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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Effect of agitation on fluidization characteristics of fine particles in a fluidized bed
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Effect of agitation on fluidization characteristics of fine particles in a fluidized bed

机译:搅拌对流化床细颗粒流化特性的影响

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The effect of agitation on the fluidization characteristics of fine particles was investigated in a fluidized bed with an I.D.of 6 cm and a height of 70 cm.The agitator used was of the pitched-blade turbine type and phosphor particles were employed as the bed material.The particle size was 22 mum and the particle density was 3938 kg/m~3.The effect of the agitation speed on the fluidization characteristics was examined by statistical (average absolute deviation (AAD),probability density function (PDF)),spectral (auto-correlation function,power spectrum) and chaos analysis (strange attractor,Hurst exponent,correlation dimension).The results showed that smoother fluidization was observed with increasing agitation speed,because the agglomeration and channeling were reduced by the mechanical agitation.The signals of the pressure drop fluctuation had the shape of a short-term correlation with different agitation speed.The void fraction increased with increasing agitation speed at the constant fluidizing gas velocity.
机译:在IDcm为6 cm,高度为70 cm的流化床中研究了搅拌对细颗粒流化特性的影响。所用的搅拌器为桨叶式涡轮机,并且将磷光体颗粒用作床层材料粒径为22μm,粒径为3938 kg / m〜3。通过统计分析(平均绝对偏差(AAD),概率密度函数(PDF)),光谱分析搅拌速度对流化特性的影响(自相关函数,功率谱)和混沌分析(奇怪的吸引子,Hurst指数,相关维数)。结果表明,随着搅拌速度的增加,流化更加顺畅,因为机械搅拌减少了团聚和通道。在不同的搅拌速度下,压降的波动具有短期相关的形状。在恒定压力下,空隙率随搅拌速度的增加而增加。 t流化气体速度。

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