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Experimental investigations on single-phase heat transfer enhancement with longitudinal vortices in narrow rectangular channel

机译:窄矩形通道内纵向涡流增强单相传热的实验研究

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摘要

Four pairs of rectangular block as longitudinal vortex generators (LVG) were mounted periodically in a narrow rectangular channel to investigate fluid flow and convective heat transfer respectively in the narrow rectangular channel with LVG and without LVG. Both the channels have the same narrow gap (d)=3 mm, the same hydraulic diameter (D_h)=5.58 mm and the same length to diameter ratio (L/D_h) = 80.65. The experiments were performed with the channels oriented uprightly and uniform heat fluxes applied at the one side of the heating plate and single-phase water was used as test fluid. The parameters that were varied during the experiments included the mass flow rate, inlet liquid temperature, system pressure, and heat flux.rnIn each of the experiments conducted, the temperature of both the liquid and the wall was measured at various locations along the flow direction. Based on the measured temperatures and the overall energy balance across the test section, the heat transfer coefficients for single-phase forced convection have been calculated. At the same time, in these experiments, the single-phase pressure drop across the channels was also measured. The correlations have been developed for mean Nusselt numbers and friction factors. Additionally, the visual experiments of infrared thermo-image recording the temperature on the outer wall of the heating plate have been conducted for validating the effects of LV.rnIn these experimental investigations, both laminar regime and turbulent regime were under the thermo-hydraulic developing conditions, laminar-to-turbulent transition occurred in advance with the help of LV when Reynolds numbers vary between 310 and 4220. In laminar regime, LV causes heat transfer enhancement of about 100.9% and flow resistance increase of only 11.4%. And in turbulent regime, LV causes heat transfer enhancement of above 87.1% and flow resistance increase of 100.3%. As a result, LV can obviously enhance heat transfer of single-phase water, and increase flow resistance mildly.
机译:将四对矩形块作为纵向涡流发生器(LVG)周期性地安装在一个狭窄的矩形通道中,以研究分别在有LVG和无LVG的狭窄矩形通道中的流体流动和对流传热。两个通道具有相同的窄间隙(d)= 3 mm,相同的液压直径(D_h)= 5.58 mm和相同的长径比(L / D_h)= 80.65。实验是在垂直放置的通道上进行的,均匀的热通量施加在加热板的一侧,单相水用作测试流体。在实验过程中改变的参数包括质量流速,入口液体温度,系统压力和热通量。rn在进行的每个实验中,沿着流动方向在各个位置测量液体和壁的温度。根据测得的温度和整个测试部分的整体能量平衡,已计算出单相强制对流的传热系数。同时,在这些实验中,还测量了通道中的单相压降。已经为平均努塞尔数和摩擦系数建立了相关性。此外,进行了红外热图像记录加热板外壁温度的视觉实验,以验证LV的影响。在这些实验研究中,层流状态和湍流状态均处于热液发展条件下,当雷诺数在310和4220之间变化时,借助LV提前发生了层流向湍流的转变。在层流状态下,LV引起的传热增强约100.9%,流阻仅增加11.4%。在湍流状态下,LV使传热增强87.1%以上,流阻增加100.3%。结果,LV可以明显增强单相水的传热,并适度增加流阻。

著录项

  • 来源
    《Nuclear Engineering and Design》 |2010年第1期|92-102|共11页
  • 作者单位

    Key Laboratory of Bubble Physics and Natural Circulation, Nuclear Power Institute of China, Chengdu 610041, China;

    Key Laboratory of Bubble Physics and Natural Circulation, Nuclear Power Institute of China, Chengdu 610041, China;

    Key Laboratory of Bubble Physics and Natural Circulation, Nuclear Power Institute of China, Chengdu 610041, China State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, Xi'an 710049, China;

    Key Laboratory of Bubble Physics and Natural Circulation, Nuclear Power Institute of China, Chengdu 610041, China;

    State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, Xi'an 710049, China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    A: heating area, A = BL(m~2); a: length of LVG(m); B: width of heating plate (m); b: width of LVG(m); C: constant; et al;

    机译:A:加热面积;A = BL(m〜2);a:LVG(m)的长度;B:加热板宽度(m);b:LVG(m)的宽度;C:常数;等;

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