电袋复合除尘器荷电粉尘层特性实验

针对电袋复合除尘系统中的粉煤灰和氧化铝粉尘层荷电电压的动态变化进行了实验研究.结果表明,粉煤灰或氧化铝粉尘荷电后,在同一粉尘负荷下,随着电场电压的升高,粉尘层的荷电电压值(稳定值)呈现出先升高后降低的趋势;而在同一电场电压下,氧化铝粉尘层的荷电电压值明显低于粉煤灰粉尘层的荷电电压值.对荷电粉尘层的研究将有助于更好地分析...     

电袋复合除尘器的应用研究

针对我国燃煤电厂的除尘现状,指出电袋复合除尘器的技术经济优势.电袋复合除尘器在新建及改扩建电厂的成功应用取得了良好的经济、环境效益,并有广阔的发展前景.其研究重点是静电除尘单元和布袋除尘单元之间的结合.     

电袋复合除尘器中产生氧化性物质的研究

针对电袋复合除尘器前级电场电晕放电有可能会产生臭氧,而臭氧又迅速与烟气中NO反应生成NO2这一猜想,通过对实际工况下电袋复合除尘器中臭氧含量和NOX浓度进行的测试,得出电袋复合除尘器中并无臭氧产生,且NO2浓度也未增加。但烟气中NO2浓度已经接近除尘器PPS滤料在使用温度下(150℃)所能承受的最高限值,PPS滤料会因发生氧化而失效,缩短滤料使用寿命。     

电袋除尘器在燃煤火电厂的应用

描述了除尘设备对于火电厂的重要性,介绍了燃煤火电厂除尘器的主要形式及除尘原理,并对各种形式的除尘器进行了技术经济比较,进而指出电袋除尘器在燃煤火电厂应用的必要性。     

电除尘器改造为电袋除尘器的应用与实践

为了满足新的大气污染物排放标准,将某钢铁企业电除尘器改造为电袋除尘器,效果表明,电袋除尘器能满足排放要求.     

烧结机尾“电改袋”除尘器数值模拟

针对现有"电改袋"除尘器不易实现在运行中更换滤袋且内部气流分布不均匀等问题,结合某烧结厂190 m2"电改袋"工程实例,提出一种可以在运行中更换滤袋的分室式"电改袋"除尘器结构,并利用CFX软件模拟其流场。结果表明,烟气由进气烟道进入袋室时速度大小和方向均发生突变,大颗粒粉尘受惯性力和重力作用易被中间灰斗捕集,有效减缓粉尘对滤袋的磨损;滤袋底部附近区域和两侧灰斗内的烟气速度分别小于5 m/s和6 m/s,可有效防止滤袋间的碰撞磨损和灰斗二次扬尘;各袋室的烟气流量分布比较均匀,标准差为0.152。     

电-袋除尘装置环形结构中的流场研究

根据静电学和流体力学理论,利用CFD软件,对圆柱形电-袋除尘装置中的气流分布情况进行研究。研究结果表明,除尘装置的内外圆收尘板间的气流速度呈梯度分布,有利于粉尘颗粒在内外圆收尘板上的沉降,但电场区后端处的气流分布不均匀,不利于过滤收尘。过滤风速与滤袋长度呈正相关,影响滤袋寿命。滤袋下方的集灰区存在漩涡,气流对集灰斗箱体产生了严重的冲刷,导致二次扬尘。     

电-袋式除尘器的仿真研究

在建立电除尘单元和袋式除尘单元仿真数学模型的基础上,开发了1套电-袋式除尘器系统仿真软件.并通过仿真实验验证了模型的合理性和可行性.     

电袋一体式除尘技术的应用解析

讲述了电袋一体式除尘技术的发展现状及操作原理,在此基础上,分别从电袋一体式除尘器电除尘区的电场数量选择、电除尘区和布袋除尘区的烟气均流问题及处理等应用方面的问题展开解析,并提出相应的措施建议,希望能为相关人士提供参考。     

Incendiary characteristics of electrostatic discharge for dust and gas explosion

Paying attention to the ignition potentiality of static electricity, the relation between the discharge characteristics and the ignition of a dust cloud and the gas produced was studied, applying an electrical power supply of which the electrical circuit is adjustable. The effect of ignition characteristics on dust and gas explosions was investigated. The results of the study indicate that the probability of an explosion is influenced by the minimum ignition energy, spark duration time, feeding rate of ignition energy, circuit capacitance, ignition voltage, etc.     

