RETRACTED: Multiphase CFD simulations of catalytic wet oxidation of phenol-like compounds in high-pressure trickle-bed reactors: Reactive flow and temperature behaviour

2012 ◽  
Vol 90 (10) ◽  
pp. 1610-1624 ◽  
Author(s):  
Rodrigo J.G. Lopes ◽  
M.L.N. Perdigoto ◽  
Teresa S.A. Almeida ◽  
Rosa M. Quinta-Ferreira ◽  
F. Larachi
2004 ◽  
Vol 103 (1-3) ◽  
pp. 51-57 ◽  
Author(s):  
A. Singh ◽  
K.K. Pant ◽  
K.D.P. Nigam

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.


2012 ◽  
Vol 180 (1) ◽  
pp. 25-33 ◽  
Author(s):  
J.J. Delgado ◽  
X. Chen ◽  
J.A. Pérez-Omil ◽  
J.M. Rodríguez-Izquierdo ◽  
M.A. Cauqui

1995 ◽  
Vol 50 (15) ◽  
pp. 2377-2389 ◽  
Author(s):  
Muthanna H. Al-Dahhan ◽  
Milorad P. Duduković

2007 ◽  
Vol 46 (25) ◽  
pp. 8380-8387 ◽  
Author(s):  
Rodrigo J. G. Lopes ◽  
Adrián M. T. Silva ◽  
Rosa M. Quinta-Ferreira

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