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111.
为了提高大功率激光二极管列阵的散热效率以便提高其寿命和波长稳定性,研制了一种封装集成度较高的屋脊式硅基微通道热沉.将田口稳健设计方法用于微通道热沉的优化设计,利用正交试验和信噪比分析实现了参数的稳健优化.以(110)单晶硅作为基片,采用KOH各向异性刻蚀和硅-玻璃-硅三层阳极键合方法制作出了通道宽度约为50 μm的微通道热沉,通道壁面粗糙度优于0.1 μm.采用激光二极管芯片对样品进行了封装和测试,利用砷化镓激光波长的温度漂移系数估算出了中间激光二极管的有源区温升,从而计算出了热沉的热阻.测试结果表明,该微通道热沉的单位面积热阻约为0.070 cm2·K/W,与有限元分析结果基本一致. 相似文献
112.
新型压电无阀微泵效率分析及试验研究 总被引:1,自引:0,他引:1
提出了一种用于无阀压电微泵的新型效率模型,根据传统扩张/收缩管型结构设计出侧面带有环形面积新型锯齿型带锥度和无锥度两种微流道.用CFD软件对传统扩张/收缩型微流道及新型锯齿型微流道进行了三维流动模拟,绘制出几种微流道特性曲线,并用新型效率模型计算了三种微流道在两种限制条件(最大流量零压力头和最大压力头零流量)下的稳态效率,并进行了分析比较,结果表明由于结构改变,锯齿型微流道最大流量和压力损失实现了预期的变化,并且带锥度锯齿型微流道微泵稳态效率均大于标准扩张/收缩型微流道及无锥度锯齿型微流道微泵.最后制作出含有标准扩张/收缩及带锥度锯齿型微流道结构微泵,并对其进行试验,结果证明由于环形面积和锥度存在,带锥度锯齿形微流道微泵性能明显优于传统扩张/收缩型微泵. 相似文献
113.
矩形微通道中环状冷凝的三维数值模拟 总被引:1,自引:1,他引:0
建立了恒热流边界条件下矩形微通道中环状冷凝过程的三维模型。通过求解气相和弯月面区动量和质量方程及薄液膜厚度方程,得到了弯月面毛细半径分布、冷凝液膜厚度分布,以及传热系数和壁面温度分布。薄液膜区液膜将沿程逐渐增厚,到达一极值后再逐渐变薄。在通道截面中,薄液膜区的传热系数大于弯月面,最大局部传热系数及壁面最高温度皆位于薄液膜区和弯月面的连接处。[JP2]在冷凝起始段,通道横截面平均传热系数沿程急剧减小至一极值;在此之后的很长一段距离内,则基本保持不变;[JP]直至接近环状冷凝终点时又再次沿程减小。 相似文献
114.
粗糙表面微通道电渗流的数值模拟 总被引:1,自引:1,他引:0
电渗流(EOF)广泛应用于微流控芯片中的流体的传输与混合。针对带有粗糙表面的平行板微通道,建立了描述EOF的控制方程,基于有限元分析方法对具有不同粗糙度和EDL厚度的微通道内的EOF进行了数值模拟。结果表明,当EDL厚度接近0.3倍粗糙度大小时,粗糙度对EDL的影响较大,EOF受到粗糙度的阻力作用较为明显,而当EDL厚度相对粗糙度较大和较小时,EOF速度受到粗糙度的影响相对较小;粗糙表面微通道中部EOF速度与相对EDL厚度的关系呈“V”型曲线,EOF平均速度呈“L”型曲线。研究结论对于微通道表面的优化设计以及微流控芯片中流体的精确操控具有一定的参考意义。 相似文献
115.
116.
This paper investigates oil–water two‐phase flows in microchannels of 793 and 667 µm hydraulic diameters made of quartz and glass, respectively. By injecting one fluid at a constant flow rate and the second at variable flow rate, different flow patterns were identified and mapped and the corresponding two‐phase pressure drops were measured. Measurements of the pressure drops were interpreted using the homogeneous and Lockhart–Martinelli models developed for two‐phase flows in pipes. The results show similarity to both liquid–liquid flow in pipes and to gas–liquid flow in microchannels. We find a strong dependence of pressure drop on flow rates, microchannel material, and the first fluid injected into the microchannel. 相似文献
117.
118.
Process characteristics of CO2 absorption using aqueous monoethanolamine(MEA) in a microchannel reactor were investigated experimentally in this work.A T-type rectangular microchannel with a hydraulic diameter of 408 μm was used.Operating parameters,i.e.temperature,pressure and molar ratio of MEA to CO2 were studied.Under 3 MPa pressure,the mole fraction of CO2 in gas phase could decrease from 32.3% to 300×10?6 at least when gas hourly space velocity ranged from 14400 to 68600 h?1 and molar ratio of MEA to CO2 was kept at 2.2.In particular,the effects of temperature on CO2 absorption flux,mass transfer driving force,gas-liquid contact time and en-hancement factor were analyzed in detail and found that mass transfer enhancement by chemical reaction was a crucial factor for the process of CO2 absorption. 相似文献
119.
Michael R. King 《Nanoscale and Microscale Thermophysical Engineering》2013,17(3):255-264
Adhesive interactions between white blood cells and the interior surface of the blood vessels they contact is important in inflammation and in the progression of heart disease. Parallel-plate microchannels have been useful in characterizing the strength of these interactions, in conditions that are much simplified over the complex environment these cells experience in the body. Recent computational and experimental work by several laboratories have attempted to bridge this gap between behavior observed in flow chamber experiments and cell-surface interactions observed in the microvessels of anesthetized animals. 相似文献
120.
The miscible liquid‐liquid two phases based on Taylor flow in microchannels was investigated by high‐speed imaging techniques and Villermaux/Dushman reaction. The mixing based on Taylor flow was much better compared with that without introducing gas in microchannels, even the ideal micromixing performance could be obtained under optimized superficial gas and liquid velocities. In the mixing process based on Taylor flow, the superficial gas and liquid velocities affected the lengths and the velocities of Taylor bubble and liquid slug, and finally the micromixing performance. The formation process of Taylor flow in the inlets, the initial uniform distribution of reactants and the internal circulations in the liquid slug, and the thin liquid films all improved the mixing performance. Furthermore, a modified Peclet number that represented the relative importance of diffusion and convection in the mixing process was proposed for explaining and anticipating micromixing efficiency. © 2011 American Institute of Chemical Engineers AIChE J, 58: 1660–1670, 2012 相似文献