首页> 外文OA文献 >Numerical simulations of lateral solid mixing in gas-fluidized beds
【2h】

Numerical simulations of lateral solid mixing in gas-fluidized beds

机译:气液床中侧向固体混合的数值模拟

代理获取
本网站仅为用户提供外文OA文献查询和代理获取服务,本网站没有原文。下单后我们将采用程序或人工为您竭诚获取高质量的原文,但由于OA文献来源多样且变更频繁,仍可能出现获取不到、文献不完整或与标题不符等情况,如果获取不到我们将提供退款服务。请知悉。

摘要

We investigated the influence of design parameters and operational conditions on lateral solid mixing in fluidized beds adopting the Eulerian-Eulerian modeling approach. To quantify the rate at which solids mix laterally, we used a lateral dispersion coefficient (Dsr). Following the usual approach employed in the literature, we defined Dsr by means of an equation analogous to Fick[U+05F3]s law of diffusion. To estimate Dsr, we fitted the void-free solid volume fraction radial profiles obtained numerically with those obtained analytically by solving Fick[U+05F3]s law. The profiles match very well. Our results show that Dsr increases as superficial gas velocity and bed height increase; furthermore, it initially increases with bed width, but then remains approximately constant. The values of Dsr obtained numerically are larger than the experimental ones, within the same order of magnitude. The overestimation has a twofold explanation. On one side, it reflects the different dimensionality of simulations (2D) as compared with real fluidized beds (3D), which affects the degrees of freedom of particle lateral motion. On the other, it is related to the way frictional solid stress was modeled: we employed the kinetic theory of granular flow model for the frictional solid pressure and the model of Schaeffer (1987) for the frictional solid viscosity. To investigate how sensitive the numerical results are on the constitutive model adopted for the frictional stress, we ran the simulations again using different frictional models and changing the solid volume fraction at which the bed is assumed to enter the frictional flow regime (ϕmin). We observed that Dsr is quite sensitive to the latter. This is because this threshold value influences the size and behavior of the bubbles in the bed. We obtained the best predictions for ϕmin=0.50. The results show that accurate prediction of lateral solid dispersion depends on adequate understanding of the frictional flow regime, and accurate modeling of the frictional stress which characterizes it.
机译:我们采用欧拉-欧拉建模方法,研究了设计参数和操作条件对流化床横向固体混合的影响。为了量化固体横向混合的速率,我们使用了横向弥散系数(Dsr)。按照文献中常用的方法,我们通过类似于Fick [U + 05F3] s扩散定律的方程式定义了Dsr。为了估算Dsr,我们将通过数值求解获得的无空隙固体体积分数径向分布图与通过求解Fick [U + 05F3] s法则而解析获得的分布图拟合。这些配置文件匹配得很好。我们的结果表明,Dsr随着表观气体速度和床层高度的增加而增加;此外,它最初随床宽增加,但随后保持近似恒定。在相同的数量级内,从数值上获得的Dsr值大于实验值。高估有双重解释。一方面,与真实流化床(3D)相比,它反映了模拟(2D)的不同维度,这会影响粒子横向运动的自由度。另一方面,它与摩擦固体应力的建模方式有关:我们将颗粒流动模型的动力学理论用于摩擦固体压力,将Schaeffer(1987)模型用于摩擦固体粘度。为了研究数值结果对采用本构关系的摩擦应力的敏感性,我们再次使用不同的摩擦模型进行了模拟,并更改了假设床层进入摩擦流态的固体体积分数(fractionmin)。我们观察到Dsr对后者非常敏感。这是因为该阈值影响床中气泡的大小和行为。我们获得了ϕmin = 0.50的最佳预测。结果表明,横向固体分散的准确预测取决于对摩擦流动状态的充分理解,以及表征其的摩擦应力的精确模型。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
代理获取

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号