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Biomass pyrolysis: Kinetic modelling and experimental validation under high temperature and flash heating rate conditions

机译:生物质热解:高温和闪速加热条件下的动力学建模和实验验证

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This work analyzes and discusses the general features of biomass pyrolysis, both on the basis of a new set of experiments and by using a detailed kinetic model of biomass devolatilization that includes also successive gas phase reactions of the released species and is therefore able to predict the main gases composition. Experiments are performed in a lab-scale Entrained Flow Reactor (EFR) to investigate iomass pyrolysis under high temperatures (1073-1273 K) and high heating fluxes (10-100 kW m~(-2)). The influence of particle dimensions and temperature has been tested versus solid residence time in the reactor. The particle size appeared as the most crucial parameter. The pyrolysis of 0.4 mm particles is nearly finished under this range of temperatures after a reactor length of 0.3 m, with more than 75 wt% of gas release, whereas the conversion is still under evolution until the end of the reactor for larger particles up to 1.1 mm, due to internal heat transfer limitations. The preliminary comparisons between the model and the experimental data are encouraging and show the ability of this model to contribute to a better design and understanding of biomass pyrolysis process under severe conditions of temperature and heating fluxes typically found in industrial gasifiers.
机译:这项工作分析和讨论了生物质热解的一般特征,既基于一组新的实验,又使用了生物质挥发的详细动力学模型,该模型还包括释放物种的连续气相反应,因此能够预测主要气体成分。在实验室规模的夹带流反应器(EFR)中进行实验,以研究高温(1073-1273 K)和高热通量(10-100 kW m〜(-2))下的热解。相对于固体在反应器中的停留时间,已经测试了颗粒尺寸和温度的影响。粒度似乎是最关键的参数。在反应器长度为0.3 m之后,在此温度范围内,几乎会完成0.4 mm颗粒的热解,释放出超过75 wt%的气体,而转化仍在进行中,直到反应器结束为止直至更大的颗粒由于内部传热限制,为1.1 mm。该模型与实验数据之间的初步比较令人鼓舞,并表明该模型有助于更好地设计和理解在工业化炉中常见的严苛温度和热通量条件下生物质热解过程的能力。

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