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双语推荐:韦伯数

介绍了一种自行发明的新的雾化方法。该方法是采用含有固体介质的高速气流即气固两相流对液体金属或合金进行雾化而制备粉末的一种方法,对比研究了同等条件下普通气体雾化与两相流雾化制备粉末的特征,研究了固体雾化过程中主要工艺参对固体雾化粉末特征的影响规律。结果表明,两相流雾化制得粉末的平均粒度约为普通气体雾化所得粉末的二分之一,而且粒度分布更集中,粉末的冷却速度比普通气体雾化高一个量级,粉末微观组织更细小;采用液体雾化破碎准则韦伯数以衡量雾化介质的破碎能力,得出两相流雾化介质的韦伯数为气体韦伯数和颗粒流韦伯数之和,建立了两相流雾化破碎的临界方程,并以此讨论了主要工艺规律。
A self-invented atomization process, in which molten metal is atomized into powder by a high-velocity gas stream carrying solid particles as the atomization medium, was introduced. The characteristics of powders prepared by common gas atomization and dual-phase flow atomization under similar conditions were compared. The experimental results show that the dual-phase flow-atomized powders have average particle sizes that are one-half that of the common gas-atomized particles;additionally, they possess a finer microstructure and higher cooling rate under the same atomization gas pressure and the same gas flow. The Weber number in the crash criteria of liquid atomization is adopted to measure the crash ability of the atomization media. The Weber number of the dual-phase flow atomization medium is the sum of that of the gas and the solid particles. Furthermore, the critical equation of the crash model in dual-phase flow atomization is established, and the main regularities associated with

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采用激光粒子成像测速仪(PIV),试验研究了不同动量比下燃油射流在横向空气流中的穿透深度特性。同时,采用值计算方法,对射流穿透特性进行了模拟,并将试验和计算结果,分别与已有的经验关系式,及考虑气动韦伯数影响修改后的关系式进行对比。结果表明:燃油射流上边界深度与幂指关系式较吻合;采用VOF两相流模型能较准确地模拟出燃油射流的喷雾核心深度;修改后的关系式与不同燃油-空气动量比范围下的喷雾核心深度较吻合;燃油-空气动量比和气动韦伯数,是影响燃油射流横流穿透深度的主要参
The Particle Image Velocity (PIV) was used to test and study the penetration characteristics of fu-el jet in air cross-flow under different fuel-air momentum ratio conditions. Furthermore, the numerical sim-ulation was applied to model the jet penetration characteristics, then the comparison were performed be-tween the test and computation results and the empirical expressions as well as the modified formula which the aerodynamic Weber number was calculated. The results indicate that the upper surface depth of fuel jet agrees well with the exponential correlation;the VOF model can be used to exactly simulate the penetration depth of spray core;the modified expressions coincide with the penetration depth of spray core with differ-ent fuel-air momentum ratio;the fuel-air momentum ratio and aerodynamic Weber number are the primary parameters that affect the penetration depth of fuel jet in cross-flow.

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为优化湿式静电除尘器清灰特性,研究喷嘴特性。采用相位多普勒粒子分析仪(PD A ),研究单喷嘴、双喷嘴同轴侧向撞击及喷嘴与壁面碰撞后的雾化特性,实验据表明液滴撞壁后形态主要由液滴自身动能、液滴表面张力和黏度决定,由韦伯数描述。距离喷嘴位置越远,喷嘴雾化角越大,索特尔平均粒径(SMD)波动越小,韦伯数分布越均匀,液膜均布性越好。在此基础上,对喷嘴布置方式与液膜均布性关系做进一步分析,得到喷淋管间距越大,喷嘴角度越大,极板上水膜更加均匀,该实验结果与喷嘴特性实验相符。
To improve the performance of collecting electrode cleaning ,spray nozzles characteristics was studied .With the Phase Droplet Particle Analyzer (PDA) applied on a pilot‐scale experiment system ,the atomization characteristics during the process of single nozzle atomization , double nozzle spray impingement and spray wall—impingement were studied .The results indicate that motion behavior of the spray wall—impingement is dominantly influenced by initial kinetic energy , surface tension and liquid viscosity which are described by the Weber number .The Sauter mean particle diameter (SMD) and Weber number become more stable when the atomization angle and distance from the atomization axes increase . Nozzle arrangements affect the uniformity of water film as well ,which were subsequently studied on a bench‐scale experiment system .The results show that the water film uniformity performs better as the atomization angle and distance from the atomization axes increase ,which agr

