三角形微通道流动冷凝的实验研究

实验研究了三角形硅微通道中的流动冷凝.通道中的冷凝流型沿程主要有珠状流、环状流、喷射流和弹状-泡状流等.在同一通道中,喷射流位置随着工质流量的增大而延后;在相同蒸气入口雷诺数下,喷射流位置则随着通道尺度的增大而延后.喷射流频率随着蒸气入口雷诺数和冷凝液韦伯数的增大而增大.较小水力直径的三角形通道中的流动冷凝不稳定性较高.冷凝通道的壁面温度呈沿程下降趋势.在同一通道中,流动冷凝的平均冷凝传热系数和平均努塞尔数,皆随着蒸气入口雷诺数的增大而增大,通道尺度的减小显著强化冷凝传热.     

水平微肋管内蒸发及冷凝换热性能研究

为了研究微肋管结构尺寸及工况等对管内流动蒸发及冷凝性能的影响,对3根管外径为9．52 mm和2根外径为7 mm的微肋管进行了蒸发及冷凝实验,所用工质为R22．所选工况为,45℃冷凝温度,30-45℃的入口过热度, 2℃的出口过冷度,7℃蒸发温度,15％-20％的入口干度,5-6℃的出口过热度,实验中质量流速变化范围为90-500 kgm-2s-1。获得了换热性能随质量流速的变化,讨论了微肋结构尺寸对蒸发换热和冷凝换热性能的影响。     

矩形微通道中环状冷凝的数值模拟

建立了一套恒热流边界条件下矩形微通道内环状冷凝过程的一维稳态模型,进行了数值计算,并将数值模拟结果与正三角形中的冷凝过程进行了比较.研究显示,在不同截面的微通道中,液相毛细半径和流速的沿程变化趋势都是相似的.同条件下,矩形通道的冷凝段长度大于正三角形通道.在矩形微通道中,通道入口蒸气压力和水力直径越大或者接触角越小,则冷凝段长度越长.     

陶瓷微通道内的传热和压降特性

本文对一种新型陶瓷微通道换热器的传热与流动阻力特性进行了实验研究。实验工质分别为3M公司的HFE-7100和水。对于HFE7100流体,在传热面温度为40℃时热流密度可达10W/cm~2;对于水,传热面温度为35℃时热流密度可达约13W/cm~2。流动阻力特性实验结果表明,无论对于水还是HFE7100流体,在本实验范围内压降小于4.8kPa。     

双层微通道换热特性优化分析

为强化微通道换热器换热效果,建立了三维双层微通道换热器模型,通过优化分析计算得出微通道最佳设计尺寸。在底部热流密度qw=100W·cm-2时,最优占空比K=74%,下层通道高度Hc1=0.5mm,上层通道高度Hc2=0.9mm,其最高温度分布于受热面中部,最大温差比未经优化时降低20.37%。并对比了凹槽微通道与普通微通道的换热特性,结果表明,在入口速度大于3m/s时,凹槽微通道换热效果比普通微通道换热效果好。     

矩形微通道中流阻特性的实验研究

以工程上常用的66%的乙二醇水溶液作为工质,对几何特性相似而高宽比不同的4种纯铝矩形微通道内的流动特性进行了实验研究,得到了微通道冷板基础性的设计数据。实验测量了Reynolds数在50~500之间的流动阻力系数。实验结果表明:通道高度H与宽度W之比对微通道流阻特性有显著的影响;当Re数小于100时,在实验误差内,流动阻力系数的值近似等于经典理论计算值;随着Re数的增大和高宽比的变化,f的值远大于理论值,这可能是由微通道内部壁面粗糙度效应所导致的。     

粗糙平板微通道流动和传热的数值模拟

以粗糙平行平板微通道为研究对象,以三角形锯齿状粗糙元模拟固体表面的粗糙度,采用CFD流体固体共轭传热技术数值研究了绝对粗糙度和相对粗糙度对平行平板微通道流动和传热特性的影响,着重分析了粗糙度和流体速度对水力入口段长度和热力入口段长度的影响规律,同时研究了相对粗糙度对微通道转捩雷诺数的影响,为进一步揭示微微通道的流动和传热机理提供了依据.     

