超临界CO2水平直管内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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Numerical simulation of convection heat transfer of supercritical carbon dioxide in horizontal straight tube
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1.School of Mechanical Engineering,Hebei University of Science and Technology,Shijiazhuang Hebei 050018;2.China

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    摘要:

    采用基于Fluent的数值模拟方法研究了超临界CO2在水平圆直管内的换热特性。主要探究了超临界CO2流体在管内冷却条件下的温度场及传热系数,并针对水平圆直管研究了制冷剂质量流量及进口温度对管内传热性能的影响。模拟结果表明,超临界CO2的传热系数随质量流量的增加而变大,质量流量增加100kg/m2.s,平均传热系数增加约为12%;随着制冷剂进口温度的增加,管内平均传热系数变小,但不会对局部传热系数的最大值产生影响,只会使局部传热系数的最大值延后。

    Abstract:

    The heat transfer performance of supercritical carbon dioxide in horizontal straight tube is conducted based on Fluent numerical simulation method. The temperature field and heat transfer coefficient of supercriticalcarbon dioxide fluid under in-tube cooling conditions are mainly investigated. The effects of mass flow rate and inlet temperature on heat transfer performance are studied for horizontal straight tubes. The simulation results show that the heat transfer coefficient of supercritical carbon dioxide increases with the increase of mass flow, the mass flow increases by 100kg/m2.s, and the average heat transfer coefficient increases by about 12%. With the increase of supercritical carbon dioxideinlet temperature, the inside of the tube The average heat transfer coefficient becomes small, but does not affect the maximum value of the local heat transfer coefficient, and only delays the maximum value of the local heat transfer coefficient.

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  • 收稿日期:2019-01-08
  • 最后修改日期:2019-02-07
  • 录用日期:2023-09-08
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