Catalytic removal of phenol from aqueous solutions in a trickle-bed reactor

2005 ◽  
Vol 80 (4) ◽  
pp. 406-412 ◽  
Author(s):  
G Ovejero ◽  
JL Sotelo ◽  
J García ◽  
A Rodríguez
Keyword(s):  
Aqueous Solutions ◽  
Trickle Bed Reactor ◽  
Trickle Bed ◽  
Catalytic Removal

Exploring the reaction conditions for Ru/C catalyzed selective hydrogenolysis of xylitol alkaline aqueous solutions to glycols in a trickle-bed reactor

2014 ◽  
Vol 234 ◽  
pp. 100-106 ◽  
Author(s):  
Florian Auneau ◽  
Maeva Berchu ◽  
Guillaume Aubert ◽  
Catherine Pinel ◽  
Michèle Besson ◽  
...  
Keyword(s):  
Aqueous Solutions ◽  
Reaction Conditions ◽  
Trickle Bed Reactor ◽  
Selective Hydrogenolysis ◽  
Trickle Bed

Glucose Hydrogenation in a Trickle-Bed Reactor

1997 ◽  
Vol 62 (9) ◽  
pp. 1423-1428 ◽  
Author(s):  
Vratislav Tukač
Keyword(s):  
Activation Energy ◽  
High Pressure ◽  
Aqueous Solutions ◽  
Catalytic Hydrogenation ◽  
Glucose Concentration ◽  
Pressure Range ◽  
Scaling Up ◽  
Supported Nickel Catalyst ◽  
Trickle Bed Reactor ◽  
Trickle Bed

Catalytic hydrogenation of 40% aqueous solutions of D-glucose to D-glucitol was studied in a high-pressure trickle-bed reactor. The reactions were performed on a supported nickel catalyst at temperatures ranging from 115 to 165 °C and in the pressure range 0.5 to 10 MPa. The order of the reaction with respect to hydrogen is 0.65 and apparent activation energy 23.8-48.5 kJ mol-1, the latter depending on initial molar glucose concentration and density and viscosity of the solution. The influence of external diffusion is necessary to take into account for scaling-up the process.

Wall flow in trickle bed reactor

1975 ◽  
Vol 40 (10) ◽  
pp. 3145-3152 ◽  
Author(s):  
J. Prchlík ◽  
J. Soukup ◽  
V. Zapletal ◽  
V. Růžička ◽  
P. Kovařík
Keyword(s):  
Trickle Bed Reactor ◽  
Wall Flow ◽  
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.

scholarly journals Selecting carrier material for efficient biomethanation of industrial biogas-CO2 in a trickle-bed reactor

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

scholarly journals Hydrodynamics in a pressurized cocurrent gas-liquid trickle-bed reactor

1991 ◽  
Vol 14 (6) ◽  
pp. 406-413 ◽  
Author(s):  
Wino J. A. Wammes ◽  
K. Roel Westerterp
Keyword(s):  
Trickle Bed Reactor ◽  
Trickle Bed
Sign in / Sign up

Export Citation Format

Share Document