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Experimental study of electrostatic precipitatorperformance and comparison with existingtheoretical prediction modelsS.H. Kim, K.W. Lee*Kwangju Institute of Science and Technology, Department of Environmental Science and Engineering,1 Oryong-dong, Puk-gu, Kwangju 500-712, South KoreaReceived 1 February 1999; received in revised form 21 May 1999; accepted 2 June 1999AbstractA laboratory-scale single-stage electrostatic precipitator (ESP) was designed, built andoperated in a wind tunnel. As a "rst step, a series of experiments were conducted to seek theoperating conditions for increasing the particle collection e$ciency by varying basic operatingparameters including the wire-to-plate spacing, the wire radius, the air velocity, the turbulenceintensity and the applied voltage. As the diameter of the discharging wires and the wire-toplatespacing are set smaller, the higher collection e$ciency has been obtained. In thesingle-stage multiwire ESP, there exists an optimum wire-to-wire spacing which providesmaximum particle collection e$ciency. As the air velocity increases, the particle collectione$ciency decreases. The turbulent #ow is found to play an important role in the relatively lowelectric "eld region. In the high electric "eld region, however, particles can be deposited on thecollection plates readily regardless of the turbulence intensity. The experimental results werecompared with existing theories and Zhibin and Guoquan (Aerosol Sci. Technol. 20 (1994)169}176) was identi"ed to be the best model for predicting the ESP performance. As the secondstep, the in#uence of particle contamination at the discharging electrode and at the collectionplates were experimentally measured. The methods were sought for keeping the high collectione$ciency of ESP over elapsed time by varying the magnitude of rapping acceleration, the timeinterval between raps, the types of rapping system (hammer/vibrator) and the particle reentrainment.The rapping e$ciency and the particle re-entrainment were increased withincreasing magnitude of rapping acceleration and time interval between raps. However, whenthe thickness of deposited #y ash layer is su$ciently high, the concentration of re-entrainedparticles starts decreasing abruptly due to the agglomeration force which can interact among0304-3886/99/$ - see front matter ( 1999 Elsevier Science B.V. All rights reserved.PII: S 0 3 0 4 - 3 8 8 6 ( 9 9 ) 0 0 0 4 4 - 3deposited particles. The combined rapping system is found more e!ective for removingdeposited particles than the hammer rapping system only. ( 1999 Elsevier Science B.V. Allrights reserved.Keywords: Electrostatic precipitation; Turbulent #ow; Rapping; Particle re-entrainment; Collection e$-ciency; Negative corona1. IntroductionElectrostatic precipitators (ESPs) are one of the most commonly employedparticulate control devices for collecting #y ash emissions from boilers, incineratorsand from many other industrial processes. They can operate in a wide range ofgas temperatures achieving high particle collection e$ciency compared with mechanicaldevices such as cyclones and bag "lters. The electrostatic precipitation processinvolves several complicated and interrelated physical mechanisms: creationof a non-uniform electric "eld and ionic current in a corona discharge, ionicand electronic charging of particles moving in combined electro- and hydrodynamic"elds, and turbulent transport of charged particles to a collectionsurface.Generally, the collection e$ciency of ESP decreases as the discharging electrodeand collection plates are contaminated with particulates. Thus, a rapping system isneeded for