某垃圾焚烧发电机组脱硝催化剂失活原因分析OA
Analysis of deactivation of deNOx catalyst used in waste incineration power plant
针对某垃圾焚烧发电机组使用的蜂窝式脱硝催化剂,以4000 h为周期对其进行定期检测.利用物理吸脱附分析仪、X射线荧光光谱分析仪、脱硝催化剂全尺寸性能评价装置对新催化剂、失活催化剂的化学组成、物理特性及催化性能分别进行了分析表征和检测评价.结果表明,催化剂运行4000 h后,表面钠、钾、钙含量增加,钒、钨两种氧化物的含量递减,由于钠、钾、钙的氧化物在催化剂表面富集覆盖了部分钒和钨造成的;催化剂运行16000 h后,催化剂表面的比表面积和孔容分别下降了43.06%、33.33%,平均孔径增大了80.99%,由于烟气中的碱金属和碱土金属元素在催化剂表面富集,导致部分催化剂微孔结构丧失、活性位数量减少,从而影响了催化剂性能的发挥;由于第一层催化剂直接面对烟气,表面容易吸附、堆积烟气中的碱金属、碱土金属氧化物,经检测第一、二层催化剂的活性分别下降到初始活性的41.4%和57.1%,第二层催化剂受影响较小.两层催化剂串联可满足机组脱硝率65%的要求,其氨逃逸浓度为3.87 mg/m3,超出国家相关标准要求.
For the honeycomb denitrification catalyst used in a waste incineration generating unit,it was periodically tested at a cycle of 4000 h. The catalysts were characterised by a physical absorption and desorption analyser and an X-ray fluorescence spectrometer. The chemical composition,physical properties and catalytic performance of the new catalyst and deactivated catalyst were analysed,characterised and evaluated using a physical adsorption and desorption analyser,an X-ray fluorescence spectrometry analyser,and a full-size performance evaluation device for denitrification catalysts,respectively. The results showed that after 4000 h of catalyst operation,the contents of sodium,potassium and calcium on the surface increased,and the contents of vanadium and tungsten oxides decreased,which was caused by the enrichment of sodium,potassium and calcium oxides on the catalyst surface covering part of vanadium and tungsten;after 16000 h of catalyst operation,the specific surface area and pore volume on the catalyst surface decreased by 43.06% and 33.33%,respectively,and the average pore diameter increased by After 16000 h of operation,the specific surface area and pore volume of the catalyst surface decreased by 43.06% and 33.33%,respectively,and the average pore size increased by 80.99%,due to the enrichment of alkali and alkaline earth metal elements in the flue gas on the surface of the catalyst,which resulted in the loss of the microporous structure of part of the catalyst and the decrease in the number of active sites,thus affecting the performance of the catalyst. After testing,the activity of the first and second layer catalysts decreased to 41.4% and 57.1% of the initial activity respectively,and the second layer catalyst was less affected. The two catalyst layers in series can meet the requirement of 65% denitrification rate of the unit,and the ammonia escape concentration is 3.87 mg/m3,which exceeds the requirement of relevant national standards.
王霂晗;宋绍伟;王慧贤;庄柯;林正根;徐莲莲
龙源(北京)碳资产管理技术有限公司,北京 100034国家能源投资集团有限责任公司,北京 100010国能龙源环保有限公司,北京 100039低碳智能燃煤发电与超净排放全国重点实验室(国家能源集团科学技术研究院有限公司),江苏 南京 210023江苏龙净科杰环保技术有限公司,江苏盐城 224051
能源与动力
催化剂比表面积孔容氨逃逸金属元素
catalystdeactivationwaste incinerationmicropore structure
《电力科技与环保》 2024 (003)
321-328 / 8
国家重点研发计划(2022YFC3701504)
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