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1998年末,鞍山静电技术研究设计院研制的静电除雾器在上海宝山钢铁公司冷轧厂首次应用,取得了非常理想的净化效果。本文概述了酸雾对该厂2030CM01酸洗工艺段的危害,并对静电除雾器的工作原理、净化过程、设计特点和现场使用等方面作出了系统论述。 相似文献
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饮食业油烟净化技术与应用 总被引:1,自引:0,他引:1
近年来,饮食业油烟污染已成为城市大气污染的主要来源之一。比较分析了目前国内使用的几类油烟净化设备的性能及应用现状,提出不同规模的饮食业单位应选择的油烟净化技术。通过比较发现,静电油烟净化技术和静电复合式油烟净化技术是目前国内油烟净化技术的主流,并提出等离子体技术、催化燃烧技术是今后油烟净化的发展趋势。 相似文献
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提出一种新型除雾装置——自由旋片除雾器。在实验室条件下,从除雾效率、压力损失两方面研究了自由旋片除雾器的性能。实验结果表明,风速在11 m/s左右时,自由旋片除雾器的除雾效率达到最大值。对比实验发现,自由旋片除雾器的除雾效率远高于固定叶片除雾器的除雾效率,二者的除雾效率最大值相差约10%。自由旋片除雾器的除雾效率变化曲线在6~13 m/s的流速范围内相当平滑,说明自由旋片除雾器对含雾气流流速的波动有很好的适应性。另外,增加液气比和雾滴粒径会提高自由旋片除雾器的除雾效率。自由旋片除雾器压力损失系数仅为4.3,而固定叶片除雾器压力损失系数为6.6。所以,自由旋片除雾器的阻力特性远优于固定叶片除雾器。 相似文献
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除雾器是用来除去烟气中细微液滴、降低污染物、保证系统正常运行的关键设备,故除雾器的研究具有重要意义。利用流体力学计算软件,分析无钩板与带钩板除雾器转折次数对除雾效率的影响。结果表明:除雾器增加转折次数和钩板都可以提高除雾效率,但同时会造成压降增大;增加钩板对除雾效率和压降的影响要高于增加转折次数的影响,带钩板的除雾器对2~10μm直径的液滴具有较理想的去除能力,对于粒径为8μm的液滴,当入口气体流速为3 m·s~(-1)、B=4时,带钩板除雾器除雾效率已达78.2%,并且增加带钩板除雾器的转折次数对除雾效率的提升要高于无钩板除雾器;液滴捕集模拟计算发现,当入口流速为3 m·s~(-1)、B=3时的除雾效率已达91.45%,比初始结构提升约20%。通过分析可知,除雾器可以通过增加钩板以及转折次数来提高对细微液滴的除去能力。 相似文献
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伞罩型除尘脱硫塔内除雾器性能研究 总被引:1,自引:0,他引:1
除雾器是湿法烟气脱硫(WFGD)系统内重要的设备之一,其性能对WFGD系统运行的可靠性有重要影响.利用Fluent6.2软件对新型伞罩型除尘脱硫塔内的三维两相流场进行数值模拟,气相采用RNG湍流模型,液相采用离散相模型,选择SIMPLE算法进行计算,分析塔内的折板除雾器和旋流板除雾器的速度场、压力场和液滴的分布情况.结果表明,烟气经过折板除雾器,产生了明显的压降,且在拐角区域湍流耗散强烈,是实现气液分离的关键区域;烟气经过旋流板除雾器,速度和压强分布具有良好的对称性,液滴被气流旋转抛向壁面实现气液分离.模拟结果对新型的WFGD除雾器的设计和运行具有一定的理论指导意义. 相似文献
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实验研究了不同操作条件、板片型式及板间距对除雾器除雾效率及压降的影响规律,并采用计算流体力学(CFD)方法对除雾器内流场进行了数值模拟与分析。研究结果表明,操作条件对压降和流场影响较小,而板片型式特别是迎风面的几何结构是影响流场与压降的关键因素;随着气速的增大,除雾效率增高,但当气速增到某一临界值(4~5 m/s)后,除雾效率随着气速的增大而迅速减小;除雾器压降的数值模拟结果与实验值吻合良好;除雾器内存在2个回流区,回流区是产生除雾器临界气速的重要原因之一。研究结果可为除雾器优化设计提供指导。 相似文献
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为了进一步提高电除尘器的收尘效率,尤其是对高比电阻粉尘的收尘效率,依据非稳态静电收集理论,对影响电除尘器粉尘收集性能各项因素的作用程度及机理进行了进一步研究。实验研究了粉尘收尘效率与不同比电阻粉尘的最优极间距、最优工作电压、粉尘层厚度和比电阻之间的相互关系。研究结果表明,随着极间距的增加,对应比收尘极面积,对于不同比电阻粉尘的收尘效率的增加幅度是不同的,其中高比电阻粉尘的收尘效率增加的趋势更加显著;粉尘比电阻越高,所对应的最优极间距越大,宽间距电除尘器对捕集高比电阻粉尘具有一定优越性;在最优极间距条件下,粉尘比电阻越高,其所对应的最优工作电压越小;相对于正常比电阻粉尘,随极板沉积粉尘层厚度的增加,高比电阻粉尘的最佳收尘效率所对应的最优工作电压升高幅度较大,而且最优工作电压所对应的收尘效率下降显著。随粉尘比电阻的增大,电除尘器收尘效率逐渐降低,特别是当粉尘比电阻大于1011Ω.cm后,粉尘收尘效率显著下降。研究结果与非稳态静电收尘理论提出的观点相吻合,有助于透彻理解电场结构和运行参数与粉尘收集性能的关系,特别是对于今后研发提高高比电阻粉尘收集性能的针对性技术措施具有指导作用。 相似文献
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Louis Theodore Joseph P. Reynolds 《Journal of the Air & Waste Management Association (1995)》2013,63(7):777-779
This paper is directed to those individuals involved in design of electrostatic precipitators. The Deutsch-Anderson model is usually employed by industry for the design of electrostatic precipitators. The so-called process design variable in this approach is the total capture area in the precipitator. Unfortunately, little is available on the equipment design of this unit, i.e., the geometric arrangement of the plates that constitute the capture area and the external dimensions of the physical structure that houses the precipitator components. These are important economic considerations, and it is to this subject that this paper is directed. It is relatively easy to predict equipment costs for “off-the-shelf” electrostatic precipitators; it is more difficult to closely predict the cost for a custom-made unit, which is more often the case encountered in practice. Once the capture area is calculated, the total precipitator cost becomes a strong function of the outer casing and outer accessories of the physical system. In this paper, a model is presented that can help minimize precipitator cost. An illustrative example complements the development of the model. 相似文献
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E. Bakke 《Journal of the Air & Waste Management Association (1995)》2013,63(2):163-167
The application of wet electrostatic precipitators is rapidly gaining popularity. The emission regulations are becoming more and more stringent and they are being enforced. The emphasis on removal of fine particles and organic liquid droplets in the submicron range is increasing. In order to meet the required outlet loadings and opacities, the pressure drop that has to be applied across a conventional scrubber has increased exponentially. The wet electrostatic precipitator is emerging as an economic alternative by virtue of its very low power consumption and its potential for removal of submicron particles with efficiencies in the high nineties. Several applications of the wet electrostatic precipitator will be reviewed in this paper. 相似文献
