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Flow and Heat Transfer in a Simple Trapezoidal Minichannel Flow System

机译:简单梯形小通道流动系统中的流动和热传递

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Incompressible flow through a minichannel system have been considered in the present study. The channel considered has a trapezoidal cross-section, the height of the cross-section being equal to the average width of the cross-section. The flow enters the channel with a uniform velocity and passes through a straight channel section that has a length that is 30 times the mean channel width. The flow then passes around a 90obend.Following the bend,the flow passes down another straight channel which also has a length of 30 times the mean channel width.A uniform heat flux is applied over the entire surface of the duct.The flow geometry does not represent any that is likely to occur in minichannel system applications but is adequate for the evaluation of the assumptions of- ten adopted regarding pressure losses,and heat transfer rates in real systems.It has been assumed that the flow is steady,that the flow is incompressible and that there is no slip on the channel walls.The governing equations have been written in dimensionless form.Solutions to these dimensionless governing equations have obtained using a commercial finite-element software package,FI- DAP.The solution has the following parameters: the Reynolds number,Re,the Prandtl number, P r,the ratio of the width of the lower surface A of the duct to the width of the upper surface A and the dimensionless radius of the bend Ri.Results are only presented for P r=0.7.Re values be- tween 3 and 300,A values between 1 and 1.5 and R_i values between 0.5 and 1.5 have been consid- ered.The effects of the governing parameters on the pressure losses,flow development lengths and heat transfer rates have been studied.
机译:在本研究中已经考虑了通过微通道系统的不可压缩流动。所考虑的通道具有梯形的横截面,该横截面的高度等于该横截面的平均宽度。流体以均匀的速度进入通道,并通过长度为平均通道宽度30倍的直通道部分。然后,气流绕90度弯曲。弯曲之后,气流沿着另一个直通道向下流动,该直通道的长度也为平均通道宽度的30倍。在管道的整个表面上施加均匀的热通量。不能代表任何可能在微通道系统应用中发生的现象,但足以评估在实际系统中采用的关于压力损失和传热速率的十种假设。已经假设流量稳定,流量该控制方程以无量纲形式编写。使用商业有限元软件包FI-DAP获得了这些无量纲控制方程的解。该解决方案具有以下参数: :雷诺数,Re,普朗特数,P r,导管下表面A的宽度与上表面A的宽度之比与be的无因次半径仅在P r = 0.7时才给出结果。考虑了Re值在3到300之间,A值在1到1.5之间,R_i值在0.5到1.5之间。控制参数对压力的影响已经研究了损失,流动发展长度和传热速率。

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