Collect. Czech. Chem. Commun.
1969, 34, 3852-3861
https://doi.org/10.1135/cccc19693852
Heat and mass transfer in heterogeneous catalysis. XI. Wall effect in a tubular catalytic reactor I
P. Kondelík and A. I. Boyarinov
Crossref Cited-by Linking
- Ziółkowska I, Ziółkowski D: Fluid flow inside packed beds. Chemical Engineering and Processing: Process Intensification 1988, 23, 137. <https://doi.org/10.1016/0255-2701(88)80012-6>
- Vortmeyer D., Michael K.: The effect of non-uniform flow distribution on concentration profiles and breakthrough curves of fixed bed adsorbers. Chemical Engineering Science 1985, 40, 2135. <https://doi.org/10.1016/0009-2509(85)87032-9>
- Kalthoff O., Vortmeyer D.: Ignition/extinction phenomena in a wall cooled fixed bed reactor. Chemical Engineering Science 1980, 35, 1637. <https://doi.org/10.1016/0009-2509(80)80056-X>
- Staněk Vladimír, Eckert Vít: A study of the area porosity profiles in a bed of equal-diameter spheres confined by a plane. Chemical Engineering Science 1979, 34, 933. <https://doi.org/10.1016/0009-2509(79)85004-6>
- Froment G. F.: Model discrimination and parameter estimation in heterogeneous catalysis. AIChE Journal 1975, 21, 1041. <https://doi.org/10.1002/aic.690210602>
