发明公开
EP1095235A2 KOKSBEHEIZTER KREISLAUFGAS-KUPOLOFEN ZUR STOFFLICHEN UND/ODER ENERGETISCHEN VERWERTUNG VON ABFALLMATERIALIEN UNTERSCHIEDLICHER ZUSAMMENSETZUNG
审中-公开
KOKSBEHEIZTER循环气冲天炉为药物英俊/或能量回收废料成分不同
- 专利标题: KOKSBEHEIZTER KREISLAUFGAS-KUPOLOFEN ZUR STOFFLICHEN UND/ODER ENERGETISCHEN VERWERTUNG VON ABFALLMATERIALIEN UNTERSCHIEDLICHER ZUSAMMENSETZUNG
- 专利标题(英): Coke-heated circulating gas cupola furnace for material and/or energetic recycling of waste materials having different compositions
- 专利标题(中): KOKSBEHEIZTER循环气冲天炉为药物英俊/或能量回收废料成分不同
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申请号: EP99923514.6申请日: 1999-05-04
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公开(公告)号: EP1095235A2公开(公告)日: 2001-05-02
- 发明人: FEUSTEL, Hans, Ulrich , MALLON, Joachim , SCHAAF, Michael , Scheidig, Klaus
- 申请人: FEUSTEL, Hans, Ulrich , MALLON, Joachim , SCHAAF, Michael , Scheidig, Klaus
- 申请人地址: An der Märchenwiese 72 042777 Leipzig DE
- 专利权人: FEUSTEL, Hans, Ulrich,MALLON, Joachim,SCHAAF, Michael,Scheidig, Klaus
- 当前专利权人: FEUSTEL, Hans, Ulrich,MALLON, Joachim,SCHAAF, Michael,Scheidig, Klaus
- 当前专利权人地址: An der Märchenwiese 72 042777 Leipzig DE
- 国际公布: WO9960320 19991125
- 主分类号: F27B1/16
- IPC分类号: F27B1/16
摘要:
The invention relates to an additional embodiment for the arrangement of a lower annular suction and gas relaxation chamber (12) on a coke-heated circulating gas cupola furnace for material and/or energetic recycling of waste materials having different composition as described in main patent P 196 40 497, in which suctioning of gaseous organic matter which has been completely broken down into its basic components CO, H2, H2O and CO2 and into its trace components or has been already reformed is not yet reliably prevented. According to the invention, the lower annular suctioning and gas relaxation chamber (12) is arranged below the melting and overheating zone which extends up to the plane formed by the position of the jet gas compressor (24). Said arrangement makes it possible to draw off the excess gas directly from the furnace shaft from the melting and overheating zone at high temperatures of around 2,000 °C. The excess gas is also guided through the burning coke layer of the melting and overheating zone of the coke-heated circulating gas cupola furnace. CO2 is converted to CO by lowering the temperature of the gas as a result of energy-consuming Boudard equilibrium reaction. Fluidic separation of the excess gas from process gas is simultaneously carried out.
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