微通道换热器的研究进展及其应用前景

详细总结了微通道换热器的研究进展以及发展前景;概括阐述了微通道换热器具有的常规尺寸设备所无可比拟的优越性;从节约能源和占地面积的角度分析了微通道换热器的应用领域及前景。     

转轮除湿器微通道形状对除湿性能的影响

本文通过对除湿转轮气流微通道建立-维传热传质数学模型,对不同形状的微通道对传热传质效果的影响进行了理论分析.在给定工况下,对比了不同形状微通道的转轮包括除湿量、单位时间除湿量等各个除湿性能评价指标.结果表明,采用优选微通道形状将提高转轮除湿器性能指标10%左右.     

有限雷诺数情况下微槽道可压缩流动滑移流模型稳定性的数值模似

通过对微槽道一阶滑移流模型稳定性的理论研究，发现在不可压缩流和雷诺数趋于零的情况下，当Knudsen数Kn大于1／9时，会出现不稳定现象．这一理论结论在可压缩流和有限雷诺数情况下是否成立，尚不清楚，采用成熟的计算方法，用数值计算来研究可压缩流和有限雷诺数情况下一阶滑移流模型的稳定性，发现随着雷诺数的减小，不稳定的临界Knudsen数也不断减小，逐渐趋近于在不可压缩流和雷诺数趋于零的情况下得到的理论分析结果。     

毛细微槽内的相变传热的实验研究

本文对矩形毛细微槽竖直板的相变传热特性进行了实验研究。结果表明毛细微槽对相变换热具有很大的促进作用。当壁面过热度较小时,相变换热形式主要是三相接触线附近的蒸发换热机制。而当过热度较大时,微槽内发生剧烈的沸腾。微槽内相变换热的临界热负荷有两种产生机理:其一是当微槽长度较大时微槽内由于流动阻力而产生的液体输运临界;另一机理是当微槽长度较小时的池内沸腾临界现象,亦即由动态微液层模型决定的临界机理。实验还得到了微槽强化传热的最佳优化尺寸。     

水蒸气在竖直微细管外凝结传热特性研究

针对不同压力和不同流速下的饱和水蒸气在竖直微细圆管(内外径分别为0.571 mm和0.793 mm)外的凝结传热特性分别进行了实验研究,分析了蒸气压力和蒸气流速对凝结传热特性的影响。实验结果表明,凝结传热表面传热系数随着蒸气流速的增加而增加,在较高的蒸气压力下增加的更明显,且大于相同实验条件下的Nusselt理论分析解。在蒸气流速为2 m·s~(-1)时,凝结传热系数随压力的变化不大;在4 m·s~(-1)和6 m·s~(-1)时,随着蒸气压力的升高,凝结表面传热系数明显增大。     

喷雾冷却换热机理和影响换热性能的因素

基于目前国内外相关研究结果,分析了喷雾冷却的传热特性,阐述了喷雾冷却换热机理,给出了强化方法,研究了影响换热性能的因素,并给出一些理论临界热流密度（CHF）模型。最后结合高功率激光器件的散热需求,提出了喷雾冷却的发展方向。     

喷雾冷却换热机理和影响换热性能的因素

 基于目前国内外相关研究结果,分析了喷雾冷却的传热特性,阐述了喷雾冷却换热机理,给出了强化方法,研究了影响换热性能的因素,并给出一些理论临界热流密度（CHF）模型。最后结合高功率激光器件的散热需求,提出了喷雾冷却的发展方向。     

Entropy Inequalities for Evaporation/Condensation Problem in Rarefied Gas Dynamics

The present paper is devoted mainly to the half space problem for stationary Boltzmann-type equations. Using only conservation laws and the Boltzmann H-theorem we derive an inequality for unknown constant fluxes of mass, energy, and momentum. This inequality is expressed in terms of three parameters (pressure p, temperature T and the Mach number M) of the asymptotic Maxwellian at infinity. Geometrically the inequality describes a physical domain with positive entropy production in the 3-d space of the parameters. The domain appears to be qualitatively different for evaporation and condensation problems. We show that for given M, the curve p=p(M), T=T(M) of maximal entropy production practically coincides with the experimental evaporation curve obtained by Sone et al. on the basis of numerical solutions of BGK equation. Similar consideration for the condensation problem is also in qualitative agreement with known numerical results.     