removing the collected particulates periodically. While there have beennumerous theoretical and experimental studies on particle collection characteristics ofelectrostatic precipitators, a relatively small number of the studies addressed thee!ects of particle accumulation both at the discharging electrodes and at the collectionplates. Both phenomena are known to in#uence adversely the performance ofelectrostatic precipitators. Many researchers, such as Deutsch [1], Cooperman [2],Leonard et al. [3], Khim et al. [4], Zhibin and Guoquan [5], and Kallio and Stock[6], conducted particle collection measurements of ESP. However, they concentratedmostly on the e!ects of both turbulent mixing and secondary wind in multiwiresingle-stage electrostatic precipitators. Speci"cally, Cooperman [2] considered reentrainmentand longitudinal turbulent mixing e!ects, Leonard et al. [3] the "nitedi!usivity, and Zhibin and Guoquan [7] the non-uniform air velocity pro"le. Amongthem, only Zhibin and Guoquan [7] measured the collection e$ciency of a singlestageESP covering a wide particle size range. Even though their experimental dataare considered to be practical and useful, their experimental conditions were notidenti"ed clearly.In the present study, well-de"ned collection e$ciency data for an ESP are presentedcovering the particle size range of 0.1}100 lm. The particles used in the present studycame from the Bo-Ryung power plant in Korea. In addition, the ESP performancewas evaluated in terms of optimum operating conditions. Finally, the optimumrapping conditions were sought under which the rapping e$ciency increases and theparticle re-entrainment decreases.4 S.H. Kim, K.W. Lee / Journal of Electrostatics 48 (1999) 3}25Fig. 1. Schematic diagram of the wind tunnel for the eight wired single-stage ESP performance test.2. Review of theoretical models2.1. Particle chargingFig. 1 shows the laboratory-scale electrostatic precipitator. The particle chargingsystem consists of discharge wires with diameter (D8) and two grounded parallelplates of length (¸). A high negative voltage (<8) is applied to the corona dischargewires, and suspended particles of diameter (d1) #ow with air between the plates ata velocity (;) in the y-direction. In the whole range of particle sizes, both "eldcharging and di!usion charging mechanisms contribute to signi"cant charges [8,9].In these theoretical analyses, it is nearly correct to sum the rates of charging from thetwo mechanisms and then solve for the particle charging as follows:dq1dt"q4q A1!qq4B2#d21eN04 S8k¹pmexpA! 2qed1k¹B (1)where q1 is the particle charge, q4 is the saturation charge,N0 is the average number ofmolecules per unit volume, e is the electronic charge ("1.6]10~19 C), b is the ionmobility ("1.4]10~4 m2/V s), e0 is the permittivity of free space ("8.85]10~12 F/m), d1 is the diameter of particle, k is the Boltzmann constant ("1.38]10~23 J/K), ¹ is the absolute temperature ("293 K), m is the mass of a particle("(p/6)d31o1), and o1 is the particle density ("2.25]103 kg/m3).2.2. Theoretical models of particle collection ezciencyTheoretical models of ESPs were provided by Deutsch [1], Cooperman [2],Leonard et al. [3], Zhibin and Guoquan [7] and others. The Deutsch model forS.H. Kim, K.W. Lee / Journal of Electrostatics 48 (1999) 3}25 5calculating the particle collection in an ESP assumes complete mixing by turbulent#ow and thereby uniform concentration pro"les. In order to improve the drasticassumption of in"nite di!usivity in the Deutsch model, many researchers tried todevelop "nite di!usivity models by dealing with the convective-di!usion equationwith various boundary conditions.Cooperman [2] developed a theory