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Heat transfer characteristic of water at near critical pressure in circumferentially non-uniformly heated vertical tubes

机译:水在接近临界压力下在周向不均匀加热的垂直管中的传热特性

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摘要

Experiments on heat transfer and characteristic of water in circumferential non-uniformly heated, vertical up flow tube at near critical pressure have been carried out at Xi'an Jiaotong University. The wall temperature and heat flux distribution along the cross section of the tube were obtained in the experiments. The critical heat flux, critical mass flow rate and critical mass quality have been analyzed. The effect of the heating method on the heat transfer characteristic has also been obtained. Experimental conditions included pressures of 19-22 MPa, mass flow velocities of 600-1200 kg/m~2 s, and heat fluxes of 200-600 kW/m~2. The experimental results showed that, for the non-uniformly heated tube, film boiling and nucleate boiling can coexist simultaneously at the different sides of one cross section of the tube when heat transfer deterioration occurs at high flux side. When the heat transfer deterioration occurs, the local critical peak heat flux of the non-uniformly heated tube and the critical heat flux of the uniformly heated tube are almost the same. So, the heat transfer deterioration is caused by the local heating condition of the non-uniformly heated tube. The minimum heat transfer coefficient of the non-uniformly and of the uniformly heated vertical tubes differs only a little when heat transfer deterioration occurs. Finally, the experimental correlations used to calculate the critical heat flux and the minimum heat transfer coefficient were given.
机译:西安交通大学已经进行了在接近临界压力的周向非均匀加热的垂直上升流管中水的传热和水特性的实验。在实验中获得了沿管横截面的壁温和热通量分布。分析了临界热通量,临界质量流量和临界质量。还已经获得了加热方法对传热特性的影响。实验条件包括压力为19-22 MPa,质量流速为600-1200 kg / m〜2 s,热通量为200-600 kW / m〜2。实验结果表明,对于不均匀加热的管,当在高通量侧发生传热恶化时,膜沸腾和核沸腾可同时存在于该管的一个横截面的不同侧。当发生传热恶化时,非均匀加热管的局部临界峰值热通量与均匀加热管的临界热通量几乎相同。因此,传热恶化是由加热不均匀的管的局部加热条件引起的。当发生传热恶化时,非均匀加热和垂直加热的垂直管的最小传热系数仅略有不同。最后,给出了计算临界热通量和最小传热系数的实验相关性。

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