Hydrogen-rich syngas production from biomass pyrolysis and catalytic reforming using biochar-based catalysts

Fuel ◽  
2022 ◽  
Vol 313 ◽  
pp. 123006
Author(s):  
Yanjie Wang ◽  
Liang Huang ◽  
Tianyu Zhang ◽  
Qiang Wang
Keyword(s):  
Biomass Pyrolysis ◽  
Catalytic Reforming ◽  
Syngas Production

Syngas production via chemical looping reforming biomass pyrolysis oil using NiO/dolomite as oxygen carrier, catalyst or sorbent

2019 ◽  
Vol 198 ◽  
pp. 111835 ◽  
Author(s):  
Tingting Xu ◽  
Bo Xiao ◽  
Gift Gladson Moyo ◽  
Fanghua Li ◽  
Zhihua Chen ◽  
...  
Keyword(s):  
Oxygen Carrier ◽  
Chemical Looping ◽  
Pyrolysis Oil ◽  
Biomass Pyrolysis ◽  
Syngas Production

Syngas production by non-catalytic reforming of biogas with steam addition under filtration combustion mode

2018 ◽  
Vol 43 (33) ◽  
pp. 15693-15702 ◽  
Author(s):  
Lorena Espinoza ◽  
Fabián Guerrero ◽  
Nicolás Ripoll ◽  
Mario Toledo ◽  
Lorna Guerrero ◽  
...  
Keyword(s):  
Filtration Combustion ◽  
Combustion Mode ◽  
Catalytic Reforming ◽  
Syngas Production

Kinetic study of the catalytic reforming of biomass pyrolysis volatiles over a commercial Ni/Al2O3 catalyst

2018 ◽  
Vol 43 (27) ◽  
pp. 12023-12033 ◽  
Author(s):  
Aitor Arregi ◽  
Gartzen Lopez ◽  
Maider Amutio ◽  
Itsaso Barbarias ◽  
Laura Santamaria ◽  
...  
Keyword(s):  
Kinetic Study ◽  
Biomass Pyrolysis ◽  
Catalytic Reforming ◽  
Al2o3 Catalyst

Syngas production from biomass pyrolysis in a continuous microwave assisted pyrolysis system

2020 ◽  
Vol 314 ◽  
pp. 123756 ◽  
Author(s):  
Nan Zhou ◽  
Junwen Zhou ◽  
Leilei Dai ◽  
Feiqiang Guo ◽  
Yunpu Wang ◽  
...  
Keyword(s):  
Biomass Pyrolysis ◽  
Syngas Production ◽  
Microwave Assisted

Study on the feasibility of using monolithic catalyst in the in-situ catalytic biomass pyrolysis for syngas production

2021 ◽  
Vol 120 ◽  
pp. 10-15
Author(s):  
Yuchen Zhou ◽  
Zezhi Chen ◽  
Huijuan Gong ◽  
Lu Chen ◽  
Huiqiang Yu
Keyword(s):  
Biomass Pyrolysis ◽  
Monolithic Catalyst ◽  
Syngas Production

Steam Reforming of Simulated Coke Oven Gas over Ni/Al2O3-MgO Catalysts for Syngas Production

2010 ◽  
Vol 152-153 ◽  
pp. 817-820 ◽  
Author(s):  
Hong Wei Cheng ◽  
Xiong Gang Lu ◽  
Wei Zhong Ding
Keyword(s):  
Calcination Temperature ◽  
Steam Reforming ◽  
Solution Structure ◽  
Coke Oven ◽  
Al2o3 Content ◽  
Coke Oven Gas ◽  
Reaction Conditions ◽  
Catalytic Reforming ◽  
Syngas Production ◽  
H2 Yield

The steam reforming of simulated coke oven gas (COG) with toluene as a model tar compound for syngas production was investigated over Ni/Al2O3-MgO catalysts. XRD results showed that the catalysts with high calcination temperature and Al2O3 content after calcination formed (Ni,Mg)Al2O4 spinel and Ni-Mg-O solid solution structure. At optimized reaction conditions, toluene and CH4 can be completely converted, while a H2 yield of 71.8% and a CO yield of 76.1% have been achieved at 800 oC. The catalysts with appropriate calcination temperature and Al2O3 content showed better catalytic activity and resistance to coking, which will be promising catalysts in the catalytic reforming of COG.

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