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Enhanced Condensation Outside Horizontal Heat Transfer Tubes

机译:水平传热管外的强化冷凝

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摘要

Experimental investigation of heat transfer and friction characteristics was conducted on the out side of horizontal carbon steel heat transfer tubes under the pressure of saturated vapour 0.04MP (gauge pressure). The test tubes included spiral-grooved tubes, corrugated tube and smooth tube. The use of water as test fluids has allowed to cover a wide range of turbulent fluid flow conditions: Reynolds number from 1 x 104 to 5×104. The heat transfer coefficients and amount of vapour condensation of spiral-grooved tube with different structure parameters are measured. The spiral-grooved tube has the best heat transfer performance compared with corrugated tube and smooth tube. The maximum heat transfer coefficients and amount of vapour condensation of spiral -groove tube is respectively 2.32 and 1.72 times as smooth tube. The maximum ηof spiral groove tube as comprehensive performance evaluation is 1.86. The corrugated tube increase heat transfer coefficients only in the Reynolds numbers lower than 1.5×104, but lower than spiral groove tube, and transfer performance is worse than smooth tube with the Reynolds numbers grow. The structure parameters influence on spiral-grooved tube performance results show that the deeper of the groove, the better heat-exchange performance with the drag coefficient increased in the same Reynolds numbers. And the greater the fin pitch and trough radius, the poorer the heat exchange effectiveness with the drag coefficient decreased.
机译:在水平蒸汽0.04MP(表压)的作用下,在水平碳钢传热管的外侧进行了传热和摩擦特性的实验研究。试管包括螺旋槽管,波纹管和光滑管。使用水作为测试流体可以覆盖各种湍流条件:雷诺数从1 x 104到5×104。测量了不同结构参数的螺旋槽管的传热系数和水蒸气凝结量。与波纹管和光滑管相比,螺旋槽管具有最佳的传热性能。螺旋槽管的最大传热系数和蒸汽冷凝量分别是光滑管的2.32和1.72倍。综合性能评估,螺旋槽管的最大η为1.86。波纹管仅在雷诺数小于1.5×104的情况下增加传热系数,但比螺旋槽管低,并且随着雷诺数的增加,传热性能差于光滑管。结构参数对螺旋槽管性能的影响表明,在相同的雷诺数下,随着阻力系数的增加,槽越深,热交换性能越好。翅片的螺距和谷底半径越大,则随着阻力系数的减小,换热效果越差。

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