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催化氧化除氨氮/锰滤料活性恢复方式优化研究
引用本文:程亚,张永志,郑佳慧,李宇洋,黄廷林.催化氧化除氨氮/锰滤料活性恢复方式优化研究[J].中国环境科学,2022,42(5):2112-2119.
作者姓名:程亚  张永志  郑佳慧  李宇洋  黄廷林
作者单位:西安建筑科技大学环境与市政工程学院, 陕西省环境工程重点实验室, 西北水资源与环境生态教育部重点实验室, 陕西 西安 710055
基金项目:国家自然科学基金资助项目(52000145,51778521);;国家重点研发计划项目(2019YFD1100101);
摘    要:以催化氧化除氨氮/锰失活滤料为研究对象,考察了3种不同恢复方式(自然恢复,投加碱度,再次挂膜)对滤料催化氧化氨氮、锰效能的影响.结果表明,自然恢复(1#)滤柱,投加碱度(2#)滤柱,再次挂膜(3#)滤柱分别于4,2,3d后氨氮去除率达到90%以上;逐渐提高氨氮浓度,3#再次挂膜滤柱出水氨氮浓度波动最大,1#自然恢复滤柱恢复期间出水亚硝氮积累时间最长且峰值最高.3根滤柱催化氧化去除锰活性恢复速度均较快.1#自然恢复滤柱和2#碱度恢复滤柱均能在2d内将锰完全去除.3#挂膜滤柱是在停止投加高锰酸钾后5d内实现将进水锰完全去除.氨氮和锰的相互影响实验结果表明,3根滤柱中投加碱度(2#)滤柱表现最优.尽管氨氮抑制锰的去除,但是投加碱度滤柱随着进水氨氮浓度的升高出水锰浓度始终低于0.1mg/L;锰对氨氮的去除影响不显著.XRD分析结果表明,受其表面负载新生成氧化膜的影响,高锰酸钾重新挂膜滤柱的滤料样品的结晶度较差.综合考虑氨氮和锰的活性恢复效率以及挂膜过程中药品的投加,提出采用自然恢复方式最适.

关 键 词:活性恢复  失活滤料  除氨氮/锰  催化氧化  地下水处理  
收稿时间:2021-09-22

Optimization of recovery method for catalytic ammonium/manganese oxidation by active filter media
CHENG Ya,ZHANG Yong-zhi,ZHENG Jia-hui,LI Yu-yang,HUANG Ting-lin.Optimization of recovery method for catalytic ammonium/manganese oxidation by active filter media[J].China Environmental Science,2022,42(5):2112-2119.
Authors:CHENG Ya  ZHANG Yong-zhi  ZHENG Jia-hui  LI Yu-yang  HUANG Ting-lin
Institution:Shaanxi Key Laboratory of Environmental Engineering, Key Laboratory of Northwest Water Resource, Ministry of Education, School of Environmental and Municipal Engineering, Xi'an University of Architecture and Technology, Xi'an 710055, China
Abstract:Taking deactivated filter media as the research object, the effects of three different recovery methods (natural recovery, adding basicity, and re-hanging film) on the catalytic oxidation efficiency of the filter media for ammonium (NH4+-N) and manganese (Mn2+) removal were investigated. The experimental results showed that the NH4+-N removal rate of natural recovery (1#) filter column, adding basicity (2#) filter column and re-hanging film (3#) filter column was above 90% after running for 4d, 2d and 3d, respectively. When the influent NH4+-N concentration increased gradually, the effluent NH4+-N concentration of 3# filter column fluctuated the most, while the effluent nitrite accumulation time of 1# filter column was the longest and the peak value was the highest. The recovery rate of Mn2+ removal activity of all three filter columns was fast. Both 1# and 2# filter columns could completely remove Mn2+ in 2 days and 3# filter column could completely remove the influent Mn2+ within 5days after stopping adding potassium permanganate. The experimental results of the interaction between NH4+-N and Mn2+ showed that 2# filter column performed the best among the three filter columns. Although NH4+-N inhibited the removal of Mn2+, with the increase of influent NH4+-N concentration, the effluent Mn2+ concentration of the 2# filter column was always lower than 0.1mg/L. Mn2+ had no significant effect on NH4+-N removal. The results of XRD analysis showed that the crystallinity of the filter media samples in 3# filter column was poor due to the influence of the new formed oxide film on its surface. Considering the recovery efficiency of NH4+-N and Mn2+ as well as the addition of chemical agents, the natural recovery method is the most suitable recovery method.
Keywords:activity recovery  deactivated filter media  ammonium/manganese removal  catalytic oxidation  groundwater treatment  
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