首页> 外文会议>Proceedings of the 11th International Conference on Fluidized Bed Technology >THE EFFECT OF JETTING GAS VELOCITY ON PARTICLE VELOCITIES IN A TWO-DIMENSIONAL JETTING FLUIDIZED BED UNDER PRESSURE
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THE EFFECT OF JETTING GAS VELOCITY ON PARTICLE VELOCITIES IN A TWO-DIMENSIONAL JETTING FLUIDIZED BED UNDER PRESSURE

机译:二维加压流化床中引流速度对颗粒速度的影响

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An optic fiber probe system was employed to investigate the profiles of vertical particle velocities in the outer regions close to the wall of a pressurized jetting fluidized bed.The influence of jetting gas velocity on the particle behavior has been systematically studied.A two-dimensional cold mode of a jetting fluidized bed coal gasifier, of 300 mm × 30 mm cross section was operated at pressures both 0.7 and 1.6 MPa and at high excess fluidizing gas velocity in the range of 0.20 to 0.40 m/s.The bed material was polystyrene with a mean particle diameter of 1.32 mm.The vertical local particle velocity (Vp) gradually accelerates with jetting gas velocity at high bed level.However, at low bed height level, Vp first increases and then is nearly constant at 0.7 MPa and gradually increases (maximum value about 0.63 m/s) at 1.6 MPa.
机译:利用光纤探针系统研究了加压喷射流化床壁附近外部区域的垂直粒子速度分布,系统地研究了喷射气体速度对粒子行为的影响。二维冷在0.7和1.6 MPa的压力下以及在0.20至0.40 m / s的高过流化气体速度下操作的截面为300mm×30mm的喷射流化床煤气化炉模式。平均粒径为1.32毫米。在高床层水平下,垂直局部颗粒速度(Vp)随着喷射气体速度逐渐加速,但是在低床层水平下,Vp首先增加,然后在0.7 MPa时几乎恒定,然后逐渐增加(最大值在1.6 MPa时约为0.63 m / s)。

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