共查询到19条相似文献,搜索用时 187 毫秒
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以去离子水和质量分数为0.3%的水基纳米流体为工质,在当量直径为1.241mm的矩形微通道内进行了两相流流动沸腾的实验研究,并借助高速摄像仪对矩形微通道内流型随着质量流量及热流密度的变化进行了观察分析。实验结果表明:单位长度上的两相摩擦压降会随着质量流速的提升而提高;单位长度上的两相摩擦压降会随着热流密度的增大而升高;减小质量流速和提高其热流密度均会加快气泡的产生并提高气泡的脱离直径,当热流密度增大到一定程度时,通道内几乎为环状流与液态单相流交替出现,且环状流占周期中的较长时间。 相似文献
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微通道流动沸腾冷却技术兼具相变潜热和微尺度效应的诸多优点,是解决微电子器件热致失效问题的重要方法之一. HFE-7100是一种安全环保的电子氟化液,特别适用于微电子器件的冷却.本文在水力直径为0.5 mm的矩形平行微通道内,对HFE-7100的流动沸腾传热和两相流动特性进行了实验研究,测量范围为常压下质量流率88.9—277.8 kg·m–2·s–1、入口过冷度20.5—35.5℃和有效热流密度12—279 kW·m–2.本文分析了质量流率、入口过冷度、有效热流密度和干度对传热系数和压降的影响,发现在较低的入口过冷度下HFE-7100出现了沸腾迟滞现象,且增大入口过冷度和质量流率会延缓沸腾起始点的发生,且会提高传热系数和临界热流密度.两相压降受有效热流密度影响较大,且在定干度下不同质量流率的两相压降在塞状流和环状流阶段有明显差异.同时,通过观测两相流型,对流动沸腾传热现象进行了分析.本文还将两相压降实验数据与文献关联式预测值进行了对比,与Lockhart提出的关联式预测值偏差为19.6%.本文研究结果可为微电子器件散热设... 相似文献
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为考察基于矩形平行细小槽道的压降及传热的综合性能,实验测试了去离子水流过三种不同截面尺寸的平行细小槽道热沉的流动与传热特性,槽道截面尺寸分别为1mm×1mm、0.5mm×1mm、0.5mm×1.2mm,表面热流密度为5.6~33.3W/cm2,工质流量为0.3~5L/min。实验测量了压降及对流换热系数随流量变化关系;综合分析了三种热沉的压降-温度随流量变化规律;得出了细小槽道热沉在给定流量范围内,表面温度为70℃时的极限热流密度。实验结果表明:随着流量增加,表面温度与压降呈相反变化趋势,存在一个最佳工况点,该工况点处的工质流量随热流密度增加而增大;文中所设计的热沉在工质流量为1.3~4.75L/min,表面温度控制在70℃时所能承受的极限热流密度为70W/cm2,此时压降约为170kPa。 相似文献
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以去离子水为工质,对高为2mm,宽分别为0.3mm、0.6mm、2mm的矩形微槽中的两相传热特性与流动阻力特性进行了实验与理论研究。实验结果表明,三种微槽的饱和沸腾传热系数随着热流密度的增加而增加,并对三种微槽传热系数随热流密度关系的实验数据进行了拟合,得出了实验条件下的传热系数与热流密度的关联式及相同热流密度或者质量流速下槽道尺寸对传热系数的影响;此外,矩形微槽道压降△p随着尺寸的减小而增大。 相似文献
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微通道内的沸腾两相流动是解决高热流密度下微电子设备散热最有潜力的手段之一。本文基于逆流式微通道热沉设计,实验研究了不同流量调配下逆流式微通道内的流动沸腾特性。讨论了流量分配对微通道内流动沸腾过程中传热特性、压降分布和壁面温度演化规律的影响。实验结果表明:当逆流式通道两侧的质量流量相同时,壁面呈现较好的温度均匀性,且两侧流动压降基本保持一致。两侧流量相差越大,其对应最大两相压降偏差越大。逆流式微通道的壁面温度分布和局部热点的位置可以通过改变两侧质量流量的大小实现有效控制。同时,微通道内流体的演化周期同样可以根据两侧质量流量的高低实现调控。 相似文献
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This study reports an experimental investigation of evaporative heat transfer and pressure drop of R-134a flowing downward inside vertical corrugated tubes with different corrugation pitches. The double tube test section is 0.5 m long with refrigerant flowing in the inner tube and hot water flowing in the annulus. The inner tubes are comprised of one smooth tube and three corrugated tubes with different corrugation pitches of 6.35, 8.46, and 12.7 mm. The test runs are performed at evaporating temperatures of 10°C, 15°C, and 20°C; heat fluxes of 20, 25, and 30 kW/m2; and mass fluxes of 200, 300, and 400 kg/m2s. The experimental data obtained from the smooth tube are plotted with flow pattern map for vertical flow. Comparisons between smooth and corrugated tubes on the heat transfer and pressure drop are also discussed. It is observed that the heat transfer coefficient and frictional pressure drop obtained from the corrugated tubes are higher than those from the smooth tube. Furthermore, the heat transfer coefficient and frictional pressure drop increase as the corrugation pitch decreases. The maximum heat transfer enhancement factor and penalty factor are up to 1.22 and 4.0, respectively. 相似文献
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Flow boiling pressure drop and flow instabilities of Ω-shaped reentrant copper micro-channels were experimentally explored. Tests were conducted in deionized water and ethanol at inlet subcoolings of 10°C and 40°C, mass fluxes of 125–300 kg/m2·s, and a wide range of heat fluxes and exit vapor qualities. The operational parameters effects, i.e., heat flux, mass flux, inlet subcooling, and coolants, on pressure drop and flow instabilities were systematically explored. The two-phase pressure drop of reentrant micro-channels were found to generally increase monotonically with increasing heat fluxes and exit vapor qualities. Nevertheless, the roles of mass flux and inlet subcooling were dependent on the test coolant. 相似文献