Effects of particle characteristics on flame propagation behavior during organic dust explosions in a half-closed chamber

To reveal the effects of particle characteristics on the mechanisms of flame propagation during organic dust explosions clearly, three long chain monobasic alcohols which are solids at room temperature and have similar physical–chemical properties were chosen to carry out experiments in a half-closed small chamber. A high-speed video camera was used to record the flame propagation process and to obtain the direct light emission photographs. Flame temperature was detected by a fine thermocouple. Based on the experimental results above, analysis was conducted on flame propagation characteristics and temperature profiles of organic particle cloud. As a result, it was found that the particle materials, especially volatility, strongly affected the flame propagation behavior. Particle concentration also affects the combustion zone propagation process significantly. With increasing the particle concentration, the maximum temperature of the combustion zone increases at the lower concentration, reaches a maximum value, and then decreases at the higher concentration. The propagation velocity of the combustion zone has a linear relationship with the maximum temperature, which implies conductive heat transfer is dominant in the flame propagation process of the three different volatile dusts.     

Effect of particle size and dust layer size on ignition characteristics of PMMA dust layer on hot surface

Deposition of combustible dust on a hot surface is a hidden danger of fire. In this work, polymethylmethacrylate (PMMA) dust was selected to analyse the influence of dust layer diameter, dust particle size and dust layer thickness on the ignition characteristics of PMMA dust layer. Critical heating temperatures and ignition time had been measured. The STA-GC/MS-FTIR analysis was used to determine that the main products of PMMA pyrolysis were MMA, CO, CO₂, and C₂H₄, of which CO and C₂H₄ were transported to the ambient to cause gas phase combustion on the surface of the dust layer. For 10 mm thick dust layer, the critical heating temperatures of 5 μm PMMA, 100 nm PMMA, and 30 μm PMMA were 300 °C, 330 °C, and 320 °C. As the thickness of the dust layer increased, the gas transport path became longer, the critical heating temperature and ignition time increased. The characteristic particle size (D [3,2]) was utilized to represent the true particle size, and the ignition time increased with the increase of the characteristic particle size. The increase in the diameter of the dust layer had a slight effect on the temperature history and ignition time of the dust layer.     

Effects of particle thermal characteristics on flame microstructures during dust explosions of three long-chain monobasic alcohols in a half-closed chamber

To reveal clearly the effects of particle thermal characteristics on flame microstructures during organic dust explosions, three long-chain monobasic alcohols, solid at room temperature and similar in physical-chemical properties, were chosen to conduct experiments in a half-closed chamber. In the experiments, the dust materials were dispersed into the chamber by air to form dust clouds and the hybrids were ignited by an electrical spark. A high-speed optical schlieren system was used to record the flame propagation behaviors. A fine thermocouple and an ion current probe were respectively used to measure the flame temperature profile and the reaction behaviors of the combustion zone. Based on the experimental results, combustion behaviors and flame microstructures in dust clouds with different thermal characteristics were analyzed in detail. As a result, it was found that the dust flame surfaces were completely covered by cellular structures that significantly increased the flame frontal areas. Flame propagated more quickly and the number of the cellular cells increased as increasing the volatility of the particles. On the contrary, maximum temperature and the thickness of the preheated zone decreased as increasing the volatility of the particles. According to the ion current profile, the particles in the preheat zone were pyrolyzed to intermediate radicals and the radicals' fraction in the higher volatile dust flame was higher than that in the lower volatile dust flame.     

试验呼吸性粉尘及防尘滤料性能研究

介绍了呼吸性粉尘的概念,试验粉尘的基本要求,研究了试验呼吸性粉尘的制备方法,并对研制的滤料阻尘效果进行了测试分析.     

