纺粘牵伸器喷射流场的测试及验证

根据纺粘非织造扁平窄狭缝流道牵伸器的特点和喷射流场的特征,采用粒子图像测速仪对纺粘牵伸器的喷射流场进行了试验测试,同时,列出用喷射流场理论模型所获得的计算数值模拟结果,并对数值模拟结果和试验结果进行比较。     

变压器油圆形浸没射流冲击换热特性

对变压器油圆形浸没射流冲击换热特性进行了系统的实验研究,分析了恢复效应、喷距、射流Re、喷嘴尺寸等因素对换热的影响.对极小尺寸射流冲击换热情况下的一些特殊现象进行了描述,并对其形成机理进行了分析.     

全方位旋转射流搅拌器流场数值模拟分析

在自行研发并制造的立体全方位旋转射流搅拌器的基础上,介绍了其结构组成和工作原理。为了考察该搅拌器的防沉降搅拌效果,采用SIMPLE算法和标准k-ε双方程湍流模型,运用Fluent软件对其三维稳态流场进行了数值模拟。通过对不同出射速度下全方位旋转射流搅拌器的3种不同偏转角度下的喷嘴与水平喷嘴喷射时在罐底产生的冲击压力、流速和湍动能进行分析并对比,结果表明:偏角喷嘴能够对罐底沉积物起到冲刷搅拌作用,但随着偏转角度的增大,冲刷搅拌效果相应减弱;相同出射速度下3种偏角喷嘴的相应参数均比水平喷嘴的数值更大,影响范围更广,防沉降效果更好;结合全方位旋转射流搅拌器立体旋转的结构特点进一步说明了全方位旋转射流搅拌器具有三维立体的搅拌作用。     

多喷嘴带相差射流冲击传热的数值模拟

采用数值模拟的方法对带相差的多喷嘴射流冲击传热进行数值模拟,分别得到不同相差和不同射流频率条件下的冲击传热效果。结果显示,在不同的射流喷射模式下,按相差顺序增加方式（B型）喷出的射流传热效果最好,两喷嘴间的相差为0°～180°之间时,传热板的传热效果随着相差角度的增加,传热效果得到增强,且在相差为120°时,整个传热板传热效果最均匀;在频率为0～10Hz时,频率越大,整个传热板传热越均匀,但频率的影响小于相差及喷射模式的影响。     

Nanofluid impingement jet heat transfer

Experimental investigation to study the heat transfer between a vertical round alumina-water nanofluid jet and a horizontal circular round surface is carried out. Different jet flow rates, jet nozzle diameters, various circular disk diameters and three nanoparticles concentrations (0, 6.6 and 10%, respectively) are used. The experimental results indicate that using nanofluid as a heat transfer carrier can enhance the heat transfer process. For the same Reynolds number, the experimental data show an increase in the Nusselt numbers as the nanoparticle concentration increases. Size of heating disk diameters shows reverse effect on heat transfer. It is also found that presenting the data in terms of Reynolds number at impingement jet diameter can take into account on both effects of jet heights and nozzle diameter. Presenting the data in terms of Peclet numbers, at fixed impingement nozzle diameter, makes the data less sensitive to the percentage change of the nanoparticle concentrations. Finally, general heat transfer correlation is obtained verses Peclet numbers using nanoparticle concentrations and the nozzle diameter ratio as parameters.     

圆形自由表面水射流冲击换热特性

对圆形自由表面水射流冲击换热特性进行了系统的实验研究,总结了喷距、射流出口速度以及相变等因素对换热的影响,并对其形成机理进行了分析,得到了驻点传热系数以及局部传热系数径向分布的关联式.     

射流搅拌器流体力学行为及结构优化

通过考察工艺操作所需要的流场,并运用射流卷吸原理,确定了光催化反应器的釜体和射流式搅拌器的结构形式。通过计算流体力学软件FLUENT对优化方案的模拟,显示了模拟结果并进行了分析,从而证明了本文设计的三维射流式搅拌器结构形式切实可行,尺寸参数完全合理。通过工业生产验证,反应除砷效率较实验室中有明显提高。     

两段上向流曝气生物滤池脱氮性能的研究

对两段上向流曝气生物滤池(UBAF)处理城市污水的脱氮性能进行了研究,探讨了水温、水力负荷、有机容积负荷、NH4+-N容积负荷和气水比对UBAF脱氮性能的影响.试验结果表明:水温是影响UBAF去除脱氮效果的主要因素,随着水力负荷的升高,UBAF脱氮效果呈下降趋势,当气水比为2∶1时,UBAF对NH4+-N、TN的平均去除效果最好.     

圆形浸没射流冲击驻点时射流速度对传热影响的实验研究

以R113为工质系统地实验研究了圆形浸没射流冲击驻点时的传热情况 ,实验涉及单相对流传热、沸腾起始温度、核沸腾传热和临界热流密度等 .结果表明 :出口速度对沸腾起始温度和核沸腾传热没有影响 ;速度增加 ,单相对流传热和临界热流密度提高 ,而温度过头值减小 .当出口速度超过 10m·s^-1后 ,高速射流冲击驻点的核沸腾曲线需要修正才能位于相应过冷度下池核沸腾曲线的延长线上 .     

Modeling of continuous self‐classifying spiral jet mills part 1: Model structure and validation using mill experiments

The objective of this work is to develop a milling model for a continuous self‐classifying spiral air jet mill. Its foundation is a population balance model with selection and breakage distribution functions that have been related to a minimal number of mill‐dependent and powder‐dependent parameters. Initially, experimentation is required to determine the mill‐dependent parameters for a specific mill, by milling a “base” powder at multiple operating conditions. Powder‐dependent parameters can be determined from either mill experiments or from material characterization measurements that require small amounts of powder (presented in Part 2). Ultimately, the milling model presented successfully predicts the product particle size using as inputs the feed particle‐size distribution and mill operating conditions. Three crystalline powders, sodium bicarbonate, lactose monohydrate, and sucrose, have been used to test the proposed milling model. © 2014 American Institute of Chemical Engineers AIChE J 60: 4086–4095, 2014     

Particle‐laden liquid jet impingement on a moving substrate

The impingement of high speed jets on a moving surface was studied. The jet fluids were dilute suspensions of neutrally buoyant particles in water–glycerin solutions. At these low particle concentrations, the suspensions have Newtonian fluid viscosity. A variety of jet and surface velocities, solution properties, nozzle diameters, mean particle sizes, and volume fractions were studied. For each case the splash‐deposition threshold was quantified. It was observed that for jets with very small particles, addition of solids to the jet enhances deposition and postpones splash relative to a particle‐free water–glycerin solution with the same viscosity. In contrast, jets with larger particles in suspension were more prone to splash than single phase jets of the same viscosity. It is speculated that the change in character of the splash response for the jets with larger particles in suspension occurs when the particle diameter is comparable to the lamella thickness. © 2017 American Institute of Chemical Engineers AIChE J, 63: 4673–4684, 2017