Author/Authors :
G. Chen a، نويسنده , , b، نويسنده , , *، نويسنده , , J. Andries، نويسنده , , H. Spliethoff، نويسنده , , M. Fang c، نويسنده , , P.J. van de Enden b، نويسنده ,
Abstract :
The use of biomass for energy generation is getting increasing attention. At present, gasification of biomass is taken
as a popular technical route to produce fuel gas for application in boilers, engine, gas turbine or fuel cell. Up to now,
most of researchers have focused their attentions only on fixed-bed gasification and fluidised bed gasification under airblown
conditions. In that case, the producer gas is contaminated by high tar contents and particles which could lead to
the corrosion and wear of blades of turbine. Furthermore, both the technologies, particularly fixed bed gasification, are
not flexible for using multiple biomass-fuel types and also not feasible economically and environmentally for large scale
application up to 10–50 MWth. An innovative circulating fluidised bed concept has been considered in our laboratory
for biomass gasification thereby overcoming these challenges. The concept combines and integrates partial oxidation,
fast pyrolysis (with an instantaneous drying), gasification, and tar cracking, as well as a shift reaction, with the purpose
of producing a high quality of gas, in terms of low tar level and particulates carried out in the producer gas, and overall
emissions reduction associated with the combustion of producer gas. This paper describes our innovative concept and
presents some experimental results. The results indicate that the gas yield can be above 1.83 Nm3/kg and the fluctuation
of the gas yield during the period of operation is 3.3% at temperature of 750 C. Generally speaking, the results
achieved support our concept as a promising alternative to gasify biomass for the generation of electricity.
2003 Elsevier Ltd. All rights reserved.