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Gasification of char from wood pellets and from wood chips: Textural properties and thermochemical conversion along a continuous fixed bed

机译:木质颗粒和木片中的焦炭的气化:沿连续固定床的质地特性和热化学转化

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摘要

In fixed bed gasifiers, the char bed gasification zone where char is converted into syngas plays a major role in terms of efficiency and control of the process. This zone is particularly complex as many phenomena compete, i.e. heterogeneous and homogeneous chemical reactions, gas flow in porous medium and flow of solid particles. This paper investigates the mechanical and thermochemical behavior of the char bed gasification zone and focuses particularly on bed compaction. To achieve this, a low-density biomass char from wood chips and a high-density one from wood pellets were gasified in a pilot scale continuous fixed bed reactor. Measurements of profiles were taken along the char bed for temperature, gas species concentration, char composition, char bed density and char particle velocity using fine instrumentation and specific char and gas sampling techniques. In our operating conditions, the char bed reactive zone is 3 times longer for chips (45 cm) than for pellets (16 cm). We show that pelletization has no effect on: char bed compaction, final char conversion (about 95%) and syngas quality (16% H2 and 13% CO). Finally, we discuss char bed compaction and the main phenomena that control it in order to propose a line of inquiry for modeling. (Résumé d'auteur)
机译:在固定床气化炉中,将炭转化为合成气的炭床气化区在工艺效率和控制方面起着重要作用。由于许多现象竞争,即异质和均相化学反应,多孔介质中的气体流动以及固体颗粒的流动,因此该区域特别复杂。本文研究了炭床气化区的机械和热化学行为,并特别着重于床的压实。为此,在中试规模的连续固定床反应器中将木屑的低密度生物质炭和木屑的高密度生物质气化。使用精细仪器和特定的炭和气体采样技术,沿着炭床测量温度,气体种类浓度,炭组成,炭床密度和炭颗粒速度的剖面图。在我们的运行条件下,切屑(45厘米)的炭化床反应区是颗粒(16厘米)的3倍。我们表明制粒对以下因素没有影响:炭床压实,最终炭转化率(约95%)和合成气质量(16%H2和13%CO)。最后,我们讨论了炭床压实及其控制的主要现象,从而提出了一条建模问题。 (Résuméd'auteur)

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