贵州铝厂石灰石矿潜孔钻的除尘

贵州铝厂石灰石矿YQ-150潜孔钻原采用布袋除尘,由于粉尘浓度高,湿度大,经常造成布袋堵塞,更换频繁,工人工作量大,因而放弃使用。 目前,国内外潜孔钻除尘一般采用干式旋风除尘和布袋除尘二级除尘系统。布袋除尘器容易被腐蚀和堵塞。在总结国内外潜孔钻除尘系统使用的经验上,我们提出干-湿式除尘系统方案,有效地解决了潜孔钻除尘问题。 潜孔钻除尘系统由捕尘罩、CLT/A5.5     

硅钢车间ST机组粉尘调质与除尘系统改造

针对某硅钢车间ST机组的除尘系统除尘效率较低、排放浓度不达标、二次污染较严重的问题,通过现场调研,对除尘系统、含尘气体组分与物性参数等进行测试和分析,运用管道伴热技术改善粉尘黏性后,再选取合适的除尘器对粉尘进行除尘处理,大大地提高了系统的除尘效率。     

电炉除尘系统运行状况的诊断

宝钢股份公司宝钢分公司电炉除尘系统自投运以来就存在一些问题,随着产能扩容,除尘系统运行状况越来越差,需要进行改造.通过对电炉除尘系统的主要设备及排烟点的运行状况进行测试,根据测试结果分析电炉除尘系统存在的问题,提出改造建议.     

综掘面风幕集尘除尘系统的参数优化与数值模拟

针对目前井下综掘面粉尘治理难的问题,研制了一种新型风幕集尘除尘系统。其中风幕风机的风速、除尘风筒的结构尺寸及出口压力是影响整个系统集尘除尘效果的决定性因素。为使风幕集尘除尘系统的防治粉尘效果达到最优,通过计算流体力学FLUENT软件,分析风幕风机风速、除尘风筒直径及出口压力改变的条件下风机的表面空气流线以及粉尘颗粒轨迹。得到风机风速、除尘风筒的直径及出口压力对整个系统集尘除尘效果影响的规律。结果表明:单方面增加风幕风机的风速或出口压力时,系统的集尘除尘效果在一定范围内可以变好,但是超过一定范围之后,风速的增加或者出口压力的增大反而使系统集尘除尘效果变差;在其他条件不变的情况下,除尘风筒直径越大系统集尘除尘效果越好。     

高炉煤气全干式布袋除尘净化技术

通过对国内外大中型高炉煤气除尘系统的分析比较，对高炉煤气除尘系统几个重大技术问题提出自己的见解，并指出新建、改建、扩建大中型高炉为避免重复投资，应不建湿式除尘系统备用，而向建干式布袋除尘方向发展。     

转炉二次除尘系统问题诊断及运行优化

针对某企业150 t转炉二次除尘系统烟气捕集效果不佳、布袋除尘器压差大、运行能耗高等问题进行了系统诊断,利用排查系统管网、实测压力和流量、分析风机特性等手段,找出了问题原因并提出改进措施。通过实施改进措施,优化了150 t转炉二次除尘系统的运行方式,确保二次除尘效果并实现节能、经济运行。     

布袋除尘器在烧结机机尾除尘中的应用

介绍了用旋风除尘器、布袋除尘器组成的二级串联除尘系统在小型烧结机机尾烟气除尘中的实际应用。实际运行结果表明，该系统运行可靠，除尘效率高，系统出口含尘浓度达到了国家允许的排放标准，并针对相关问题进行了探讨。     

高炉出铁场除尘系统改造设计探讨

通过实例介绍了我国高炉出铁场烟尘治理技术,从划分除尘系统、确定风量和烟气捕集罩形式以及对主要除尘设备的选型等方面阐述了在类似除尘系统改造设计过程中应引起重视的问题.     

低压脉冲袋式除尘器在硅铁电炉烟气中的应用

介绍了低压脉冲袋式除尘器在6300 kVA半封闭式硅铁电炉烟气除尘系统中的应用,通过对铁合金半封闭式硅铁电炉烟气性质的分析,对除尘系统在运行过程中出现的问题以及解决方案进行了分析和阐述,最后指出低压脉冲袋式除尘器在半封闭式硅铁电炉除尘系统中使用时应该注意的问题。     

移动除尘电气安全控制系统的设计

介绍了铁合金浇注池用移动除尘系统的原理,同时对铁合金浇注池用移动除尘电气安全控制系统的原理、设计进行了阐述。通过多方案对比,选出了安全控制的设计方案,很好地解决了移动除尘系统中行车与烟气捕集罩之间同步安全的相关问题。     

Large-scale dust explosions in vessel-pipe systems

This study investigates dust explosions in vessel-pipe systems to develop a better understanding of dust flame propagation between interconnected vessels and implications for the proper application of explosion isolation systems. Cornstarch dust explosions were conducted in a large-scale setup consisting of a vented 8-m³ vessel and an attached pipe with a diameter of 0.4 m and a length of 9.8 m. The ignition location and effective dust reactivity were varied between experiments. The experimental results are compared against previous experiments with initially quiescent propane-air mixtures, demonstrating a significantly higher reactivity of the dust explosions due to elevated initial turbulence, leading to higher peak pressures and faster flame propagation. In addition, a physics-based model developed previously to predict gas explosion dynamics in vessel-pipe systems was extended for dust combustion. The model successfully predicts the pressure transients and flame progress recorded in the experiments and captures the effects of ignition location and effective dust reactivity.     

