435 m2烧结机机头化学团聚强化细颗粒物及重金属脱除试验研究

针对某435 m²烧结机机头,在静电除尘器前安装化学团聚强化除尘系统,研究化学团聚强化细颗粒物及重金属（As、Cr、Cd、Ni、Cu、Pb、Zn七种）脱除特性。实验结果表明,化学团聚后,细颗粒团聚成较大颗粒,静电除尘器后烟气中PM₁₀、PM_2.5、PM₁颗粒质量浓度均降低49%以上,静电除尘器飞灰平均粒度增长46%以上,细颗粒物团聚效果显著,提升了静电除尘器脱除细颗粒物效率;静电除尘器飞灰及细颗粒物中重金属质量浓度上升,静电除尘器后烟气中重金属质量浓度均下降,表明化学团聚作用促使气态重金属向颗粒态重金属及飞灰中迁移,细颗粒重金属团聚长大。化学团聚不仅可以强化细颗粒物的脱除,同时有效提升了重金属的脱除效率。     

燃烧源PM2.5凝结洗涤脱除实验研究

利用蒸汽在燃烧源PM2.5表面凝结,促使PM2.5凝结长大,建立一套燃烧源PM2.5凝结洗涤的实验台;考察了颗粒粒径分布、蒸汽添加量、液气比等对两种燃烧源PM2.5凝结洗涤脱除效果的影响。采用电称低压冲击器 (ELPI)在线测试分析燃煤和燃油PM2.5凝结洗涤前后的数浓度和粒径分布特性,并用SEM和XPS对两种不同燃烧源的颗粒进行了形貌和元素组分分析。结果表明,燃煤和燃油产生的PM2.5形貌和组分具有较大的差别,燃煤PM2.5主要为硅铝矿物质,而燃油PM2.5主要为含炭物质;相同条件下,燃煤PM2.5相变脱除效果优于燃油PM2.5;随着蒸汽添加量的增加,两者的脱除效率均升高;随粒径的增大,脱除效率提高;蒸汽添加量为0.08kg/m3时,粒径为0.4μm的燃煤和燃油细颗粒的脱除效率分别81％和72％;此外,适当增加液气比有利于凝结长大含尘液滴的脱除。     

脱硫废水蒸发增强电除尘脱除PM2.5和SO3实验研究

搭建燃煤热态实验系统,研究脱硫废水蒸发对电除尘和脱硫系统的影响;考察脱硫废水蒸发前后细颗粒粒径的变化、电除尘出口PM_2.5和SO₃浓度变化;分析增强电除尘脱除PM_2.5和SO₃机理。结果表明,脱硫废水蒸发后,蒸发室出口细颗粒粒径峰值由0.1 μm增大到1.1 μm,观察脱硫废水蒸发前后扫描电镜,明显观察到废水蒸发后颗粒团聚长大,颗粒间存在絮状物;采用脱硫废水烟道蒸发后,电除尘细颗粒脱除效率提高5%左右,PM_2.5数量浓度脱除效率提高25%左右;SO₃脱除效率为60%-80%,烟气中SO₃浓度对增强电除尘脱除PM_2.5和SO₃均有影响;脱硫废水蒸发对脱硫系统的效率和脱硫浆液的pH值没有影响。     

两种不同类型的声场与声化学产额的关系

采用声源频率为1.8 MHz的连续声波在声强0～5 W•cm－2间,研究了连续混响声场中声化学产领(以溶液的电导率改变、溶液pH值改变和KI溶液的I2析出量以及空化水中的水合负电子()表征)与声强和超声辐照时间之间的关系.理论推论与实验结果均表明,连续声场中声化学产额与声强、超声辐照时间之间呈线性关系.并证明了声场中声化学反应动力学方程具有简单线性关系,与Henglein等人对脉冲声场中声化学产额与声场参数之间呈非线性关系的研究结果比较,证明对实际工业化运行的声化学反应器,采用连续声波更利于目标反应生成物的控制。     

