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»ùÓÚ¶à·½Ãæ ×ۺϿ¼ÂÇ£¬Ñ°Çó ×î¼ÑÑÌÆø´¦Àí ·½°¸£¬Ê¹µÃ ÑÌÆøÅÅ·Å ´ïµ½ Ïà¹ØÖ¸±ê ÒªÇ󡣸ù¾Ý ´¦ÀíϵͳµÄ Ñ¡ÔñÔ­Ôò£¬×îÖÕ È·¶¨ Éè¼Æ·½°¸Îª£ºÏÈÍÑÏõ£¬ÔÙ³ý³¾£¬×îºóÍÑÁò£»ÆäÖÐ ÍÑÏõ ²ÉÓà ѡÔñÐÔ·Ç´ß»¯»¹Ô­·¨£¨SNCR£©£¬³ý³¾ ²ÉÓà ´üʽ³ý³¾Æ÷£¬ÍÑÁò ²ÉÓà ʯ»Òʯʪ·¨¡£
On the basis of comprehensively considering multiple aspects, we sought for the optimal treatment scheme of flue gas in the hope of meeting the criteria on flue gas emission. According to selection principle of treatment system, the final design scheme was: denitration, then dust extraction, finally desulfuration. Denitration was implemented by Selective Non-Catalytic Reduction£¨SNCR£©; dust extraction was performed using bag type dust collector; desulfuration was conducted by limestone washing method.

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Regarding the design of denitration technology, SNCR denitration was conducted inside of boiler furnace, in which liquid ammonia, serving as reducing agent, was sprayed into furnace by multi-nozzle ejector, and the consumption rate of NH3 was 14.7kg/h. As for the design of dust remover, we used a pulse-jet bag type dust collector, of which the length and width were both 2.4m, the height was 14.0m including a 8m-long filter-bag and a 1.6m ash bucket.
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