脱硫系统中CEMS的应用

摘要：对浙江板桥纸业1#、2#炉脱硫系统中CEMS的改造进行分析,提出了CEMS的选型、安装及运行的解决方案。     

火电厂脱硫技术浅析

随着公众对SO2污染危害的进一步认识,火电厂SO2的污染控制问题已越来越得到广泛的重视。现有火电厂多采用湿法石灰石-石膏烟气脱硫法,其脱硫效率可达95％以上。脱硫后的废水因含有多种污染因子,需经水、污泥系统处理后方可排放。     

循环流化床干法脱硫除尘一体化工艺去除汞探讨研究

目前,由于人类污染源每年向大气排汞量日益增长,使国际上对汞排放的控制研究成为热点,本文通过理论计算及工程实例说明了循环流化床干法烟气脱硫除尘一体化工艺系统可以有效地控制燃煤电厂汞的排放。     

双碱法烟气脱硫技术影响因素分析

双碱法在中小型燃煤锅炉的烟气脱硫上有着较广泛的应用,它克服了其他湿法脱硫容易结垢的缺点,且脱硫效率高。主要介绍近几年国内双碱法烟气脱硫效率主要影响因素的理论和实验研究现状,分析了pH值、钠离子浓度、液气比、硫酸根离子的比例和进口二氧化硫浓度等因素对该技术的脱硫效果的影响,提出了该技术目前存在的问题及其今后的发展方向。     

燃煤火电厂石灰石—石膏湿法烟气脱硫系统日常运行环保监督考核方法探讨

从二氧化硫总量减排环保监督管理的实际出发,结合日常监督工作的实例,分析影响烟气脱硫效率的因素,找出脱硫系统容易出现的故障,提出对脱硫系统日常监督考核的重点,探索建立烟气脱硫系统监督考核方法。     

无动力（微动力）除尘技术

无动力或微动力除尘工艺,打破传统的除尘原理,对运输转运系统进行高效除尘,成功地运用于昆钢龙山冶金熔剂矿白云石破碎系统、云锡大屯选厂、昆钢烧结厂等,投资少、除尘效果好、运行费用低。比传统的布袋除尘工艺节省投资约20％,大幅度地节约运行费用。     

云铝炭素煅烧回转窑尾气低浓度SO2脱硫技术优选方案探讨

为达到削减二氧化硫总量,通过探讨炉内喷钙法、半干法、氨法的优缺点比较,优选脱硫技术方案.     

核桃壳质活性炭的制备及吸附恶臭气体的研究

研究了用ZnCl2活化法制备核桃壳质活性炭的工艺条件及其改性前后吸附典型恶臭气体硫化氢的硫容量及穿透行为：结果表明：ZnCl2质量分数60％,300℃炭化80min,500℃活化60min,制得的活性炭脱硫硫容量高,穿透时间长;性能表征测得其碘吸附值可达880mg／g以上,吸附效果明显优于市售活性炭。用质量分数为1％的KIO3改性后的活性炭脱硫性能明显提高。     

燃煤锅炉烟气氨法脱硫技术的应用

电厂燃煤锅炉烟气脱硫是减少和控制酸雨的有效手段。LS氨法喷雾脱硫技术具有脱硫效率高、环境效益好、资源综合利用的特点。以合成氨生产装置回收的低浓度氨水为吸收剂,实施锅炉烟气脱硫技术改造．取得良好的应用效果。     

Evaluation of mercury speciation and removal through air pollution control devices of a 190 MW boiler

Air pollution control devices (APCDs) are installed at coal-fired power plants for air pollutant regulation. Selective catalytic reduction (SCR) and wet flue gas desulfurization (FGD) systems have the co-benefits of air pollutant and mercury removal. Configuration and operational conditions of APCDs and mercury speciation a ect mercury removal e ciently at coal-fired utilities. The Ontario Hydro Method (OHM) recommended by the U.S. Environmental Protection Agency (EPA) was used to determine mercury speciation simultaneously at five sampling locations through SCR-ESP-FGD at a 190 MW unit. Chlorine in coal had been suggested as a factor a ecting the mercury speciation in flue gas; and low-chlorine coal was purported to produce less oxidized mercury (Hg2+) and more elemental mercury (Hg0) at the SCR inlet compared to higher chlorine coal. SCR could oxidize elemental mercury into oxidized mercury when SCR was in service, and oxidation e ciency reached 71.0%. Therefore, oxidized mercury removal e ciency was enhanced through a wet FGD system. In the non-ozone season, about 89.5%–96.8% of oxidized mercury was controlled, but only 54.9%–68.8% of the total mercury was captured through wet FGD. Oxidized mercury removal e ciency was 95.9%–98.0%, and there was a big di erence in the total mercury removal e ciencies from 78.0% to 90.2% in the ozone season. Mercury mass balance was evaluated to validate reliability of OHM testing data, and the ratio of mercury input in the coal to mercury output at the stack was from 0.84 to 1.08.