鼓泡流化床气化炉上无砂床物料的稻壳流态化实验研究

Abeth Novria Sonjaya, K. Safitri, Adi Surjosatyo
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引用次数: 1

摘要

本研究旨在确定稻壳流化的影响以及无砂床材料鼓泡流化床气化器当量比的变化。它还旨在通过减小稻壳的直径来提高流化质量。因此,堆积密度增加,而空隙率降低,这两者都是提高固体颗粒流化质量的主要参数。实验在0.82m/s的速度下进行,通过在0.20至0.35范围内改变当量比,并分析合成气组成、冷气体和碳转化效率、低热值和温度分布。鼓泡流化床气化器的当量比为0.30,H2、CO、CH4、CO2和N2的合成气组成分别为7.415%、15.674%、3.071%、17.839%和56.031%。在这些条件下,我们获得了冷气体和碳的转化效率,以及分别为31.340%、37.120%和3.881MJ/Nm3的低热值。
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Experimental Study of Rice Husk Fluidization Without a Sand Bed Material on a Bubbling Fluidized Bed Gasifier
This study aimed to determine the effect of rice husk fluidization and variation in the equivalence ratio of bubbling fluidized bed gasifiers without sand bed materials. It also aimed to improve the fluidization quality by reducing the diameter of rice husks. Therefore, the bulk density increases, whereas voidage decreases, both of which are the main parameters for improving the quality of fluidization in solid particles. Experiments were carried out at a velocity of 0.82 m/s, by varying the equivalent ratios ranging from 0.20 to 0.35, and analyzing the syngas composition, cold gas and carbon conversion efficiencies, lower heating value, and temperature distribution. An equivalence ratio of 0.30 was obtained for a bubbling fluidized gasifier with syngas compositions of 7.415%, 15.674%, 3.071%, 17.839%, and 56.031% for H2, CO, CH4, CO2, and N2, respectively. Under these conditions, we obtained cold gas and carbon conversion efficiencies and a lower heating value of 31.340%, 37.120%, and 3.881 MJ/Nm3, respectively.
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来源期刊
CiteScore
4.50
自引率
16.00%
发文量
83
审稿时长
8 weeks
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