纳米结构表面浸润性质的分子动力学研究

采用分子动力学方法研究了氩纳米液滴在铂金属及其模型固体表面的浸润现象,获得了液滴在平滑表面和三角纳米结构阵列表面的接触角和展布特性.研究表明,液滴与壁面的势能作用较强时,液滴与纳米结构表面为均匀浸润,但是由于迟滞效应,接触角受表面纳米结构的影响不明显;势能作用较弱时,纳米结构间隙中存在类似蒸汽的低密度相,液滴与纳米结构表面为非均匀浸润,接触角受纳米结构的影响而增大;表面纳米结构可以使表面具有超疏水性.     

臭氧氧化结合湿法喷淋对玻璃窑炉烟气同时脱硫脱硝实验研究

采用臭氧氧化结合湿法喷淋对模拟玻璃窑炉烟气开展了同时脱硫脱硝实验研究.采用不同溶液(NaOH、Na₂S)进行了喷淋实验.结果表明,保证溶液pH值在10以上,NaOH浓度对NO_x脱除效率无影响,SO₂的存在促进了NO_x吸收.当O₃/NO物质的量比为1.6、溶液NaOH浓度为0.5%时,NO_x脱除效率可达70%,SO₂脱除效率在99%以上.往喷淋液中添加Na₂S,NO_x脱除效率随Na₂S浓度增加而提高,SO₂的存在对NO_x脱除效率无影响.当O₃/NO物质的量比为1.2、溶液中NaOH浓度为0.5%、添加剂Na₂S浓度为0.6%时,NO_x脱除效率可达70%,SO₂脱除效率在95%以上.60 min长时间运行实验证明,模拟烟气中的NO_x经碱液和添加剂吸收后主要以NO^-₂的形式存在于喷淋液中,且NO_x脱除效率不随溶液pH值的变化而变化.     

纳米结构表面上冷凝液滴的生长模式及部分润湿液滴的形成机制

分析并计算了纳米结构表面上冷凝液滴按照不同途径长大的过程中液滴能量的增加速率, 并以能量增加最小为判据来确定液滴的生长途径. 结果表明, 纳米结构内形成的冷凝液斑在初期按接触角(CA)增加的模式生长时, 其能量增加速率远低于其它模式, 于是, 初始液斑先按增大接触角、并保持底面积不变的模式生长, 直至液滴达到前进角状态. 此后, 沿接触角增加的模式长大所导致的能量增加速率开始远高于其它生长模式, 于是液滴三相线开始移动, 底面积开始增加, 但接触角保持不变. 液滴所增加的底面积可以呈润湿或复合两种状态, 分别形成Wenzel 液滴及部分润湿液滴, 前者的表观接触角一般小于160°, 而后者则明显大于160°. 液滴的生长模式及其润湿状态均与纳米结构参数密切相关, 仅当纳米柱具有一定高度、且间距较小时, 冷凝液滴才能呈现部分润湿状态. 最后, 本模型对纳米结构表面上冷凝液滴润湿状态的计算结果与绝大部分实测结果相一致, 准确率达到91.9%, 明显高于已有公式的计算准确率.     

粘胶/炭黑复合纤维素纤维的结构与性能研究

将炭黑水悬浮溶液与粘胶原液共混制得不同添加比例的纺丝溶液,通过湿法纺丝制备炭黑复合粘胶纤维。采用扫描电镜(SEM)、广角X射线衍射仪(WAXD)及纤度强度仪等分析所制备纤维的结构与性能。WAXD分析结果表明,不同添加比例炭黑的复合纤维均为纤维素Ⅱ型晶体结构,结晶度随着炭黑添加量的增加逐渐降低;SEM结果显示,不同添加比例的炭黑在粘胶基体中的分布都较均匀,没有明显团聚现象,但是随着添加量的增加,纤维的孔隙增大增多,光滑性下降,但纤维仍然保持锯齿截面形状;对纤维力学性能分析结果表明,添加适量的炭黑可使复合纤维素纤维力学性能提高,而添加过量时,力学性能反而降低。     

