短脉冲激光作用下丙酮液池沸腾现象的瞬态观测

本文对短脉冲激光作用下试件表面的温度变化和丙酮液体汽泡行为进行了瞬态观测,研 究了激光参数和细小金属颗粒等因素对丙酮液体沸腾行为的影响。结果表明：激光参数中,脉宽是 影响温度曲线和汽泡行为的主要因素,随着激光脉宽增大,大汽泡的长大时间和脱离直径减小;汽 泡长大速度与常规沸腾时的完全不同,没有出现等温生长阶段,在激光脉冲后很长时间内汽泡长大 速度快速增大;试件表面覆盖细小金属颗粒后,沸腾过程变得非常剧烈。     

高温壁面液体射流冲击瞬态沸腾传热的实验研究

以水作为冷却介质,对高温壁面在射流冲击淬冷时的瞬态换热特性进行了实验研究,获得了介质在不同过冷度、不同射流速度下的完整沸腾曲线。实验结果表明。无论是增大工质过冷度还是提高射流速度,总会使得热壁面的冷却速率加大。在一定的过冷度和射流速度下壁温变化呈现快－慢－快的特点。临界热流密度随平均壁温变化率的增大而增大,二者之间存在线性关系．     

水封对于阻止汞的挥发真的不起作用吗

用热力学原理说明了汞面上的水封对于汞的挥发在热力学上有非常有效的阻止作用,并且,对于多组分完全不互溶系统,如果平稳放置,密度较大的那些相的挥发都会被最上面密度最小的相所阻止。指出了长期存在于某些物理化学教材、课件以及许多物理化学教学工作者教学过程中的相关错误概念,分析了错误的原因。     

Dependence of the critical heat flux at boiling on the coolant physical properties

It has been experimentally proved that heat transfer at boiling appears to be the problem with the conjugated boundary conditions. Heat transfer and critical heat fluxes at boiling depend both on physical properties of the boiling liquid and on the number of characteristics of the heat transferring wall. Various experimental data of the problem of boiling liquid with various physical properties have been analysed. To eliminate or minimize influence of the properties of the cooled wall on the value of critical heat transfer, the data obtained at boiling on the thick cooled wall only from the stainless steel or nichrome are considered. To eliminate effect of capillary forces specific linear size of heat transferring wall satisfied the condition ≥ 2.0.     

微小圆通道内流动沸腾换热特性的研究

微小通道内相变换热具有热流密度高、单位体积内换热面积大、结构紧凑等特点,成为高效紧凑式换热器设计的重要途径。本文以氟利昂R113为工质,完成了0.7、1.1和1.4 mm的圆形小通道内的流动沸腾实验,对小通道内流动沸腾换热特性进行了分析,拟合了计算沸腾换热特性的实验关联式,为工程实际应用提供参考。     

环状狭缝通道流动沸腾换热的实验研究

以蒸馏水为工质进行了实验研究。分析了影响流动总压降的因素,给出了计算摩擦压降的经验关系式,实验数据与计算结果误差约±15％,此关系式可以用来预测该实验范围内的摩擦压降。同时还给出了计算流动沸腾传热系数的经验关系式,实验数据与计算结果误差为-17％～13％,此关系式可以用来预测该实验范围内的流动沸腾传热系数。     

Modeling on debonding dynamics of pressure-sensitive adhesives

We propose a simple mechanical model describing viscoelasticity and cavitation during the debonding process in pressure-sensitive adhesives (PSA). Our calculation qualitatively reproduces typical stress-strain curves in the probe-tack test, such as the steep stress maxima and the following plateau region. It is shown that in the thin-film geometry the stress-strain curve is essentially determined by the cavities created by the large negative pressure. Effects of pre-existent air bubbles due to surface roughness are also discussed.     

Periodic flow boiling in a non-uniformly heated microchannel heat sink

Hydrodynamic and thermal characteristics of flow boiling in a non-uniformly heated microchannel were studied. Experiments were performed with a single microchannel and a series of microheaters to study the microscale boiling of water under axially non-uniform heat input conditions. A simultaneous real time visualization of the flow pattern was performed with the measurement of experimental parameters. Tests were performed over a mass flux of 309.8 kg/m² s, and heat flux of 200–600 kW/m². Test results showed different fluctuations of heated wall temperature, pressure drop, and mass flux with variations of the heat input along the flow direction. The unique periodic flow boiling in a single microchannel was observed at all heat flux conditions except for the increasing heat input distribution case which is the nearly uniform effective heat input distribution condition. The instability is correlated with flow pattern transition. For the nearly uniform effective heating condition, no fluctuation of the wall temperature, pressure drop, or mass flux was observed. We can relieve the instability by increasing total heat input along the flow direction and predict the instability using the transition criteria and flow pattern map.     

Experimental study of bubble departure characteristics in forced convective subcooled nucleate boiling

Visualization experiments in upward forced convective nucleate boiling flows were carried out. The bubble growth and collapse have been measured using high-speed photography technique with distilled water under atmospheric pressure. The experiments show that the bubbles depart from nucleating sites shortly after nucleation and slide along the heater surface. The bubbles grow while sliding, attain a maximum size, then lift from the surface sometime during condensation, and quickly vanish in the bulk liquid. Parametric studies show that bubble diameter and departure frequency increases with an increase in heat flux, a decrease in subcooling, and a decrease in mass flux.