闪速炉烟尘收尘装置的改造

简要概述了闪速炉气力输送系统收尘装置的改造和圆筒型布袋收尘装置在气力输送系统中使用的效果.     

炼钢炼铁除尘污泥直接应用于烧结配料的实践

介绍了炼钢炼铁除尘污泥直接用于烧结配料的新工艺。     

武钢烧结厂401转运站除尘管道堵塞的原因分析

对武钢烧结厂401转运站除尘管道经常堵塞的原因进行了理论分析和计算,计算结果与工艺要求的有关参数进行对照,找出了现有除尘管道堵塞的原因,并提出了相关的改进措施.     

虚拟现实及其在粉尘扩散研究中的应用

探讨了国际上流行的虚拟现实技术 ,并针对大气中粉尘扩散的规律 ,以相关数学模型为基础 ,采用 Open GL开发了可精确地调整流场参数和观察视角的粉尘扩散三维动态场景 ,以及在重力、风速等影响因素和射流作用下粉尘扩散的三维场景。该方法为更好地掌握粉尘扩散规律 ,寻求合理预防措施提供了科学依据。此项技术在安全科学的其它领域也有很好的应用前景     

沙尘暴事件中大气颗粒物化学组分的浓度变化和硫酸盐的形成

应用电感耦合等离子体原子发射光谱、质谱和离子色谱分析了2002年3月28日-4月8日在山东长岛县采集的共11对粗、细大气颗粒物样品的化学组成,探讨4月6-8日沙尘暴事件中大气颗粒物化学组分的变化和硫酸盐的形成.沙尘暴事件应区分前锋和后续部分,前锋与大气中各种污染物相互作用,具有硫富集的特征.后续部分较好地保持了长距离传输风沙尘本身的特征.硫酸盐的形成机理可能是多相氧化而不是简单的酸碱中和.硫酸铵是首先生成的含硫物种,这是细颗粒主导的形成过程.硫酸铵逐渐转化为其他硫酸盐,硫的成分也逐渐向粗颗粒转移.在沙尘暴事件中含硫污染物不但有一个从气相向颗粒物转变的过程,也有一个从细颗粒向粗颗粒转化的过程.      

Effect of pyrolysis and oxidation characteristics on lauric acid and stearic acid dust explosion hazards

The effect of pyrolysis and oxidation characteristics on the explosion sensitivity and severity parameters, including the minimum ignition energy MIE, minimum ignition temperature MIT, minimum explosion concentration MEC, maximum explosion pressure P_max, maximum rate of pressure rise (dP/dt)_max and deflagration index K_st, of lauric acid and stearic acid dust clouds was experimentally investigated. A synchronous thermal analyser was used to test the particle thermal characteristics. The functional test apparatuses including the 1.2 L Hartmann-tube apparatus, modified Godbert-Greenwald furnace, and 20 L explosion apparatus were used to test the explosion parameters. The results indicated that the rapid and slow weight loss processes of lauric acid dust followed a one-dimensional diffusion model (D1 model) and a 1.5 order chemical reaction model (F1.5 model), respectively. In addition, the rapid and slow weight loss processes of stearic acid followed a 1.5 order chemical reaction model (F1.5 model) and a three-dimensional diffusion model (D3 model), respectively, and the corresponding average apparent activation energy E and pre-exponential factor A were larger than those of lauric acid. The stearic acid dust explosion had higher values of MIE and MIT, which were mainly dependent on the higher pyrolysis and oxidation temperatures and the larger apparent activation energy E determining the slower rate of chemical bond breakage during pyrolysis and oxidation. In contrast, the lauric acid dust explosion had a higher MEC related to a smaller pre-exponential factor A with a lower amount of released reaction heat and a lower heat release rate during pyrolysis and oxidation. Additionally, due to the competition regime of the higher oxidation reaction heat release and greater consumption of oxygen during explosion, the explosion pressure P_m of the stearic acid dust was larger in low concentration ranges and decayed to an even smaller pressure than with lauric acid when the concentration exceeded 500 g/m³. The rate of explosion pressure rise (dP/dt)_m of the stearic acid dust was always larger in the experimental concentration range. The stearic acid dust explosion possessed a higher P_max, (dP/dt)_max and K_st mainly because of a larger pre-exponential factor A related to more active sites participating in the pyrolysis and oxidation reaction. Consequently, the active chemical reaction occurred more violently, and the temperature and overpressure rose faster, indicating a higher explosion hazard class for stearic acid dust.     