无模板剂预晶化液添加法合成ZSM-5分子筛

研究了旋转烘箱中无模板剂条件下,预晶化液添加对合成ZSM-5分子筛的影响。系统研究了预晶化液加入量对合成分子筛晶化速率及颗粒大小的影响。采用X射线衍射,扫描电镜,N2吸附-脱附,和激光粒度分布等分析方法对合成的ZSM-5分子筛样品的物化性能进行了表征。结果表明,预晶化液的添加可以明显加快分子筛的晶化速率,预晶化液添加量为33.3wt%时达到最大结晶度的合成时间由未添加时的48 h减少到24 h。添加预晶化液的母液在150℃晶化24 h时所得ZSM-5分子筛团聚体的颗粒大小随着预晶化液加入量的增大而增大,由5.5μm增大到26.3μm。团聚体颗粒的比表面积比未添加预晶化液得到的分子筛(292 m2.g-1)有了不同程度的提高,如添加量为33.3wt%时为394 m2.g-1。对预晶化液添加法合成ZSM-5分子筛团聚体颗粒的生长机理进行了讨论。     

Fe~(2+)协同热活化过一硫酸氢钾盐诱导自由基脱除NO的研究

在气液撞击流反应器中,研究了Fe~(2+)协同热活化过一硫酸氢钾盐诱导自由基脱除模拟烟气中的NO。考察了主要工艺参数(溶液温度、Fe~(2+)浓度、过一硫酸氢钾盐浓度、溶液pH值、NO入口浓度)对NO脱除效率的影响。分析检测了反应产物和自由基。基于不同系统的对比研究、反应产物检测和活性自由基的捕获,揭示了NO脱除过程的机制和反应路径。结果表明,提高溶液温度、Fe~(2+)浓度和过一硫酸氢钾盐浓度均提高了NO的脱除效率,而提高溶液pH值和NO入口浓度均降低了NO的脱除效率。Fe~(2+)和热对活化过一硫酸氢钾盐产生自由基有显著的协同效应。自由基氧化是NO脱除的主要路径,而过一硫酸氢钾盐直接氧化是次要的脱除路径。Fe~(2+)和热的协同活化体系具有比其他体系高得多的NO脱除率。     

炉前煤低温干馏工艺中的挥发分除尘

为了寻求优化的炉前煤低温干馏工艺中的挥发分除尘方案，在使用400目金属滤网对间歇式粉煤固体热载体热解装置挥发分除尘研究的基础上，将颗粒床过滤器用于该过程的除尘研究。热态除尘实验表明，颗粒床的使用有效地降低了滤网的过滤负荷。选用2mm石英砂和φ5mm×2mm瓷环作为滤料，通过对比实验发现，两种滤料除尘效率均在90％以上；随着过滤操作的进行，由于颗粒床内粉尘的沉积使其过滤效率有所提高，而对气、液收率的影响很小。结果表明，颗粒床与滤网结合可作为粉煤炉前低温干馏工艺中可供选择的挥发分除尘方案。     

LIFAC烟气脱硫中应用蒸汽相变促进细颗粒物脱除的实验研究

在炉内喷钙尾部增湿活化(LIFAC)脱硫后的低温高湿烟气中添加适量蒸汽建立蒸汽相变所需的过饱和环境,促进水汽在细颗粒物表面凝结,进而由高效除雾器脱除凝结长大的含尘液滴.采用电称低压冲击器(ELPI)实时测定细颗粒物数量浓度及粒径分布,维萨拉温湿度变送器测试烟气温度和湿度.考察了活化水添加量、蒸汽添加量、细颗粒物数量浓度...     

