超临界水在套管换热器中的流动传热试验研究

Investigation of flow and heat transfer of supercritical water in double-pipe heat exchanger

  • 摘要:
      目的  超临界流体流动换热具有复杂性,已有的研究大多是基于定壁面温度或者定热流边界条件,而工程实际中多为变热流密度条件下的耦合流动换热。为深入了解相关机理,对超临界流体在套管换热器内的耦合流动传热规律进行深入研究。
      方法  设计套管换热器试验段,通过在内、外侧管布置温度、压力测点,采集温度压力数据,分析超临界水在套管换热中的流动与传热特性。
      结果  试验分析结果表明,临界点附近物性参数的巨大变化,是导致超临界水换热出现不同于平常换热现象的主要原因;传热段的温度梯度和热物性变化使得峰值换热系数温度与拟临界温度存在差异,且差异随着压力的增加而增大;当主流温度低于拟临界温度时,由于浮力效应同时减小,外管换热系数随内管入口温度的升高而增大;而当主流温度高于拟临界温度时,由于浮力效应不显著,浮力效应几乎与内管入口温度无关。
      结论  研究结果对换热器的设计以及超临界流体在套管换热器中耦合流动传热的研究和机理分析具有一定的指导意义。

     

    Abstract:
      Objective  The flow and heat transfer of supercritical fluid is complex, and most of the existing research is based on the conditions of constant wall temperature and constant heat flux. However, in practical engineering, heat transfer often occurs under the conditions of variable heat flux. In order to better understand the relevant performance, this paper studies the coupled flow and heat transfer of supercritical fluid in a double-pipe heat exchanger.
      Method  The experimental section of this paper focuses on a double-pipe heat exchanger. The flow and heat transfer characteristics of supercritical water in the double-pipe heat exchanger are analyzed by collecting temperature and pressure data from the temperature and pressure measuring points arranged on the inside and outside of the double pipe.
      Results   The experimental results show that great changes in physical parameters near pseudo-critical points are the main reasons for the phenomenon of supercritical water heat transfer, and they differ from those of ordinary heat transfer. There is a difference between the peak heat transfer coefficient temperature and pseudo-critical temperature which increases with the increase of pressure. This phenomenon is caused by the temperature gradient and variations in thermal-physical properties in the heat transfer section. The heat transfer coefficient of the outer pipe increases with the increase in water temperature at the inlet of the inner pipe when the mean bulk temperature is lower than the pseudo-critical temperature due to the buoyancy effect decreasing at the same time, while the buoyancy effect is almost independent of the water temperature at the inlet of the inner pipe when the mean bulk temperature is higher than the pseudo-critical temperature and the buoyancy effect is non-significant.
      Conclusion  The results can provide valuable references for the design of double-pipe heat exchangers and research and mechanism analysis of the coupled flow and heat transfer of supercritical fluid in double-pipe heat exchangers.

     

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