收尘区脉冲供电对电除尘器收集性能的影响

建立了双区电除尘器实验模型,研究了预荷电压、不同供电方式下极板间距、电极型式对双区电除尘器收尘效果的影响.结果表明:随着预荷电压逐渐升高,除尘效率也随之增加,双区除尘效果明显优于单区的除尘效果.脉冲供电对电除尘器的除尘性能影响明显,与直流供电相比,脉冲供电对PM25的分级效率可提高16.9%;在较高的电压时,极板间距为...     

泛比电阻电除尘器收尘性能实验研究

泛比电阻电除尘器是一种具有辅助电极和交错平板收尘电极的新型电除尘器.通过对其伏安特性及除尘效率的试验研究,并与传统线板式静电除尘器进行比较,结果表明辅助电极对电晕电流具有明显的抑制作用,在相同的外加电压下,泛比电阻电除尘器对高比电阻锅炉飞灰的收尘效率比普通的线板式电除尘器明显要高.     

颗粒层非稳态过滤捕集效率的研究

为计算颗粒层非稳态过滤效率,通过改进经典过滤理论模型,考虑颗粒在过滤介质中的沉积,理论推导得出非稳态过滤效率的计算公式,而经典颗粒层过滤效率计算公式仅为此计算公式的特例。因为理论计算公式是隐函数,不便于工程实际应用,所以,在常温条件下,对非稳态过滤时的过滤时间、过滤风速、过滤层厚度、粉尘浓度和颗粒层滤料均粒径等五个因素进行了正交实验研究。采用多元回归的方法得出各影响因素与过滤效率呈显性关系的效率关联计算公式,其计算结果与实验测试结果基本吻合。     

粉尘性质对电除尘器性能影响的试验研究

在半工业化的电除尘器实验系统装置上进行了烧结灰、飞灰、煤铁混合样的粒径分布及粉尘的真密度对电除尘器性能影响的实验研究。结果表明,电除尘器能有效捕集亚微米粉尘,对烧结灰净化最适合的粒径范围为1．37～2．03μm(η高达100％);对煤铁混合样的最适合粒径范围为3．30～7．25μm(η高达100％);电除尘器对煤铁混合样的粒径小于2．24μm的分级效率η高达92．36％。在同等试验条件下,电除尘器对烧结灰和煤铁混合样的总除尘效率为96．87％,高于飞灰的总除尘效率92．61％。     

ESP粉尘收集性能的影响因素

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。     

湿式纤维层非稳态过滤净化阻力的研究

在干式纤维层过滤净化阻力的理论基础上,提出清洗水均匀分布于纤维丝表面的基本假设,使湿式过滤中对液滴、液膜、液珠的分析简单具体化。并通过实验结论归纳出净化阻力随时间的变化规律,导出湿式纤维层非稳态过滤净化阻力的表达式,并用实验验证了其准确性。     

影响催化转化器非稳态性能的因素分析

建立数学模型对催化转化器起燃温度特性曲线进行模拟,模拟结果与实验测量结果吻合较好。用数学模型考察和分析了气流状态和催化剂参数和载体参数等因素对催化器非稳态转化性能的影响。     

生物滴滤器净化低浓度甲苯废气的非稳态工况研究

生物法处理大气污染物时，经常会遇到条件波动或污染物间歇排放等非稳态工况。在不同非稳态条件下，考察了甲苯废气间歇排放对生物滴滤器净化性能的影响。实验方案分3种情况：无甲苯废气排放、无循环液供应或同时没有甲苯废气和循环液的供应。间歇排放时间从2-47d不等。结果表明，不管何种形式的停运或故障，甲苯净化能力4d以内基本不下降；停运时间超过5d，则甲苯去除能力严重下降，仅为原来的1／3-1／2；停运时间在10d以内，24h内即可恢复，47d的长期停运，3d内也可恢复净化能力。     

电除尘器进气烟箱参数对气流分布影响的仿真研究

电除尘器进气烟箱结构参数不仅对除尘器内部气流分布的均匀性产生重要影响,而且还会影响除尘效率和排放指标。针对电除尘器进气烟箱结构参数选取与气流分布均匀性问题,采用欧拉-拉格朗日多相流模型,对进气烟箱扩散角,气流分布板孔形、开孔率和导流板角度等参数,进行了三维流场模拟仿真计算,获得各参数对气流均匀性的影响关系规律。仿真结果表明:方形孔的气流分布板能获得较佳的气流分布均匀性;合理调节进气烟箱扩散角、开孔率和导流板角度可有效地改善电场内气流分布状况。研究结果可为电除尘器进气烟箱的设计与改进提供依据。     

生物滴滤器净化低浓度甲苯废气的非稳态工况研究

生物法处理大气污染物时,经常会遇到条件波动或污染物间歇排放等非稳态工况。在不同非稳态条件下,考察了甲苯废气间歇排放对生物滴滤器净化性能的影响。实验方案分3种情况:无甲苯废气排放、无循环液供应或同时没有甲苯废气和循环液的供应。间歇排放时间从2~47 d不等。结果表明,不管何种形式的停运或故障,甲苯净化能力4 d以内基本不下降;停运时间超过5 d,则甲苯去除能力严重下降,仅为原来的1/3~1/2;停运时间在10 d以内,24 h内即可恢复,47 d的长期停运,3 d内也可恢复净化能力。     

