Oxidation-separation kinetics of nitric oxide from flue gas using ferrate (VI) reagent in a spraying reactor

被引:3
作者
Yang, Wei [1 ]
Liu, Yangxian [1 ]
Xu, Wen [1 ]
Wang, Qian [1 ]
Zhao, Liang [2 ]
Pan, Jianfeng [1 ]
机构
[1] Jiangsu Univ, Sch Energy & Power Engn, Zhenjiang 212013, Jiangsu, Peoples R China
[2] Southeast Univ, Key Lab Energy Thermal Convers & Control, Minist Educ, Nanjing 210096, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
ferrate (VI); nitric oxide (NO); SO2; oxidation-separation kinetics; spraying reactor; SIMULTANEOUS REMOVAL; SULFUR-DIOXIDE; NO REMOVAL; SIMULTANEOUS DESULFURIZATION; SIMULTANEOUS ABSORPTION; SO2; REDUCTION; DENITRIFICATION; ULTRAVIOLET; MERCURY;
D O I
10.1002/cjce.22778
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Oxidation-separation kinetics of nitric oxide (NO) from flue gas using ferrate (VI) reagent in a spraying reactor was studied. Effects of several key parameters on NO absorption rate were studied, and the results show that increasing ferrate (VI) concentration, solution pH, and NO concentration increases the NO absorption rate. Increasing reaction temperature and SO2 concentration decrease NO absorption rate. The results of kinetic studies show that when <mml:msubsup>CFe<mml:msubsup>O42-</mml:msubsup></mml:msubsup><=0.16mol/L, the oxidation-absorption process of NO can be seen as a pseudo-2.28 order reaction (the reaction order is higher and the effect of reactant concentrations on reaction rate will become more obvious) and a pseudo-1.0 order reaction when <mml:msubsup>CFe<mml:msubsup>O42-</mml:msubsup></mml:msubsup>>0.16mol/L. The oxidation-absorption process of NO is a fast reaction, which shows that the mass transfer process is the key rate control step of the whole NO absorption process. When <mml:msubsup>CFe<mml:msubsup>O42-</mml:msubsup></mml:msubsup>>0.16mol/L, the mass transfer coefficient of gas phase and interfacial area play an important role for the oxidation-absorption process of NO.
引用
收藏
页码:1364 / 1372
页数:9
相关论文
共 49 条
[1]   Aqueous absorption and oxidation of nitric oxide with oxone for the treatment of tail gases: Process feasibility, stoichiometry, reaction pathways, and absorption rate [J].
Adewuyi, YG ;
Owusu, SO .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (17) :4084-4100
[2]   Simultaneous Absorption and Oxidation of Nitric Oxide and Sulfur Dioxide by Aqueous Solutions of Sodium Persulfate Activated by Temperature [J].
Adewuyi, Yusuf G. ;
Sakyi, Nana Y. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (33) :11702-11711
[3]   Dry De-NOx via Gas-Phase Photochemical Oxidation Using an Ultraviolet and Aerosolized H2O/H2O2 Hybrid System [J].
Choi, Jeongan ;
Lee, Kang Soo ;
Choi, Dong Yun ;
Kim, Yong Jin ;
Kim, Sang Soo .
ENERGY & FUELS, 2014, 28 (08) :5270-5276
[4]   Simultaneous absorption of SO2 and NO from flue gas with KMnO4/NaOH solutions [J].
Chu, H ;
Chien, TW ;
Li, SY .
SCIENCE OF THE TOTAL ENVIRONMENT, 2001, 275 (1-3) :127-135
[5]  
Danckwerts P.V., 1970, GAS LIQUID REACTIONS
[6]   Removal of NO from flue gas by aqueous chlorine-dioxide scrubbing solution in a lab-scale bubbling reactor [J].
Deshwal, Bal Raj ;
Jin, Dong Seop ;
Lee, Si Hyun ;
Moon, Seung Hyun ;
Jung, Jong Hyeon ;
Lee, Hyung Keun .
JOURNAL OF HAZARDOUS MATERIALS, 2008, 150 (03) :649-655
[7]   Simultaneous removal of NOX and SO2 from coal-fired flue gas by catalytic oxidation-removal process with H2O2 [J].
Ding, Jie ;
Zhong, Qin ;
Zhang, Shule ;
Song, Fujiao ;
Bu, Yunfei .
CHEMICAL ENGINEERING JOURNAL, 2014, 243 :176-182
[8]   Simultaneous removal of SO2 and NOx by wet scrubbing using urea solution [J].
Fang, Ping ;
Cen, Chaoping ;
Tang, Zhixiong ;
Zhong, Peiyi ;
Chen, Dingsheng ;
Chen, Zhihang .
CHEMICAL ENGINEERING JOURNAL, 2011, 168 (01) :52-59
[9]  
Feng B. H., 1982, CHEM ENG HDB
[10]   Effect of CaO on the selective non-catalytic reduction deNOx process: Experimental and kinetic study [J].
Fu, Shi-long ;
Song, Qiang ;
Tang, Jun-shi ;
Yao, Qiang .
CHEMICAL ENGINEERING JOURNAL, 2014, 249 :252-259