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Thermodynamic modelling of fate and removal of alkali species and sour gases from biomass gasification for production of biofuels

机译:命运的热力学模型以及从生物质气化中去除碱物质和酸性气体以生产生物燃料的热力学模型

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The development of advanced synthesis gas cleaning technologies based on chemical conversion and physical separation can improve the efficiency of gasification processes for production of biofuels. This paper outlines thermodynamic equilibrium calculations on the release and removal of alkali species and sour gases during gasification of 24 different types of herbaceous and woody biomass under the conditions of the gasifier in Güssing, Austria. In general, the calculation results are in good agreement with former experimental results. The composition of the gasifier derived as well as the cleaned gas strongly depends on the used feedstock. The alkali concentration can be limited to values below 100 ppbv using aluminosilicates at 850 °C. The H_2S concentration cannot be limited to values below 200 ppmv using conventional Ca- or Cu-based sorbents but can be limited to values below 1 ppmv by stabilised BaO at 850 °C. The HC1 concentration can be limited to values below 1 ppmv by alkali carbonates at temperatures below 550 °C.
机译:基于化学转化和物理分离的先进合成气净化技术的开发可以提高用于生产生物燃料的气化过程的效率。本文概述了在奥地利居辛市气化炉条件下,在气化器条件下,对24种不同类型的草本和木质生物质进行气化过程中碱物质和酸性气体的释放和去除的热力学平衡计算。通常,计算结果与以前的实验结果吻合良好。衍生的气化炉以及净化后的气体的组成很大程度上取决于所用的原料。在850°C下使用铝硅酸盐可以将碱浓度限制在100 ppbv以下。使用常规的基于钙或铜的吸附剂不能将H_2S的浓度限制在200 ppmv以下,而可以通过在850°C下稳定的BaO将H_2S的浓度限制在1 ppmv以下。在低于550°C的温度下,碱金属碳酸盐可将HCl的浓度限制在1 ppmv以下。

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