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NucleatePoolBoilingofPureLiquidsandBinaryMixtures:PartI-AnalyticalModelforBoilingHeatTransferofPureLiquidsonSmoothTubesGuoqin... 相似文献
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垂直矩形窄缝内的过冷流动沸腾换热性能 总被引:1,自引:0,他引:1
用高速摄像等方法研究了有压模化介质在单一垂直矩形窄缝流道内的气泡形态和传热情况 ,发现窄缝流动沸腾换热强化的原因在于流道尺寸较小 ,气泡的形状发生变化 ,增加了界面体积浓度 ,并强化了对加热面附近的扰动 ,使换热有所强化。通过与实际测量的壁温数据进行比较 ,发现用于计算大流道和池过冷沸腾换热的 Rohsenow关系式预测窄流道内高热流密度下的过冷流动沸腾换热的误差不大 ,但对于较低热流密度下的过冷流动沸腾时误差较大 ;通过最小二乘法对 Rohsenow关系式进行修正后 ,误差低于± 2 5 %。 相似文献
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An experimental investigation of the effect of mechanical vibrations of a copper flat circular surface on the pool boiling heat transfer coefficient of water at atmospheric pressure are presented in this paper. A vibration exciter was used to vibrate this copper test surface vertically. Effect of frequency and amplitude of vibration on the boiling heat transfer coefficient was studied. An increase in the heat transfer coefficient was observed at low frequency and amplitudes, at higher amplitude and frequency heat transfer deteriorates. Heat transfer coefficient increases up to 26% with vibration intensity, represented by vibrational Reynolds number. 相似文献
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强化管外CFC11与HCFC123沸腾换热系数的对比试验研究 总被引:2,自引:0,他引:2
本文通过强化管外CFC11与HCFC123沸腾换热系数的对比试验分析与研究,分别得出了HCFC123与CFC11沸腾换热系数,并对这两种工质的实际应用情况进行了分析。 相似文献
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对R290制冷剂在微细通道内的流动沸腾换热特性进行了实验研究。研究管径分别为1和2 mm,热流密度为20~65 k W/m~2,质量流率为100~200 kg/m~2·s,饱和温度为15和25℃,干度范围为0.1~0.9。通过实验数据分析管径、热流密度、质量流率、饱和温度对流动沸腾换热的影响。结果表明:随着管径的下降,换热系数呈现出大幅上升的趋势,其平均增幅为31%;随着热流密度的上升,换热系数呈现出大幅上升的趋势,其平均增幅达到了131%;随着质量流率的上升,换热系数呈现出小幅上升的趋势,其平均增幅为14%;随着饱和温度的上升,大部分换热系数呈现出小幅上升的趋势,其平均增幅为12.6%。 相似文献
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An experiment on pool boiling in methanol was performed for a case in which the boiling space was controlled by an interference plate with many holes. The narrow space, 0.12 mm in thickness, between the heat transfer surface and the interference plate was hermetically sealed at the perimeter. Therefore, the vapor and liquid were only exchanged through the holes in the interference plate. The degree of superheat at the onset of boiling was 0.7 K without overshoot at 10‐mm plate thickness, 1‐mm hole diameter, and 3.85‐mm hole pitch. The critical heat flux obtained was the same value without the interference plate mentioned above. The interference plate disturbed free convection and a superheat layer was provided under small heat flux on the heat transfer surface. The critical bubble diameter for the onset of boiling was decreased as the temperature of the superheat layer was increased. Thus, the degree of superheat at the onset of boiling was decreased. © 2004 Wiley Periodicals, Inc. Heat Trans Asian Res, 33(7): 462–471, 2004; Published online in Wiley InterScience ( www.interscience.wiley.com ). DOI 10.1002/htj.20028 相似文献
