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首页> 外文期刊>Fuel Processing Technology >Technical demonstration of the novel Fraunhofer ISE biomass gasification process for the production of a tar-free synthesis gas
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Technical demonstration of the novel Fraunhofer ISE biomass gasification process for the production of a tar-free synthesis gas

机译:新型Fraunhofer ISE生物质气化工艺生产无焦油合成气的技术演示

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A novel fixed-bed biomass gasification process (Fraunhofer ISE gasification process) for the production of tar-free synthesis gas was developed and demonstrated in a small-scale 50 kW_(LHV(biomass)) pilot plant The process consists of four zones/Separated by moving grates to control the residence time in every zone. Thermal cracking of all higher hydrocarbons and tars occurs due to temperatures in the cracking zone of up to 1000 °C, ensured via partial combustion of the raw gas. In addition, coke in the cracking zones acts catalytically. In order to increase the heating value of the product gas all remaining carbon is partially oxidized and the produced CO/CO2 is blended with the product gas. To demonstrate feasibility of the process, a pilot plant was designed, commissioned and tested. The gasifier produced a combustible gas with a lower heating value of 5.8 MJ/Nm~3 and CO, H2 and CH4 concentrations of 24,14 and 2 vol.%, respectively, far contents below 50 mg/Nm~3 were achieved in continuous operation. The results suggested a considerable effect of the temperature and the bed height in the tar cracking zone on the reduction of the tar content in the produced gas.
机译:开发了一种用于生产不含焦油的合成气的新型固定床生物质气化工艺(Fraunhofer ISE气化工艺),并在小型50 kW_(LHV(生物质))中试装置中进行了示范。该工艺包括四个区域/分离通过移动炉排来控制每个区域的停留时间。所有高级碳氢化合物和焦油的热裂化均是由于裂化区的温度高达1000°C所致,这是通过原料气的部分燃烧来确保的。另外,裂化区中的焦炭起催化作用。为了增加产物气的热值,所有剩余的碳被部分氧化,并且将产生的CO / CO 2与产物气混合。为了证明该方法的可行性,设计,调试和测试了中试工厂。气化炉产生的可燃气体的热值较低,为5.8 MJ / Nm〜3,CO,H2和CH4的浓度分别为24.14和2 vol。%,连续达到远低于50 mg / Nm〜3的含量操作。结果表明焦油裂化区中的温度和床高度对降低产出气中焦油含量具有显着影响。

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