石油炼制与化工 ›› 2015, Vol. 46 ›› Issue (9): 65-70.

• 基础研究 • 上一篇    下一篇

喷嘴直径和位置对环流反应器流动影响的数值模拟

杜峰,杨志方,邓文安,王晓杰   

  1. 中国石油大学(华东)化学工程学院
  • 收稿日期:2015-03-02 修回日期:2015-03-31 出版日期:2015-09-12 发布日期:2015-08-19
  • 通讯作者: 杜峰 E-mail:dufeng@upc.edu.cn
  • 基金资助:

    环流反应器工程放大基础研究2013.1-2014.12青年基金

NUMERICAL SIMULATION OF EFFECT OF NOZZLE DIAMETER AND POSITION ON HYDRODYNAMICS IN AIRLIFT LOOP REACTOR

  • Received:2015-03-02 Revised:2015-03-31 Online:2015-09-12 Published:2015-08-19

摘要: 在油-氢气体系下使用欧拉-欧拉双流体模型考察了喷嘴直径和喷嘴位置对气升式环流反应器内气-液两相流动的影响为悬浮床工业装置提供理论指导。模拟结果表明:相对于喷嘴直径为40 mm和80 mm,喷嘴直径为20 mm时环流动力较大,上升区和下降区的环流液速较大,而气含率改变不大;喷嘴高置时的气含率明显大于喷嘴低置和平置时,喷嘴低置和平置时的气含率相差不大,3种喷嘴位置下的环流液速大小为:低置>平置>高置。综合考虑,喷嘴直径为20 mm和低置时的流动特性较好。

Abstract: Euler-euler two flow model was applied to simulate the effect of nozzle diameter and nozzle position on the hydrodynamics in airlift loop reactor in the oil-hydrogen system to provide theoretical guidance for suspension bed industrial equipment. The simulation results show that related to the nozzle diameters of 40 mm and 80 mm, the circulation power is larger when nozzle diameter is 20 mm; the liquid circulation velocity in the rising and dropping is larger, but the gas holdups change small. The gas holdup when the nozzle was set at higher location is obviously higher than that of the gas holdup at the horizontal and low location, while there is not much difference of gas holdup between the horizontal and low location. The liquid circulation velocity magnitudes at three nozzle locations are: low>flat>high location. It is concluded by comprehensive consideration that the flow characteristics is better when the nozzle diameter is 20 mm at low location.