Li Chaoqun, Han Qingzhen, Zhu Tingyu, Xu Wenqing
Research Center of Process Pollution Control, National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, State Key Laboratory of Multiphase Complex Systems, Institute of Process Engineering, Chinese Academy of Sciences No. 1, 2nd North Lane, ZhongGuanCun Beijing 100190 China
University of Chinese Academy of Sciences Beijing 100049 China.
RSC Adv. 2020 Jun 19;10(39):23491-23497. doi: 10.1039/d0ra00064g. eCollection 2020 Jun 16.
The catalytic reduction behaviours between NO and CO on a CaFeO surface were studied using flue gas recirculation. The reaction mechanism and control principle were investigated experiment and theoretical calculations. The experiment results show that CaFeO can catalyse the reduction of NO by CO, and the NO conversion rate increases with the increase in CO concentration. The theoretical calculations indicate that the CO-NO reaction on CaFeO surfaces complies with the Eley-Rideal mechanism, and the reaction path is controlled by nitrogen, oxygen and isocyanate radicals. Specifically, the dissociation of NO into nitrogen and oxygen radicals, and the formation of subsequent isocyanate radicals dominate the reaction. The results provide new insight into the intrinsic reaction mechanism and the meso-scale control principle, allowing us to propose a novel process design scheme to improve the NO emission reduction efficiency in the flue gas recirculation process.
采用烟气再循环研究了CaFeO表面上NO与CO之间的催化还原行为。通过实验和理论计算对反应机理及控制原理进行了研究。实验结果表明,CaFeO可催化CO还原NO,且NO转化率随CO浓度的增加而提高。理论计算表明,CaFeO表面上的CO-NO反应符合埃里-里德尔机理,反应路径由氮、氧和异氰酸酯自由基控制。具体而言,NO分解为氮和氧自由基以及随后异氰酸酯自由基的形成主导了该反应。这些结果为内在反应机理和中尺度控制原理提供了新的见解,使我们能够提出一种新颖的工艺设计方案,以提高烟气再循环过程中NO的减排效率。