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该文结合了Ott提出的修正连续性方程和Adami改进的动量方程,对空气中的液滴碰撞问题进行了二维值模拟.为有效提高计算精度,推导了适用于大密度差多相流的人工黏性和人工应力方程.通过表面张力作用下方形液滴自然变化和空气中两液滴互溶的算例,验证了算法的有效性;对不同韦伯数(8.8,19.8)、不同碰撞参(0,0.5)下的液滴碰撞过程进行了值模拟,并与VOF方法对比,取得了较为一致的结果;进一步计算多个韦伯数、多个碰撞参下的液滴碰撞,得到了空气中二维液滴碰撞结果分布图,与实验结果相符合.结果表明,该算法对于求解涉及大密度差多相流的液滴碰撞破碎问题十分有效,而且该方法容易拓展到三维,从而为进一步模拟火箭发动机的二次雾化过程奠定了基础.
In this paper, the corrective continuity equation proposed by Ott and the momentum equation improved by Adami combine to solve two-dimensional simulation problems of droplet collisions in air. To effectively improve the calculation accuracy, the artificial viscosity equation and the artificial stress equation are derived which are suited for multi-phase flows with large density differences. This method is validated to be effective via examples of an initially square droplet under surface tension and in evolution process of two droplets in air. Droplet collisions for different Weber numbers (8.8, 19.8) and different impact parameters (0, 0.5) are simulated, all of which are compared with the results of VOF simulation. Through further calculation, distribution map of the two-dimensional droplet collision outcomes in air is obtained, which is in agreement with the experimental results. It is demonstrated that this method can be effective for solving problems of droplet collisions which ar

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水溶液中气泡聚并行为是化工流体力学研究中的一个重要内容,在化工、海洋和军事防护等诸多气液两相流相关领域中广泛存在并发挥着重要作用,研究气泡聚并具有重要的理论和应用价值。根据国内外关于气泡聚并的主要研究工作,对静止流场、复杂流场中气泡聚并机理以及韦伯数(We)、液体黏度、表面活性剂等影响气泡聚并的主要因素进行了综述,讨论了相关研究的不足,并对未来的研究方向进行了展望。
Bubble-coalescence at aqua solution is an important content of chemical hydrodynamics and exists at a lot of fields such as chemical engineering,ocean,military defend and plays an important role.So,it is very worthy to study its mechanism and the factor in theory and application.According to the study about bubble-coalescence at home and abroad,in this paper the mechanism at the statics and complex flows and the factor such as weber-number (WE),liquid viscosity,surfactants were summarized,the shortage of the research was discussed,and a primary expectation for the bubble-coalescence'' s future study was proposed.

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为了得到适用于微小通道内流动沸腾换热的预测方法,本文以近些年发表的9篇文献中的2924个实验据点组成据库,考虑到随着通道直径减小,表面张力对微小通道内两相流动和换热的影响起到主要作用,将Chen形式的换热模型中的核态沸腾和对流换热两部分的修正系进行了优化.沸腾抑制系和对流增强系由气相韦伯数、两相雷诺、沸腾、气泡抑制等量纲为1组成,反映出了表面张力、水力直径、流动条件、热力条件对于换热的综合影响.结果表明,拟合出的微小通道中沸腾换热的新模型,适于预测水力直径3 mm以下的细管道中CHF(临界热流密度)点以前的换热系.与实验据比较,新模型预测的平均绝对误差为19.0%.
In order to get a method for predicting the flow boiling heat transfer in mini-channels, 2924 experimental data of flow boiling in mini-channels from 9 literatures were analyzed. As the tube diameter decreases,the surface tension rather than the buoyancy affects the two phase flow and heat transfer. The enhancement factor of convective evaporation and suppression factor of nucleate boiling of Chen-type correlation were optimized. The non-dimensional number vapor Weber number,two-phase Reynolds number,boiling number and confinement number were used to express the effects of surface tension,diameter,flow conditions and heat flux. A new model was presented to predict the heat transfer coefficient of pre-dryout in mini-channels. A mean absolute deviation of 19.0%was achieved with this new correlation.

