scholarly journals Review of catalyst materials and catalytic steam reforming reactions in SOFC anodes

2011 ◽  
Vol 35 (15) ◽  
pp. 1340-1350 ◽  
Author(s):  
Martin Andersson ◽  
Hedvig Paradis ◽  
Jinliang Yuan ◽  
Bengt Sundén
Keyword(s):  
Steam Reforming ◽  
Catalytic Steam Reforming ◽  
Reforming Reactions

ChemInform Abstract: Review of Catalyst Materials and Catalytic Steam Reforming Reactions in SOFC Anodes

ChemInform ◽  
2012 ◽  
Vol 43 (42) ◽  
pp. no-no
Author(s):  
Martin Andersson ◽  
Hedvig Paradis ◽  
Jinliang Yuan ◽  
Bengt Sunden
Keyword(s):  
Steam Reforming ◽  
Catalytic Steam Reforming ◽  
Reforming Reactions

Pyrolysis-catalytic upgrading of bio-oil and pyrolysis-catalytic steam reforming of biogas: a review

2021 ◽  
Author(s):  
Mira Abou Rjeily ◽  
Cédric Gennequin ◽  
Hervé Pron ◽  
Edmond Abi-Aad ◽  
Jaona Harifidy Randrianalisoa
Keyword(s):  
Steam Reforming ◽  
Catalytic Upgrading ◽  
Bio Oil ◽  
Catalytic Steam Reforming

Silica Sol-Gel Supported Nickel Nano-Catalyst for Hydrogen Production Using Microreactors

2005 ◽  
Vol 885 ◽  
Author(s):  
Krithi Shetty ◽  
Shihuai Zhao ◽  
Wei Cao ◽  
Naidu V. Seetala ◽  
Debasish Kuila
Keyword(s):  
Steam Reforming ◽  
Average Pore Size ◽  
Sol Gel ◽  
Supported Catalyst ◽  
Silica Sol ◽  
Average Pore ◽  
Steam Reforming Of Methanol ◽  
Nano Catalyst ◽  
Before And After ◽  
Reforming Reactions

ABSTRACTThe goal of this research is to investigate the activities of a non-noble nano-catalyst (Ni/SiO2) using Si-microreactors for steam reforming of methanol to produce hydrogen for fuel cells. The supported catalyst was synthesized by sol-gel method using Ni (II) salts and Si(C2H5O)4 as starting materials. EDX results indicate that the actual loading of Ni (5-6%) is lower than the intended loading of 12 %. The specific surface area of the silica sol-gel encapsulated Ni nano-catalyst is 452 m2/g with an average pore size of ∼ 3 nm. Steam reforming reactions have been carried out in a microreactor with 50 µm channels in the temperature range of 180-240 °C and atmospheric pressure. Results show 53% conversion of methanol with a selectivity of 74 % to hydrogen at 5 l/min and 200 °C. The magnetic properties of the catalysts were performed using a Vibrating Sample Magnetometer (VSM) to study the activity of the catalysts before and after the steam reforming reactions. The VSM results indicate much higher activity in the microreactor compared to macro-reactor and Ni forms non-ferromagnetic species faster in the microreactor.

Catalytic steam reforming of the aqueous fraction of bio-oil using Ni-Ce/Mg-Al catalysts

2017 ◽  
Vol 209 ◽  
pp. 346-357 ◽  
Author(s):  
F. Bimbela ◽  
J. Ábrego ◽  
R. Puerta ◽  
L. García ◽  
J. Arauzo
Keyword(s):  
Steam Reforming ◽  
Aqueous Fraction ◽  
Bio Oil ◽  
Catalytic Steam Reforming

Catalytic Steam Reforming of Fast Pyrolysis Bio-Oil in Fixed Bed and Fluidized Bed Reactors

2010 ◽  
Vol 33 (12) ◽  
pp. 2021-2028 ◽  
Author(s):  
P. Lan ◽  
Q. Xu ◽  
M. Zhou ◽  
L. Lan ◽  
S. Zhang ◽  
...  
Keyword(s):  
Fluidized Bed ◽  
Steam Reforming ◽  
Fast Pyrolysis ◽  
Fixed Bed ◽  
Fluidized Bed Reactors ◽  
Bio Oil ◽  
Catalytic Steam Reforming

Catalytic steam reforming of simulated bio-oil for green hydrogen production using highly active LaNixCo1-xO3 perovskite catalyst

2022 ◽  
Author(s):  
Piyush Pratap Singh ◽  
Neelkanth Nirmalkar ◽  
Tarak Mondal
Keyword(s):  
Hydrogen Production ◽  
Waste Management ◽  
Steam Reforming ◽  
Energy Production ◽  
Sustainable Energy ◽  
Agricultural Waste ◽  
Perovskite Catalyst ◽  
Highly Active ◽  
Bio Oil ◽  
Catalytic Steam Reforming

Catalytic steam reforming (SR) of agricultural waste derived bio-oil for hydrogen production is a unique technology, offering twin benefits of waste management as well as sustainable energy production. In the...

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