首页> 外文会议>ASME summer heat transfer conference;HT2009 >CFD INVESTIGATION INTO THE FLOW FIELD IN A FOUR ROW STAGGERED PLATE FIN-AND-TUBE HEAT EXCHANGER EXPERIENCING GROSS FIN-SIDE FLOW MALDISTRIBUTION USING THE K-ω TURBULENCE MODEL
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CFD INVESTIGATION INTO THE FLOW FIELD IN A FOUR ROW STAGGERED PLATE FIN-AND-TUBE HEAT EXCHANGER EXPERIENCING GROSS FIN-SIDE FLOW MALDISTRIBUTION USING THE K-ω TURBULENCE MODEL

机译:使用K-ω湍流模型对四行交错板翅片和管式换热器中的流场进行CFD研究

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The flow field in a section of a four-row staggered plate fin-and-tube heat exchanger with gross inlet flow maldistribution has been investigated using CFD modelling. The commercial CFD code Fluent 6.3 has been used to carry out 3D unsteady flow modelling using the low Reynolds number variation of the standard k-ω turbulence model. A significant amount of flow dispersion is shown to occur upstream of the heat exchanger inlet resulting in a 37 % reduction in inlet velocity before the flow enters the heat exchanger. Flow dispersion as the fluid passes through the heat exchanger results in a further 28 % reduction in the average flow velocity. Significant sections of the heat exchanger experience angled flow resulting in a flow pattern commonly seen in inline tube arrangements. The lower friction factor of the inline flow regime results in a higher mass flux when compared to areas exhibiting the staggered flow regime. This variation results in off-centre velocity peaks entering and leaving the heat exchanger. On average the non-uniform flow cases resulted in a 29.4 % increase in pressure drop across the heat exchanger system when compared to uniform flow conditions. Average heat transfer coefficients for the non-uniform flow conditions showed a 20.3 % increase over uniform flow conditions of equal mass flow.
机译:使用CFD模型研究了总行流量分布不均的四排交错板翅片管式换热器截面中的流场。商业CFD代码Fluent 6.3已用于使用标准k-ω湍流模型的低雷诺数变化来进行3D非稳态流动建模。大量的流动分散显示在热交换器入口的上游,导致流体进入热交换器之前入口速度降低了37%。流体通过热交换器时的流量分散会导致平均流速进一步降低28%。热交换器的重要部分经历了成角度的流动,从而形成了在直列式管道布置中常见的流动模式。与表现出交错流动状态的区域相比,在线流动状态的较低摩擦系数会导致较高的质量通量。这种变化导致偏心速度峰值进入和离开热交换器。与均匀流动条件相比,非均匀流动情况平均导致整个热交换器系统的压降增加29.4%。非均匀流动条件下的平均传热系数比等质量流量的均匀流动条件下增加了20.3%。

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