喷钙脱硫系统中增湿活化器的作用以及液滴和固体颗粒的碰撞实验研究

本文介绍了喷钙脱硫系统的实验研究结果，在调试工况和Ｃａ／Ｓ＝２．１３下采用增湿活化器能增加脱硫率１２．２％；此值和液滴蒸发所需时间有关。本文还利用多脉冲激光全息冷态试验台，对雾化液滴与固体颗粒的碰撞做了初步研究，证实了碰撞的存在，为增湿脱硫机理中的碰撞模型提供了依据。     

增湿活化反应器内气—液滴—固三相流场的数值模拟

本文给出了气—液滴—固三相流体的双流体模型下的各控制方程组。颗粒动理学方法模拟颗粒相湍动能。模型中考虑了气、液滴和固相的相互作用以及液滴与固相的非弹性作用造成的能量传递和耗散。模型预测在增湿活化反应器内相速度和浓度等参数空间分布,以及操作参数、结构布置等对相速度等参数的影响。     

脱硫塔内单液滴捕集颗粒物的数值模拟

针对脱硫塔内单液滴捕集颗粒物,建立了考虑惯性、拦截、布朗扩散、热泳和扩散泳作用的单液滴捕集颗粒物模型。基于数值模拟结果分析了温度、液滴直径和颗粒粒径对单液滴捕集过程及效率的影响规律。无量纲分析表明,对脱硫塔环境下亚微米颗粒物的捕集,泳力作用强于惯性作用。推导了考虑Stefan流的扩散泳效率计算公式,经数值模拟结果检验,采用该公式能够准确地计算湿法脱硫过程对颗粒物的脱除效率。     

液滴振荡模型及与数值模拟的对比

由于碰撞壁面后液滴内部流动的复杂性, 以及气-液-固三相间的相互作用, 对液滴碰撞壁面形态变化的数学理论研究有较大的难度, 因此所见者多为实验和数值模拟. 本文通过对液滴受力状态的分析, 得到了惯性力、黏性力和表面张力带经验系数的表达式, 并进一步建立了液滴碰撞壁面振荡模型, 得到了液滴铺展半径的振荡表达式, 以及表面张力、黏性系数等参数对液滴铺展的影响. 最后通过与液滴衰减振荡数值模拟结果的对比, 确定了液滴振荡模型中的修正系数, 验证了模型的可行性. 关键词： 液滴碰撞 振荡 铺展半径/高度 数值模拟     

等直径微液滴碰撞过程的改进光滑粒子动力学模拟

运用一种改进光滑粒子动力学(SPH)方法模拟了相溶和不相溶两种情况下的等直径微液滴碰撞动力学过程. 为提高传统SPH方法的数值精度和稳定性, 采用一种不涉及核导数计算的核梯度改进形式; 为处理液滴界面张力采用修正的van der Waals表面张力模型. 通过模拟牛顿液滴碰撞聚并变形过程并与相关文献或试验结果进行对比, 验证了改进SPH 方法模拟微液滴碰撞过程的可靠性. 随后, 研究了基于van der Waals模型相溶聚合物微液滴碰撞聚并变形过程及不相溶微液滴碰撞后的反弹、分离过程, 讨论了碰撞过程中碰撞速度、碰撞角度、密度比等参数对碰撞变形过程的影响, 分析了流体桥、旋转角度等因素的变化情况. 关键词： 光滑粒子动力学 微液滴 聚合物液滴 碰撞     

基于大密度差多相流SPH方法的二维液滴碰撞数值模拟

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数值模拟. 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)、不同碰撞参数 (0, 0.5)下的液滴碰撞过程进行了数值模拟, 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、多个碰撞参数下的液滴碰撞, 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. 关键词： 光滑粒子流体动力学 大密度差 多相流 液滴碰撞     

脱硫废水液滴与飞灰颗粒碰撞特性数值研究

在利用烟道余热喷雾蒸发脱硫废水时,烟道中的飞灰会与喷雾液滴发生碰撞,进而影响废水处理效率.本文利用大涡模拟(LES)和离散相模型(DPM),模拟脱硫废水喷入烟道的雾化过程及粒径分布,重点考察了烟道飞灰与喷雾液滴碰撞时烟道流场分布及液滴空间分布,分析了Stokes数和喷雾角对流场和空间分布的影响规律.研究结果表明,采用空气雾化喷嘴雾化333.33 L·h~(-1)的脱硫废水,喷雾液滴的粒径分布为20～250μm;无飞灰进入烟道时,Stokes小于1时喷雾液滴速度衰减极快,Stokes大于1时喷雾液滴速度衰减最慢,且喷雾角较大时衰减更快;含飞灰进入烟道时,由于动量交换,喷雾液滴速度衰减更快,且碰撞主要发生于速度衰减到35 m·s~(-1)后的位置.     

