GONG Hui, WANG Xuesheng, CHEN Qinzhu, CHEN Shuo. Removal of SO2 and NO from flue gas by wet process of NaClO2/urea composite absorbent[J]. Chinese Journal of Environmental Engineering, 2017, 11(9): 5114-5121. doi: 10.12030/j.cjee.201610125
Citation: GONG Hui, WANG Xuesheng, CHEN Qinzhu, CHEN Shuo. Removal of SO2 and NO from flue gas by wet process of NaClO2/urea composite absorbent[J]. Chinese Journal of Environmental Engineering, 2017, 11(9): 5114-5121. doi: 10.12030/j.cjee.201610125

Removal of SO2 and NO from flue gas by wet process of NaClO2/urea composite absorbent

  • Received Date: 28/11/2016
    Accepted Date: 20/10/2016
    Available Online: 26/08/2017
    Fund Project:
  • The experiment was performed to study the removal of SO2 and NO from the flue by NaClO2/urea composite absorbent in the spray tower designed by ourselves,the mechanism of removal of SO2 and NO from the flue gas by NaClO2/urea composite absorbent was analyzed. The results indicated that SO2 was absorbed liquid absorption process was divided into two parts,a part of SO2 dissolved in water was oxidized to SO42- by NaClO2, another part of the SO2 dissolved in water and reacted with urea and oxygen to generate (NH4)2SO4. NO which was insoluble in water was oxidized into NO3- by NaClO2 and then absorbed by urea,NO was reduced to environmentally friendly gas N2. Furthermore,the experiments mainly explored the effect of NaClO2 concentration,urea concentration,SO2 inlet concentration,NO inlet concentration,initial pH value and temperature on the removal efficiency of NO,optimize the process conditions,the average removal rate of SO2 and NO were 100% and 95.2%, respectively when the absorption liquid NaClO2 concentration was 4 mmol·L-1,urea concentration was 0.5 mol·L-1,the initial pH was 7,the temperature was 50℃.
  • [1] CHIEN T,CHU H. Removal of SO2 and NO from flue gas by wet scrubbing using an aqueous NaClO2 solution[J]. Journal of Hazardous Materials,2001,80(1/2/3):43-57

    Google Scholar Pub Med

    [2] PARK H W,CHOI S,PARK D W. Simultaneous treatment of NO and SO2 with aqueous NaClO2 solution in a wet scrubber combined with a plasma electrostatic precipitator[J]. Journal of Hazardous Materials,2015,285:117-126

    Google Scholar Pub Med

    [3] 钟毅,高翔,骆仲泱,等.KMnO4/NaOH溶液吸收SO2/NO的动力学研究[J]. 浙江大学学报(工学版),2009,43(5):948-952

    Google Scholar Pub Med

    [4] MA S C,ZHAO Y,ZHENG F L,et al. Study on reducing SO2/NOx in flue gas by aqueous catalytic oxidation[J].China Environmental Science,2001,21:33-37

    Google Scholar Pub Med

    [5] WANG L,ZHAO W R,WU Z B. Simultaneous absorption of NO and SO2 by Fe(Ⅱ) EDTA combined with Na2SO3 solution[J].Chemical Engineering Journal, 2007,132:227-232

    Google Scholar Pub Med

    [6] DING J,ZHONG Q,ZHANG S L,et al. Simultaneous removal of NOx and SO2 from coal-fired flue gas by catalytic oxidation-removal process with H2O2[J].Chemical Engineering Journal,2014,243:176-182

    Google Scholar Pub Med

    [7] FANG P,CEN C P,TANG Z X,et al. Simultaneous removal of SO2 and NOx by wet scrubbing using urea solution[J].Chemical Engineering Journal, 2011,168(1):52-59

    Google Scholar Pub Med

    [8] ZHAO Y,GUO T X,CHEN Z Y,et al. Simultaneous removal of SO2 and NO using M/NaClO2 complex absorbent[J]. Chemical Engineering Journal, 2010,160:42-47

