共查询到18条相似文献，搜索用时 265 毫秒
1.
基于加热表面核化点遵循泊松与分形分布,提出了临界热流密度的一个数学模型,从该模型中发现大空间临界热流密度(CHF)是壁面过热度、接触角和流体物理特性的函数.对不同的接触角,模型预测的结果与实验数据进行了比较.两者很好地吻合. 相似文献
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提出过冷流动沸腾热传递的分形模型,根据加热表面活化点的分形分布得到了过冷流动沸腾热流密度的表达式。从该模型中发现过冷流动沸腾热流密度是壁面过热度、流体的过冷度、流体的主流速度与流体的接触角、流体物理特性的函数关系,并且没有增加新的经验常数。模型预测的结果与实验数据进行了比较,两者是极好的吻合。 相似文献
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引入分形理论来研究摩擦表面 .根据摩擦表面几何特征、形貌参数建立分形布朗运动模型 ,对分形数的求解进行了探讨 ,重点阐述分形数的物理意义和在摩擦表面形貌研究中运用分形数的优点 相似文献
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为了降低包晶钢铸坯表面纵裂纹发生率,需要优化现有包晶钢保护渣的传热性能。热流密度数值直接反映传热性能。通过选取某钢厂使用的A、B、C、D、E、F六种包晶钢保护渣,经过对比得出A渣具有较低的热流密度。从影响热流密度的碱度、结晶度、结晶温度三个因素进行分析,发现保护渣高碱度(不低于1.4),高结晶率,高结晶温度有利于降低保护渣的热流密度。 相似文献
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证明了过冷流动沸腾中加热表面活化穴的分形分布,得到了过冷流动沸腾中活化穴分形维数的数学表达式,此分形维数与盒子维计算得到的结果非常吻合.提出了过冷流动沸腾换热的一个分形模型.对流体不同主流速度,模型预测的结果与实验数据进行了比较,两者能较好地吻合. 相似文献
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文章采用改进的RSNG模型(Random Successive Nucleation Growth Model)，总结了三种计算聚集体分形维数的方法；运用逼近法确定分形向均匀结构的临界阈值；使用两种方法计算了在三种近邻条件下的逾渗阈值。计算结果表明：计算分形维数三种方法的结果相同；而计算逾渗阈值两种方法的结果完全一致。 相似文献
8.
传热学是研究热量传递规律的科学,其中表征热量传递速率的热流密度是一个十分重要的概念。在传热学教材中,对于热流密度的定义还不统一,影响对其含义的理解。下面就此问题谈一点看法。一、热流密度的几种定义 相似文献
9.
结合面接触问题对数控机床动态特性影响非常大,是决定机床系统总刚度和总阻尼的主要因素.本文总结了机床机械结合面接触刚度研究中常用的三种模型,即赫兹接触模型、G-W统计接触模型和分形接触模型,并根据三维W-M函数,利用Matlab仿真模拟了表面的三维粗糙形貌,分析了分形参数G和D的含义. 相似文献
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ZRP的临界密度是我们所关注的,同样杂质ZRP的临界密度是也是我们关注的。在单杂质ZRP中,已经能解析得出临界密度,我们推广为多杂质ZRP同样解析可以求出临界密度,同时我们引入局域化系数数值得出临界密度。 相似文献
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王迅 《天津大学学报(英文版)》2004,10(1)
Thecriticalheatflux (CHF)intheforcedconvec tiveboilingwithawalljethasbeenstudied.KattoandIshii[1 ] measuredtheCHFofsaturatedwater,R1 1 3 ,andtrichloroethane (ρl/ ρg =2 0 3— 1 60 3)atatmosphericpressureforadownwardfacingplanewalljet,varyingthevelocityufrom 1 .5to 1 5m/sandtheheaterlengthLfrom 1 0to 2 0mm ,andproposedEq.(1 )topredicttheirCHFdata. qcoρghfgu=0 .0 1 6 4(ρl/ ρg) 0 .867(σρlu2 L) 1 / 3 (1 ) KattoandHaramura[2 ] ,further,haveextendedtheirvelocityrangefromu =1 .8t… 相似文献
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Inverse heat conduction method （IHCM） is one of the most effective approaches to obtaining the boiling heat transfer coefficient from measured results. This paper focuses on its application in cryogenic boiling heat transfer. Experiments were conducted on the heat transfer of a stainless steel block in a liquid nitrogen bath, with the assumption of a 1D conduction condition to realize fast acquisition of the temperature of the test points inside the block. With the inverse-heat conduction theory and the explicit finite difference model, a solving program was developed to calculate the heat flux and the boiling heat transfer coefficient of a stainless steel block in liquid nitrogen bath based on the temperature acquisition data. Considering the oscillating data and some unsmooth transition points in the inverse-heat-conduction calculation result of the heat-transfer coefficient, a two-step data-fitting procedure was proposed to obtain the expression for the boiling heat transfer coefficients. The coefficient was then verified for accuracy by a comparison between the simulation results using this expression and the verifying experimental results of a stainless steel block. The maximum error with a revised segment fitting is around 6%, which verifies the feasibility of using IHCM to measure the boiling heat transfer coefficient in liquid nitrogen bath. 相似文献
