Flow of Non-Newtonian Fluids in Curved Pipes : Turbulent Flow

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A developing turbulent flow of power law fluids in the entrance region of curved pipes has been investigated by measuring an axial component of the mean and the fluctuating velocity with an optical fiber LDV under the condition of power index n>0.75, two curvature radius ratios R_C=10 and 30, and Reynolds numbers Re=10000〜33000. Turbulent flow develops more mildly than laminar flow, which leads to longer inlet length. A Reynolds stress equation model is applied to predict a fully developed turbulent flow. Numerical results are in moderate agreement with experimental results within the power index n=1〜0.9. In addition, an approximate expression for the turbulent friction coefficient is presented on the basis of the boundary layer theory.

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詳細情報 詳細情報について

  • CRID
    1572824502013525888
  • NII論文ID
    110002491524
  • NII書誌ID
    AA10680596
  • ISSN
    09148817
  • 本文言語コード
    en
  • データソース種別
    • CiNii Articles

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