风沙跃移中颗粒与多粒径床面碰撞的数值模拟

采用考虑颗粒碰撞的欧拉-拉格朗日数值模拟方法,对风沙跃移中颗粒冲击多粒径床面的碰撞过程进行了数值计算。在模型中,对气相采用欧拉方法建立控制方程,对离散颗粒采用拉格朗日方法模拟,颗粒间碰撞作用采用软球模型描述。计算结果表明该模型可以模拟风沙运动中颗粒冲击多粒径床面的动态运动过程。而且在多粒径非均匀床面上的颗粒起跳具有较大的随机性。这有助于进一步揭示风沙运动中颗粒碰撞起跳机理。     

超细CaO粉炉内喷射脱硫的实验研究

本文对超细ＣａＯ粉炉内喷射脱硫进行了实验研究，分析了可能影响超细ＣａＯ粉炉内脱硫效率的多种因素，实验结果表明：使用预先锻烧生成的超细ＣａＯ粉在并不苛刻的反应条件下脱硫效果很好，颗粒大小、反应区温度、反应时间和Ｃａ／Ｓ比对炉内喷钙脱硫的效率有重要的影响．     

外加液滴条件下固体细颗粒声凝并特性

外加声场激励下固体细颗粒的声凝并在燃烧污染物超低排放中具有应用潜力,添加大粒径液滴有望提高细颗粒声凝并效果.本文从颗粒运动、碰撞、凝并与反弹的动力学过程出发,基于直接模拟蒙特卡罗方法,建立气相中液滴与固体颗粒共存的气-液-固三相体系的声凝并模型,对外加液滴条件下固体细颗粒声凝并的过程和效果开展数值模拟.将模拟结果与实验相对比,验证模型可靠性.在此基础上,探究外加液滴条件下细颗粒声凝并动力学行为,考察外加液滴直径和数目浓度对细颗粒声凝并效果的影响规律.结果表明,外加液滴条件下,固体细颗粒迅速与大粒径液滴凝并,形成液-固混合相颗粒,细颗粒凝并效率显著提升.外加液滴直径和数目浓度是影响细颗粒声凝并的重要因素,随着直径的增大或数目浓度的提高,细颗粒凝并效率增大,而增幅趋于减小.研究结果可为复杂颗粒系统凝并模型的建立提供理论基础,并可为燃烧源细颗粒超低排放提供方法指导.     

深空环境下液滴辐射相变过程分析模拟

太空中固体粒子比液体粒子对航天器危害性大,计算液滴相变时间和温度变化对评估粒子危害性有重要意义.本文建立了太空环境下液滴辐射相变模型,分析了三种相变凝固模型,估计了水滴蒸发量,考虑了太阳辐射对液滴温度变化的影响,分别计算了水和氧化铝液滴的温度变化.结果表明:液滴粒径越小液滴冷却速率越大,三种相变凝固模型的相变时间差别较小;水滴蒸发比例均大于10%,其蒸发量不可忽略;水滴受太阳周期性辐射时,其温度在50 K至266 K之间周期性振荡变化.     

带凹槽的微通道中液滴运动数值模拟

运用改进的耗散粒子动力学方法模拟了液滴在由凹槽所构成的粗糙表面微通道内的运动行为.改进的耗散粒子动力学方法采用新近提出的一种短程排斥、长程吸引相互作用势能函数,从而可以模拟带有自由面的流体,如液滴等.模拟了新势能函数下液滴与固体壁面的静态接触角,并用2次多项式拟合了"接触角-a_wf/a_f"变化曲线.研究了液滴在带凹槽的微通道中运动时,微通道壁面浸润性、外场力、液滴温度对液滴流动特性的影响.研究表明壁面浸润性和外场力对液滴流动特性的影响较大,液滴温度对液滴流动特性的影响较小.研究结果对运用耗散粒子动力学方法模拟并分析微流体在复杂微通道的流动有一定的参考价值.     

Peculiarities of heat transfer in water droplets with a solid inclusion during heating in a high-temperature gas medium

A physical model and a mathematical model of heat transfer in the conditions of inhomogeneous (with a solid inclusion—a carbon particle) liquid droplet evaporation while moving through high-temperature (800–1500 K) gases are formulated. Numerical investigations were performed using, as an example, a spherical inhomogeneous water droplet during heating in the air medium. The most probable mechanism of phase transitions in a water–carbon particle–heated air system is considered (the initial droplet size, radius, varied in the range from 0.5 mm to 1.5 mm, the inclusion radius was 0.1–1 mm). It has been found that in certain conditions, besides water evaporation from the outer (free) droplet surface, intensive vaporization is possible at the liquid–solid inclusion interface. Conditions of realization of these phase transitions in inhomogeneous water droplet–high-temperature gas medium systems are identified.     

