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Gasification of Miscanthus x giganteus Pellets in a Fixed Bed Pilot-Scale Unit

机译:固定床试验规模装置中的芒草x气粒的气化

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Gasification of Miscanthus x giganteus (Mxgig), is highly promising due to the high efficiency of the process and the many advantageous properties of this crop. Pilot-scale, fixed bed gasification studies were performed utilizing this fuel at three temperatures (750, 850, 950 ºC) to determine the process effects of temperature on gas quality and tar yields. Simple thermodynamic equilibrium modeling was successfully applied to the pilot-scale gasification process. The Mxgig crop performed well, with best process stability reached at temperatures of 800 ºC or higher. Average calorific values of the product gases were highest at around 850 ºC at 5.2 MJ.m-3. Tar yields gradually increased with increasing temperature and dropped after 900 ºC. The presented thermodynamic equilibrium model conformed well with experimental results, deviating little in terms of O2, CO2, H2 and CH4 and no more than 8.1% in the case of CO. This indicates that simple modeling methods can be utilized to predict gas compositions for the pilot-scale.
机译:由于该方法的高效率和该农作物的许多有利特性,气化芒草(Mscangus x giganteus)(Mxgig)前景广阔。使用这种燃料在三种温度(750、850、950ºC)下进行了中试固定床气化研究,以确定温度对气体质量和焦油产率的过程影响。简单的热力学平衡模型已成功应用于中试规模的气化过程。 Mxgig作物表现良好,在800ºC或更高的温度下具有最佳的过程稳定性。产物气体的平均热值在850 Mc.m-3时约为850ºC。焦油产量随着温度的升高而逐渐增加,而在900ºC之后下降。提出的热力学平衡模型与实验结果非常吻合,O2,CO2,H2和CH4的偏差很小,而对于CO的偏差不超过8.1%。这表明可以使用简单的建模方法来预测天然气的组成试点规模。

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