Synthesis Gas Production with NiO−MgO/γ-Al2O3/Cordierite Monolithic Catalysts in a Pilot-Scale Biomass-Gasification-Reforming System
Author:
Affiliation:
1. Key Laboratory of Renewable Energy and Gas Hydrate, Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangzhou 510640, People’s Republic of China
Publisher
American Chemical Society (ACS)
Subject
Energy Engineering and Power Technology,Fuel Technology,General Chemical Engineering
Link
https://pubs.acs.org/doi/pdf/10.1021/ef1015268
Reference19 articles.
1. Investigation of Reforming Catalyst Deactivation by Exposure to Fly Ash from Biomass Gasification in Laboratory Scale
2. Two Advanced Models for the Kinetics of the Variation of the Tar Composition in Its Catalytic Elimination in Biomass Gasification
3. Commercial Steam Reforming Catalysts To Improve Biomass Gasification with Steam−Oxygen Mixtures. 2. Catalytic Tar Removal
4. Hot Gas Cleaning and Upgrading with a Calcined Dolomite Located Downstream a Biomass Fluidized Bed Gasifier Operating with Steam−Oxygen Mixtures
5. Hydrogen Production by Biomass Gasification with Steam−O2 Mixtures Followed by a Catalytic Steam Reformer and a CO-Shift System
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1. Effect of Calcination Time on the Catalytic Activity of Ni/γ-Al2O3 Cordierite Monolith for Dry Reforming of Biogas;International Journal of Hydrogen Energy;2021-02
2. Gas reforming and tar decomposition performance of nickel oxide (NiO)/SBA-15 catalyst in gasification of woody biomass;Journal of the Air & Waste Management Association;2019-02-11
3. Decomposition of methane over alumina supported Fe and Ni–Fe bimetallic catalyst: Effect of preparation procedure and calcination temperature;Journal of Saudi Chemical Society;2018-02
4. Reforming solutions for biomass-derived gasification gas – Experimental results and concept assessment;Fuel;2015-05
5. Thermochemical Conversion;Biomass as a Sustainable Energy Source for the Future;2014-10-03
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