Particle capture processes and evaporation on a microscopic scale in wet filters

This paper details results of an experimental study of the capture of solid and liquid aerosols on fibrous filters wetted with water. A microscopic cell containing a single fibre (made from a variety of materials) was observed via a microscope, with a high speed CCD camera used to dynamically image the interactions between liquid droplets, zeolite and PSL particles and fibres. Variable quantities of liquid irrigation were used, and the possibility for subsequent fibre regeneration after clogging or drying was also studied. It was found that drainage of the wetting liquid (water) from the fibres occurred, even at very low irrigation rates when the droplet consisted almost completely of captured particles. It was also found that the fibre was rapidly loaded with captured particles when the irrigation was not supplied. However, almost complete regeneration (removal of the collected cake) by the liquid droplets occurred shortly after recommencement of the water supply. The study also examined the capture of oily liquid aerosols on fibres wetted with water. A predominance of the barrel shaped droplet on the fibre was observed, with oil droplets displacing water droplets (if the oil and fibre combination created a barrel shaped droplet), creating various compound droplets of oil and water not previously reported in literature. This preferential droplet shape implies that whatever the initial substance wetting a filter, a substance with a greater preferential adherence to the fibre will displace the former one.     

Removal of fine powders from film surface. I. Effect of electrostatic force on the removal efficiency

A novel fine particle removal system composed of a corona-discharge neutralizer, a pulse-jet air unit and an image processing system has been developed. First of all, adhesion force between particle and film was directly measured and effect of electrostatic force on the adhesion force was calculated experimentally and theoretically. The electrostatic force was found to be significant, leading to the suggestion that the countermeasure for the electrostatic force was required to effectively remove fine particles. This system was then applied to the removal of fine particles from surface of a gelatin film used for conventional capsule material. The number of particles removed by the system was calculated by an image processing system and number base removal efficiency was computed with and without the elimination of electrostatic charge by the neutralizer. It was found that the difference between the removal efficiency of particles with elimination of electrostatic charge and that of without the elimination showed linear relationship with the electrostatic adhesion force. The data confirmed the necessity of electrostatic charge elimination for the effective removal of fine particles.     

EWOD driven cleaning of bioparticles on hydrophobic and superhydrophobic surfaces

Environmental air monitoring is of great interest due to the large number of people concerned and exposed to different possible risks. From the most common particles in our environment (e.g. by-products of combustion or pollens) to more specific and dangerous agents (e.g. pathogenic micro-organisms), there are a large range of particles that need to be controlled. In this article we propose an original study on the collection of electrostatically deposited particles using electrowetting droplet displacement. A variety of particles were studied, from synthetic particles (e.g. Polystyrene Latex (PSL) microsphere) to different classes of biological particle (proteins, bacterial spores and a viral simulant). Furthermore, we have compared ElectroWetting-On-Dielectric (EWOD) collecting efficiency using either a hydrophobic or a superhydrophobic counter electrode. We observe different cleaning efficiencies, depending on the hydrophobicity of the substrate (varying from 45% to 99%). Superhydrophobic surfaces show the best cleaning efficiency with water droplets for all investigated particles (MS2 bacteriophage, BG (Bacillus atrophaeus) spores, OA (ovalbumin) proteins, and PSL).     

Microparticle sampling by electrowetting-actuated droplet sweeping

This paper describes a new microparticle sampler where particles can be efficiently swept from a solid surface and sampled into a liquid medium using moving droplets actuated by the electrowetting principle. We successfully demonstrate that super hydrophilic (2 microm and 7.9 microm diameter glass beads of about 14 degrees contact angle), intermediate hydrophilic (7.5 microm diameter polystyrene beads of about 70 degrees contact angle), and super hydrophobic (7.9 microm diameter Teflon-coated glass beads and 3 microm size PTFE particles of over 110 degrees contact angles) particles on a solid surface are picked up by electrowetting-actuated moving droplets. For the glass beads as well as the polystyrene beads, the sampling efficiencies are over 93%, in particular over 98% for the 7.9 microm glass beads. For the PTFE particles, however, the sampling efficiency is measured at around 70%, relatively lower than that of the glass and polystyrene beads. This is due mainly to the non-uniformity in particle size and the particle hydrophobicity. In this case, the collected particles staying (adsorbing) on the air-to-water interface hinder the droplet from advancing. This particle sampler requires an extremely small amount of liquid volume (about 500 nanoliters) and will thus be highly compatible and easily integrated with lab-on-a-chip systems for follow-up biological/chemical analyses.     

