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首页> 外文期刊>Journal of Fluids Engineering: Transactions of the ASME >Friction factor in U-type undulated pipe flow
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Friction factor in U-type undulated pipe flow

机译:U型波纹管流动中的摩擦系数

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摘要

Measurements of pressure losses in a U-type undulated hydraulically smooth wall pipe, having constant radius curvature, are presented. The effect of the dimensionless curvature radius 2R/d on the Darcy friction factor was investigated in the range of the Reynolds number from about 50 to 10,000 and for the dimensionless pipe curvature radiuses 2R/d = 6.62, 7.95, 11.13, 16.03, 22.58, and 27.85. A smooth transition from laminar to turbulent region in the friction factor versus Reynolds number plot, typical for curved pipe flows, was observe. The experimental data were correlated with the relatively simple equation using new Dean number De(n) = Re* (De(n) = Re*(d/2R): ln(f(w)* Re/64) = a + b(ln (De(n)))(2), which is not valid for larger values of De(n) and 2R/d, e.g., for De(n)>200 at 2R/d = 22.58, and for De(n)>70 at 2R/d = 27.85. The new Dean number, below which the influence of the pipe curvature in comparison to the straight tube was not seen, is De(n)less than or equal to similar to3. [S0098-2202(00)02802-9]. [References: 11]
机译:介绍了具有恒定半径曲率的U型起伏的液压光滑壁管中压力损失的测量结果。研究了在约50至10,000的雷诺数范围内无量纲曲率半径2R / d对达西摩擦系数的影响,并且对于无量纲管曲率半径2R / d = 6.62、7.95、11.13、16.03、22.58,和27.85。在摩擦因数对雷诺数图中,观察到了从层流到湍流区域的平滑过渡,这对于弯管流动是典型的。使用新的Dean数De(n)= Re *(De(n)= Re *(d / 2R):ln(f(w)* Re / 64)= a + b将实验数据与相对简单的方程式相关(ln(De(n)))(2),对于较大的De(n)和2R / d值无效,例如,对于在2R / d = 22.58时De(n)> 200,对于De( [S0098-n] n)> 70,在2R / d = 27.85时,新的Dean值小于或等于3,低于该值,则看不到管曲率相对于直管的影响。 2202(00)02802-9]。[参考:11]

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