发明授权
EP2227312B1 VERFAHREN UND VORRICHTUNG ZUR WIEDERAUFBEREITUNG VON CO2-HALTIGEN ABGASEN 有权
方法和设备进行回收含CO2废气

  • 专利标题: VERFAHREN UND VORRICHTUNG ZUR WIEDERAUFBEREITUNG VON CO2-HALTIGEN ABGASEN
  • 专利标题(英): Method and device for reprocessing co2-containing exhaust gases
  • 专利标题(中): 方法和设备进行回收含CO2废气
  • 申请号: EP08864685.6
    申请日: 2008-12-18
  • 公开(公告)号: EP2227312B1
    公开(公告)日: 2012-07-25
  • 发明人: MÖLLER, Roland
  • 申请人: Ecoloop Gmbh
  • 申请人地址: Geheimrat-Ebert-Strasse 12 38640 Goslar DE
  • 专利权人: Ecoloop Gmbh
  • 当前专利权人: Ecoloop Gmbh
  • 当前专利权人地址: Geheimrat-Ebert-Strasse 12 38640 Goslar DE
  • 代理机构: Erb, Henning
  • 优先权: DE102007062413 20071220
  • 国际公布: WO2009080297 20090702
  • 主分类号: B01D53/62
  • IPC分类号: B01D53/62 C10B49/06 C10J3/14 C10J3/66
VERFAHREN UND VORRICHTUNG ZUR WIEDERAUFBEREITUNG VON CO2-HALTIGEN ABGASEN
摘要:
The invention relates to a method for reprocessing CO2-containing exhaust gases in a multistage reduction process. The CO2-containing exhaust gas is conducted in the counter stream to a solid mass stream of inert bulk material and organic material that can be thermally decomposed through a plurality of zones (4, 3, 2, 1) into a pressure equalization region and is thereby converted into pyrolysis gases. In the flow direction of the solid mass stream in a fuel gas production stage (1) at 250 - 700°C, the organic matter is thermally decomposed under reducing conditions into short-chained hydrocarbons, hydrogen and carbon monoxide to produce coke and residue. In an intermediate stage (2) with increasing temperature, oxidation of the pyrolysis coke is carried out, wherein the developing carbon monoxide is suctioned off counter to the solid mass stream in the direction of the fuel gas production stage (1). In a carbon monoxide production stage (3) at 800 - 1,600°C, the remaining coke residue is converted with carbon dioxide into carbon monoxide by setting the pressure and temperature according to the Boudouard equilibrium. In a cooling stage (4), the developing solid residual material and the bulk material are cooled in the CO2 counter stream to below 100°C and are separated, wherein the bulk material is returned to the cycle.
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