Gasification of biomass with steam in a novel fluedised bed system
Usually gasification of biomass is carried out in fixed or fluidized bed reactors with air as gasification agent. In this case the product gas has a low calorific value (around 4-6MJ/m³) and a high nitrogen content.
Fig. 9: Scheme of a Gasification of biomass with steam in a novel fluedised bed system
Source: Energy from Biomass - R&D in Austria (Ministry of Science and Transport) |
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A novel fast internally circulating fluidized bed gasifier (FICFB) developed in a cooperation by the Vienna Technical University and Austrian Energy and Environment Inc. yields a high calorific gas with up to 15 MJ/m³ and very low nitrogen (<3%) and tar content (<0,8g/m³).
The gasification process is based on an internally circulating fluidised bed system and consists of a gasification zone fluidized with steam and a combustion zone fluidized with air. In the combustion zone char is burned and produces the heat necessary for gasification. The circulating bed material acts as a heat carrier from the combustion to the gasification zone. Gas mixing between these zones is avoided by construction measures so the flue gas from combustion is not mixed with the product gas. The resulting high quality of the product gas can be further enhanced with catalytic bed material. Olivine has proved highly efficient for this purpose.
After two years of successfully operating a 100 kWth laboratory unit a 4 MWth gasifier and a gas engine will be integrated into an existing district heating system and deliver heat and electric power. In an international pilot project catalysts will be used to achieve up to 55% hydrogen content in the product gas which could subsequently be used in a fuel cell for electricity production.
Contact: Technical University of Vienna, AE Energietechnik

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