首页> 外文会议>International Symposium on Advances in Computational Heat Transfer >BIOMASS FAST PYROLYSIS PROCESS AT LABORATORY SCALE: RESIDENCE TIME AND HEATING UP EVALUATION IN A SHAFTLESS SCREW REACTOR BY MEANS OF A DISCRETE ELEMENT MODEL APPROACH
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BIOMASS FAST PYROLYSIS PROCESS AT LABORATORY SCALE: RESIDENCE TIME AND HEATING UP EVALUATION IN A SHAFTLESS SCREW REACTOR BY MEANS OF A DISCRETE ELEMENT MODEL APPROACH

机译:生物量在实验室规模处快速热解过程:停留时间和通过离散元模型方法在无轴螺旋反应器中加热评估

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Screw reactors may be specifically and effectively designed for small scale fast pyrolysis processes but very few models are so far available to describe their behaviour as an aid for their design and optimization. In present work, an analysis of Solid Residence Time and heating up process is proposed for this type of reactor, studying the system through of a 3-D CFD model. The screw reactor where the pyrolysis process takes place, has been modelled by means of a Discrete Element Model DEM approach based on the multiphase code "MFIX". In this case, gas phase and related interactions occurring with particles, are taken into account while evaporating phenomena and chemical reactions are neglected. This approach, allows for investigating more in detail some characteristic effects related to the perturbation of operating parameters to compare numerical and experimental data. The simulated particle heat flux is in line with experimental results at an average value of about 100W corresponding to 1 kg/h biomass flow rate with a 7% moisture content w.b. For the solid phase, the residence rime in the pyrolysis zone (less than half of the whole reactor length) is in the order of 5.5 seconds that is in typical for such components.
机译:螺杆电抗器可以专门和有效地设计用于小型快速热解过程,但迄今为止,较少的型号可用于描述其行为作为其设计和优化的辅助行为。在目前的工作中,提出了对这种类型的反应器的固体停留时间和加热过程的分析,研究了一个3-D CFD模型的系统。发生热解过程的螺旋反应器,通过基于多相代码“MFIX”的离散元件模型DEM方法进行了建模。在这种情况下,在蒸发现象和化学反应的同时考虑与颗粒发生的气相和相关的相互作用。这种方法允许更详细地研究与操作参数的扰动相关的一些特征效果,以比较数值和实验数据。模拟颗粒热通量与实验结果一致,平均值为约100W,对应于1kg / h生物质流速,具有7%的水分含量W.b。对于固相,热解区域中的居住霜(少于整个反应器长度的一半)的尺寸为5.5秒,这些组件是典型的。

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