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A CHEMICAL APPROACH TO BIOMASS GASIFICATION

机译:生物质气化的化学方法

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This paper describes GASDS, a comprehensive model of a biomass gasifier on a travelling grate. Thisgeneral mathematical model deals with the complex multiphase gas-solid problem of biomass gasification both at thereactor and the particle scale. Mass and energy balances plus proper closure equations describe the behavior of boththe phases. Key elements of the model are the detailed kinetic schemes describing the biomass volatilization,including the formation of TAR species and char, and the secondary gas phase as well as the heterogeneous reactions.The model has been already tested and validated on semi-quantitative basis in comparisons with a 12 MW biomasscombustor operating in Belgium. In this paper, the model is extended and compared to recent experimental dataobtained in a biomass regenerative gasifier. The comparison with experimental data highlights the role ofdevolatilization, mass transfer phenomena, and mainly the kinetics of char gasification in controlling system’sreactivity and syngas composition. An alternative configuration for biomass gasification is also presented anddiscussed. It is based on three different steps, including biomass pyrolysis through the convective heating of a syngasrecycle stream, followed by the oxidation of volatile products (gas and tar compounds) with an air/steam mixture anda final char gasification. The advantage of the proposed configuration lies in the direct oxidation of the released tarsto form the hot stream used for char gasification.
机译:本文介绍了GASDS,这是移动炉排上生物质气化炉的综合模型。这 通用数学模型处理生物质气化的复杂多相气固问题 反应器和粒子规模。质量和能量平衡以及适当的闭合方程描述了两者的行为 阶段。该模型的关键要素是描述生物质挥发的详细动力学方案, 包括TAR物种和焦炭的形成,次级气相以及非均相反应。 该模型已经过测试和验证,并与12兆瓦生物质进行了比较 在比利时运营的燃烧室。本文对该模型进行了扩展,并与最近的实验数据进行了比较 在生物质再生气化炉中获得。与实验数据的比较突出了 脱挥发分,传质现象,主要是控制系统中炭气化的动力学 反应性和合成气组成。还提出了生物质气化的替代配置,并且 讨论过。它基于三个不同的步骤,包括通过对流加热合成气进行生物质热解 循环流,然后用空气/蒸汽混合物氧化挥发性产物(气体和焦油化合物),并 最后的焦炭气化。所提出的构造的优点在于释放的焦油的直接氧化 形成用于焦炭气化的热流。

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