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Gas-liquid two-phase flow and heat transfer can be encountered in numerous fields, such as chemical engineering, refrigeration, nuclear power reactor, metallurgical industry, spaceflight. Its critical heat flux (CHF) is one of the most important factors for the system security of engineering applications. Since annular flow is the most common flow pattern in gas-liquid two-phase flow, predicting CHF of annular two-phase flow is more significant. Many studies have shown that the liquid film dryout model is successful for that prediction, and determining the following parameters will exert predominant effects on the accuracy of this model: onset of annular flow, inception criterion for droplets entrainment, entrainment fraction, droplets deposi-tion and entrainment rates. The main theoretical results achieved on the above five parameters are reviewed; also, limitations in the existing studies and problems for further research are discussed. 相似文献
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Gas-liquid two-phase flow and heat transfer can be encountered in numerous fields, such as chemical engineering, refrigeration, nuclear power reactor, metallurgical industry, spaceflight. Its critical heat flux （CHF） is one of the most important factors for the system security of engineering applications. Since annular flow is the most common flow pattern in gas-liquid two-phase flow, predicting CHF of annular two-phase flow is more significant. Many studies have shown that the liquid film dryout model is successful for that prediction, and determining the following parameters will exert predominant effects on the accuracy of this model： onset of annular flow, inception criterion for droplets entrainment, entrainment fraction, droplets deposition and entrainment rates. The main theoretical results achieved on the above five parameters are reviewed; also, limitations in the existing studies and problems for further research are discussed. 相似文献
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基于FLUENT软件对制冷剂R134a在水平螺旋槽管管外沸腾换热进行了三维数值模拟,得到了其饱和泡状沸腾过程中体积含汽率的分布规律和换热系数,并和光管进行了比较。结果表明螺旋槽管外侧能够很好地强化沸腾传热。此外,还通过改变边界条件分析了质量流量、热流密度的变化对螺旋管管外沸腾换热系数的影响。 相似文献
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In this paper based on the experiment principle of evaluating adhesion property by scratch testing, the peeling mechanism of thin films is discussed by applying contact theory and surface physics theory. A mathematical model predicting the critical load is proposed for calculating critical load as determined by scratch testing. The factors for correctly evaluating adhesion of coatings according to the experimental data are discussed. 相似文献
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INTRODUCTIONHardceramicfilmsdepositedbychemicalva pordeposition (CVD)andphysicalvapordeposi tion (PVD)techniqueshadbeenwidelyappliedinindustry .Coatingadhesionisaveryimportantpropertyforevaluatingthecoatingquality.Themethodevaluatingtheadhesionstrengthoft… 相似文献
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A circulating fluidized bed evaporator(including down-flow, horizontal, and up-flow beds) was constructed to study the effect of flow directions on multiphase flow boiling heat transfer. A range of experimental investigations were carried out by varying amount of added particles(0-2%), circulation flow rate(2.15-5.16 m~3/h) and heat flux(8-16 kW/m~2). The comparison of heat transfer performance in different vertical heights of the horizontal bed was also discussed. Results reveal that the glass bead particle can enhance heat transfer compared with vapor-liquid two-phase flow for all beds. At a low heat flux(q = 8 kW/m), the heat-transfer-enhancing factor of the horizontal bed is obviously greater than those of the up-flow and down-flow beds. With the increase in the amount of added particles, the heat-transfer-enhancing factors of the up-flow and down-flow beds increase, whereas that of the horizontal bed initially increases and then decreases. However, at a high heat flux(q=16 kW/m), the heat-transfer-enhancing factors of the three beds show an increasing tendency with the increase in the amount of added particles and become closer than those at a low heat flux. For all beds, the heat-transfer-enhancing factor generally increases with the circulation flow rate but decreases with the increase in heat flux. 相似文献