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Numerical study on pressure prediction and its main influence factors in pneumatic conveyors

机译:气力输送机压力预测及其主要影响因素的数值研究

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The flow characteristics of multiphase gas-solid flow in a pneumatic conveyor were investigated numerically and experimentally to predict the important pressure within the pipeline. The effects of particle size, particle density, and bend radius ratio on pressure drop over the bend pipeline were also analysed. Experiments were conducted to obtain the static pressure at certain cross-sections of a fine powder pneumatic conveying pipeline with a length of 26. m and an inner diameter of 53. mm. The conveyed material was flyash with a mean particle size of 30 μm and the solids loading ratio was in the range 20-70. A numerical study of gas-solid flow in complex three-dimensional systems was undertaken by means of commercial CFD software Fluent 6.3. The simulation was performed using the Euler-Euler approach, accounting for four-way coupling. The calculated results of pressure gradient were found to be in good agreement with the measured data, with a fitting slope of 0.781 for the first horizontal straight pipeline and 1.017 for horizontal bend. It was also found that the pressure gradients increase with increase in particle diameter rapidly and reach the peak value when particle diameter is 150 μm, and then begin to decrease and show a slight steepening with increase in particle diameter with a value greater than 150μm. An increase in particle density results in increase in pressure gradient. The pressure drop is much smaller when the roughness height is zero. The pressure gradient over the horizontal bend increases gradually with the increase of roughness height. The larger the roughness constant is defined, the greater the pressure drop will be. The bend pressure gradient decreases significantly when the bend radius ratio increases from 1 to 3, and then much slowly for bend radius ratios 3-6. With the increase of velocity difference, the pressure drop decrease is different at first, after 0.2-0.3. m, the pressure reduces the same.
机译:数值和实验研究了气力输送机中多相气固流的流动特性,以预测管道内的重要压力。还分析了颗粒大小,颗粒密度和弯曲半径比对弯曲管线上压降的影响。进行实验以获取长度为26.m,内径为53.mm的细粉气动输送管道在某些横截面上的静压。所输送的材料是粉煤灰,平均粒径为30μm,固体含量为20-70。通过商用CFD软件Fluent 6.3对复杂三维系统中的气固流动进行了数值研究。使用Euler-Euler方法进行了模拟,考虑了四向耦合。压力梯度的计算结果与实测数据吻合良好,第一条水平直管的拟合斜率为0.781,水平弯曲的拟合斜率为1.017。还发现压力梯度随粒径的增加而迅速增加,并在粒径为150μm时达到峰值,然后开始减小,并随粒径的增加而逐渐变陡,值大于150μm。颗粒密度的增加导致压力梯度的增加。当粗糙度高度为零时,压降小得多。水平弯曲处的压力梯度随粗糙度高度的增加而逐渐增加。定义的粗糙度常数越大,压降越大。当弯曲半径比从1增加到3时,弯曲压力梯度显着降低,然后在弯曲半径比3-6时缓慢下降。随着速度差的增加,压降的减小在0.2-0.3之后首先有所不同。 m,压力降低相同。

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