Pilot plant studies on fixed bed reactor system for biomethanation of distillery spent wash

1992 ◽  
Vol 41 (1-2) ◽  
pp. 87-107 ◽  
Author(s):  
T. Nandy ◽  
S. N. Kaul ◽  
P. P. Pathe ◽  
C. V. Deshpande ◽  
R. A. Daryapurkar
Keyword(s):  
Pilot Plant ◽  
Fixed Bed ◽  
Reactor System ◽  
Fixed Bed Reactor ◽  
Spent Wash ◽  
Distillery Spent Wash

Experimental Study on Biomass Char Combustion in O2/CO2 Atmosphere

2014 ◽  
Vol 694 ◽  
pp. 136-141 ◽  
Author(s):  
Jing Hong Lian ◽  
Zi Fang Wang ◽  
Wei Ji ◽  
Guang Yang ◽  
Lian Sheng Liu ◽  
...  
Keyword(s):  
Experimental Study ◽  
Fixed Bed ◽  
Reactor System ◽  
Fixed Bed Reactor ◽  
No Emission ◽  
Char Combustion ◽  
Biomass Char

Experiments of biomass char combustion in 10%O2/90%CO2, 21%O2/79%CO2, 10%O2/90%N2 and 21%O2/79%N2 atmospheres were performed in the fixed-bed reactor system at the temperature of 800°C-1200°C. The results show that at the same temperature, NO emission is higher in O2/N2 atmosphere than that in O2/CO2 atmosphere. The higher the O2 concentration is, the higher the NO yield is. As the temperature rises, the NO yield rises at first and then decreases at the same O2 concentration and atmosphere.

Hydrogen production via catalytic pyrolysis of biomass in a two-stage fixed bed reactor system

2014 ◽  
Vol 39 (25) ◽  
pp. 13128-13135 ◽  
Author(s):  
Shaomin Liu ◽  
Jinglin Zhu ◽  
Mingqiang Chen ◽  
Wenping Xin ◽  
Zhonglian Yang ◽  
...  
Keyword(s):  
Hydrogen Production ◽  
Catalytic Pyrolysis ◽  
Fixed Bed ◽  
Reactor System ◽  
Fixed Bed Reactor ◽  
Two Stage ◽  
Pyrolysis Of Biomass

Studies on the Role of Nitrogen in the Feed for Fischer-Tropsch Synthesis Under Fixed-Bed Reactor System

2016 ◽  
Vol 16 (2) ◽  
pp. 1894-1897 ◽  
Author(s):  
Gi Hoon Hong ◽  
Jae-Sun Jung ◽  
Na-Young Kim ◽  
Sang Yong Lee ◽  
Dong Ju Moon
Keyword(s):  
Fixed Bed ◽  
Tropsch Synthesis ◽  
Reactor System ◽  
Fixed Bed Reactor ◽  
Fischer Tropsch ◽  
Fischer Tropsch Synthesis

Catalytic Wet Peroxide Oxidation Process for the Continuous Treatment of Polluted Effluents on a Pilot Plant Scale

2008 ◽  
Vol 11 (1) ◽  
Author(s):  
Fernando Martínez ◽  
M Isabel Pariente ◽  
Juan Antonio Melero ◽  
Juan Ángel Botas
Keyword(s):  
Pilot Plant ◽  
Fixed Bed ◽  
Pilot Scale ◽  
Fixed Bed Reactor ◽  
Continuous Treatment ◽  
Continuous Stirred Tank Reactor ◽  
Peroxide Oxidation ◽  
Wet Peroxide Oxidation ◽  
Pilot Plant Scale ◽  
Catalytic Wet Peroxide Oxidation

AbstractCatalytic Wet Peroxide Oxidation (CWPO) for the continuous treatment of a phenolic aqueous solution has been studied on a pilot scale process. The pilot plant has been designed by integration of a catalytic fixed bed reactor (FBR) with a continuous stirred tank reactor (CSTR). The CSTR is used as reservoir for the continuous delivering of a recirculation stream through the catalytic bed. The main part of phenol mineralization takes place by catalytic oxidation in the FBR. The mesoporous SBA-15 silica-supported iron oxide (Fe

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