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Modelling fuel flexibility in fixed-bed biomass conversion with a low primary air ratio in an updraft configuration

机译:燃料柔韧性在上升装置中具有低初级空气比的固定床生物质转化率

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摘要

Fixed-bed biomass conversion with a low primary air ratio and a counter-current configuration has a high feedstock flexibility, as it resembles updraft gasification, and the potential to reduce emissions when integrated in biomass combustion systems. A 1D bed model was validated with experimental results from a biomass combustion boiler with such a bed conversion system, predicting with a good accuracy the temperatures in the reactor and producer gas composition. The model was applied for different cases to investigate the fuel flexibility of this combustion system, including the influence of moisture content and the maximum temperatures achieved in the bed. It was shown that with variations in fuel moisture content from 8 to 30% mass w.b. the producer gas composition, char reduction to CO or maximum temperatures at the grate were not affected due to the separation of the char conversion and pyrolysis/drying zones. Flue gas recirculation was the only possible measure with the tested configuration to reduce the maximum temperatures close to the grate, which is beneficial e.g. to avoid slagging with complicated fuels. A higher tar content was obtained than in conventional updraft gasifiers, which is attributed to the absence of tar condensation in the bed due to the limited height of the reactor and the integration in the combustion chamber. The presented model can support the development of such combustion technologies and is a relevant basis for detailed CFD simulations of the bed or gas phase conversion.
机译:具有低初级空气比和逆流配置的固定床生物质转化具有高原料柔韧性,因为它类似于上升气化,以及在生物质燃烧系统中集成时减少排放的可能性。通过具有这种床转换系统的生物质燃烧锅炉的实验结果验证了1D床模型,预测反应器和生产者气体组合物的温度良好。该模型用于探讨该燃烧系统的燃料灵活性的模型,包括水分含量的影响和床上所达到的最大温度。结果表明,燃料水分含量的变化从8-30%的质量为W.B。生产者气体组合物,炉排中的CO或最大温度的CHAR还原由于CHAR转化和热解/干燥区的分离而受到影响。烟气再循环是测试配置唯一可能的措施,以减少靠近炉排的最大温度,这是有益的。避免用复杂的燃料粘合。获得了较高的焦油含量,其常规上升气体含量归因于床中没有沥青缩小,由于反应器的有限高度和燃烧室中的集成。该模型可以支持这种燃烧技术的发展,是床或气相转换的详细CFD模拟的相关基础。

著录项

  • 来源
    《Fuel》 |2021年第15期|120687.1-120687.9|共9页
  • 作者单位

    Graz Univ Technol Inst Thermal Engn Inffeldgasse 25b A-8010 Graz Austria;

    Graz Univ Technol Inst Thermal Engn Inffeldgasse 25b A-8010 Graz Austria;

    Hargassner GesmbH Anton Hargassner Str 1 A-4952 Weng Austria;

    Bioenergy & Sustainable Technol GmbH BEST Inffeldgasse 21b A-8010 Graz Austria;

    Graz Univ Technol Inst Thermal Engn Inffeldgasse 25b A-8010 Graz Austria|Bioenergy & Sustainable Technol GmbH BEST Inffeldgasse 21b A-8010 Graz Austria;

    Graz Univ Technol Inst Thermal Engn Inffeldgasse 25b A-8010 Graz Austria|Bioenergy & Sustainable Technol GmbH BEST Inffeldgasse 21b A-8010 Graz Austria;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Fixed-bed; Model; Updraft; Counter-current; Biomass gasification; Biomass combustion;

    机译:固定床;模型;上升机;反电流;生物质气化;生物量燃烧;

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