期刊文献+

非牛顿流体中气液两相流流场结构的小波分析 被引量:1

Wavelet Analysis of Gas-Liquid Two-Phase Flow Field Structure in Non-Newtonian Fluid
下载PDF
导出
摘要 为了揭示流体流动中的隐含结构及湍流运动规律,利用三维激光多普勒测速仪对非牛顿流体中气泡上升过程液相速度场进行了测量,并借助小波方法对瞬时速度时间序列进行分析.局部间歇测度(LIM)峰分布的相似性说明湍流中存在大旋涡和小旋涡的串级结构,而LIM峰分布的不完全一致性说明湍流中存在相干结构.对不同小波尺度下能量分布的比较发现,在中尺度区,由于气泡的连续通过,该尺度范围内的能量占据了总能量的绝大部分,说明气泡的通过对液相的能量传递有很大贡献.另外,黏度增大使得小涡占据的能量减小,由小涡传递和耗散的能量减少,因此含能尺度的能量分布变宽. In order to detect the hidden structures and the pattern of turbulence in fluid flow,the liquid velocity field was measured with 3D laser Doppler velocimeter (LDV) during the single bubble seriate rising process in non-Newtonian fluid, and wavelet method was adopted to analyze the time series of instantaneous velocity. The comparability of local intermit- tency measure (LIM) distribution displayed the existence of the cascade structure of big eddy and small eddy,and the incon- sistency of LIM distribution showed the existence of coherent structure. Comparison of the power distribution at various wavelet levels indicated that power at the middle level occupied most part of the total power due to bubble seriate pass,and the pass of bubble made great contribution to the power transfer of liquid. In addition, the increase of viscosity of the solution brought about decrease of the power occupied by small eddy ,and the power of transfer and dissipation through small eddy decreased, therefore the power distribution of energy range was widened.
出处 《天津大学学报》 EI CAS CSCD 北大核心 2009年第5期448-452,共5页 Journal of Tianjin University(Science and Technology)
基金 国家自然科学基金资助项目(20476073)
关键词 小波分析 流场结构 非牛顿流体 激光多普勒测速仪 局部间歇测度 能量分布 wavelet analysis flow field structure non-Newtonian fluid laser Doppler velocimeter local intermittency measure power distribution
  • 相关文献

参考文献14

  • 1Hassager O. Negative wake behind bubbles in non- Newtonian liquids [J]. Nature, 1979,279 (31) :402-403.
  • 2Harlen O G. The negative wake behind a sphere sedimenting through a viscoelastic fluid[J]. Journal of Non- Newtonian Fluid Mechanics, 2002,108 (1/2/3) :411-430.
  • 3Funfschilling D,Li H Z. Flow of non-Newtonian fluids around bubbles:PIV measurements and birefringence visualisation[J]. Chemical Engineering Science,2001, 56(3) :1137-1141.
  • 4Mudde R F,Groen J S,Van Den Akker H E A. Liquid velocity field in a bubble column:LDA experiments [J]. Chemical Engineering Science, 1997,52 (21/22) :4217- 4224.
  • 5Groen J S,Mudde R F,Van Den Akker H E A. On the application of LDA to bubbly flow in the wobbling regime [J]. Experiments in Fluids,1999,27(5):435- 449.
  • 6Becker S,de Bie H,Sweeney J. Dynamic flow behavior in bubble columns[J]. Chemical Engineering Science, 1999,54 (21) :4929-4935.
  • 7Armenante P M ,Luo Changgen,Chou C C ,et al. Velocity profiles in a closed,unbaffied vessel:Comparison between experimental LDV data and numerical CFD predictions[J]. Chemical Engineering Science, 1997,52 (20) :3483-3492.
  • 8Mudde R F,Groen J S,Van Den Akker H E A. Application of LDA to bubbly flows [J]. Nuclear Engineering and Design, 1998,184 (2/3) :329-338.
  • 9Farge M. Wavelet transforms and their applications to turbulence [J]. Annual Review of Fluid Mechanics, 1992, 24:395-458.
  • 10Kulkarni A A,Joshi J B, Kumar V R,et al. Application of multiresolution analysis for simultaneous measurement of gas and liquid velocities and fractional gas hold-up in bubble column using LDA[J]. Chemical Engineering Science, 2001,56 (17) : 5037-5048.

