首页> 外文会议>Proceedings of the 17th annual north American waste to energy conference >RETROFIT INJECTION OF HUMID GAS FROM SLUDGE DRYER AND SECONDARY AIR IN WTE FURNACES OF QUEBEC CITY
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RETROFIT INJECTION OF HUMID GAS FROM SLUDGE DRYER AND SECONDARY AIR IN WTE FURNACES OF QUEBEC CITY

机译:魁北克市垃圾焚烧炉中的污泥干燥器和二次空气对湿气的反吹

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This paper discusses the retrofit injection of humid gas from sludge dryer with secondary air in the WTE furnaces in Quebec City. In 1992, a municipal sludge treatment plant was added in the WTE building. Three sludge dryers, each connected to a furnace, were added. Direct contact with hot furnace gas was used to dry sludge in a rotary drum. Humid gas from the dryer was returned to the rear wall of the furnace just above the finishing grate. CFD modeling showed cold flow of humid gas on the rear furnace wall, restriction of the combustion area on the principal grate, and stratification of the flow inside the boiler. A retrofit of the first chamber of the boiler was designed using injection of humid gas from the sludge dryer with secondary air on the front and rear walls. The main purpose of the retrofit was to maintain CO levels of under 57 mg/m3 on a 4 hour mobile average. The first boiler was retrofitted in winter 2008 and results have been very encouraging.
机译:本文讨论了魁北克市WTE炉中污泥干燥器中湿气的二次空气注入改造。 1992年,在WTE大楼中增加了市政污泥处理厂。添加了三个污泥干燥器,每个污泥干燥器均连接到炉子。直接与热炉气体接触用于干燥转鼓中的污泥。来自干燥机的湿气返回到炉膛的后壁,刚好位于精加工炉排的上方。 CFD模型显示出湿气在炉后壁上的冷流,主炉排上燃烧区域的限制以及锅炉内部流的分层。锅炉第一室的改造是通过使用污泥干燥机注入的湿气和前后壁上的二次空气进行设计的。改造的主要目的是在4小时的移动平均值上将CO含量保持在57 mg / m3以下。第一台锅炉于2008年冬季进行了改造,结果令人鼓舞。

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