Homogeneous nucleation at high supersaturation and heterogeneous nucleation on microscopic wettable particles: A hybrid thermodynamic/density-functional theory

Homogeneous nucleation at high supersaturation of vapor and heterogeneous nucleation on microscopic wettable particles are studied on the basis of Lennard-Jones model system. A hybrid classical thermodynamics and density-functional theory (DFT) approach is undertaken to treat the nucleation problems. Local-density approximation and weighted-density approximation are employed within the framework of DFT. Special attention is given to the disjoining pressure of small liquid droplets, which is dependent on the thickness of wetting film and radius of the wettable particle. Different contributions to the disjoining pressure are examined using both analytical estimations and numerical DFT calculation. It is shown that van der Waals interaction results in negative contribution to the disjoining pressure. The presence of wettable particles results in positive contribution to the disjoining pressure, which plays the key role in the heterogeneous nucleation. Several definitions of the surface tension of liquid droplets are discussed. Curvature dependence of the surface tension of small liquid droplets is computed. The important characteristics of nucleation, including the formation free energy of the droplet and nucleation barrier height, are obtained.     

330 MW燃煤机组异相凝并对重金属排放控制的实验研究

湖北某电厂1号机组容量为330 MW，配备双室四电场静电除尘器，为了考察异相凝并技术对细颗粒物以及重金属脱除效率的影响，对1号机组除尘器前后，脱硫塔后进行颗粒物与重金属采样测试。结果表明，在烟道中喷射凝并吸附剂后，ESP入口颗粒态重金属占比增加，其中，Se元素在PM_2.5和PM₁₀上增加尤为明显，而气态的重金属含量有所降低，表明凝并吸附剂增强了颗粒态重金属的凝并效果，小颗粒态与气态重金属通过异相凝并过程转移至大颗粒态。喷入凝并吸附剂后，石膏中重金属含量显著降低，说明能够进入脱硫石膏的重金属含量减少，异相凝并提升了ESP对重金属的脱除作用；在尾部烟道末端烟囱排放口采样点，重金属含量相较于未喷入凝并吸附剂的工况，有着明显的降低，表明了经过异相凝并之后，排放至大气中的重金属显著减少，异相凝并对于重金属的控制起到关键作用。     

纸张涂料用纳米CaCO3表面改性的研究

利用铝锆偶联剂对纳米CaCO₃进行表面改性。采用红外光谱(IR)、X射线衍射分析(XRD)、热分析(TG-DTG)对改性前后的纳米CaCO₃进行了表征。通过透射电镜(TEM)、粒度分析、吸油值、比表面积及静滴接触角等实验对纳米CaCO₃的表面改性效果进行评价。红外光谱分析表明，偶联剂以化学键合的方式在纳米CaCO₃的表面形成化学吸附。TEM及粒度分析结果显示，未改性纳米CaCO₃存在严重的团聚现象，而改性后纳米CaCO₃的分散性有很大改善。经表面改性，水滴在纳米CaCO₃粉体压片表面静滴接触角变大，改性纳米CaCO₃同时具有亲水性和亲油性，能够较好地分散在水和有机相中。将改性前后的纳米CaCO₃分别加入到纸张涂料体系中，制得纳米CaCO₃复合纸张涂料。涂料流变实验表明，经铝锆偶联剂表面改性的纳米CaCO₃制得的复合纸张涂料具有较高的动态弹性模量和粘性模量。