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In this study, heat transfer coefficients and pressure drops of R-134a inside round and flat tubes are investigated experimentally with mass flux of 450, 550, and 650 kg m?2 s?1 at saturation temperatures of 35°, 40°, and 45°C. The effects of mass flux and saturation temperature on heat transfer coefficient and pressure drop are examined. The maximum enhancement factor and pressure drop penalty are obtained by flat tube (FT-2) up to 2.101 at 450 kg m?2 s?1 and 3.01 at 650 kg m?2 s?1, respectively. The correlation for flat tubes is proposed to predict the heat transfer coefficient within ±20% error. 相似文献
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This article directly investigates the effect of a cooling medium's coolant temperature on the condensation of the refrigerant R-134a. The study presents an experimental investigation into condensation heat transfer, vapor quality, and pressure drop of R-134a flowing through a commercial annular helicoidal pipe under the severe climatic conditions of a Kuwait summer. The quality of the refrigerant is calculated using the temperature and pressure obtained from the experiment. Measurements were performed for refrigerant mass fluxes ranging from 50 to 650 kg/m2s, with a cooling water flow Reynolds number range of 950 to 15,000 at a fixed gas saturation temperature of 42°C and cooling wall temperatures of 5°C, 10°C, and 20°C. The data shows that with an increase of refrigerant mass flux, the overall condensation heat transfer coefficients of R-134a increased, and the pressure drops also increased. However, with the increase of mass flux of cooling water, the refrigerant-side heat transfer coefficients decreased. Using low mass flux in a helicoidal tube improves the heat transfer coefficient. Furthermore, selecting low wall temperature for the cooling medium gives a higher refrigerant-side heat transfer coefficient. 相似文献
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In this study, condensation of pure refrigerant R134a vapor inside a smooth vertical tube was experimentally investigated. The test section was made of a copper tube with inside diameter of 7.52 mm and length of 1 m. Experimental tests were conducted for mass fluxes in the range of 20–175 kg/m2s with saturation pressure ranging between 5.8 and 7 bar. The effects of mass flux, saturation pressure, and temperature difference between the refrigerant and tube inner wall (ΔT) on the heat transfer performance were analyzed through experimental data. Obtained results showed that average condensation heat transfer coefficient decreases with increasing saturation pressure or temperature difference (ΔT). In addition, for the same temperature difference (ΔT), heat can be removed from the refrigerant at a higher rate at relatively low pressure values. Under the same operating conditions, it was shown that average condensation heat transfer coefficient increases as mass flux increases. Finally, the most widely used heat transfer coefficient correlations for condensation inside smooth tubes were analyzed through the experimental data. The best fit was obtained with Akers et al.'s (1959) correlation with an absolute mean deviation of 22.6%. 相似文献
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Dai Jiakun Michael A. Delichatsios Yang Lizhong 《Proceedings of the Combustion Institute》2013,34(2):2497-2503
In order to investigate the effects of ambient pressure and igniter location on piloted ignition of solid fuels, the ignition mass flux of PMMA was experimentally determined for locations of the igniter between 6 and 70 mm above the solid surface, under two external heat fluxes of 21.2 and 25.4 kW/m2. The experimental results show that the ignition mass flux decreases as the igniter approached the solid surface until it reached a minimum, and then the ignition mass flux remains nearly constant followed by a slight increase with a further decrease of the igniter location. In addition, in another series of experiments the ignition mass flux for elm wood decreases by a factor 0.6 at reduced pressure 0.67 (Tibet 0.67 atm) compared to the ignition mass flux at normal pressure (Hefei, 1.0 atm). The results of this work are explained well by a numerical piloted ignition model which also explains recent observations on the ignition mass flux at reduced pressures in a forced-flow ignition and flame spread apparatus. 相似文献
