缩放管内插旋流片对水与油介质复合传热强化规律的研究
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摘要
本论文采用数值模拟和实验研究相结合的方法以水、50%甘油和85%甘油为传热工质,分别对光滑管和缩放管插入2种不同结构形式旋流片的局部流阻与传热性能进行了数值模拟研究,对不同管内流体介质的温度场和速度场进行了对比分析探讨。结果表明:
在水为流动介质高湍流(15000缩放管内插旋流片使得管道流体产生了强烈的漩涡流,旋流片产生的自旋流在旋流片下游18倍管径处消失;在有旋流片的一段管道中传热系数Nu和阻力系数都达到最大值,但是由于阻力的增加幅度远大于传热量的提高幅度使得有旋流片的一段管道中综合传热性能很差为0.55,最大值在旋流片下游产生约为1.23。整体综合传热因子小于1,为0.89。所以管内插旋流片在高度湍流条件下综合传热性能不理想的主要原因是:有旋流片的一段产生了太高的形体阻力和旋流片产生的自旋流在下游迅速衰减结束。
在50%甘油为流动介质过度流(3000缩放管内间隔插入旋流片的局部流阻与传热性能与介质水的情况相似。但是旋流片产生的自旋流在旋流片下游约15倍管径处消失,有旋流片一段管道的综合传热性能得到很大的改善为0.8,综合传热性能评价因子j的峰值为1.38。从总体而言传热综合性能提高1.08。在85%甘油为流动介质层流(400 综上所述,缩放管内插旋流片对液体进行复合强化传热,在Re大于15000的湍流条件下综合传热性能不理想,综合传热性能小于1;在过渡流条件下综合传热性能超过1,但强化的幅度小于10%;在层流的条件下综合传热性能超过1,且强化的幅度大于18%。不同结构旋流片强化传热性能的比较显示出:旋转角为270度的旋流片在提高换热系数的同时带来了更大的形体阻力,其综合传热性能不如旋转角为180度的旋流片。层流条件下,由于管内流体的传热系数的提高幅度大于阻力系数的增加量使得缩放管内插旋流片复合强化传热方式更适用于传热介质在低雷诺数下的流动状态。
In this paper, the combining methods of numerical simulation and experimental study were used. Respectively with water, 50% glycerol and 85% glycerol as the heat transfer working fluid, the local flow resistance and heat transfer performance of smooth tube and converging-diverging tube with 2 different twisted-tapes inserted were studied in numerical simulation method. At the same time, both temperature field and velocity field of different pipes fluid mediums were compared and analyzed. The results show that at the condition of high turbulence (15000 Under the condition of 50% glycerol as the flow fluid medium with low turbulent (3000 In summary, the use of twisted tapes for the liquid to enhance heat transfer, comprehensive heat transfer performance is at 0.89 which duces poor heat transfer. Integrated under the transitional flow, the result of enhance heat transfer is better, but the enhanced rate less than 10%. Laminar flow conditions in the integrated heat transfer is best, and the enhanced rate of is greater than 18%.mparison performance of enhanced heat transfer capability of different structure twisted-tapes shows that the rotation angle of 270 degrees swirl chip at the same time increases the heat transfer coefficient has brought a greater physical resistance to flow fluid, which Heat transfer performance is not as good as 180-degree rotation angle of swirl tapes. In laminar flow, because the heat transfer coefficient increased in magnitude is greater than the increased in the amount of drag coefficient, the method of compound heat transfer enhancement of a converging-diverging tube with regularly spaced twisted-tapes is more suitable for the heat transfer medium fluid flowing at low Reynolds number condition.
在水为流动介质高湍流(15000
在50%甘油为流动介质过度流(3000
In this paper, the combining methods of numerical simulation and experimental study were used. Respectively with water, 50% glycerol and 85% glycerol as the heat transfer working fluid, the local flow resistance and heat transfer performance of smooth tube and converging-diverging tube with 2 different twisted-tapes inserted were studied in numerical simulation method. At the same time, both temperature field and velocity field of different pipes fluid mediums were compared and analyzed. The results show that at the condition of high turbulence (15000
引文
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