首页> 外文OA文献 >The effect of gas-phase density on bubble formation at a single orifice in a two-dimensional gas-fluidised bed.
【2h】

The effect of gas-phase density on bubble formation at a single orifice in a two-dimensional gas-fluidised bed.

机译:气相密度对二维气体流化床中单个孔口气泡形成的影响。

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

In this study the effect of the gas-phase density on the process of bubble formation at a single orifice in a two-dimensional gas-fluidized bed has been studied experimentally and theoretically. Specifically, a detailed comparison between experimentally observed and theoretically calculated bubble growth curves has been made in the case where the density of the gas injected through the orifice (He and SF6) differs significantly from the density of the primary fluidizing agent (air). The calculations have been carried out using an earlier developed, first principles hydrodynamic model of gas-fluidized beds which has been extended with a species conservation equation to calculate the composition of the fluidizing gas in the vicinity of the evolving bubbles. Besides, the present experimental and theoretical results were compared with predictions obtained from adapted versions of approximate bubble formation models previously reported in the literature. The advanced hydrodynamic model appears to predict the experimentally observed diameters satisfactorily. In addition, the model correctly predicts the effect of the gas-phase density on the experimentally observed bubble growth. This effect can be explained satisfactorily in terms of the dependence of the interphase momentum transfer coefficient on gas-phase density. Finally, calculations with a three-dimensional version of our hydrodynamic model have been carried out to account for the effect of the front and back wall of the pseudo two-dimensional gas-fluidized bed used in our experiments. Our preliminary computational results indicate that the magnitude of the wall effect strongly depends on the boundary condition enforced for the gas-solid dispersion at these walls. In the case that the no-slip boundary condition was enforced in the calculations for the solid phase, the wall effect was significant and a considerable deviation between computed and experimentally observed bubble growth curves was found. However, when a more realistic partial slip boundary condition for the solid phase was implemented the agreement between theory and experiment could be improved by altering the slip parameter in the partial slip boundary condition expression.
机译:在这项研究中,已通过实验和理论研究了气相密度对二维气化床中单个孔口气泡形成过程的影响。具体而言,在通过孔口注入的气体(He和SF6)的气体密度与主要流化剂(空气)的密度显着不同的情况下,已对实验观察到的气泡增长曲线与理论计算得出的气泡增长曲线进行了详细比较。该计算是使用较早开发的第一原理的气化床流体力学模型进行的,该模型已通过物种守恒方程进行了扩展,可以计算出气泡附近流化气体的成分。此外,将当前的实验和理论结果与从文献中先前报道的近似气泡形成模型的改编版本中获得的预测结果进行了比较。先进的流体动力学模型似乎可以令人满意地预测实验观察到的直径。此外,该模型可以正确预测气相密度对实验观察到的气泡生长的影响。关于相间动量传递系数对气相密度的依赖性,可以令人满意地说明该效果。最后,我们用流体力学模型的三维版本进行了计算,以说明实验中使用的伪二维气化床的前壁和后壁的影响。我们的初步计算结果表明,壁效应的大小在很大程度上取决于对这些壁上的气固弥散施加的边界条件。在固相计算中强制采用无滑移边界条件的情况下,壁效应是显着的,并且在计算出的气泡膨胀曲线和实验观察到的气泡生长曲线之间发现了相当大的偏差。然而,当对固相实施更现实的局部滑移边界条件时,通过改变局部滑移边界条件表达式中的滑移参数可以改善理论与实验之间的一致性。

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