Numerical study on the desorption processes of oil droplets inside oil-contaminated sand under cavitation micro-jets

The removal of the adsorbed oil droplet is critical to deoiling treatment of oil-bearing solid waste. Ultrasonic cavitation is regarded as an extremely useful method to assist the oil droplets desorption in the deoiling treatment. In this paper, the effects of cavitation micro-jets on the oil droplets desorption were studied. The adsorbed states of oil droplets in the oil-contaminated sand were investigated using a microscope. Three representative absorbed states of the oil droplets can be summarized as: (1) the individual oil droplet adsorbed on the particle surface (2) the clustered oil droplets adsorbed on the particle surface; (3) the oil droplet adsorbed in a gap between particles. The micro-jet generation during the bubble collapse near a rigid wall under different acoustic pressure amplitudes at an ultrasonic frequency of 20 kHz was investigated numerically. The desorption processes of the oil droplets at the three representative absorbed states under micro-jets were also simulated subsequently. The results showed that the acoustic pressure has a great influence on the velocity of micro-jet, and the initial diameter of cavitation bubbles is significant for the cross-sectional area of micro-jets. The wall jet caused by a micro-jet impacting on the solid wall is the most important factor for the removal of the absorbed oil droplets. The oil droplet is broken by the jet impinging, and then it breaks away from the solid wall due to the shear force generated by the wall jet. In addition to a higher sound pressure, the cavitation bubble at a larger initial diameter is more important for the desorption of the clustered oil droplets. Conversely, the micro-jet generated by the cavitation bubble at a smaller initial diameter (0.1 mm) is more appropriate for the desorption of the oil droplet in a narrow or sharp-angled gap.     

液体物性对雾化射流液雾粒径的影响

对不同液体在空气中湍动雾化射流的气液两相流场进行了数值模拟.建立了一次雾化的一维模型,分析了粘度、表面张力和气液质量流量比对液雾粒径的影响趋势,采用基于粒子追踪法的二次雾化三维模型,分析了物性和各种工况对液雾粒径沿轴向分布的影响程度.计算结果和已公开发表的实验数据进行比对,得到了较好的吻合,在此基础上,分析了影响气泡雾化喷嘴雾化质量的主要因素.     

溶液液滴蒸发变干的环状沉积

液体蒸发驱动的颗粒自组装现象在许多的工业技术中有重要应用. 本文利用显微镜观测含有颗粒物质的液滴变干后留在固体表面的颗粒形成的环状沉积图案. 采用微米粒径的SiO₂小球水溶液液滴蒸发变干模拟咖啡环的形成过程, 结果发现液滴蒸发过程中接触线的钉扎是环状沉积的必要条件. 在液滴蒸发过程中颗粒随着补偿流不断的向液滴边缘移动, 聚集在接触线处形成环. 液滴蒸发变干后残留在液滴内部的颗粒数随颗粒质量分数的增加而增加, 可以达到单层的颗粒排列. 而玻璃衬底上的颗粒环在颗粒质量分数很小时, 形成单层排列, 且一排一排地生长. 蒸发过程中颗粒环由于液滴边缘的尺寸限制向液滴中心缓慢移动. 这会导致液滴中不同大小颗粒的分离. 关键词： 液滴 接触线 蒸发 颗粒     

激波诱导的液滴变形和破碎

 建立液滴变形与破碎的模型,提出初始雾化时间概念,由此分析激波后液滴变形和破碎雾化的特征。液滴变形率、完全破碎时间的数值分析结果与实验结果基本一致。     

Enhanced nanoparticle detection with liquid droplet resonators

Whispering gallery mode particle sensing experiments are commonly performed with solid resonators, whereby the sensing volume is limited to the weak evanescent tail of the mode near the resonator surface. In this work we discuss in detail the sensitivity enhancements achievable in liquid droplet resonators wherein the stronger internal fields and convenient means of particle delivery can be exploited. Asymptotic formulae are derived for the relative resonance shift, line broadening and mode splitting of TE and TM modes in liquid droplet resonators. As a corollary the relative fraction of internal and external mode energy follows, which is shown to govern achievable sensitivity enhancements of solute concentration measurements in droplet sensors. Experimental measurements of nanoparticle concentration based on whispering gallery mode resonance broadening are also presented.     

Estimating critical surface tension from droplet spreading area

Critical surface tension (CST) is a measure of solid surface tension and is mainly determined by measuring the contact angle of a droplet on a target solid surface. The concept of CST makes it possible to determine solid surface tension without any unprovable assumptions such as the Fowkes hypothesis. However, it requires somewhat special devices and skills for measuring the contact angle. In this work, we propose a simple method to determine the CST of a solid by measuring the droplet spreading area. This method is developed by combining the conventional CST with a simple analytical droplet model. The difference in estimated CSTs between our method and the conventional one is within 3.0%. Our method enables a quick and simple evaluation of the solid surface tension without special devices for measuring the contact angle.     

Size Measurement of Very Small Spherical Particles by Mie Scattering Imaging (MSI)

The Mie Scattering Imaging method (MSI) gathers out‐of‐focus images of dispersed spherical particles present in a laser light sheet and extracts the individual particle diameter from these images. The general idea of the method has been around for more than a decade and a number of papers has dealt with it over recent years. Our work focuses on small particle sizes from 20 μm down to 2 μm, a range which has not been tackled so far although it is of great importance in particle systems. We present an optical set‐up with a special arrangement of camera lenses that allows to work in this range. An evaluation algorithm based on correlation of the experimental optical information with theoretical Mie scattering was found to give the most accurate results for particle sizing. Besides accuracy measurements on solid spheres the versatility of the method is demonstrated by an example of transient droplet growth between 2–7 μm.