which modi"es the Deutsch model to accountfor the e!ects of turbulence and particle turbulent di!usion. The major limitations ofthe Cooperman model lie absence of a general method to estimate the re-entrainmentfactor and the particle di!usivity. Leonard et al. [3] developed a more complicatedtwo-dimensional model using the method of the separation of variables from theconvective-di!usion equation. He assumed uniformity of velocity components ofcharged particles and particle di!usivity. This assumption fails to adequately describethe particle di!usivity near the collection plates, where it is governed mainly by themolecular transport and, therefore, the di!usivity near the wall is signi"cantly lowerthan the di!usivity in the turbulent core. Zhibin and Guoquan [7] suggested a newmodel for the single-stage ESP which takes into account the e!ect of turbulencemixing by electric wind. Predicted collection e$ciencies of the above theoreticalmodels are summarized as follows:gDe"1!exp(!De), (2)gCoo"1!expC;¸2D!SG A;¸2DB2#(1!R)PeA¸=B2HD, (3)gLeo"1!P10PA m!DeJ2De/PeBdm, (4)gZhi"1!S Pe4pDeP10expC!Pe4De(m!De)2Ddm, (5)where

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王海宁,男,1965年12月出生,安徽怀宁人,中共党员,工学博士,江西理工大学安全工程、环境工程专业教授。 王海宁1987年毕业于中国矿业大学矿山通风与安全专业,2005年获中南大学安全技术及工程专业博士学位。江西省中青年学科带头人,江西省新世纪百千万人才人选,金川集团有限公司“荣誉职工”,铜陵市人民政府“科技特派员”,《矿业研究与开发》理事会常务理事,《矿业快报》编辑委员会委员。现任江西理工大学科技处副处长。 主要从事安全理论及技术、废水处理剂开发与应用、脱硫除尘理论技术及设备研究等方向的研究,已获省部级科技成果二等奖5项,中国发明专利1项,软件著作权1项,实用新型专利3项;发表学术论文70余篇(EI等检索论文13篇),学术著作2部;指导硕士研究生30余人,其中10人考取博士研究生。 所授课程大气污染控制、烟气脱硫技术、大气物理化学、水处理剂等。 科研项目在研科研项目 1、铜陵公司六座矿山通风系统普查(38万元); 2、安中国企业2010专利排名徽金安矿业风流调控技术研究(19.6万元); 3、金川公司三矿区1428和1150m斜坡道空气幕(18.43万元); 4、左拔矿井通风仿真系统开发与应用研究(6万元); 5、行洛坑钨矿选矿厂除尘系统设计与研究(245万元)。 获奖情况1.“复杂条件下矿井风流有效流动与控制技术应用研究”2007年获江西省科技进步二等奖,排名第一; 2.“高阶段强化开采深井通风系统优化及调控新技术研究”成果2004年获国家安全生产监督管理局科技成果二等奖,排名第一; 3.“矿用空气幕及其应用研究”成果2006年获国家安全生产监督管理局科技成果二等奖;优秀推广成果奖,排名第一; 4.“化学抑尘剂的基础研究及应用”成果2004年国家安全生产监督管理局科技成果二等奖,排名第六; 5.“大型深井矿山可靠通风及清洁生产关键技术与装备”2008年获中国有色金属协会科技成果二等奖,排名第一; 学术成果1.专利:“矿山高溜井挡风板”和“矿用空气幕引射风流装置”获实用新型专利授权;“DW型高会计中级职称报名条件效湿式除尘器”已申报发明专利; 2.出版《矿井风流流动与控制》专著1部(2007年冶金工业出版社); 3.已发表学术论文70余篇,主要论文如下: (1)矿用空气幕试验研究与应用(煤炭学报,2006,EI收录) (2)TestofAirCurtaininMine(国际学术会议,2006,EI收录) (3)ApplicationofAirCurtainonMinePollutionControl(国际学术会议,2005,ISTP收录) (4)TestofSuperWaterAbsorbingResintasDustSuperssantfor DustRoads(国际学术会议) (5)多机并联增阻空气幕的现场应用研究(中南大学学报,2005,EI收录) (6)空气幕内气流场的数值模拟与分析(矿业研究与开发,中文核心) (7)灾变预测在矿山安全生产目标管理中应用(矿业研究与开发,中文核心) (8)矿山高溜井多片式挡风板应用研究(金属矿山,中文核心,EI刊源) (9)选矿厂破碎车间高效湿式除尘器的应用(中国钨业,中文核心) (10)MATLAB语言在风门空气幕理论模型中的应用研究(矿业安全与环保,中文核心) (11)多机并联空气幕引射风流及其应用研究(矿冶工程,中文核心,EI刊源) 平面设计毕业论文(12)多机并联空气幕隔断风流的现场试验研究(中国矿业,中文核心) (13)多机并联增阻空气幕在龙首矿的应评职称论文格式用研究(有色金属,中文核心) (14)湿法烟气脱硫的腐蚀机理与防腐技术(能源环境保护) (15)表面活性剂在矿山防尘中的应用(煤矿安全,中文核心) (16)一种路面抑尘高倍吸水树脂的研制(中南大学学报,CA收录) 相关信息 1. 高效湿式除尘器产品获专利2010年07月22日,王海宁教授“高效湿式除尘器产品”获发明专利[1]。 国家人社部、科技部、教育部等7部委联合下发人社部发【2009】189号文件,公布了2009年“新世纪百千万人才工程”国家级人选名单,我校王海宁教授成功入选。 王海宁,现为我校工程研究院常务副院长,江西省中青年学科带头人,跨世纪百千万人才工程人选,金川集团有限公司“荣誉职工”,铜陵市人民政府“科技特派员”。 近年来,王海宁教授主要在矿山安全理论及技术等方面开展了卓有成效的研究,已获得一批研究成果,并在多个大型地采矿山推广应用,有效解决了大量的现场技术难题,经济和社会效益显著。 2. 新世纪百千万人才工程2010年02月25日,王海宁教授入选“新世纪百千万人才工程”国家级人选[2] 近日,江西理工大学王海宁教授申请的发明专利“高效湿式除尘器”获中华人民共和国国家知识产权局发明专利授权。 该发明是一种高效湿式除尘器,由箱体、除尘器进气口、通道、水箱、除雾挡板、排浆蝶阀、水位计等构成,其特征在于除尘器箱体的进气端焊接了振动筛板和导流板,除尘器箱体内焊接安装有防腐耐磨材质的“W”型通道上叶片和下叶片。 本发明专利具有除尘效率高、能耗低、使用寿命长、结构紧凑、耗水量小等特点。该发明专利目前在镍矿山、铜矿山、铁矿山、金矿山、锅炉等行业广泛应用,可有效解决矿业粉尘控制过程中耗水量大、能耗高、除尘效率不高、设备维护量大等难题,取得了良好的经济效益和环境效益。 编辑本段中国煤炭地质总局副局长王海宁,1962年7月出生,1986年7月参加工作,1985年10月入党,1986年6月毕业于西北大学,高级工程师。曾任中国煤炭地质总局航测遥感局地图制印厂副厂长、党总支书记、副总经理,1999年--2005陕西煤航数码测绘(集团)股份有限公司副董事长、总经理,煤航(集团)实业发展有限公司副总裁,陕西煤航数码测绘(集团)股份有限公司总经理,2007年6月任中国煤炭地质总局经营管理部主任,2011年中国煤炭地质总局副局长

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