1.3、水平烟道及烟囱酸腐蚀
烟囱及水平烟道内衬涂层主要为耐火泥,其主要成分为Al2O3,部分为Ca(OH)2、CaO,其耐酸腐蚀能力不强,附着在烟囱内壁的H2SO4与耐火泥中Ca(OH)2、CaO等会发生化学反应,生成物体积松散、膨胀,遇水后极易水解粉化,致使混凝土或抹灰层逐渐被腐蚀解体,反应方程式如下:
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使用碱性废水除尘脱硫后,因碱水pH值在11.5~12.8,且稀白液及EO段碱性废水中含有纤维等杂质,易在除尘脱硫水管道内壁形成碱垢。送到电厂的漂白EO段碱性废水水温在70~80℃,更易形成碱垢。为避免因管道结垢过多而阻塞除尘水管道,应制定方案定期进行酸洗除垢工作。
2、系统运行建议
由于现有烟气脱硫系统存在烟气带水、腐蚀、结垢等问题,在未对除尘脱硫系统进行技改前,为保证烟气的排放达标,尽量延长设备运行时间及减轻对设备的酸腐蚀,在运行过程中,应做好以下工作。
2.1、锅炉运行
(1)调整好锅炉燃烧及风量配比,维持炉内适当的过剩空气系数,既保证煤的充分燃烧,又保证尾部烟道含氧量维持在较低水平,减少SO3的生成率,减缓烟道及风机腐蚀。调整以二次风(助燃风)为主,控制好二次风量。
(2)继续试用消化渣及白泥与煤掺烧,逐渐加大掺烧比例,试用中注意避免对锅炉燃烧及锅炉本体结构产生不良影响,必要时可外购石灰石粉碎试用。若条件成熟,可采用以炉内脱硫为主的运行方式,减少稀白液、液碱、EO段漂白废水用量,减轻烟气带水现象。
(3)在原煤中掺加适量脱硫剂,脱硫剂有一定节煤效果及固硫能力,使用后可缓
解除尘脱硫系统运行压力,减少稀白液、液碱、EO段漂白碱性废水用量。
2.2、除尘脱硫系统运行及维护
(1)把开孔型文丘里除尘器喷头更换成不易结垢堵塞的螺旋型喷头,更换后因除尘脱硫水雾化良好,对除尘脱硫有更好效果。
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