不同粒径镁铝合金粉尘爆炸与抑爆特性研究

为了研究镁铝合金粉爆炸危险特性,利用20L球形爆炸容器进行测试,结果表明:180目 (80 μm)、 120目(125 μm) 和60目(250 μm)3种粒径下的金属粉尘爆炸下限浓度分别为45 g/m3,55 g/m3和95 g/m3。相同浓度下最大爆炸压力随粒径增大的而减小。以碳化硅和石墨为代表的研究中,60目,120目和180目的镁铝合金粉以10%的浓度梯度加入碳化硅浓度分别至50%,70%和80%,石墨浓度至30%,50%和60%时,镁铝合金粉不会发生爆炸。表明碳化硅及石墨等惰性粉尘都能对粉尘爆炸有抑制作用,其中石墨对镁铝合金粉的抑爆作用明显优于碳化硅。     

Coal dust particle size survey of US mines

The National Institute for Occupational Safety and Health (NIOSH) and the Mine Safety and Health Administration (MSHA) conducted a joint survey to determine the range of coal particle sizes found in dust samples collected from intake airways of US coal mines. The last comprehensive survey of this type was performed in the 1920s. The size of the coal dust is relevant to the amount of rock dust required to inert the coal dust, with more rock dust needed to inert finer sizes of coal dust.

Dust samples were collected by MSHA inspectors from several mines in each of MSHA's 10 bituminous Coal Mine Safety and Health Districts. Samples were normally collected in several intakes at each mine. The laboratory analysis procedures included acid leaching of the sample to remove the limestone rock dust, sonic sieving to determine the dust size, and low-temperature ashing of the sieved fractions to correct for any remaining incombustible matter. The results indicate that particle sizes of mine coal dust in intake airways are finer than those measured in the 1920s. This finer size coal dust in intake airways would require more incombustible matter to be effectively inerted than the 65% incombustible specified in current regulations.     

Charge reduction on polypropylene granules and suppression of incendiary electrostatic discharges by using a novel AC electrostatic ionizer

As a method to prevent or mitigate electrostatic charge and/or discharges, we have developed a novel AC electrostatic ionizer. In this study, we evaluated experimentally the practical version of the novel AC electrostatic ionizer with a modeling test system and a pneumatic powder transport facility. In addition, electrostatic discharges generated inside a silo while loading polypropylene (PP, 3 mm) granules were observed visually with/without the novel AC ionizer. The specific charge was clearly decreased with the novel AC electrostatic ionizer. The specific charge obtained with the four arranged AC electrostatic ionizers used was approximately one eighth of that without the AC ionizer. The incendiary bulk surface discharges completely died out inside the silo by using the four arranged ionizers.     

袋式除尘器反吹风清灰效果实验研究

通过实验对袋式除尘器反吹风清灰效果进行了研究.实验表明,清洁滤袋阻力与粉尘层阻力相比可忽略不计,滤袋阻力与过滤风速成正比;反吹风清灰时,滤袋上粉尘负荷越大,清灰效果越好;粉尘剥离率随反吹风风速的增加而提高,当反吹风风速增加到3.5m/min时,剥离率增加趋于平缓.实验结果为袋式除尘器清灰时反吹风风速的选择提供了参考数据.     

不饱和聚酯树脂钮扣粉尘静电爆炸敏感性研究

针对某不饱和聚酯树脂钮扣厂在除尘设备维修过程中发生的粉尘爆炸事故,探究静电引起此次事故的可能性并提出防护措施。通过实验测定不饱和聚酯树脂钮扣粉尘的爆炸特性参数,进而确定其静电爆炸敏感性。结果发现:不饱和聚酯树脂钮扣粉尘云最小点火能MIE为4～10 mJ、最低着火温度MIT为480 ℃、粉尘层最低着火温度LIT＞400 ℃。表明,此粉尘属易燃粉尘,其粉尘爆炸敏感度极高,被静电火花点燃的可能性极大,在生产过程中,应采取静电防护措施。