首页> 外文期刊>Chemical Engineering & Technology: Industrial Chemistry -Plant Equipment -Process Engineering -Biotechnology >Simulations of gas distributors in the design of shallow bubble column reactors
【24h】

Simulations of gas distributors in the design of shallow bubble column reactors

机译:浅鼓泡塔反应器设计中气体分布器的模拟

获取原文
获取原文并翻译 | 示例
       

摘要

Computational fluid dynamics (CFD) was used to simulate the effect of sparger construction in gas holdup and liquid axial velocity in a shallow bubble column reactor for the air-water system. Model parameters were evaluated in 2- and 3-D simulations by using a two-fluid model and the standard k-epsilon turbulence model. The Eulerian-Eulerian approach was employed to predict the height of column that is affected by the sparger. It was found that increasing the number of orifices in the sparger increases the total gas holdup. Moreover, each orifice causes an increase in the circulation and mixing of liquid in the column. The results of the simulations follow the trends observed in the findings of Dhotre and Joshi [1].
机译:计算流体动力学(CFD)用于模拟在空气-水系统的浅气泡塔反应器中,分布器构造对气体滞留率和液体轴向速度的影响。通过使用双流体模型和标准k-ε湍流模型,在2-D和3-D模拟中评估了模型参数。使用欧拉-欧拉方法来预测受喷头影响的柱高。发现增加喷射器中的孔的数量会增加总的气体滞留量。而且,每个孔口导致塔中液体的循环和混合增加。模拟结果遵循Dhotre和Joshi [1]的发现中观察到的趋势。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

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