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Numerical investigation of the heat and mass transfer performance of a two-phase closed thermosiphon based on a modified CFD model

机译:基于改进的CFD模型的两相闭虹吸管热输出性能的数值研究

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A modified CFD model was developed to investigate the heat and mass transfer performance of a two-phase closed thermosiphon (TPCT). In this model, the phase-change temperature of the working fluid was considered to be dependent on the local pressure. Meanwhile, an auto-adjust and control strategy was established for the condensation mass transfer time relaxation parameter, which could balance the phase-change pressure to the working pressure. The modified phase-change model was verified by experiments and then used to investigate the heat and mass transfer behaviors of the TPCT under different heat flux of 12.31-15.95 kW/m2. The results indicated that the maximum relative errors of wall temperature and working pressure of the TPCT were 0.25-0.48% and 0.14-0.46%, respectively. The wall temperature gradually decreases from the bottom of evaporator to adiabatic section, and then increases from the bottom to the top of the condenser due to the temperature difference between the inlet and outlet of the cooling water. Also, as the heat flux increase, the overall thermal resistance reduces from 0.060 to 0.055 K/W. These results indicate that the proposed model can be used to predict the heat and mass transfer of the TPCT.
机译:开发了一种改进的CFD模型,以研究两相封闭热虹吸管(TPCT)的热量和传质性能。在该模型中,将工作流体的相变温度被认为取决于局部压力。同时,为冷凝质量传递时间弛豫参数建立了自动调整和控制策略,这可能会使相变压平衡到工作压力。通过实验验证改性相变模型,然后用于研究TPCT在不同热通量下的TPCT的热量和传质行为为12.31-15.95 kW / m 2。结果表明,TPCT的壁温和工作压力的最大相对误差分别为0.25-0.48%和0.14-0.46%。壁温从蒸发器的底部逐渐减小到绝热部分,然后由于冷却水的入口和出口之间的温差,从冷凝器的底部增加到顶部。而且,随着热通量增加,总热阻从0.060℃降低至0.055 k / w。这些结果表明,所提出的模型可用于预测TPCT的热量和传质。

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