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首页> 外文期刊>Experimental Thermal and Fluid Science: International Journal of Experimental Heat Transfer, Thermodynamics, and Fluid Mechanics >Friction losses of Newtonian and non-Newtonian fluids flowing in laminar regime in a helical coil
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Friction losses of Newtonian and non-Newtonian fluids flowing in laminar regime in a helical coil

机译:层流状态下螺旋线圈中流动的牛顿流体和非牛顿流体的摩擦损失

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摘要

This study aimed to carry out experimental work to determine, for Newtonian and non-Newtonian fluids, the friction factor (f_c) with simultaneous heat transfer, at constant wall temperature as boundary condition, in fully developed laminar flow inside a vertical helical coil. The Newtonian fluids studied were aqueous solutions of glycerol, 25%, 36%, 43%, 59% and 78% (w/w). The non-Newtonian fluids were aqueous solutions of carboxymethylcellulose (CMC), a polymer, with concentrations of 0.2%, 0.3%, 0.4% and 0.6% (w/w) and aqueous solutions of xanthan gum (XG), another polymer, with concentrations of 0.1% and 0.2% (w/w). According to the rheological study done, the polymer solutions had shear-thinning behavior and different values of viscoelasticity. The helical coil used has an internal diameter, curvature ratio, length and pitch, respectively: 0.00483. m, 0.0263, 5.0. m and 11.34. mm. It was concluded that the friction factors, with simultaneous heat transfer, for Newtonian fluids can be calculated using expressions from literature for isothermal flows. The friction factors for CMC and XG solutions are similar to those for Newtonian fluids when the Dean number, based in a generalized Reynolds number, is less than 80. For Dean numbers higher than 80, the friction factors of the CMC solutions are lower those of the XG solutions and of the Newtonian fluids. In this range the friction factors decrease with the increase of the viscometric component of the solution and increase for increasing elastic component. The change of behavior at Dean number 80, for Newtonian and non-Newtonian fluids, is in accordance with the study of Ali [4]. There is a change of behavior at Dean number 80, for Newtonian and non-Newtonian fluids, which is in according to previous studies. The data also showed that the use of the bulk temperature or of the film temperature to calculate the physical properties of the fluid has a residual effect in the friction factor values.
机译:这项研究旨在开展实验工作,以确定牛顿和非牛顿流体在壁面温度恒定为边界条件下同时传热的摩擦系数(f_c),该壁面温度在垂直螺旋形线圈内部充分展开的层流中。所研究的牛顿流体是25%,36%,43%,59%和78%(w / w)的甘油水溶液。非牛顿流体是浓度为0.2%,0.3%,0.4%和0.6%(w / w)的聚合物羧甲基纤维素(CMC)的水溶液以及另一种聚合物黄原胶(XG)的水溶液浓度为0.1%和0.2%(w / w)。根据所做的流变学研究,聚合物溶液具有剪切稀化行为和不同的粘弹性值。所使用的螺旋线圈的内径,曲率比,长度和螺距分别为:0.00483。 m,0.0263,5.0。 m和11.34。毫米结论是,可以使用等温流文献的表达式来计算牛顿流体的同时传热的摩擦系数。当基于广义雷诺数的Dean数小于80时,CMC和XG解决方案的摩擦因数与牛顿流体的摩擦因数相似。对于Dean数大于80的Dean数,其CMC和XG溶液的摩擦因数小于XG解决方案和牛顿流体。在此范围内,摩擦因数随溶液粘度成分的增加而降低,而随着弹性成分的增加而增加。对于牛顿流体和非牛顿流体,在迪安数为80时的行为变化与Ali的研究一致[4]。根据先前的研究,对于牛顿流体和非牛顿流体,在Dean数为80时行为发生了变化。数据还表明,使用整体温度或薄膜温度来计算流体的物理特性对摩擦系数值有残留影响。

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