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Flow and Loss of Newtonian Fluids in Pipes with an Axisymmetric Sudden Contraction

机译:轴对称突然收缩管道中牛顿流体的流动与损失

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摘要

A steady flow of an incompressible Newtonian fluid in pipelines with anaxisymmetric sudden contraction was studied in the range of 102"'104 of Reynoldsnumber by experiments on pressure drops and a theoretical analysis using thefinite difference methods. The main results obtained are as follows:(1) The sudden contraction loss decreases with increase in Reynolds numberand approaches a certain value at high Reynolds number. Besides, thesudden contraction loss has a kind of transition phenomenon at Reynoldsnumber equal to (2~4) x 103.(2) The numerical prediction of the pressure distribution at pipe wall in thedirection of flow does not agree with experimental results in higher Reynoldsnumber than about 103. This disagreement increases with increase inReynolds number.(3) The recovery distance of pressure due to sudden contraction lengthenswith increase in Reynolds number and the pressure gradient after recoverybecomes more gent1e.(4) 1n Reynolds number over about 103,the separation bubble is formed inthe downstream side of sudden contraction and it increases with increasein Reynolds number in the range of (103~104)of Reynolds number.
机译:通过压降实验和有限差分方法的理论分析,研究了轴对称突然收缩的不可压缩牛顿流体在轴对称“雷诺数”为102“'104范围内的稳定流动,得到的主要结果如下:(1 )突然的收缩损失随着雷诺数的增加而减小,并在高雷诺数下接近一定值;此外,突然的收缩损失在雷诺数等于(2〜4)x 103.时具有一种过渡现象。当雷诺数大于约103时,管壁沿流动方向的压力分布与实验结果不一致。随着雷诺数的增加,这种分歧增加。(3)突然收缩长度导致的压力恢复距离随雷诺数的增加而增大。 (4)1n雷诺数超过约103,分离气泡i s在突然收缩的下游形成,并在雷诺数(103〜104)的范围内随雷诺数的增加而增加。

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