首页> 外文会议>AWMA's (Air Waste Management Association) annual conference exhibition >MEMBRANE WESP-A Lower Cost Technology to Reduce PM2.5, SO_3 Hg~(+2) Emissions
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MEMBRANE WESP-A Lower Cost Technology to Reduce PM2.5, SO_3 Hg~(+2) Emissions

机译:膜WESP-A低成本技术,可减少PM2.5,SO_3和Hg〜(+2)排放

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Multi-pollutant control technologies will become more important in the future. This newmembrane wet electrostatic precipitator (WESP) system is ideally suited to, and very costeffective for, removing PM2.5, SO_3 and Hg~(+2) after limestone wet flue gas desulphurization(WFGD) scrubbers in the utility industry.Several coal-fired utilities have been experiencing increased SO_3 emissions from their existingWFGD scrubbers, especially after installing a Selective Catalytic Reduction (SCR) for NOxControl. Achieving co-benefits of Hg removal by installing SCR's and WFGD systems is alreadybecoming a key strategy for reducing mercury levels after coal fired power plants.WESP can readily collect acid aerosol and fine particulate due to greater corona power andvirtually no re-entrainment. The WESP can also enhance collection of Hg (Hg ash & Hg~(+2)). Themain historical limitation associated with wet precipitators has been the higher cost of specialalloys and stainless steel material used in their manufacture. This new technology WESP, basedon fabric membrane for the collecting electrodes, dramatically reduces weight and cost,compared to conventional, metallic WESPs.Cleaning of the corrosion resistant fabric membranes, is facilitated by capillary action betweenthe fibers, providing even water distribution, & continuous flushing, which removes collectedmaterial without spraying, so the entire precipitator remains on line.Operation of several pilot units using the membrane technology has demonstrated excellent PMremoval efficiency. The first commercial size unit, collecting fine particulate and sulfuric acidmist after two boilers firing No. 6 oil with 4% sulfur, shows high SO_3 removal as well. Theoperation and performance of this two-module, upflow, membrane, single-field unit, along withsome of the problems encountered and overcome in the start-up, will be described.Cost estimates comparing the membrane design to conventional metal plate WESP's arepresented. Recommendations are made to show how the membrane technology can be used after
机译:未来,多污染物控制技术将变得越来越重要。这个新的 膜湿式静电除尘器(WESP)系统非常适合且非常经济 有效去除石灰石湿法烟气脱硫后的PM2.5,SO_3和Hg〜(+2) 公用事业行业中的(WFGD)洗涤塔。 数家燃煤公用事业公司的现有SO_3排放量不断增加 WFGD洗涤塔,尤其是在安装了选择性催化还原(SCR)的NOx之后 控制。通过安装SCR和WFGD系统实现除汞的共同效益 成为降低燃煤电厂汞含量的关键策略。 由于电晕功率更大,WESP可以很容易地收集酸性气溶胶和细颗粒。 几乎没有重新夹带。 WESP还可以增强汞的收集(Hg灰分和Hg〜(+2))。这 与湿式除尘器相关的主要历史局限性是专用粉的成本较高 制造中使用的合金和不锈钢材料。这种基于WESP的新技术 用于收集电极的织物膜上,大大减少了重量和成本, 与传统的金属WESP相比。 织物之间的毛细作用促进了耐腐蚀织物膜的清洁 纤维,提供均匀的水分配和连续冲洗,从而去除收集到的水 物料无需喷涂,因此整个除尘器都保持在线状态。 使用膜技术的多个中试装置的运行证明了出色的PM 去除效率。第一个商业规模的单位,收集细颗粒和硫酸 两台锅炉燃烧含4%硫的6号机油后产生的雾气也显示出高的SO_3去除率。这 这两个模块,上流膜式单场装置的运行和性能,以及 将描述在启动过程中遇到和克服的一些问题。 将膜设计与传统金属板WESP进行比较的成本估算为 提出了。提出了一些建议,以说明膜技术在之后如何使用。

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