Fe/Activated Carbon as a Catalyst in Wet Oxidation of Phenolic Compounds in a Trickle Bed Reactor

2013 ◽  
Vol 35 (4) ◽  
pp. 299-311 ◽  
Author(s):  
W. T. Mohamed ◽  
S. A. Ghani ◽  
S. M. Rasheed
Keyword(s):  
Activated Carbon ◽  
Phenolic Compounds ◽  
Wet Oxidation ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Mass Transfer Limited Wet Oxidation in Trickle-Bed Reactor

1998 ◽  
Vol 63 (11) ◽  
pp. 1938-1944 ◽  
Author(s):  
Vratislav Tukač ◽  
Jiří Vokál ◽  
Jiří Hanika
Keyword(s):  
Supported Catalyst ◽  
Reaction Rates ◽  
Gas Transfer ◽  
Wet Oxidation ◽  
Reactor Performance ◽  
Catalytic Wet Oxidation ◽  
Environmental Application ◽  
Trickle Bed Reactor ◽  
Fine Glass ◽  
Trickle Bed

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.

Catalytic wet oxidation of phenol in a trickle bed reactor

2004 ◽  
Vol 103 (1-3) ◽  
pp. 51-57 ◽  
Author(s):  
A. Singh ◽  
K.K. Pant ◽  
K.D.P. Nigam
Keyword(s):  
Wet Oxidation ◽  
Catalytic Wet Oxidation ◽  
Trickle Bed Reactor ◽  
Oxidation Of Phenol ◽  
Trickle Bed
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