An Experimental Investigation of Forced Convection Heat Transfer from a Coiled Heat Exchanger Embedded in a Packed Bed

Forced convection heat transfer from a helically coiled heat exchanger embedded in a packed bed of spherical glass particles was investigated experimentally. With dry air at ambient pressure and temperature as a flowing fluid, the effect of particle size, helically coiled heat exchanger diameter, and position was studied for a wide range of Reynolds numbers. It was found that the particle diameter, the helically coiled heat exchanger diameter and position, and the air velocity are of great influence on the convective heat transfer between the helically coiled heat exchanger and air. Results indicated that the heat transfer coefficient increased with increasing the air velocity, increasing helically coiled heat exchanger diameter, and decreasing the particle size. The highest heat transfer coefficients were obtained with the packed-bed particle size of 16 mm and heat exchanger coil diameter of 9.525 mm (1/4 inch) at a Reynolds number range of 1,536 to 4,134 for all used coil positions in the conducted tests. A dimensionless correlation was proposed for Nusselt number as a function of Reynolds number, particle size, coil size, and coil position.     

CO2/H2O混合气体在水平管外凝结换热与分离特性研究

本文通过实验研究了CO₂质量分数为11.39%~70.95%,壁面过冷度为5~25 K,总压力为5~15 kPa的CO₂/H₂O混合气体自然对流条件下在水平管外的凝结换热规律,结果表明CO₂/H₂O的凝结换热系数随CO₂含量和壁面过冷度的增大而降低,但随总压力的增大而增大。根据实验结果建立了新关联式,将关联式应用到凝汽器的设计计算与分析,且对凝汽器进行了分离特性和经济性分析。     

Design and Experimental Investigation of a Gas-to-Gas Counter-Flow Micro Heat Exchanger

In this work, a double-layered microchannel heat exchanger is designed for investigation on gas-to-gas heat transfer. The micro-device contains 133 parallel microchannels machined into a polished polyether ether ketone plate for both the hot side and cold side. The microchannels are 200 μm high, 200 μm wide, and 39.8 mm long. The design of the micro-device allows tests with partition foils in different materials and of flexible thickness. A test rig is developed with the integration of customized pressure and temperature sensors for in situ measurements. Experimental tests on the counter-flow micro heat exchanger have been carried out for five different partition foils and various mass flow rates. The experimental results, in terms of pressure drop, heat transfer coefficients, and heat exchanger effectiveness are discussed and compared with the predictions of the classic theory for conventionally sized heat exchangers.     

微纳卫星COTS器件应用研究

大量采用宇航级元器件进行航天器研制的模式,由于其“成本高、研制周期长、元器件性能不足”等缺点,已经难以满足微纳卫星“周期短、成本低、集成度高”的要求。因此提出了在微纳卫星上使用COTS(Commercial off-the-shelf)器件的方法;针对微纳卫星的特点,首先分析了微纳卫星对COTS器件的需要和风险,提出了COTS器件微纳卫星应用的选用原则、选用依据;在此基础上经过分析,提出了COTS元器件微纳卫星应用流程,有针对性提出了COTS器件应用的器件级和板级筛选方法,并开展了COTS器件的微纳卫星抗单粒子效应加固设计,进一步提高COTS器件应用的可靠性。通过在轨应用验证,结果表明,通过该方法选用筛选的COTS器件,在进行有效加固后可以满足微纳卫星在轨稳定运行的要求,同时为微纳卫星降低成本缩短研制周期提供了保障。该方法对COTS器件在微纳卫星中的应用提供了一般性指导意义。     

Accurate prediction of the critical heat flux for pool boiling on the heater substrate

While the influence of liquid qualities, surface morphology, and operating circumstances on critical heat flux (CHF) in pool boiling has been extensively studied, the effect of the heater substrate has not. Based on the force balance analysis, a theoretical model has been developed to accurately predict the CHF in pool boiling on a heater substrate. An analytical expression for the CHF of a heater substrate is obtained in terms of the surface thermophysical property. It is indicated that the ratio of thermal conductivity (k) to the product of density (ρ) and specific heat (c_p) is an essential substrate property that influences the CHF. By modifying the well-known force-balance-based CHF model (Kandlikar model), the thermal characteristics of the substrate are taken into consideration. The bias of predicted CHF values are within 5% compared with the experimental results.