Research on different venting performance between flat and curved bursting panels

There is a noticeable discrepancy in the ability to control reduced explosion overpressure between flat bursting panels and curved bursting panels with the same static activation overpressure. Flat bursting plates were observed to leak at approximately 80% of the static activation overpressure lower than curved bursting plates. A new experimental technique is proposed in our paper. Three different vent areas of flat and curved bursting panels were tested, there was significant difference in structural stiffness between flat bursting panels and curved bursting panels, which is the reason the discrepancy in the ability to control reduced explosion overpressure. The structural stiffness of the flat bursting panels is poorer than that of the other, and a greater deformation of the flat bursting panels occurs under the same load. The membrane stress caused by the explosion overpressure therefore produces a larger value in the flat bursting panels which causes it to open prematurely. Moreover, the smaller the vent area that is, the more significant discrepancy in controlling the reduced explosion overpressure between both bursting panels is. This experimental and theoretical result in our paper provides some useful experience for the method of explosion venting.     

Numerical study on premixing characteristics and explosion process of starch in a vertical pipe under turbulent flow

Fire and explosion accidents are frequently caused by combustible dust, which has led to increased interest in this area of research. Although scholars have performed some research in this field, they often ignored interesting phenomena in their experiments. In this paper, we established a 2D numerical method to thoroughly investigate the particle motion and distribution before ignition. The optimal time for the corn starch dust cloud to ignite was determined in a semi-closed tube, and the characteristics of the flame propagation and temperature field were investigated after ignition inside and outside the tube. From the simulation, certain unexpected phenomena that occurred in the experiment were explained, and some suggestions were proposed for future experiments. The results from the simulation showed that 60–70 ms was the best time for the dust cloud to ignite. The local high-temperature flame clusters were caused by the agglomeration of high-temperature particles, and there were no flames near the wall of the tube due to particles gathering and attaching to the wall. Vortices formed around the nozzle, where the particle concentration was low and the flame spread slowly. During the explosion venting, particles flew out of the tube before the flame. The venting flame exhibited a “mushroom cloud” shape due to interactions with the vortex, and the flame maintained this shape as it was driven upward by the vortex.     

CFD simulations of dust dispersion in the 1 m3 explosion vessel

According to standard procedures, flammability and explosion parameters for dusts and dust mixtures are evaluated in 20 L and/or 1 m³ vessels, with equivalent results provided a correct ignition delay time (60 ms in the 20 L vessel; 600 ms in the 1 m³ vessel). In this work, CFD simulations of flow field and dust concentration distribution in the 1 m³ spherical vessel are performed, and the results compared to the data previously obtained for the 20 L. It has been found that in the 1 m³ vessel, the spatial distribution of the turbulent kinetic energy is lower and much more uniform. Concerning the dust distribution, as in the case of the 20 L, dust is mainly concentrated at the outer zones of the vortices generated inside the vessel. Furthermore, an incomplete feeding is attained, with most of the dust trapped in the perforated annular nozzle. Starting from the maps of dust concentration and turbulent kinetic energy, the deflagration index K_St is calculated in both vessels. In the conditions of the present work, the K_St is found to be 2.4 times higher in the 20 L than in the 1 m³ vessel.     

Implications of high altitude desert dust transport from Western Sahara to Nile Delta during biomass burning season

The air over major cities and rural regions of the Nile Delta is highly polluted during autumn which is the biomass burning season, locally known as black cloud. Previous studies have attributed the increased pollution levels during the black cloud season to the biomass or open burning of agricultural waste, vehicular, industrial emissions, and secondary aerosols. However, new multi-sensor observations (column and vertical profiles) from satellites, dust transport models and associated meteorology present a different picture of the autumn pollution. Here we show, for the first time, the evidence of long range transport of dust at high altitude (2.5-6 km) from Western Sahara and its deposition over the Nile Delta region unlike current Models. The desert dust is found to be a major contributor to the local air quality which was previously considered to be due to pollution from biomass burning enhanced by the dominant northerly winds coming from Europe.