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New Life for a Dual Loop Wet FGD System

机译:双回路湿式烟气脱硫系统的新生活

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Indianapolis Power & Light (IP&L) installed a dual-loop, limestone, inhibited-oxidation wet flue gas desulfurization (FGD) system in 1986 on its Petersburg Unit 4. The unit has a capacity of 550 MW and fires high sulfur coal. The wet FGD system included three modules, each with an integral quencher section and tank plus a separate absorber section with an external absorber reaction tank. The wet FGD installation did not include a wet stack and, instead, bypassed 6% of the hot flue gas around the absorber modules to reheat the treated flue gas to allowable stack temperatures. With addition of sodium formate, the wet FGD system achieved approximately 84% sulfur dioxide (SO_2) removal from the remaining 94% of the flue gas passing through the system. In 2008, IP&L began working with the Babcock & Wilcox Power Generation Group (B&W PGG) to convert the absorbers to a modern, state-of-the-art single loop limestone wet FGD system with forced oxidation while increasing SO_2 removal without gas bypass or sodium formate. Major modifications included raising the gas inlet, cross-tying the integral quencher tank to the external absorber reaction tank, installing an upgraded absorber tray, modifying the spray levels and adding a forced oxidation air system. The limestone slurry preparation and slurry bleed dewatering systems were also upgraded to support the higher SO_2 removal rates and processing of high quality gypsum. B&W PGG provided most of the process design for the new system. Balance-of-plant (BOP) upgrades and expansions required to support the wet FGD process changes and conversion to a wet stack. The upgraded equipment was started up in November 2011 and performance testing was conducted in February 2012. Test data indicates SO_2 removal is in excess of 95% while operating within expected pressure drop and gypsum quality requirements.
机译:印第安纳波利斯电力与照明(IP&L)于1986年在其彼得斯堡4号机组安装了双回路石灰石抑制氧化湿法烟气脱硫(FGD)系统。该机组的容量为550 MW,可燃烧高硫煤。湿法烟气脱硫系统包括三个模块,每个模块都具有一个整体式淬火器部分和一个罐,以及一个带有外部吸收器反应罐的独立吸收器部分。湿法烟气脱硫装置不包括湿烟囱,而是绕过吸收器模块周围6%的热烟气,以将处理过的烟气重新加热到允许的烟囱温度。加入甲酸钠后,湿法烟气脱硫系统从流经该系统的其余94%的烟道气中去除了约84%的二氧化硫(SO_2)。在2008年,IP&L开始与Babcock&Wilcox发电集团(B&W PGG)合作,将吸收器转换为具有强制氧化功能的现代,先进的单回路石灰石湿法烟气脱硫系统,同时增加SO_2的去除而无需气体旁路或甲酸钠。主要的修改包括提高进气口,将整体式淬火箱与外部吸收塔反应罐交叉绑扎,安装升级的吸收塔盘,改变喷雾量以及增加强制氧化空气系统。石灰石浆液制备和浆液脱水系统也进行了升级,以支持更高的SO_2去除率和高质量石膏的加工。 B&W PGG为新系统提供了大多数过程设计。支持湿法烟气脱硫工艺变更和转换为湿法烟囱所需的工厂平衡(BOP)升级和扩展。升级后的设备于2011年11月启动,并于2012年2月进行了性能测试。测试数据表明,SO 2的去除率超过95%,同时在预期的压降和石膏质量要求范围内运行。

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