    Google Scholar Pub Med

    [9] DESHWAL B R, SI H L, JUNG J H,et al. Study on the removal of NOx from simulated flue gas using acidic NaClO2 solution[J]. Journal of Environmental Sciences,2008,20(1):33-38

    Google Scholar Pub Med

    [10] JIN D S,DESHWAL B R,PARK Y S,et al. Simultaneous removal of SO2 and NO by wet scrubbing using aqueous chlorine dioxide solution[J]. Journal of Hazardous Materials,2006,135(1/2/3):412-417

    Google Scholar Pub Med

    [11] SADA E,KUMAZAWA H,KUDO I,et al. Absorption of no in aqueous mixed solutions of NaClO2 and NaOH[J]. Chemical Engineering Science,1978,33(3):315-318

    Google Scholar Pub Med

    [12] SADA E,KUMAZAWA H,YAMANAKA Y,et al. Kinetics of absorption of sulfur dioxide and nitric oxide in aqueous mixed solutions of sodium chlorite and sodium hydroxide[J]. Journal of Chemical Engineering of Japan,1978,11(4):276-282

    Google Scholar Pub Med

    [13] SADA E,KUMAZAWA H,KUDO I,et al. Absorption of lean NOx in aqueous solutions of NaClO2 and NaOH[J]. Industrial & Engineering Chemistry Process Design & Development,1979,18(2):275-278

    Google Scholar Pub Med

    [14] WEI J C,LUO Y B,YU P,et al. Removal of NO from flue gas by wet scrubbing with NaClO2/(NH2)2CO solutions[J]. Journal of Industrial and Engineering Chemistry,2009,15(1):16-22

    Google Scholar Pub Med

    [15] 杨一理. 尿素与氧化剂复合吸收液同时脱硫脱硝试验研究[D]. 杭州:浙江工业大学, 2013

    Google Scholar Pub Med

    [16] 谭天恩,金一中,骆有寿. 传质·反应过程[M]. 杭州:浙江大学出版社,1990

    Google Scholar Pub Med

    [17] DANCKWERTS P V. Gas-Liquid Reactions[M].New York:McGraw-Hill Book Company,1970

    Google Scholar Pub Med

    [18] 赵静,严金英,邱婧伟,等. NaClO2/NaClO复合吸收液同时脱硫脱硝[J]. 环境工程学报,2012, 6(10):3684-3688

    Google Scholar Pub Med

    [19] 方平,岑超平,唐志雄,等. 尿素/H2O2溶液同时脱硫脱硝机理研究[J]. 燃料化学学报,2012,40(1):111-118

    Google Scholar Pub Med

    [20] 尹凤交. 尿素/Ca(ClO)2湿法同时脱硫脱硝技术的试验研究[D].济南:山东大学,2010

    Google Scholar Pub Med

    [21] JOSHI J B,MAHAJANI V V,JUVEKAR V A. Invited review:Absorption of NOx gases[J]. Chemical Engineering Communications,1985,33:1-92

    Google Scholar Pub Med

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Removal of SO2 and NO from flue gas by wet process of NaClO2/urea composite absorbent

Fund Project:

Abstract: The experiment was performed to study the removal of SO2 and NO from the flue by NaClO2/urea composite absorbent in the spray tower designed by ourselves,the mechanism of removal of SO2 and NO from the flue gas by NaClO2/urea composite absorbent was analyzed. The results indicated that SO2 was absorbed liquid absorption process was divided into two parts,a part of SO2 dissolved in water was oxidized to SO42- by NaClO2, another part of the SO2 dissolved in water and reacted with urea and oxygen to generate (NH4)2SO4. NO which was insoluble in water was oxidized into NO3- by NaClO2 and then absorbed by urea,NO was reduced to environmentally friendly gas N2. Furthermore,the experiments mainly explored the effect of NaClO2 concentration,urea concentration,SO2 inlet concentration,NO inlet concentration,initial pH value and temperature on the removal efficiency of NO,optimize the process conditions,the average removal rate of SO2 and NO were 100% and 95.2%, respectively when the absorption liquid NaClO2 concentration was 4 mmol·L-1,urea concentration was 0.5 mol·L-1,the initial pH was 7,the temperature was 50℃.

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