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首页> 外文期刊>化学工学論文集 >Algebraic Expression of the Minimum Gas Velocity Restraining Downward-Flowing Particles through the Contraction Midway of a Circulating Fluidized Bed Riser
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Algebraic Expression of the Minimum Gas Velocity Restraining Downward-Flowing Particles through the Contraction Midway of a Circulating Fluidized Bed Riser

机译:通过循环流化床提升机的收缩中间抑制向下流动颗粒的最小气体速度的代数表达

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Using a circulating fluidized bed (CFB) as a typical column-type solid/gas system,this study aimed to determine the minimum gas velocities restraining the downward-flowing particles through the contraction midway of the CFB riser,and to formualte an algebraic expression of these critical velocities.Using glass-beads as circualting particles,change i nthe amount of downward-flowing particles at the contraction with change in gas velocity was examined experientally for different solid feeding rates.Algebraic expression of critical velocities was performed with a growing chain model (GCM) and a revised GCM (RGCM).The GCM proposed by us and others is an ideal cluster model that assumes a vertical chain of particles of a constant size.The RGCM further takes account of the size distribution of circulating particles.The experimental results with circualting particles of different size range of 125-280,90-225 and 28-90 mum revealed that the critical gas velocities are proportional to the soklid feeding rates,and the slopes of those curves are almost the same,irrespective of the size distribution of circulating particles.The critical velocities obtainedf by extrapolating the curves of experimental critical velocity towards zero of solid feeding rate showed a lienar relations with the theoretical terminal gas velocities of an infinitely long chain of particles given by the GCM and RGCM.From this,the critical velocity can be presented as a linear expression of the solid feeding rate and the theoretical terminal gas velocity of an infinitely long chain of particles.The theoretical expression of the critical velocity using the theoretical terminal gas velocity of an infinitely long chain of particles by the RGCM is confirmed to be adequate,since this expression can also predict experimental critical velocities for 28-280 mum circualting particles with an error of only +-10%.
机译:使用循环流化床(CFB)作为典型的柱式固体/气体系统,该研究旨在通过CFB提升板的收缩和形成代数表达来确定抑制向下流动的颗粒的最小气体速度,并形成代数表达这些临界速度。对于玻璃珠作为循环颗粒,在实际上对与气体速度的变化进行了变化I n的变化颗粒的量,以进行不同的固体进料速率。用生长链模型进行临界速度的成本表达(GCM)和修订的GCM(RGCM)。我们和其他人提出的GCM是一个理想的群集模型,假设恒定尺寸的颗粒垂直链。RGCM进一步考虑了循环粒子的尺寸分布。实验结果,不同尺寸范围为125-280,90-225和28-90妈妈的通路颗粒透露,临界气体速度与SOKL成比例ID馈送速率,并且这些曲线的斜率几乎相同,而不管循环颗粒的尺寸分布。通过将实验临界速度的曲线推断到固体进料速率的零的尺寸,显示了与理论终端的李安萨尔关系的临界速度。由GCM和RGCM给出的无限长链颗粒的气体速度。从而可以将临界速度呈现为固体进料速率的线性表达和无限长的粒子的无限长链的理论末端气体速度。理论使用RGCM使用无限长的粒子的理论末端气体速度的临界速度的表达被证实是足够的,因为该表达还可以预测28-280毫米通路颗粒的实验临界速度,仅+ - 10%。

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