Continuous Operation of a 10 kWth Chemical Looping Integrated Fluidized Bed Reactor for Gasifying Biomass Using an Iron-Based Oxygen Carrier
Authors:
- 12 December 2014
- journal article
- research article
- Published by American Chemical Society (ACS) in Energy & Fuels
- Vol. 29 (1) , 233-241
Abstract
No abstract availableKeywords
Funding Information
- National Natural Science Foundation of China (51076154)
- Ministry of Science and Technology of the People's Republic of China (2011BAD15B05)
This publication has 41 references indexed in Scilit:
- Direct synthesis of dimethyl ether from biomass-derived syngas over Cu–ZnO–Al2O3–ZrO2(x)/γ-Al2O3 bifunctional catalysts: Effect of Zr-loadingFuel Processing Technology, 2014
- Hydrogen production from steam gasification of biomass: Influence of process parameters on hydrogen yield – A reviewRenewable Energy, 2014
- Catalytic performance and characterization of Co/Mg/Al catalysts prepared from hydrotalcite-like precursors for the steam gasification of biomassApplied Catalysis B: Environment and Energy, 2014
- Interaction and kinetic analysis for coal and biomass co-gasification by TG–FTIRBioresource Technology, 2014
- Steam gasification of biomass coupled with lime-based CO2 capture in a dual fluidized bed reactor: A modeling studyFuel, 2014
- Co-gasification of coal–biomass blended char with CO2 at temperatures of 900–1100 °CFuel, 2014
- A review of cleaning technologies for biomass-derived syngasBiomass and Bioenergy, 2013
- Gasification of biomass in a fixed bed downdraft gasifier – A realistic model including tarBioresource Technology, 2012
- Experimental investigation of chemical-looping hydrogen generation using Al 2 O 3 or TiO 2 -supported iron oxides in a batch fluidized bedInternational Journal of Hydrogen Energy, 2011
- Evaluation of a chemical-looping-combustion power-generation system by graphic exergy analysisEnergy, 1987