneider, P. and Smith, J.M.:AIChE J.,14, 886 (1968).
Gruber, O.:Adv. Chromatogr.,6, 173 (1968).
Furusawa, T., Suzuki, M. and Smith, J.M:Catal. Rev. 13, 43 (1976).
Anderssen, A.S. and White, E.T.:Chem. Eng. Sci.,25, 1015 (1970).
Wakao, N. and Kaguei, S.: “Heat and Mass Transfer in Packed Beds”, Gordon and Breach, New York, N.Y. (1982).
Hays, J.R., Clements Jr., W.C. and Harris, T.R.:AIChE J. 13, 374 (1967).
Gangwal, S.K., Hudgins, R.R., Bryson, A.W. and Silveston, P.L.:Can. J. Chem. Eng.,49, 113 (1971).
Haynes, Jr., H.W.:Chem. Eng. Sci.,30, 55 (1975).
Wakao, N., Tanisho, S.:Chem. Eng. Sci.,29, 1991 (1974).
Wakao, N., Tanaka, K., and Nagai, H.:Chem. Eng. Sci,31, 1109(1976).
Rasmuson, A., and Neretnieks, I:AlChE J.,26, 686 (1980).
Rasmuson, A.:AIChE J.,27, 1032 (1981).
Kim, D.H., Ma, G.Y., and Chang, K.S.:Chem. Eng. Commun. 28, 283 (1984).
Ramkrishna, D., and Amundson, N.R.:Chem. Eng. Sci.,29, 1353 (1974).
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Kim, D.H., Ma, G.Y. & Chang, K.S. The unsteady-state solution for a finite dispersion-type catalytic packed-bed tubular reactor. Korean J. Chem. Eng. 2, 125–132 (1985). https://doi.org/10.1007/BF02697498
Received:
Accepted:
Issue Date:
DOI: https://doi.org/10.1007/BF02697498