1.湘潭大学化工学院,湖南 湘潭 411105
2.中国科学院过程工程研究所多相复杂系统国家重点实验室,北京 100190
3.沈阳化工大学,辽宁 沈阳 110142
王超(1993—),男,硕士研究生,wang_chao999058@163.com
余剑(1979—),男,博士,副研究员,yujian@ipe.ac.cn
收稿:2018-09-19,
修回:2018-12-11,
网络首发:2026-07-24,
纸质出版:2019-03-05
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王超, 李长明, 皇甫林, 李萍, 杨运泉, 高士秋, 余剑, 许光文. 赤泥催化剂的制备及其对模拟烟气中微量氨的脱除性能[J]. 化工学报, 2019, 70(3): 1056-1064
WANG Chao, LI Changming, HUANGFU Lin, LI Ping, YANG Yunquan, GAO Shiqiu, YU Jian, XU Guangwen. Preparation of red mud-based catalyst and performance for trace ammonia in simulative tail gas[J]. CIESC Journal, 2019, 70(3): 1056-1064
王超, 李长明, 皇甫林, 李萍, 杨运泉, 高士秋, 余剑, 许光文. 赤泥催化剂的制备及其对模拟烟气中微量氨的脱除性能[J]. 化工学报, 2019, 70(3): 1056-1064 DOI: 10.11949/j.issn.0438-1157.20181051.
WANG Chao, LI Changming, HUANGFU Lin, LI Ping, YANG Yunquan, GAO Shiqiu, YU Jian, XU Guangwen. Preparation of red mud-based catalyst and performance for trace ammonia in simulative tail gas[J]. CIESC Journal, 2019, 70(3): 1056-1064 DOI: 10.11949/j.issn.0438-1157.20181051.
以赤泥固废为原料,采用酸解-碱沉淀法制备了赤泥粉体催化剂,并提出一种将催化剂直接喷入SNCR尾气中的除氨工艺,考察了催化剂加入点温度、空速、NH
3
浓度及水蒸气对氨去除能力的影响。研究发现,该催化过程具有很高的活性和N
2
的选择性,450℃以上NH
3
的转化率可达100%,同时在400~500℃间,N
2
的选择性高于80%,达到了很好的除氨效果;在500℃,空速为3×10
6
~6×10
6
h
-1
之间时,出口NH
3
浓度均为0;此工艺对于逃逸NH
3
浓度的适用性较强,入口[NH
3
]
= 50×10
-6
~1000×10
-6
mol/L范围内均可完全脱除,且具有一定的抗水能力。通过一系列表征发现,该种方法制备的赤泥催化剂不仅消除了原始固废的强碱性,还提高了其表面酸性,具有较高的比表面积、孔容和丰富的表面微观结构,使NH
3
的吸附及活化反应能力大大增加;该催化剂过程遵循iSCR机理,在400~500℃温度区间主要发生NH
3
-SCO反应,低于400℃主要发生NH
3
-SCR反应,粉体催化剂通过NH
3
-SCR和NH
3
-SCO协同反应达到了去除尾气中微量氨的目的。
A Fe-based powder catalyst was prepared from red mud (RM) solid waste with acid base neutralization method
which was used to eliminate the trace ammonia thought the proposed process of directly spraying the catalyst into SNCR tail gas. The effects of temperature
space velocity
NH
3
concentration and water vapor on ammonia removal capacity of the catalyst were investigated in details
and excellent removal efficiency could be achieved with 100% NH
3
conversion above 450℃ as well as
>
80% selectivity of N
2
between 400—500℃. Especially
the trace ammonia in the tail gas can completely be cleared with 0 left between the space velocity of 3×10
6
—6×10
6
h
-1
at 500℃. Meanwhile
the catalytic process is also effective for the removal of NH
3
with wide concentration of (40×10
-6
~800×10
-6
mol/L) even in the presence of water. The multiple characterizations further revealed that the strong alkalinity of the original solid waste was removed together with the increase of surface acidity as well as large specific surface area and rich surface microstru
cture for the obtained red mud catalyst
which accounts for its significant increase of adsorption and activation of NH
3
. Moreover
it was found the removal process of NH
3
follows the internal selective catalytic reduction (iSCR) mechanism
and the NH
3
was eliminated through both the NH
3
-SCR and NH
3
-SCO reactions
which mainly function below 400℃ and between 400-500℃
respectively.
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