二级参考文献17

  • 1King, C.J., Separation Processes, Mc Graw-Hill Book Company, New York, 146-211 (1971).
  • 2Sherwood, T.K., Pigford, R. L., Wilke, C.R., Mass Transfer,Mc Graw-Hill Book Company, New York, 593-666 (1975).
  • 3Dudukovic, M.P., Larachi, F., Mills, P.L., "Multiphase reactors-revisited", Chem. Eng. Sci., 54, 1975-1995(1999).
  • 4Sololey, A.W., "Should you switch to high capacity trays?",Chem. Eng. Prog., 94, 23-35 (1999).
  • 5Kemoun, A., Rados, N., Li, F., Al-Dahhan, M.H.,Dudukovic, M.P., MiUs, P.L., Leib, T.M., Lerou, J.J., "Gas holdup in a trayed cold-flow bubble column", Chem. Eng.Sci., 56, 1197-1205 (2001).
  • 6Farge, M., "Wavelet transforms and their applications to turbulence", Ann. Rev. Fluid Mech., 24, 395-458 (1992).
  • 7Bakshi, B.R., Zhong, H., Jiang, P., Fan, L.S., "Analysis of flow in gas-liquid bubble columns using multi-resolution methods", Trans. Ins. Chem. Eng., 73 (A), 608-614(1995).
  • 8Kulkarni, A.A., Joshi, J.B., Kumar, V.R., Kulkarni, B.D.,"Wavelet transform of velocity-time data for the analysis of turbulent structures in a bubble column", Chem. Eng.Sci., 56, 5305-5315 (2001).
  • 9Park, S.H., Kang, Y., Kim, S.D., "Characterization of pressure signals in a bubble column by wavelet transport", J.Chem. Eng. Japan, 34, 158-165 (2001).
  • 10Park, S.H., Kang, Y., Kim, S.D., "Wavelet transform analysis of pressure fluctuation signals in a pressurized bubble column", Chem. Eng. Sci., 56, 6259-6265 (2001).

共引文献1

同被引文献34

  • 1焦利芳,李凤臣,苏文涛,杨治金,魏进家,宇波,王屹.表面活性剂减阻剂在集中供热系统中的应用试验研究[J].节能技术,2008,26(3):195-201. 被引量:27
  • 2Liberatore M W, Nettesheim F, Vasquez P A, et al. Microstructure and shear rheology of entangled wormlike micelles in solution [ J ]. Journal of Rheology, 2009,53 (2) : 441-458.
  • 3Arhuoma M, Dong M Z, Yang D Y, et al. Determination of water-in-oil emulsion viscosity in porous media [ J ]. Industrial & Engineering Chemistry Research, 2009, 48 (15) :7092-7102.
  • 4张成伟,魏进家,宇波,等.一种表面活性剂溶液流变性的影响因素[c].吉林:中国工程热物理学会多相流学术会议,2009.
  • 5Xu J Y, Wu Y X, Li H, et al. Study of drag reduction by gas injection for power-law fluid flow in horizontal stratified and slug flow regimes [ J ]. Chemical Engineering Journal,2009,147 (2/3) :235-244.
  • 6Eisa Al-Matroushi, Ali Borhan. Coalescence of drops and bubbles rising through a non-Newtonian fluid in a tube [ J ]. Interdisciplinary Transport Phenomena: Ann N Y Acad Sci,2009,1161:225-233.
  • 7Diego Gomez-Diaz, Jose M Navaza, L C Quintaus Riveiro, et al. Gas absorption in bubble column using a non-New-tonian liquid phase [ J ]. Chemical Engineering Journal, 2009,146( 1 ) :16-21.
  • 8马倩.非牛顿流体在环管中流动与换热特性的数值研究[D].南京:南京理工大学,2008.
  • 9Firouzi M, Hashemabadi S H. Extract solution of two phase stratified flow through the pipes for non-Newtonian Herschel-Bulkley fluids [ J ]. International Communications in Heat and Mass Transfer,2009,36 (7) :768-775.
  • 10殷谷良.关于非牛顿流体衰减性的一个注记.数学季刊,2009,24(1):69-74.

引证文献1

二级引证文献19

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