Experiment and modeling of low-concentration methane catalytic combustion in a fluidized bed reactor

2016 ◽  
Vol 93 ◽  
pp. 660-667 ◽  
Author(s):  
Zhongqing Yang ◽  
Peng Yang ◽  
Li Zhang ◽  
Mingnv Guo ◽  
Jingyu Ran
Keyword(s):  
Fluidized Bed ◽  
Catalytic Combustion ◽  
Fluidized Bed Reactor ◽  
Low Concentration ◽  
Methane Catalytic Combustion

Nonpremixed Catalytic Combustion of Methane in a Fluidized Bed Reactor

2006 ◽  
Vol 45 (3) ◽  
pp. 1009-1013 ◽  
Author(s):  
Mario Iamarino ◽  
Paola Ammendola ◽  
Riccardo Chirone ◽  
Raffaele Pirone ◽  
Giovanna Ruoppolo ◽  
...  
Keyword(s):  
Fluidized Bed ◽  
Catalytic Combustion ◽  
Fluidized Bed Reactor ◽  
Catalytic Combustion Of Methane

Anaerobic treatment of low concentration waste water in an inverse fluidized bed reactor

2000 ◽  
Vol 41 (4-5) ◽  
pp. 245-251 ◽  
Author(s):  
P. Castilla ◽  
M. Meraz ◽  
O. Monroy ◽  
A. Noyola
Keyword(s):  
Fluidized Bed ◽  
Removal Efficiency ◽  
Suspended Solids ◽  
Municipal Wastewater ◽  
Specific Activity ◽  
Biomass Concentration ◽  
Fluidized Bed Reactor ◽  
Anaerobic Treatment ◽  
Low Concentration ◽  
Inverse Fluidized Bed

Low concentration synthetic and municipal wastewaters were treated at HRT as short as 3 and 0.6 h respectively in an anaerobic inverse fluidized bed. Both bioreactors showed gas hold up due to the liquid downflow pattern of the prototype. The bioreactor operated at 3 h had a removal efficiency of 83%, specific activity of 4.5 kg CODremoved/kg IVS (d and the gas hold up varied from 23 to 55%. The reactor treating municipal wastewater had a removal efficiency of 44% when operating at 0.6 h, the specific activity was 4.2 kg CODremoved/kg IVS (d and no biogas was detected apparently because an important fraction was dissolved in the liquid phase. The biomass concentration was 13.8 and 1.1 kg IVS/m3 for synthetic and municipal wastewater and the SEM microphotographs showed a bacterial diversity for the first run and only cocci cells for the second run. The system does not remove suspended solids, so a polishing postreatment to improve water quality has to be implemented.

The effect of low-concentration oxygen in sweep gas during pyrolysis of red oak using a fluidized bed reactor

Fuel ◽  
2014 ◽  
Vol 124 ◽  
pp. 49-56 ◽  
Author(s):  
Kwang Ho Kim ◽  
Xianglan Bai ◽  
Marjorie Rover ◽  
Robert C. Brown
Keyword(s):  
Fluidized Bed ◽  
Fluidized Bed Reactor ◽  
Red Oak ◽  
Low Concentration

Catalytic combustion of methane in a fluidized bed reactor under fuel-lean conditions

2002 ◽  
Vol 174 (11-12) ◽  
pp. 361-375 ◽  
Author(s):  
M. Iamarino ◽  
R. Chirone ◽  
R. Pirone ◽  
G. Russo ◽  
P. Salatino
Keyword(s):  
Fluidized Bed ◽  
Catalytic Combustion ◽  
Fluidized Bed Reactor ◽  
Catalytic Combustion Of Methane ◽  
Lean Conditions

Catalytic combustion of methane and propane in a fluidized-bed reactor

2002 ◽  
Vol 29 (1) ◽  
pp. 827-834 ◽  
Author(s):  
M. Iamarino ◽  
P. Salatino ◽  
R. Chirone ◽  
R. Pirone ◽  
G. Russo
Keyword(s):  
Fluidized Bed ◽  
Catalytic Combustion ◽  
Fluidized Bed Reactor ◽  
Catalytic Combustion Of Methane
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