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Experimental Investigation of Tar Reduction Properties by Coupling Oxidative Pyrolysis and Partial Oxidation in a Continuous Reactor for Biomass Gasification

机译:用氧化热解和偏氧化在生物质气化中连续反应器中氧化热解和部分氧化的实验研究

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摘要

To develop a deep understanding of multistage biomass gasification technology, the effect of oxygen concentration in the pyrolysis stage on the overall performance of the gasification process was investigated. The results showed that oxygen in the pyrolysis stage promoted the yields of permanent gases and reduced the yield of tar. The GC–MS analysis of pyrolyzed tar compounds indicated that oxidative pyrolysis promoted the conversion of the reactive primary tar compounds to more stable secondary tar compounds. The FTIR analysis of pinewood char showed that oxidative pyrolysis reduced the content of oxygen-containing functional groups and improved the aromatization of char. The partial oxidation results showed that the CO and CO2 yields both increased with the increase of oxygen concentration in the first stage. The tar yield after the partial oxidation stage was reduced from 0.0809 (0% O2 in the first stage) to 0.0064 kg kg_(pinewood)~(-1) (15%O2 in the first stage).
机译:为了深入了解多级生物量气化技术,研究了氧浓度在热解阶段对气化过程整体性能的影响。 结果表明,热解阶段的氧促进了永久性气体产量并降低了焦油的产率。 热解焦油化合物的GC-MS分析表明,氧化热解促进了反应性原色焦油化合物转化为更稳定的仲焦油化合物。 Pinewood Char的FTIR分析表明,氧化热解减少了含氧官能团的含量并改善了炭的芳香化。 部分氧化结果表明,在第一阶段中的氧浓度的增加增加,CO和CO 2产生。 部分氧化阶段在部分氧化阶段的焦油产率从0.0809(第一阶段0%O 2)降低至0.0064kg kg_(松木)〜(-1)(第一阶段中的15%O 2)。

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