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高锰酸钾吸收气态汞的传质-反应研究 被引量:24

Mass transfer-reaction of Hg^0 absorption in potassium permanganate
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摘要 为了考查氧化剂高锰酸钾吸收气体态元素汞Hg0的行为,在鼓泡反应器中,通过改变各种影响因素,采用冷原子吸收(CVAA)测汞仪测定了反应器进口和出口的气态汞浓度.系统地研究了高锰酸钾初始浓度、pH值、汞初始度和反应温度等主要参数对气态汞去除效率的影响,并分析了KMnO4氧化Hg0的反应热力学和传质-反应动力学问题.研究结果表明,高猛酸钾初始浓度的增加、强酸或强碱条件均有利于Hg0的去除,H2SO4的存在促进了Hg0在MnO2上的吸附,而强碱水溶液中产生的OH间接氧经了Hg0;反应温度的升高抑止了Hg0的去除,而Hg0初始质量浓度对反应的影响可忽略;KMnO4氧化Hg0的反应为二级反应,活化能为27.22 kJ/mol. The conditions for potassium permanganate oxidizing gaseous mercury were examined. Gaseous mercury concentration at the inlet and outlet of a bubble column reactor was measured by cold vapor atom absorption (CVAA) mercury analyzer. The effects of KMnO4 concentration, pH value, initial Hg^0 concentration and temperature on Hg^0 removal efficiency were investigated, as well as the thermodynamics and mass transfer-reaction between Hg^0 and KMnO4. The results showed that both increasing the KMnO4 concentration and using acidic or alkaline solution promoted the removal of Hg^0. The reasons are that H2 SO4 in solution facilitates the adsorption of Hg^0 on MnO2, and that free radical OH produced in alkaline solution can oxidate Hg^0. High temperature has a negative effect on the removal of Hg^0 , and the effect of Hg^0 initial concentration can be neglected. The oxidation of Hg^0 by KMnO4 is a two-order reaction and the acti- vated energy is 27.22 kJ/mol.
出处 《浙江大学学报(工学版)》 EI CAS CSCD 北大核心 2007年第5期831-835,870,共6页 Journal of Zhejiang University:Engineering Science
基金 国家自然科学基金资助项目(20476094)
关键词 高锰酸钾 气态汞 吸收 传质-反应 potassium permanganate gaseous mercury absorption mass transfer-reaction
作者简介 叶群峰(1977-),男,浙江金华人,博士生,主要从事大气汞污染控制研究.E—mail:qunfengye@163.com通讯联系人:徐新华,男,教授,博导.E—mail:xuxinhua@zju.edu.cn
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参考文献14

  • 1BROWN T D,SMITH D N,HARGIS R A,et al.Mercury measurement and its control:What we know,have learned,and need to further investigate[J].Journal of the Air & Waste Management Association,1999,49(6):628-640.
  • 2王起超,沈文国,麻壮伟.中国燃煤汞排放量估算[J].中国环境科学,1999,19(4):318-321. 被引量:264
  • 3任建莉,周劲松,骆仲泱,岑可法.燃煤过程中汞的析出规律试验研究[J].浙江大学学报(工学版),2002,36(4):397-403. 被引量:28
  • 4LAUDAL L D,BROWN D T,NOTT R B.Effects of flue gas constituents on mercury speciation[J].Fuel Processing Technology,2000(6566):157-165.
  • 5MONKMAN J L,MAFFETT P A,DOHERTY T F.The determination of mercury in air samples and biological materials[J].American Industrial Hygiene Association Journal,1956,17:418-420.
  • 6HARA N.Capture of mercury vapor in air with potassium permanganate solution[J].Industrial Health,1975,13:243-251.
  • 7SHENDRIKAR A D,FILBY R,MARKOWSKI G R,et al.Trace element loss onto polyethylene container walls from impinger solutions from flue gas sampling[J].Air Pollution Control Association,1984,34:233-236.
  • 8HUANG Kun-chang,HOAG G E,CHHEDA P.Chemical oxidation of trichloroethylene with potassium permanganate in a porous medium[J].Advances in Environmental Research,2002,7(1):217-229.
  • 9刘锐平,李星,夏圣骥,武荣成,李圭白.高锰酸钾强化三氯化铁共沉降法去除亚砷酸盐的效能与机理[J].环境科学,2005,26(1):72-75. 被引量:30
  • 10FASANMI F O.Treatment of toxic organic wastewaters with chemical oxidation,carbon absorption and bioaugmentation[D].Cleveland:Cleveland State University,1999.

二级参考文献23

  • 1叶常明.环境中的邻苯二甲酸酯[J].环境科学进展,1993,1(2):36-47. 被引量:102
  • 2Masscheleyn PH, Delaune RD, William HPJ. Effect of redox potential and pH on arsenic speciation and solubility in a contaminated .soil [J]. Environ. Sci. Technol., 1991, 25(8): 1414--1419.
  • 3Meng XG, Korfiatis GP, Christodoulatos C, Bang S. Treatment of arsenic in Bangladesh well water using a household co-precipitation and filtration system [J]. War. Res. , 2001, 35 (12) :2805--2810.
  • 4Gregor J. Arsenic removal during conventional aluminium-based drinking-water treatment [J]. Wat. Res. , 2001, 35(7) : 1659-- 1664.
  • 5Munoz JA, Gonzalo A, Valiente M. Arsenic adsorption by Fe( Ⅲ )-loaded open-celled cellulose sponge: Thermodynamic and selectivity aspects [J]. Environ. Sci. Teehnol., 2002, 36(15): 3405--3411.
  • 6Philip B, Gary A. Alternative methods for membrane filtration of arsenic from drinking water [J]. Desalination, 1998, 117:1--10.
  • 7Vagliasindi FGA, Benjamin MM. Arsenic removal in fresh and non-preloaded ion exchange packed bed adsorption reactors [J ].War. Sci. Technol. , 1998, 38(6): 337--343.
  • 8Borho M, Wilderer P. Optimized removal of arsenic( nl ) byadaptation of oxidation and precipitation processes to the filtration step [J]. War. Sci. Technol. , 1996, 34 (9): 25--31.
  • 9Colthurst JM, Singer PC. Removing trihalomethane precursors by permanganate oxidation and manganese dioxide adsorption[J]. J. AWWA, 1982, 74: 78--83.
  • 10Posselt HS, Anderson FJ, Walter JWJ. Cation sorption on colloidal hydrous manganese dioxide [J]. Environ. Sci. Technol. ,1968, 2(12): 1087--1093.

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