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在势流假设下,考虑表面张力以及黏性修正,建立自由液面在气泡破碎后全非线性运动的值模型,给出射流断裂和水滴撕裂的值处理方法.同时进行上浮气泡在自由液面破裂的实验研究,值解与实验值符合良好.为了研究自由液面在气泡破碎后的运动学机理和规律,运用开发的程序研究了不同尺寸气泡破碎后的动态特性,包括从气泡底部顶起的射流、射流断裂以及水滴分裂等复杂的物理现象,总结了从射流上撕裂出的第一个水滴尺寸、撕裂时间以及最大射流速度的变化规律.最后讨论了雷诺韦伯数对气泡破碎后自由液面运动的影响.
10.7498/aps.62.124704

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气泡在近自由液面运动过程中与自由液面发生强烈的耦合作用,自由液面会出现极其复杂的物理现象,形成的水冢类型繁多。本文将针对皇冠型水冢,基于势流理论,建立气泡与自由液面耦合作用的值模型,并在气泡完成射流向下运动时,忽略气泡对自由液面的影响,继续模拟自由液面的运动过程。同时利用高速摄影对近自由面的电火花气泡进行实验研究,值结果与实验符合良好,相对误差在10%以内。通过值计算,发现了围裙卷缩和主峰珠化等特殊的物理现象,研究了气泡初始条件与韦伯数对皇冠型水冢动态特性的影响,旨为皇冠型水冢的研究提供参考。
Strong interaction between bubble and free-surface will cause complex phenomena, producing many different types of spike. Based on potential flow theory, a numerical model was established to simulate the crown spike. A downward jet was formed during the bubble’s collapsing, and simulation of the free-surface was continued regard less of the ring bubble’s effect on it. Simulation results show good agreement with the experiment conducted with a high speed camera and a spark-generated device, and the relative error was less than 10%. Some special phenomena were found through numerical calculation, such as apron-shrink and peak-dropped. Finally, the effects of initial condition and Weber number on crown-type water column were studied.

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转子结构为相互嵌套填料环的新型旋转填料床是基于强化气膜控制传质过程的新型高效传质设备,可适用于受气膜控制的吸收、精馏和低浓度工业气体的净化等过程。分别以化学吸收体系CO2-NaOH和物理吸收体系NH3-H2O测定了不同气量、液气比和超重力因子条件下的有效比表面积a和气相体积传质系kya,并由此得到气相传质系ky,对其传质性能进行研究。实验结果表明:a、kya和ky均随着气量、液气比和超重力因子的增大而增大。通过对比可知,新型旋转填料床的气相体积传质系在相近操作条件下是文献逆流旋转填料床的2倍。并对实验据进行了回归,拟合出了a、kya和ky分别与气相雷诺ReG、液相韦伯数WeL和伽利略Ga之间的关联式。
A novel rotating packed bed (RPB) with the rotor consisting of nested packing rings is a new efficient apparatus for intensifying the gas-film controlled mass transfer process,and is used in the processes of absorption,distillation and purification for low concentration of industrial gas,which are controlled by gas-film mass transfer resistance. The mass transfer characteristics of the novel RPB were studied experimentally,interfacial area (a) was determined by chemical absorption with CO2-NaOH system and gas volumetric mass-transfer coefficient (kya) was measured by physical absorption with NH3-H2O system under different gas flux,liquid-gas ratio and super gravity factor conditions,and gas mass-transfer coefficient (ky) was obtained. The results showed that a,kya and ky increased with the increase of gas flux,liquid-gas ratio and super gravity factor. The kya of the novel RPB was two times higher compared to that of a conventional rotating packed bed under the same operational conditi

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本文针对毫米量级的上浮气泡在壁面处的弹跳现象进行值研究.基于势流方法求解气泡的运动,同时考虑气泡的表面张力作用.在伯努利方程中,对气泡与壁面之间水膜中因黏性引起的压力梯度进行修正,开发相应的计算程序,计算值与实验值符合良好.从气泡弹跳的基本现象入手,研究了特征参对气泡弹跳过程的动态特性以及最终平衡形态的影响.发现随着泡在撞击壁面之前上浮距离增大,气泡回弹距离和弹跳周期增加,但是当上浮距离增加到一定程度后将不会影响气泡的弹跳特性;表面张力是影响气泡弹跳特性的重要因素,气泡的弹跳周期随其增大逐渐减小,但回弹距离却呈现先增后减的规律;最后,影响气泡最终平衡形态的主要因素是气泡的浮力参韦伯数.
Some numerical studies were carried out on micrometer-sized rising bubble bouncing near a rigid boundary. Taking surface tension into consideration, the bubble motion could be solved using the potential flow theory. A correction should be made in Bernoulli equation because the pressure gradient was caused by the viscosity between the bubble and the wall. The numerical result agree well with the experimental data. Based on the fundamental phenomenon, we have studied the influence of characteristic parameter on bubble bouncing behavior, and the balanced shape due to the action of the wall. With the increase of the rising distance of the bubble, the distance of the bubble bouncing downward and the period of bouncing would increase. However, they would not change obviously when the rising distance is large enough. Surface tension has great effect on the dynamic behavior of the bubble. The bouncing period decreases when surface tension becomes large, but the bouncing distance will have an i

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