Mathematical models for the transient behavior of a packed bed Reactor, The Canadian Journal of Chemical Engineering, vol.8, issue.2, pp.205-211, 1970. ,
DOI : 10.1002/cjce.5450480220
Trickle-bed reactors: state of art and perspectives, Chemical Engineering Science, vol.47, issue.13-14, pp.13-14, 1992. ,
DOI : 10.1016/0009-2509(92)85029-B
Trickle-bed reactors: A review, AIChE Journal, vol.29, issue.1, pp.1-18, 1983. ,
DOI : 10.1002/aic.690290102
Solid-Liquid Mass Transfer in Concurrent Two-Phase Flow through Packed Beds, Industrial & Engineering Chemistry Process Design and Development, vol.17, issue.3, pp.362-367, 1978. ,
DOI : 10.1021/i260067a027
Sélectivité en réacteur catalytique triphasique : analyse expérimentale et théorique d'hydrogénations consécutives en lit fixe catalytique à co-courant ascendant de gaz et de liquide, 1995. ,
Modelling of three phase catalytic upflow reactor: A significant chemical determination of liquid-solid and gas-liquid mass transfer coefficients, Chemical Engineering Science, vol.51, issue.10, pp.51-2161, 1996. ,
DOI : 10.1016/0009-2509(96)00073-5
Prediction of pressure drop for two-phase, two-component concurrent flow in packed beds, AIChE Journal, vol.13, issue.6, pp.1196-1202, 1967. ,
DOI : 10.1002/aic.690130630
Dynamic operation of a three-phase upflow reactor for the hydrogenation of phenylacetylene, Catalysis Today, vol.20, issue.3, pp.485-500, 1994. ,
DOI : 10.1016/0920-5861(94)80140-1
Dynamic modelling of catalytic three phase reactors, Computers & Chemical Engineering, vol.20, issue.1, pp.39-47, 1996. ,
DOI : 10.1016/0098-1354(95)00005-M
Modeling and design of industrial reactors with a stationary bed of catalyst and two-phase gas-liquid flow -a review, Int. Chem. Eng, vol.30, issue.1, pp.57-102, 1990. ,