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Effects of pyrolysis conditions on the heating rate in biomass particles and applicability of TGA kinetic parameters in particle thermal conversion modelling

机译:热解条件对生物质颗粒加热速率的影响及TGA动力学参数在颗粒热转化模型中的适用性

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摘要

A one-dimensional single particle model is utilised to investigate the effects of radiation temperature, moisture content, particle size and biomass physical properties on the heating rate in biomass particles during pyrolysis. The model divides the particle into four layers - drying, pyrolysis, char and ash layer -corresponding to the four main stages of biomass thermal conversion. The average of the time derivative of the pyrolysis layer centre temperature weighted by the pyrolysis rate is introduced as an appropriate indicator for the heating rate in the particle during pyrolysis. The influencing parameters on the heating rate are summarised in the Biot number and the thermal time constant, to make the investigation of their effects easier. The heating rate is inversely proportional to the thermal time constant. The effect of a variation of the Biot number on the heating rate is negligible in comparison to the thermal time constant. Therefore, the thermal time constant can be sufficiently used to specify the heating rate regimes during pyrolysis. It is found that for thermal time constants of more than 50 s, pyrolysis takes place in a low heating rate regime, i.e. less than 50 K/min. Additionally, the heating rate during pyrolysis of various biomass types under a wide range of thermal conversion conditions has been examined, in order to classify the heating rate regime of pyrolysis in state-of-the-are combustion/gasification plants. The pyrolysis of wood dust and wood pellets is found to happen always in high heating rate regimes. Therefore, the kinetic parameters obtained by conventional TGA systems (typically with heating rates lower than 50 K/min) are not applicable for them. On the contrary, the pyrolysis of wood logs always happens in low heating rate regimes, which indicates that kinetic parameters obtained by conventional TCA systems can be applied. However, pyrolysis of wood chips can undergo low or high heating rate regimes depending on their particle size. Concerning the moisture content, it can be stated that it does not strongly influence the heating rate regime of certain biomass particles.
机译:利用一维单粒子模型研究热解过程中辐射温度,水分含量,粒度和生物质物理性质对生物质颗粒加热速率的影响。该模型将颗粒分为四层-干燥,热解,炭和灰层-对应于生物质热转化的四个主要阶段。引入由热解速率加权的热解层中心温度的时间导数的平均值作为热解期间颗粒中加热速率的合适指标。影响加热速率的参数总结在比奥数和热时间常数中,以便更轻松地研究其影响。加热速率与热时间常数成反比。与热时间常数相比,Biot数变化对加热速率的影响可以忽略不计。因此,热时间常数可充分用于指定热解过程中的加热速率范围。已经发现,对于大于50s的热时间常数,热解在低加热速率状态下进行,即小于50K / min。另外,已经检查了在广泛的热转化条件下各种生物质类型在热解过程中的加热速率,以便对现有燃烧/气化装置中热解的加热速率进行分类。发现木屑和木屑的热解总是在高加热速率下发生。因此,通过常规TGA系统获得的动力学参数(通常加热速率低于50 K / min)不适用于它们。相反,原木的热解总是在低加热速率下发生,这表明可以应用常规TCA系统获得的动力学参数。但是,木片的热解取决于颗粒的大小,可能会经历低速或高速加热。关于水分含量,可以说它不会强烈影响某些生物质颗粒的加热速率范围。

著录项

  • 来源
    《Fuel》 |2012年第2012期|p.567-575|共9页
  • 作者单位

    BIOENERGY 2020+ GmbH, Inffeldgasse 21b, 8010 Graz, Austria,Institute for Process and Particle Engineering, Graz University of Technology, Inffeldgasse 21b, 8010 Graz, Austria;

    BIOENERGY 2020+ GmbH, Inffeldgasse 21b, 8010 Graz, Austria,Institute for Process and Particle Engineering, Graz University of Technology, Inffeldgasse 21b, 8010 Graz, Austria,BIOS BIOENERGIESYSTEME GmbH, Inffeldgasse 21b, 8010 Graz, Austria;

    BIOENERGY 2020+ GmbH, Inffeldgasse 21b, 8010 Graz, Austria,Institute for Process and Particle Engineering, Graz University of Technology, Inffeldgasse 21b, 8010 Graz, Austria,BIOS BIOENERGIESYSTEME GmbH, Inffeldgasse 21b, 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

    biomass; pyrolysis; TGA; heating rate;

    机译:生物质热解TGA;加热速率;

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