期刊文献+

数值研究扩散式旋风分离器流场与颗粒分离特性 被引量:3

Numerical Study of the Flow Field and Particle Separation Characteristics for a Diffusion Type Cyclone Separator
在线阅读 下载PDF
导出
摘要 针对气固分离装置中的扩散式旋风分离器,分别采用RNGk-ε湍流模型、离散相随机轨道模型(DPM)对其内部的流场和颗粒分离行为进行了数值模拟:计算了一定流速下不同粒径颗粒的轨迹;讨论了多种入口浓度和流速对分离效率的影响,以及反射屏对分离效率和颗粒停留时间的作用。计算表明,分离器内整体成双层流动结构,并且有较好的对称性,径向速度总体上比轴向和切向速度小,在反射屏内流速非常低;排气管入口存在短路流动;该类分离器对4μm以下的小颗粒分离效果不高;流速对分离效率的影响比较大;反射屏能使小颗粒在分离器内停留更长的时间从而加大被分离下来的机会。 With respect to a diffusion type cyclone separator in a gas/solid separation device,a RNG k-ε turbulent-flow model and discrete-phase random trajectory model were adopted respectively to perform a numerical simulation of its inner flow field and particle separation behavior.The trajectory of particles with different diameters at a constant flow speed was calculated and the impact of various inlet concentrations and flow speeds on the separation efficiency as well as the effect of a reflector screen on separation efficiency and particle residence time were discussed.The calculation results indicate that the separator as a whole assumes a double-layer flow structure and features a relatively good symmetry.In general,the radial speed is lower than the axial and tangential speed with an extremely low flow speed within the reflector screen.There exists a short-circuit flow at the inlet of exhaust pipes.This kind of separators provides a low separation efficiency for small particles with a diameter less than 4 μm.The flow speed has a relatively high impact on separation efficiency.The reflector screen can make small particles stagnate in the separator for a longer time,thus enhancing their chances of being separated out.
出处 《热能动力工程》 EI CAS CSCD 北大核心 2006年第3期270-274,共5页 Journal of Engineering for Thermal Energy and Power
关键词 扩散式旋风分离器 两相流动 颗粒分离 数值模拟 diffusion type cyclone separator,two-phase flow,particle separation,numerical simulation
作者简介 谭晓军(1972-),男,重庆丰都人,浙江大学硕士研究生.
  • 相关文献

参考文献6

二级参考文献12

  • 1由长福 岳光溪 等.方形分离器三维流场的测定及数值模拟[J].动力工程,1995,15(5):1-6.
  • 2[1]岑可法,倪明江,严建华,等.气固分离理论及技术[M].浙江大学出版社,1993.
  • 3[3]Stairmand C J. The Design and Performance of Cyclone Sep arators [J]. Trans Inst, Chem. Eng, 1951, 29,356.
  • 4程乐鸣 骆仲泱 方梦祥 等.卧式方型热交换分离器[P].中国专利,专利号:ZL00201914.0.2000.
  • 5Cheng Le-ming, Zhou Qiang, Luo Zhong-yang, Ni Ming-jiang, Cen Ke-fa. Development of a horizontal heat-exchanger square cyclone[C]. Pro of the 7^th International Conf. on Circulating Fluidized Bed, 2002, (5) : 551-558.
  • 6Saha S K, Basu P, Dytta A. Performance of a novel horizontal gas-solid separator in a circulating fluidized bed riser[C]. Pro of the 7^th International Conf on Circulating Fluidized Bed.2002(5) : 567-574.
  • 7Cheng Le-ming, Zhou Qiang, Luo Zhong-yang, Ni Mingjiang, Cen Ke-fa. Development of a horizontal heat-exchanger square cyclone[C]. Pro. of the 7th International Conf. on Circulating Fluidized Bed, 2002, (5) :551~558.
  • 8Saha S K, Basu P, Dytta A. Performance of a novel horizontal gas-solid separator in a circulating fluidized bed riser[C]. Pro.of the 7th International Conf. on Circulating Fluidized Bed.2002(5) : 567-574.
  • 9李勇,刘志友,安亦然.介绍计算流体力学通用软件——Fluent[J].水动力学研究与进展(A辑),2001,16(2):254-258. 被引量:166
  • 10程乐鸣,周强,骆仲泱,岑可法.一种应用于锅炉改造的新型分离器——方形卧式分离器[J].电站系统工程,2003,19(3):1-3. 被引量:5

共引文献14

同被引文献12

引证文献3

二级引证文献8

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