Overpressure characteristics of aluminium dust explosion vented through a relief pipe

A parametric experimental study of an aluminium dust explosion, initiated in a vessel and vented through a relief pipe, was performed. The aim is to clarify the overpressure characteristics in a vessel and relief pipe, during aluminium dust explosion venting, especially when a burn-up phenomenon occurs. For a vessel of fixed size, the influence of pipe diameter and pipe length on burn-up was discussed. Results demonstrate that burn-up occurs shortly after flame only enters the initial part of the relief pipe when the original dust concentration in the vessel is at relatively high level, which is usually higher than the optimum concentration obtained from the confined vessel. When burn-up occurs, the maximal overpressure continues to increase rather than to decay along the initial part of the relief pipe. If burn-up is vigorous, a second peak on overpressure-time curve in the vessel could appear. By adding 0.1 g aluminium powders on the membrane, the second overpressure peak may even surpass the first peak. Extending pipe lengths can strengthen the overpressures around the position where burn-up occurs in the relief pipe. Reducing the pipe diameter can increase the burn-up severity in the relief pipe owing to the increased dust concentration and the pressure accumulation.     

粉尘捕集效率与定风量阀应用研究

分析了造成除尘系统风量阻力不平衡的因素,提出在除尘支管上装设定风量阀来稳定各吸尘点风量,通过实验证明,在除尘管网支管上装设定风量调节阀,可以有效的消除系统阻力不平衡和管网压力波动造成的吸尘点风量偏差问题。     

烧结车间抽尘风管尘垢防治探讨

钢铁厂的铁矿烧结车间用抽风系统将生产过程混入空气中的粉尘和有害气体抽走。烧结热量作用使抽尘气流温度较高且含水汽偏大,风管外面的冷气作用使风管内表面累积一层粘结强度高的尘垢,影响正常生产。探讨尘垢生成机理,介绍采用夹层风管预防内表面累积尘垢。     

浅析除尘系统的设计原则

主要通过对除尘工程(涉及电力、冶金、建材、化工等行业)系统中除尘点源密闭、除尘管网布置、耐磨弯头等相关主要零部件的使用进行分析,阐述了在除尘系统设计中的一些思路和应该注意的事项.     

电厂输煤系统煤尘治理中应注意的几个问题

通过电厂煤尘治理的实践,本文提出了电厂输煤系统煤尘治理中应注意的一些问题。     

Effects of multiple annular obstacles on flame propagation of local corn starch dust in a vertical pipe

With high-speed camera technology, the propagation behavior of explosion flame for the local dust cloud of corn starch in a semi-open vertical pipe under the action of the annular obstacle was studied experimentally, and the blockage rate and the annular obstacle numbers as well as impact of dust cloud concentration on the flame propagation were investigated. The researches showed that both the blockage rate and the annular obstacle numbers have significant effects on the flame speed and propagation process for the dust cloud explosion of corn starch. The increase of the blockage rate of such annular obstacles will cause that the combustion of dust cloud with high concentration is mainly concentrated in the lower part of the pipe. The increase of the annular obstacle numbers will lead to the acceleration of combustion of the dust cloud. With the increase of the blockage rate and the annular obstacle numbers, the maximum flame speed shows a trend of the first increasing and then decreasing, and the phenomenon of accelerated propagation of the flame becomes more and more obvious, however, the distance of continuous acceleration for the flame is gradually decreased and the maximum flame speed is farther from the outlet of the pipe. Under the action of such annular obstacles, the concentration of dust cloud has a significant effect on the flame speed and shape of the dust cloud of the corn starch. The increase of the concentration of the dust cloud will decrease the acceleration effect of such annular obstacles to result in maximum flame speed showing a trend of the first increasing and then decreasing. However, the acceleration distance of the flame is longer, and the maximum flame speed is closer to the outlet of the pipe. The increasing concentration will make the flame speed develop more slowly, the flame color will be darker, and the flame segmentation phenomenon will be more obvious.     

Effects of obstacles and deposited coal dust on characteristics of premixed methane–air explosions in a long closed pipe

An experimental system including pressure transducer, electric spark ignition device, data acquisition and control unit was set up to investigate methane–air explosions in a horizontal pipe closed at both ends with or without the presence of obstacles and deposited coal dust. The experimental results show that explosion characteristics depended on the methane content, on the layout of obstacles, and on the deposited coal dust. Pressure fluctuation with a frequency of 150 Hz appeared in its crest when the methane content was close to the stoichiometric ratio (9.5% methane percentage by volume). The pressure rise rate increased locally when a single obstacle was mounted in the pipe, but it had little effect on the pressure peak. Repeated obstacles mounted in the pipe caused the pressure to rise sharply, and the mean maximum explosion overpressure increased with the increase of the obstacle’s number. The amplitude of pressure fluctuation was reduced when deposited coal dust was paved in the bottom of the pipe. However, when repeated obstacles were arranged inside, the maximum overpressures were higher with coal dust deposited than pure gas explosions.     

韶钢新石灰窑烟气除尘技术的应用

韶钢新石灰窑烟气除尘系统要用旋风除尘器、金属管式换热器、高效陶瓷多管除尘器的组合方式。介绍了该系统的设计参数、工艺流程、主要设备及其功能。