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Performance analysis of a downdraft and fluidized bed biomass gasification using thermodynamic equilibrium model

机译:基于热力学平衡模型的下流流化床生物质气化性能分析

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摘要

Gasification is a process of producing fuel gas or synthesis gas from biomass using gasifier. The gas produced through this process particularly hydrogen will be utilized further as an input for power generation in order to produce energy. Due to the environmental concern and sustainability issues, energy from biomass has become one of the most promising renewable sources of energy. Current research points to improve the gasifier performance in order to elevate more economical product from the gasifier. For this purpose, the thermodynamic equilibrium model can be employed to predict the gas composition and to optimize important gasifier parameters for various kinds of gasifiers as well as utilizing various types of biomasses. In this work, the biomasses consisting of wood, rice husk, saw dust and empty fruit brunch are selected considering their low cost and availabilities as an abundant resource in Malaysia. These biomass sources are then served as the inputs for downdraft and fluidized bed gasifier for producing the hydrogen gas and through this study, the performance analysis in terms of the optimal parameters and gas output composition are then carried out. Here the air is used as an input reactant for downdraft gasifier and the fluidized bed gasifier is employing steam for the gasification process. In this work, the model validation is carried out first where the gas composition data obtained from thermodynamic equilibrium model show good agreement with experimental result from Zainal et al. (2001) for downdraft gasifier employing wood and Karmakar and Datta (2011) for fluidized bed gasifier using rice husk. Afterwards the performance analysis is performed to investigate the optimum parameters for downdraft and fluidized bed gasifiers. Based on this analysis, the optimum parameters obtained are at temperature 770°C with moisture content of 0.2 and steam biomass ratio 1.32, the hydrogen gas produced from wood, rice husk, sawdust and empty fruit bunch in downdraft gasifier is 16.38%, 17.02%, 16.30% and 50.12% respectively, while in the fluidized bed gasifier is 38.75%, 50.00%, 73.30% and 71.77% respectively. The result of the performance analysis shows that the fluidized bed gasifier is more efficient than downdraft gasifier in term of hydrogen gas production.
机译:气化是使用气化炉从生物质生产燃料气或合成气的过程。通过该过程产生的气体,特别是氢气,将进一步用作发电的输入,以产生能量。由于环境问题和可持续性问题,生物质能源已成为最有希望的可再生能源之一。当前的研究点在于提高气化炉性能,以提高气化炉的经济性。为此,可以使用热力学平衡模型来预测气体组成并为各种气化炉以及利用各种类型的生物质优化重要的气化炉参数。在这项工作中,选择了由木材,稻壳,锯末和空果早午餐组成的生物质,因为它们的低成本和可利用性是马来西亚的一种丰富资源。然后将这些生物质来源用作向下气流和流化床气化炉生产氢气的输入,并通过该研究,然后根据最佳参数和气体输出成分进行性能分析。在此,空气用作向下气流气化炉的输入反应物,而流化床气化炉则采用蒸汽进行气化过程。在这项工作中,首先进行模型验证,其中从热力学平衡模型获得的气体成分数据与Zainal等人的实验结果显示出良好的一致性。 (2001年)适用于采用木材的下浮式气化炉,Karmakar和Datta(2011年)适用于采用稻壳的流化床气化炉。然后进行性能分析,以研究下浮式和流化床气化炉的最佳参数。根据此分析,获得的最佳参数是在770°C的温度下,水分含量为0.2和蒸汽生物量比为1.32的条件下,由下浮式气化炉中的木材,稻壳,锯末和空果串产生的氢气为16.38%,17.02%分别为16.30%和50.12%,而在流化床气化炉中分别为38.75%,50.00%,73.30%和71.77%。性能分析结果表明,就氢气生产而言,流化床气化炉比下流式气化炉效率更高。

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    Gan Gek Hian;

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  • 年度 2015
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