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Spray cooling is an effective tool to dissipate high heat fluxes from hot surfaces. This article thoroughly investigates the effect of thickness of a hot stainless steel plate on the cooling time, cooling rate, heat flux, and heat transfer coefficient under constant mass flow rate maintained at 1 MPa using water as the coolant. Cylindrical samples of stainless steel with constant diameter (D = 25 mm) and thickness (δ = 7.5, 12, 16.5, and 21 mm) were used in the present study. Critical droplet diameter to achieve an ultra-fast cooling rate of 300°C/s was estimated by using an analytical model for samples of varying thicknesses. The analytical model (one side spray cooling) showed good agreement with experimental results with a relative error of 3.2% in the plate thickness range of 1–12 mm. An increasing trend in maximum heat flux was found with increasing thickness of the plate. Maximum heat flux as high as 1,800 kW/m2 was achieved for a 21-mm-thick sample. Heat transfer coefficients in the range 0.092–96.24 kW/m2K, 0.111–98.9 kW/m2K, 0.074–63.4 kW/m2K, and 0.127–55.63 kW/m2K were reported for sample of varying thicknesses in the present study. Limited published work is available with reference to water spray cooling dynamics and thickness of stainless steel plate. Therefore, the present study focuses on the correlation between the thickness of the plate and spray dynamics of water spray cooling. 相似文献
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Presented are results of an experimental study of local heat transfer characteristics in boiling of the dielectric liquid perfluorohexane under forced convection in a horizontal microchannel heat exchanger. The experiments with a copper microchannel heat exchanger comprising 21 channels with sections of 335 × 930 μm were conducted with a mass velocity of 250 to 1000 kg/m2s and a heat flux through the outer wall of the heat exchanger of 3 to 60 W/cm2. The dependence of the local heat transfer coefficient on the heat flux density on the inner wall of the microchannels was established, as well as the critical heat flux. The experimental data are compared with calculations based on known models of heat transfer. 相似文献
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In this study, condensation of pure refrigerant R134a vapor inside a vertical 18° helical microfin tube was experimentally investigated. Tests were performed at saturation pressure of 5.7–5.9 bar with mass fluxes of 20–100 kg/m2s and heat fluxes of 1.7–5.3 kW/m2. The effects of mass flux and the temperature difference between the refrigerant and tube wall (ΔT) on the heat transfer performance were analyzed throughout experimental data. For experiments in which ΔT is more than 2.5°C, the average condensation Nusselt number showed a tendency to be independent from ΔT. Heat transfer enhancement ratio was found to be 1.59–1.71, which is always higher than the heat transfer area enhancement factor (1.55). Fins always act as a turbulence promoter in the given experimental data range. Finally, the most widely used heat transfer coefficient correlations for condensation inside microfin tubes were analyzed through the experimental data. Best fit was obtained with Yu and Koyama's correlation with an absolute mean deviation of 17% and Kedzierski and Goncalves's correlation with an absolute mean deviation of 19%. 相似文献