Fine particle migration and collection in a wet electrostatic precipitator

Electrostatic precipitation is considered as an effective technology for fine particle removal. A lab-scale wet electrostatic precipitator (ESP) with wire-to-plate configuration was developed to study particle migration and collection. The performance of the wet ESP was evaluated in terms of the corona discharge characteristics, total removal efficiency and fractional removal efficiency. The corona discharge characteristics and particle removal abilities of the wet ESP were investigated and compared with dry ESP. Particle removal efficiency was influenced by discharge electrode type, SO₂ concentration, specific collection area (SCA) and particle/droplet interaction. Results showed that the particle removal efficiency of wet ESP was elevated to 97.86% from 93.75% of dry ESP. Three types of discharge electrodes were investigated. Higher particle removal efficiency and larger migration velocity could be obtained with fishbone electrode. Particle removal efficiency decreased by 2.87% when SO₂ concentration increased from 0 ppm to 43 ppm as a result of the suppression of corona discharge and particle charging. The removal efficiency increased with higher SCA, but it changed by only 0.71% with the SCA increasing from 25.0 m²/(m³/s) to 32.5 m²/(m³/s). Meanwhile, the increasing of particle and droplet concentration was favorable to the particle aggregation and improved particle removal efficiency.

Implications: This work tends to study the particle migration and collection under spraying condition. The performance of a wet electrostatic precipitator (ESP) is evaluated in terms of the corona discharge characteristics, total particle removal efficiency, and fractional particle removal efficiency. The effects of water droplets on particle removal, especially on removal of particles with different sizes, is investigated. The optimization work was done to determine appropriate water consumption, discharge electrode type, and specific collection area, which can provide a basis for wet ESP design and application.     

基于Monte-Carlo方法的静电除尘器除尘效率

针对经典除尘效率未考虑诸多随机因素影响的问题,提出了基于Monte-Carlo方法的效率分析模型,并通过实验数据验证其可靠性。通过该模型分析了粒径大小、电场气流速度、电晕电压、两极间距、粒子浓度等因素对收尘效率的影响规律,结果表明:基于Monte-Carlo方法的仿真结果精度更高,能有效预测静电除尘器的收尘效率,对于改进静电除尘器设计具有一定的理论意义和实用价值。     

旋风静电除尘器流场分布测试研究

利用五孔探针系统对直筒式旋风静电除尘器模型的三维流场进行了测定与分析。结果表明：随着入口风速、供电电压增加，旋风静电除尘器内气流的切向和径向速度分别增加，各截面轴向速度沿半径的分布基本相似；与旋风除尘器相比，旋风静电除尘器内气流的切向速度和径向速度的变化更为平缓，入口风速为8．5m／s时，在0．3～0．5倍简体直径时，切向速度达最大。     

旋风静电除尘器流场分布测试研究

利用五孔探针系统对直筒式旋风静电除尘器模型的三维流场进行了测定与分析.结果表明:随着入口风速、供电电压增加,旋风静电除尘器内气流的切向和径向速度分别增加,各截面轴向速度沿半径的分布基本相似;与旋风除尘器相比,旋风静电除尘器内气流的切向速度和径向速度的变化更为平缓,入口风速为8.5 m/s时,在0.3～0.5倍简体直径时,切向速度达最大.     

磁场作用下烟气流速对静电旋风除尘器收集微粒影响的模拟研究

为了提高静电旋风除尘器(ECP)中微粒的除尘效率,利用磁场能有效抑制微粒逃逸的机理,将磁场引入ECP中,建立多场耦合作用下的微粒运动数学模型,利用Fluent软件数值模拟了有无磁场环境下烟气流速对微粒逃逸率的影响。结果表明:磁场的引入有效降低了ECP中微粒的逃逸率;低烟气流速更有利于微粒在ECP内的捕集;微粒的除尘效率随着磁感应强度的增加而增大,但这一过程中磁场的贡献量逐步减小。研究结果可为新型ECP的设计提供技术参考。     

电除尘器伏安特性规律研究

对以480C型板为阳极板、不同阴极线类型、不同极距、不同极线距以及不同辅助电极配置的共计384组典型极配的伏安特性进行了全面系统的试验分析。提出了以I=aV^b幂函数的形式来数学表征常规极配的伏安特性曲线,并给出了对应极配的a、b值,对比结果表明,实测值与函数计算值的符合度均在99.5％以上。     

Experimental study of cross-flow wet electrostatic precipitator

This paper reports development and testing of a novel cross-flow wet electrostatic precipitator (WESP), recently patented at Ohio University, that utilizes vertical columns of permeable material in the form of polypropylene ropes placed in a cross-flow configuration within a flue gas stream. The cross-flow design has large surface area, which provides scrubbing action; therefore, it has the potential for removing multiple pollutants, including particulates, gases, vapors, and mists. In this new method, the ropes are kept wet by the liquid (water) introduced from the top of the cells running downward on the ropes by capillary action, making the permeable materials act as the ground electrode for capturing particles from the flue gas. Preliminary testing has shown an efficiency of well above 80% using two cells and three sets of discharge electrodes. Since the material of construction is primarily corrosion-resistant polymeric material, both weight and cost reductions are expected from this new design.

Implications: The newly invented cross-flow WESP exhibit particulate collection efficiency of well above 80% when introduced in particulate-laden exhaust flow. This value was obtained using a two cells and three discharge electrodes configuration. The electric field strength has a substantial effect on the collection efficiency. Also, the pressure drop test results indicate that there is a potential to increase the collection area, which, in turn, will increase the collection efficiency further.