1.华北电力大学热电生产过程污染物监测与控制北京市重点实验室,北京 102206
2.中国科学院过程工程研究所湿法冶金清洁生产技术国家工程实验室,北京 100190
曲江源(1993—),男,博士研究生,qujy_ncepu@163.com
张锴(1968—),男,博士,教授,kzhang@ncepu.edu.cn
收稿:2019-04-21,
修回:2019-08-16,
纸质出版:2019-11-05
移动端阅览
曲江源, 刘霄龙, 关彦军, 齐娜娜, 滕阳, 徐文青, 朱廷钰, 张锴. 基于CFD模拟的臭氧低温氧化烧结烟气中NO过程分析[J]. 化工学报, 2019, 70(11): 4387-4396
QU Jiangyuan, LIU Xiaolong, GUAN Yanjun, QI Nana, TENG Yang, XU Wenqing, ZHU Tingyu, ZHANG Kai. CFD simulation of low-temperature NO oxidation using ozone in sintering flue gas[J]. CIESC Journal, 2019, 70(11): 4387-4396
曲江源, 刘霄龙, 关彦军, 齐娜娜, 滕阳, 徐文青, 朱廷钰, 张锴. 基于CFD模拟的臭氧低温氧化烧结烟气中NO过程分析[J]. 化工学报, 2019, 70(11): 4387-4396 DOI: 10.11949/0438-1157.20190418.
QU Jiangyuan, LIU Xiaolong, GUAN Yanjun, QI Nana, TENG Yang, XU Wenqing, ZHU Tingyu, ZHANG Kai. CFD simulation of low-temperature NO oxidation using ozone in sintering flue gas[J]. CIESC Journal, 2019, 70(11): 4387-4396 DOI: 10.11949/0438-1157.20190418.
以256 m
2
烧结机O
3
氧化烧结烟气中NO过程为研究对象,采用CFD数值模拟方法考察了含O
3
喷射气体与烧结烟气流动及NO低温氧化特性。通过与76步复杂反应机理的对比验证了11步简化机理的适用性,分析了反应温度、O
3
/NO摩尔比以及O
3
分布特性对NO氧化效率和不同价态NO
x
转化率的影响规律。通过对简单结构反应器的模拟结果表明:NO
3
稳定性较差,烟道内主要氧化产物为NO
2
与N
2
O
5
;随反应温度升高,NO氧化效率基本保持不变,NO
2
转化率提高且提升速率逐渐增大而N
2
O
5
呈相反规律;随O
3
/NO摩尔比增大,NO氧化效率提高但提升速率逐渐减小,NO
2
转化率先增大后在摩尔比高于1.25时开始减小,而各工况均产生N
2
O
5
且生成量逐渐增大,其原因为射流核心区可提供高O
3
/NO摩尔比条件;通过优化O
3
分布器结构改善O
3
与烟气接触与混合条件,O
3
与NO摩尔比为1.0、停留时间为0.87 s时NO氧化率可提高约12.8%,摩尔比为2.0、停留时间为1.73 s时N
2
O
5
转化率可提高约15.6%。
The flue gas from a 256 m
2
sintering machine was selected to explore the characteristics of NO oxidized by ozone at low temperature. The flow characteristics of O
3
injection gas and sintering flue gas and NO oxidation characteristics were investigated by CFD numerical simulation method. By compared with 76-step complex reaction mechanism
11-step simplified mechanism was verified to be reasonable for the above process. The effects of process conditions
including reaction temperature
O
3
/NO molar ratio and O
3
distribution
on the conversion rates of NO
x
with different chemical valences were examined. The results from the simulation for the reactor
which is simple in structure
show that NO
2
and N
2
O
5
are the main oxidation products in the flue gas
whilst NO
3
is consumed due to its poor chemical stability. The oxidation efficiency of NO changes little with the increase of reaction temperature
the conversion rate of NO
2
increases and performs more significant change at higher temperature. However
the conversion rate of N
2
O
5
presents an opposite trend compared with that of NO
2
. With the raise of O
3
/NO molar ratio
the oxidation rate of NO increases slowly and that of NO
2
increases firstly and then decreases when the molar ratio higher than 1.25
while N
2
O
5
emerges in the condition even the O
3
/NO molar ratio less than 1.0 and the N
2
O
5
production increases gradually
resulting from a higher O
3
/NO ratio in the injection core regions. Furthermore
the structural optimization for the ozone distributor could improve the homogeneity of O
3
in the sintering flue gas. Afterwards the oxidation efficiency of NO increases by 12.8% approximately when the O
3
/NO molar ratio is 1.0 and the average residence time is 0.87 s
while the increase for N
2
O
5
conversion rate of about 15.6% was obtained when the O
3
/NO molar ratio is 2.0 and the average residence time is 1.73 s.
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