首页> 外文会议>Combined Power Plant Air Pollutant Control Mega Symposium >COMPARISON OF METALLIC vs. MEMBRANE BASED WET ESP TECHNOLOGY FOR PM2.5, SO{sub}3 MIST AND MERCURY CONTROL AT A COAL-FIRED POWER PLANT
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COMPARISON OF METALLIC vs. MEMBRANE BASED WET ESP TECHNOLOGY FOR PM2.5, SO{sub}3 MIST AND MERCURY CONTROL AT A COAL-FIRED POWER PLANT

机译:PM2.5金属与膜基湿ESP技术的比较,所以炮发电厂{Sub} 3雾气和汞控制

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Several coal-fired utilities have experienced increased SO{sub}3 emissions from their existing Wet FGD Scrubbers, especially after installing an SCR for NO{sub}x Control. The SO{sub}3 goes largely uncollected through the Wet Scrubber appearing as a dense plume at the FGD stack. Sub micron SO{sub}3 (H{sub}2SO{sub}4 mist) is extremely difficult to remove with conventional technologies, however, Wet Electrostatic Precipitators can readily collect acid aerosol and fine particulate due to greater corona power and virtually no reentrainment. The historical limitations on Wet Precipitators have been their high cost because of stainless steel metal used in their manufacture. Ohio U/ SEI/CRCAT have developed a new membrane based, Wet ESP with dramatically reduced cost and weight compared to metallic wet ESPs. Cleaning of the corrosion resistant fabric membranes, is facilitated by capilliary action between the fibers, providing even water distribution, & continuous flushing removes collected material without spraying, so the entire precipitator remains on line. DOE's National Energy Technology Laboratory has awarded SEI/CRAT and Ohio University a grant to compare metallic and membrane based wet ESP technology in a pilot unit at Penn Power's Bruce Mansfield Plant in Shippingport, Pa. This paper will present the work & results to date. Phase 1 will establish baseline performance with the existing metallic wet ESP. Previous test results demonstrated 97% removal of PM2.5 and SO{sub}3 mist. Upward gas velocity from 12 ft/sec to 20s ft/sec will be tested. Additionally, longevity and reliability of the membrane material over time will be measured.
机译:几种燃煤实用程序经历了来自其现有的湿FGD洗涤器的{Sub} 3排放量,特别是在安装SCR以进行NO {sub} x控制后。所以{sub} 3在很大程度上通过湿式洗涤器而在FGD堆叠上作为密集的羽毛进行了不摄影。亚微米因此{sub} 3(H {sub} 2so {sub} 4雾)极难用常规技术去除,然而,由于更大的电晕功率,湿静电除尘器可以容易地收集酸气溶胶和细颗粒,并且几乎没有重新磨损。由于其制造中使用的不锈钢金属,对湿法除尘器的历史局限性是其高成本。俄亥俄州U / SEI / CRCAT开发了一种基于新的膜,湿特别是与金属湿效率相比显着降低的成本和重量。通过纤维之间的毛细血管作用促进耐腐蚀织物膜的清洁,提供均匀的水分布,并连续冲洗去除收集的材料而不喷涂,因此整个除尘器保持在线。 Doe的国家能源技术实验室已获得SEI / CRAT和OHIO大学获得PENN Power Pain,PA的Penn Power Bruce Mansfield工厂的试点单元中的金属和膜的湿ESP技术。本文将展示工作和结果。第1阶段将与现有的金属湿尤其建立基线性能。以前的测试结果证明了PM2.5的97%,因此{Sub} 3雾。将测试12英尺/秒至20s FT / SEC的向上的气体速度。另外,将测量膜材料随时间随时间的寿命和可靠性。

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