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Adding gas from biomass to the gas grid - SGC

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Aspect Unit ValueManure M 3 /day 6Bio<strong>gas</strong> production, 60% methane atM 3 /day 10017m 3 bio<strong>gas</strong>/m 3 <strong>biomass</strong>InvestmentsPlant investment incl. powerK€ 100 - 300generationPrice of <strong>gas</strong> C€/m 3bio<strong>gas</strong>n.a.Table 4: ‘Farm Plant’ characteristicsBio<strong>gas</strong> <strong>from</strong> farms is always used locally for heat and power production, no examples are knownwhere it has been upgraded and added <strong>to</strong> <strong>the</strong> <strong>gas</strong> <strong>grid</strong>.Sewage plantsNo consistent figures are available.LandfillNo consistent figures are available. The high content of nitrogen makes <strong>the</strong> <strong>gas</strong> unsuitable forupgrading and injection in<strong>to</strong> a high calorific natural <strong>gas</strong> <strong>grid</strong>.3.2 SYNGAS FROM BIOMASS PYROLYSIS AND GASIFICATION3.2.1 General aspects of <strong>the</strong>rmal <strong>biomass</strong> <strong>gas</strong>ificationGasification technology for syn<strong>gas</strong> production <strong>from</strong> <strong>biomass</strong>The technology for <strong>the</strong> <strong>the</strong>rmal <strong>gas</strong>ification of <strong>biomass</strong> is mainly derived <strong>from</strong> <strong>the</strong> <strong>gas</strong>ification ofcoal. There is a tremendous worldwide experience basis in <strong>the</strong> <strong>gas</strong>ification of coal. The coal<strong>gas</strong>ification is a mature technology able <strong>to</strong> fulfil any rational commercial requirements. Thisexperience started already in <strong>the</strong> 1850’s when <strong>the</strong> first coal <strong>gas</strong> pipelines came on stream. Currentcoal <strong>gas</strong>ification technology has three branches <strong>to</strong> be distinguished by <strong>the</strong>ir reac<strong>to</strong>r characteristics.These three branches are fixed bed, fluidised bed and entrained flow <strong>gas</strong>ifiers.In <strong>the</strong> fixed bed <strong>the</strong> <strong>biomass</strong> is embedded in a flow of <strong>the</strong> reactant. During <strong>the</strong> <strong>gas</strong>ification <strong>the</strong>remaining ashes are removed and new <strong>biomass</strong> is added. This causes some movement in <strong>the</strong><strong>biomass</strong>. In some <strong>gas</strong>ifiers rotating <strong>the</strong> <strong>gas</strong>ifier enhances this movement by some rotatingmovement in <strong>the</strong> reacting chamber. This movement is <strong>to</strong> remove <strong>the</strong> ashes and <strong>to</strong> enhance <strong>the</strong>interaction of <strong>the</strong> reactant <strong>gas</strong>es with <strong>the</strong> <strong>biomass</strong>.Essentially this reac<strong>to</strong>r shows plug flow and has an essentially high conversion efficiency.page: 20

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