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Isothermal flow distribution in coupled manifolds: comparison of results from cfd and an integral model

机译:耦合歧管中的等温流动分布:cfd和积分模型的结果比较

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Isothermal, incompressible flow distribution in the coupled manifold continues to be of interest to the industrial, engineering, and scientific communities. Several investigations carried out in the past have considered the suitability of a CFD code (Fluent) for predicting detailed velocity and pressure distributions for three dimensional dividing flow in a 90 deg tee junction. Results from these cast doubt on the successful use of CFD to model the complex flow in a tee. The focus of the present work is to determine if the same code can accurately predict the larger scale features of three dimensional branching flows and in a coupled manifold having three risers. Simulations were performed for flow in the coupled manifold and for both laminar and turbulent, dividing and combining flow in a tee section for a brad range of fow branching conditions. The ratio of riser diameter to manifold diameter is fixed at 0.75 for this study. The turbulent models used are the standard and renormalization group k- epsilon models. All constants in tehse models are set tto their respective default values. Static pressure re-gain factors are calculated from the results of CFD simulations nad are favorably compared with the data of others. These data are then used in an existing integral model for flow in coupled manifolds. The good agreement between the results from the integral model and the CFD model for flow in the coupled manifold attests to the suitabliity of the integral model for this problem. The advantage of the integral approach is the speed at which the problem can be solved by the computer, and the fact that there is no need for the time-consuming and expensive geometrical modeling and mesh generation normally associated with finite element and finite difference models.
机译:等温,不可压缩流在耦合歧管中的分布仍然是工业界,工程界和科学界所关注的。过去进行的一些研究已经考虑了CFD代码(Fluent)是否适合预测90度三通中三维分流的详细速度和压力分布。这些结果使人们对成功使用CFD建模三通中的复杂流动产生怀疑。本工作的重点是确定同一代码是否可以准确地预测三维分支流以及在具有三个立管的耦合歧管中的较大尺度特征。针对流分支条件的大范围变化,对耦合歧管中的流动以及层流和湍流进行了模拟,对三通段中的流动进行了分流和合并。对于本研究,立管直径与歧管直径之比固定为0.75。所使用的湍流模型是标准和重归一化组k-ε模型。这些模型中的所有常量均设置为各自的默认值。从CFD模拟的结果计算出静压恢复系数,并将其与其他数据进行比较。这些数据然后在现有的集成模型中用于耦合歧管中的流量。积分模型和CFD模型在耦合歧管中流动的结果之间的良好一致性证明了积分模型对于此问题的适用性。积分方法的优点是计算机可以解决问题的速度,并且不需要通常与有限元和有限差分模型关联的耗时且昂贵的几何建模和网格生成这一事实。

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