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Characteristics of Minimum Fluidization Velocity and Pressure Fluctuations in Annular Fluidized Beds

机译:环形流化床中最小流化速度和压力波动的特征

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Characteristics of minimum fluidization velocity and pressure fluctuations were investigated in an annular fluidized bed whose diameter was 0.102 m and 2.0 m in height Effects of gas velocity, particle size and bed temperature on the minimum fluidization velocity and pressure fluctuations were examined. The values of minimum fluidization velocity obtained by means of three different methods were very similar each other. The correlation dimension could be a quantitative parameter for expression the resultant complex behavior of gas and solid mixture in the annular fluidized bed. The value of correlation dimension increased with increasing gas velocity, fluidized particle size and temperature in the bed. The minimum fluidization velocity could be determined by means of correlation dimension of pressure fluctuations as well as pressure drop in the bed and standard deviation of pressure fluctuations. The minimum fluidization velocity increased with increasing particle size but decreased with increasing bed temperature in annular fluidized beds. The minimum fluidization velocity was well correlated in therms of correlation dimension as well as operating variables within experimented conditions of this study.
机译:研究了直径为0.102 m和高度为2.0 m的环形流化床中最小流化速度和压力波动的特性,研究了气体流速,粒度和床温对最小流化速度和压力波动的影响。通过三种不同方法获得的最小流化速度值彼此非常相似。相关维数可以是定量参数,用于表达在环形流化床中气体和固体混合物的合成复杂行为。相关尺寸的值随着气体速度,流化粒度和床内温度的增加而增加。最小流化速度可以通过压力波动的相关尺寸以及床中的压降和压力波动的标准偏差来确定。在环形流化床中,最小流化速度随粒径的增加而增加,但随床温的增加而降低。在本研究的实验条件下,最小流化速度与相关维数以及操作变量的相关性很好。

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