扭曲椭圆管内超临界CO2冷却换热的数值模拟
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河北科技大学机械工程学院

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TB657.5;TK12

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河北省自然科学基金项目(E2014208005


Numerical Simulation of Cooling Heat Transfer of Supercritical Carbon Dioxide in Twisted Elliptical Tubes
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China

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    摘要:

    基于Fluent的数值模拟方法研究了不同质量流量下扭距为100mm及无扭曲状态下的水平椭圆管管内超临界CO2冷却换热特性及二次流的变化规律。并针对竖直椭圆管引入局部换热系数和压降研究了长短轴比及扭矩对扭曲管换热性能的影响。模拟结果表明,低质量流量下扭曲椭圆管内浮升力的作用明显大于椭圆管扭曲结构的作用,对于低质量流量 下的超临界CO2流体时,椭圆管具有更大强度的浮升力所造成的二次流,强化传热更明显;对于高质量流量 下的超临界CO2流体时,扭曲椭圆管具有更大强度自身结构所产生的周期性二次流,强化传热;管内的传热系数及压降随着扭曲程度及压扁程度的增大而增大。

    Abstract:

    The cooling heat transfer performance and change regulation of secondary flow of supercritical CO2 whose mass flow rate varies are studied in horizontal elliptical tube whose torque is 100mm or one infinity number based on Fluent. And the influence of axial ratio and torque of twisted elliptical tube on the heat transfer performance is studied. Simulation results show that, the effect of buoyancy on the twisted elliptical tube is significantly larger than that of elliptical tube under low mass flow, for the elliptical tube when supercritical CO2 is under the low mass flow , the elliptical tube has a greater intensity of secondary flow caused by buoyancy, and the enhanced heat transfer is more pronounced, when supercritical CO2 is under the high mass flow , the twisted elliptical tube has a greater intensity of periodic secondary flow caused by self-structure, and the enhanced heat transfer is more pronounced. The heat transfer coefficient and pressure drop increase with the degree of twist and flattening.

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  • 收稿日期:2018-03-02
  • 最后修改日期:2018-03-30
  • 录用日期:2023-08-21
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