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An experimental study was conducted to investigate transient local heat transfer around a bubble at onset of boiling on a thin glass heating plate immersed in saturated n-hexane at low pressure. Eight rapid response Cu-Ni thermocouples consisting of a vacuum deposited thin film were used to measure the temperature change of the heating surface. Simultaneous high-speed video photographs were also obtained. The surface temperatures near a nucleation site decreased rapidly owing to the evaporation of a thin layer (microlayer) of liquid formed beneath the bubble in the early period and the rate of bubble growth increased with increasing incipient boiling superheat (ΔTIB). The thickness of the microlayer decreased markedly with increasing ΔTIB. © 1998 Scripta Technica, Heat Trans Jpn Res, 26(7): 484–492, 1997 相似文献
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通过实验研究了R404A在5 mm微肋管内的流动沸腾换热特性。热流密度为5~25 kW/m~2、质量流速为200~500 kg/(m~2·s)、饱和温度为-5~5℃、干度为0.1~0.9。结果表明:提高饱和温度可以提高换热系数,在0.1~0.3低干度区提升作用较为明显,在0.3~0.6中干度区提升作用逐渐降低;随着质量流速的增大,换热系数呈上升趋势,其对换热系数的影响主要体现在中干度区;热流密度的增大也能够有效提升换热系数,同时使换热系数的峰值提前出现,加速干涸现象的发生。针对本实验数据,修正后的Gungor模型预测精度较高,修正系数为1.372,统计得出平均绝对偏差仅9.30%,高达98.18%的数据偏差度小于±30%。 相似文献
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BoilingDelayPhenomenoninaThermosyphonHeatSinkandItsEffectonDevicePerformanceWeilinHu;YihuiZhou;AijunWang(DepartmentofEngineer... 相似文献
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强化管内沸腾换热实验研究 总被引:2,自引:0,他引:2
主要研究在低过热度下微槽对流动沸腾换热特性的影响,分别以单工质甲醇和甲醇与甲苯的混合物为工质对不同流量情况下光管、直槽管和螺旋槽管的流动沸腾换热特性进行了实验研究。研究结果表明:对单工质甲醇来说,螺旋槽管可以明显起到强化传热作用,而且流量越低,强化传热效果越明显。对混合工质来说,当流量较低时,螺旋槽管强化传热效果不明显,而在流量较高时,强化传热效果比较明显。无论是单工质还是混合工质,直槽管在实验所能达到的壁面温度条件下不能起到明显的强化传热效果。还给出了螺旋槽管强化传热的定性解释。 相似文献
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有扰流片的矩形通道内空气流动和传热过程的数值模拟 总被引:1,自引:0,他引:1
以高温透叶片尾部区内部冷却为应用背景,对带顺排、错排扰流片肋的通道内空气流动和传热过程进行了数值模拟。计算结果表明,在相同雷诺数下,错排扰流片的阻力系数比针肋和顺排绕流片的阻力因子均增大约2%,而冷却能力分别增大约50%和9%。 相似文献
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电场作用下气泡的行为研究 总被引:1,自引:0,他引:1
为进一步揭示EHD强化沸腾换热机理,分析了电场作用下气泡的受力情况,综述了国内外对电场作用下气泡的行为研究成果,系统总结了电场对气泡行为及其动力学特性的影响,并对该领域的进一步研究提出了建议。 相似文献
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INTanDUCTI0NBoilingheattransferandcriticalheatflux(CHF)inaconfinednarrowspacehavebeenstudiedexperi-melltallybyanumberofinvestigatorsinthepastfewdecades.However,thereisnoanypopularlyacceptedmodelintheheattransferinnarrowspaceboiling,althoughsomepopularknowledgeabouttheboilingheattransferinthenarrowspacehavebeenacceptedbymanyresearchers.Theknowledgecanbecon-cludedasthatthenucleateboilingheattransferisenhancedatlowheatfluxregionanddeterioratedathighheatfiuxregi0nespeciallyatCHF.Theenhanceme… 相似文献
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An experimental study of flow boiling of binary organic solution was conducted in a horizontal tube. An organic mixture of miscible fluids, chlorodifluoromethane (R22)–dimethylacetamide (DMAC) was circulated through the experimental system. The influence of the heat source, flow rate, solution concentration and operating pressure on the flow characteristics and the heat transfer coefficient was examined experimentally. Based on the experimental observation an appropriate flow pattern map was constructed. The experimental values of the heat transfer coefficient (HTC) were compared with predicted HTC obtained by several known correlations. Based on these comparisons the well know Dittus & Boelter correlation deviated up to 30%. A better agreement (up to 15%) was obtained by modified the Kattan et al. 10, 11 and 12 correlation. The modification includes using the Forster and Zuber correlation [21] for nucleate boiling HTC and multiplying the predicted HTC by a constant of 1.4. 相似文献