期刊文献+

喷射混合器放大效应的计算流体力学模拟 被引量:3

Computational Fluid Dynamics Simulation on the Scale-up Effect in Ejectors
下载PDF
导出
摘要 选用Realizable k-ε湍流模型,对有扩散角度和无扩散角度的两种喷射器进行了计算流体力学(CFD)模拟,以研究喷射器的放大效应。在射流和引射速度不变的前提下,将两种喷射器的尺寸在初始尺寸的基础上分别放大3,5,8和10倍进行模拟计算。结果表明:对于两种喷射器,尺寸的放大对速度场以及湍动能的分布均无显著影响,而喷射器内湍流耗散率与涡量均随着喷射器尺寸放大倍数的增加而减小,近似成反比例关系,达到完全混合所需的距离与放大倍数成正比,无量纲距离略有变化。因为湍流耗散率及涡量等是表征湍动程度的重要指标,因此这也说明喷射器放大后湍动程度显著降低,不利于混合,这与喷射器是否存在扩散角度无关。 Computational Fluid Dynamics (CFD) simulation was employed to investigate the scale-up effect in ejectors with the Realizable k-e turbulent model. Two kinds of ejector models, with and without diffuser angle, were established. Keeping the velocities of jet flow and suction flow, the geometric sizes of ejectors were enlarged to 3, 5, 8 and 10 times based on the original sizes and the simulations were carried out respectively. The results showed that the velocity and turbulent kinetic energy were not changed apparently after scaled up, while the turbulent dissipation rate reduced significantly as well as the vorticity magnitude. There was an approximate inverse proportional relationship between the turbulent dissipation rate and the geometric size. Moreover, the distance required for mixing completely was proportional to the scale-up factor and the dimensionless distance changed slightly. Since the turbulent dissipation rate and the vorticity were important parameters to describe the turbulent flow, it might imply that the turbulent extent would drop significantly after scaled up, which was unfavorable for the mixing behavior. It had no relationship with the angle of the diffuser.
出处 《化学反应工程与工艺》 CAS CSCD 北大核心 2013年第6期495-501,共7页 Chemical Reaction Engineering and Technology
关键词 喷射器 放大效应 计算流体力学模拟 湍流耗散率 ejector scale-up effect Computational Fluid Dynamics simulation turbulent dissipation rate
  • 相关文献

参考文献4

二级参考文献36

  • 1徐海涛,桑芝富,顾斌,柴宁,徐卫东.蒸汽喷射真空泵性能的CFD模拟研究[J].高校化学工程学报,2005,19(1):22-29. 被引量:26
  • 2黄雄斌,包雨云,施力田,王英琛.应用电导探针测定固-液两相流的局部速度[J].高校化学工程学报,1995,9(2):187-190. 被引量:9
  • 3黄雄斌.大型高效轴流式搅拌装置[J].化工进展,1996,15(4):44-45. 被引量:4
  • 4骆培成,程易,汪展文,金涌,杨万宏.液-液快速混合设备研究进展[J].化工进展,2005,24(12):1319-1326. 被引量:66
  • 5肖洋,唐洪武,华明,王志良.同向圆射流混合特性实验研究[J].水科学进展,2006,17(4):512-517. 被引量:14
  • 6van DIERENDONCK L L, JINDRICH Z. Loop venturi reactor--a feasible alternative to stirred tank reactors [ J ]. Ind Eng Chem Res, 1998,37 (3) :734-738.
  • 7DIRIX C A, van der WIELE K. Mass transfer in jet loop reactors [ J ]. Chemical Engineering Science, 1990,45 (8) :2 333-2 340.
  • 8CRAMERS P H, van DIERENDONCK L L, BEENACKERS A A. Influence of the gas density on the gas entrainment rate and gas hold-up in loop-venturi reactors [ J ]. Chemical Engineering Science ,1992,47 (9-11) :2 251-2 256.
  • 9ZAHRADNIK J, FIALOVA M, LINEK V, et al. Dispersion efficiency of ejector-type gas distributors in different operating modes [J]. Chemical Engineering Science, 1997,52(24) :4 499-4 510.
  • 10LENE K H, BJORN H H, TRON S. CFD modeling of fast chemical reactions in turbulent liquid flows [ J ]. Computer and Chemical Engineering, 2002,6 (4/5) : 507- 515.

共引文献44

同被引文献19

引证文献3

二级引证文献2

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部