圆台型螺旋能量桩换热特性的模拟分析与验证

    Simulation analysis and verification of heat transfer characteristics of truncated cone helix energy pile

    • 摘要: 为了减少地源热泵的热干扰、提高其换热效率,该文提出了一种新型"圆台型螺旋能量桩(truncated cone helix energy pile,CoHEP)"。同时为了更加准确地模拟新型圆台型螺旋能量桩的换热特性,综合考虑初始土壤温度的不均匀性和土壤上表面动态边界条件,建立了三维数值模型,分析了不同锥角下圆台型螺旋能量桩的换热特性。结果表明:圆台型螺旋能量桩沿水流方向可以分成4个换热阶段:入口阶段→热短路阶段→小温差阶段→出口阶段。圆台型螺旋能量桩的底部热干扰现象较为严重,且锥角越大,底部热干扰越明显。相反,由于顶部螺旋半径较大,热干扰效应较弱。圆台型螺旋能量桩的单位管长换热量随着锥角的增加而线性增大,当系统运行时间为12 h时,锥角从0增加到10?再增加到20?,单位管长换热量增长率分别为2.54%和3.53%。新型圆台型螺旋能量桩单位管长换热量大于传统圆柱型螺旋能量桩,20?锥角条件下的单位管长换热量比传统圆柱型螺旋能量桩高了约6.16%。通过对新型圆台型螺旋能量桩的换热特性进行探析,相对于传统圆柱型螺旋能量桩,提升了换热效率,同时为后续的推广应用和工程设计奠定了理论基础。

       

      Abstract: Abstract: In order to reduce the thermal interference and to improve the heat transfer efficiency, a novel "truncated cone helix energy pile (CoHEP)" was proposed in this study. And in order to simulate the thermal performance of the novel CoHEP more accurately, a three-dimensional numerical model was established with consideration of the inhomogeneous initial soil temperature and the dynamic boundary condition above the soil surface. The heat transfer characteristic of the novel CoHEP of different cone angles was studied. In addition, in order to verify the accuracy of the numerical model, a verification test was conducted. The results showed that the novel CoHEP can be divided into four heat transfer stages along the flow direction: entrance stage → thermal short circuit stage → small temperature difference stage → exit stage. Among them, the heat transfer capacity of the entrance stage was the strongest, and the heat transfer capacity continued to decrease during the thermal short circuit stage and the small temperature difference stage, eventually the heat transfer capacity rebounded during the exit stage. The thermal interference at the bottom of the CoHEP was more serious, and the larger the cone angle, the more serious the thermal interference at the bottom. In contrast, the thermal interference effect was weaker at the top of the CoHEP due to the larger helix radius at the top. The heat flux per unit pipe length of the CoHEP increased linearly with the increase of cone angle. That was because with the same pipe length (Lpipe), pitch in the depth direction (b) and energy pile height (hpipe), increasing the cone angle would increase the top radius (rt) of the CoHEP, leading to small thermal interference in the upper part of the CoHEP. At the same time, more high-temperature fluid was located in the upper part of the CoHEP which directly contacted with the covered soil area. Thus the heat transfer capacity increased. When the system operating time was 12 h, the cone angle increased from 0? to 10? to 20?, the increasing rate of the heat flux was 2.54% and 3.53%, respectively. The thermal interference in the upper part of the novel CoHEP was much smaller than that of the traditional CyHEP, and more high-temperature fluid was located in the upper part of the energy pile which was good for heat transfer. In addition, the distance between the adjacent pipes in the axial direction (d) of the novel CoHEP was significantly larger than that of the traditional CyHEP under the same pitch in the depth direction (b), which can effectively reduce the axial thermal interference. Thus the heat flux per unit pipe length of the novel CoHEP was greater than the traditional CyHEP. And when the cone angle was 20?, the heat flux per unit pipe length of the novel CoHEP was 6.16% higher than that of the traditional CyHEP.

       

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