电厂锅炉汞排放控制技术应用的性能和成本的初步估计:最新进展

R. Srivastava, J. Staudt, W. Jozewicz
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引用次数: 22

摘要

美国环境保护署(Environmental Protection Agency)最近提议减少燃煤电厂的汞排放。目前正在开发两种广泛的方法来控制燃煤电力锅炉的汞排放。(1)粉状活性炭(PAC)注射;(2)多污染物控制,在现有和新的二氧化硫(SO{sub 2})、氮氧化物(NOx)和颗粒物(PM)控制装置中加强汞捕获。为了帮助了解最近的EPA规则制定提案,对与上述汞控制方法相关的绩效水平和相关成本进行了估计。这项工作提出了这些估计。PAC注入成本估计范围为0.003至3.096磨/千瓦时。一般来说,较高的成本与使用喷雾干燥机和静电除尘器(esp)的电厂或使用热侧静电除尘器的电厂有关,这些电厂只占电厂的少数。不包括这些电厂,成本估计范围在0.003至1.903米尔斯/千瓦时之间。在成本范围的低端,0.003磨/千瓦时,假设不需要额外的控制技术,但汞监测将是必要的。在这些情况下,高汞去除可能是目前使用的氮氧化物和硫控制措施的结果,例如在燃煤烟煤锅炉上结合选择性催化还原和湿法烟气脱硫或喷雾干燥器与织物过滤器。由于汞控制方法目前还在发展中,成本和性能估计是初步的,预计随着汞控制技术成熟到商业地位,将得到完善。可能影响这些技术性能的因素包括:烟气中汞的形态、吸附剂的特性以及所使用的PM、NOx和SO的类型。«少
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Preliminary estimates of performance and cost of mercury emission control technology applications on electric utility boilers: An update
The Environmental Protection Agency has recently proposed a reduction in mercury emissions from coal-fired power plants. There are two broad approaches under development to controlling mercury emissions from coal-fired electric utility boilers. (1) powdered activated carbon (PAC) injection; and (2) multipollutant control, in which Hg capture is enhanced in existing and new sulfur dioxide (SO{sub 2}), nitrogen oxides (NOx), and particulate matter (PM) control devices. To help inform the recent EPA rulemaking proposal, estimates of performance levels and related costs associated with the above mercury control approaches were developed. This work presents these estimates. Estimates of cost for PAC injection range from 0.003 to 3.096 mills/kWb. In general, the higher costs are associated with the plants using spray dryers and electrostatic precipitators (ESPs) or plants using hot-side ESPs, which represent a minority of power plants. Excluding these plants, cost estimates range between 0.003 and 1.903 mills/kWh. At the low end of the cost ranges, 0.003 mills/kWb, it is assumed that no additional control technologies are needed, but mercury monitoring will be necessary. In these cases, high mercury removal may be the result of the type of NOx and SO{sub 2} control measures currently used, such as combinations of selective catalyticmore » reduction and wet flue gas desulfurization or spray drier absorbers with fabric filters on bituminous coal-fired boilers. Because mercury control approaches are under development at present, cost and performance estimates are preliminary and are expected to be refined as mercury control technologies are matured to commercial status. Factors that may affect the performance of these technologies include speciation of mercury in flue gas, the characteristics of the sorbent, and the type(s) of PM, NOx, and SO, controls used.« less
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