Modeling the hydrotreating reactions of a heavy residual oil in a pilot trickle-bed reactor

1985 ◽  
Vol 24 (3) ◽  
pp. 531-537 ◽  
Author(s):  
Antonio Iannibello ◽  
Sergio Marengo ◽  
Gerlando Burgio ◽  
Giancarlo Baldi ◽  
Silvio Sicardi ◽  
...  
1975 ◽  
Vol 40 (10) ◽  
pp. 3145-3152 ◽  
Author(s):  
J. Prchlík ◽  
J. Soukup ◽  
V. Zapletal ◽  
V. Růžička ◽  
P. Kovařík

1998 ◽  
Vol 63 (11) ◽  
pp. 1938-1944 ◽  
Author(s):  
Vratislav Tukač ◽  
Jiří Vokál ◽  
Jiří Hanika

Catalytic activity of CuO-supported catalyst in phenol oxidation, and the influence of reaction conditions, viz. temperature (125-170 °C), oxygen partial pressure (1-7 MPa) and liquid feed (30-760 ml h-1), in the continuous operation using 17.9 mm i.d. trickle-bed reactor is presented. The hydrodynamic impact on the three-phase trickle-bed reactor performance in an environmental application of catalytic wet oxidation was also investigated. The results of trickle-bed operation were strongly influenced by wetting efficiency. An insufficient catalyst wetting can be to compensated by filling the catalyst bed voids by fine glass spheres. In the case of the gas transfer limited reaction, a better wetting of the catalyst can lead to worse reactor performance due to lower reaction rates.


2021 ◽  
Vol 51 ◽  
pp. 101611
Author(s):  
Mads Borgbjerg Jensen ◽  
Súsanna Poulsen ◽  
Bjarke Jensen ◽  
Anders Feilberg ◽  
Michael Vedel Wegener Kofoed

1991 ◽  
Vol 14 (6) ◽  
pp. 406-413 ◽  
Author(s):  
Wino J. A. Wammes ◽  
K. Roel Westerterp

1995 ◽  
Vol 24 (1-2) ◽  
pp. 29-34 ◽  
Author(s):  
N. Déchamp ◽  
A. Gamez ◽  
A. Perrard ◽  
P. Gallezot

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