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L.I. Kropp I.N. Shmigol G.S. Chekanov Sabert Oglesby Jr R.E. Bickelhaupt 《Journal of the Air & Waste Management Association (1995)》2013,63(6):665-669
An electrostatic precipitator preceded by a wet scrubber was tested at the Reftinskaya Power Station. The unit collects a high resistivity fly ash from the combustion of low sulfur Ekibastuz coal. The operating parameters of the precipitator were measured as well as the mass emissions and the in-situ electrical resistivity of the fly ash. Density, particle size distribution, electrical resistivity, and chemical composition were determined for collected samples of the fly ash. The fly ash was also characterized by x-ray diffraction and scanning electron microscopy. When a centrifugal wet wall scrubber was installed ahead of the electrostatic precipitator, the temperature of the flue gas entering the precipitator was decreased and the moisture content increased. The electrical resistivity of the fly ash was attenuated a decade, but not enough to overcome the adverse effects of back corona in the precipitator. Lowering the flue gas temperature to about 85°C by the addition of a venturi scrubber ahead of the centrifugal scrubber reduced the electrical resistivity of the fly ash another decade and allowed the operation of the precipitator without back corona. 相似文献
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David V. Bubenick 《Journal of the Air & Waste Management Association (1995)》2013,63(3):279-283
Compliance with particulate standards for utility boilers burning low sulfur western coal has resulted in the installation and proposed installation of several fabric filter collectors where cold or hot electrostatic precipitators would have traditionally been applied. Recently, SO3 conditioning has been used to improve cold precipitator performance resulting in considerable reduction in specific collection area (SCA). All this suggests that trade-offs exist indicating ranges of SCA, A/C ratio, and power plant size (Mw) where fabric filters become competitive with electrostatic precipitators. Conceptual cost models are presented which indicate total capital investment and annual costs for the control devices. Precipitator costs are correlated with collecting area, gas flow rate, and power input and are presented as functions of SCA and Mw. Fabric filter costs are keyed to gross filter area, pressure drop, and gas flow rate. Fabric filters become competitive when a cold precipitator requires SCAs in excess of 600 to 800 and competitive when a hot precipitator requires equivalent cold precipitator SCAs in excess of 600 to 1000 depending on A/C ratio, Mw, and hot precipitator SCA credit allowance. The S03 conditioned precipitator scenario is shown to be economically competitive with fabric filters. 相似文献
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Jacob Katz 《Journal of the Air & Waste Management Association (1995)》2013,63(11):525-528
The relationship between sulfur in coal, boiler exit gas temperature, and the carbon portion of fly ash have a major effect on the electrical properties of fly ash. Whether effective collection of fly ash is obtained by the electrostatic precipitator installation alone or the precipitator—mechanical combination depends primarily on a knowledge of this relationship. Fly ash electrical properties can range from a highly "resistive" to a highly "conductive" state which can appreciably alter the precipitator collection performance. A correlation of coal sulfur and boiler exit flue gas temperature is given to indicate the probability of expecting an optimum voltage—current relationship with different combinations of these factors. Carbon affects the electrical conditioning of fly ash by providing parallel paths of current leakage through the deposited dust layer. Therefore, removal of the carbon particles in a mechanical collector placed before the precipitator can alter the precipitator electrical characteristics. 相似文献
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C. C. Shale 《Journal of the Air & Waste Management Association (1995)》2013,63(3):159-160
Current-voltage relationships for negative corona are given for a pilot-scale electrostatic precipitator with 3-in. electrode spacing at 80°–1500°F and 35–80 psig. Direct comparison is made with the electrical characteristics for a 1-in. spacing at 1200°F over the same pressure range. Experimental results on both spacing agree well with electrostatic theory. Initial dust removal efficiencies for the pilot-scale precipitator ranged from 90 to 98% at 1460°F and 80 psig, but continuous operation was not achieved owing to excessive thermal expansion of the internal parts of the unit. 相似文献