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    臧学轲. 羟胺促进柠檬酸-Fe2+活化过碳酸钠降解三氯乙烯[J]. 华东理工大学学报(自然科学版), 2018, (3): 454-462. DOI: 10.14135/j.cnki.1006-3080.20170925001
    引用本文: 臧学轲. 羟胺促进柠檬酸-Fe2+活化过碳酸钠降解三氯乙烯[J]. 华东理工大学学报(自然科学版), 2018, (3): 454-462. DOI: 10.14135/j.cnki.1006-3080.20170925001
    ZANG Xue-ke. Enhanced Degradation of Trichloroethylene with Hydroxylamine Hydrochloride Addition in Citric-Acid Chelated Fe2+-Catalyzed Percarbonate System[J]. Journal of East China University of Science and Technology, 2018, (3): 454-462. DOI: 10.14135/j.cnki.1006-3080.20170925001
    Citation: ZANG Xue-ke. Enhanced Degradation of Trichloroethylene with Hydroxylamine Hydrochloride Addition in Citric-Acid Chelated Fe2+-Catalyzed Percarbonate System[J]. Journal of East China University of Science and Technology, 2018, (3): 454-462. DOI: 10.14135/j.cnki.1006-3080.20170925001

    羟胺促进柠檬酸-Fe2+活化过碳酸钠降解三氯乙烯

    Enhanced Degradation of Trichloroethylene with Hydroxylamine Hydrochloride Addition in Citric-Acid Chelated Fe2+-Catalyzed Percarbonate System

    • 摘要: 研究了柠檬酸(CA)螯合Fe2+活化过碳酸盐体系中投加盐酸羟胺(HAH)对三氯乙烯(TCE)的去除效果。结果发现,HAH能有效将Fe3+还原为Fe2+,强化TCE的去除效果。当TCE初始浓度为0.15 mmol/L时,nSPCnFe2+nTCE=5:3:1时,在CA浓度为0.5 mmol/L条件下,HAH最佳投加浓度为1.5 mmol/L,此时TCE去除率为99.6%。·OH对TCE降解的贡献度为79.2%,O2-·的贡献度为21.9%。HAH可减轻HCO3-对TCE降解的抑制效应,中间产物为甲酸、NO2-和NO3-。HAH利于SPC/Fe2+/CA体系降解TCE,该结果可为实际TCE污染地下水修复提供技术支撑。

       

      Abstract: The impact of hydroxylamine hydrochloride (HAH) addition on the enhancement of trichloroethylene (TCE) degradation in the citric acid (CA)-chelated Fe2+-catalyzed sodium percarbonate (SPC) system was investigated. The effects of HAH dosage and solution martirx (Cl-, HCO3- and hurmic acid) on TCE removal were examined and the results indicated that HAH promoted TCE degradation significantly by transferring Fe3+ to Fe2+, therefore maintaining a sustainable activation of Fe2+. Under the optimum molar ratio of nSPC:nFe2+:nTCE=5:3:1 at the initial concentration of TCE 0.15 mol/L and CA 0.50 mmol/L, the final TCE removal efficiency was 99.6%. HCO3- had significant inhibitory effect on the degradation of TCE, whereas the effects of Cl- and humic acid on the degradation of TCE could be ignored. In addition, TCE removal inhibition rate of HCO3- were 59.9%, 15.5% and 14.9% respectively when HCO3- concentration was all 1.0 mmol/L in SPC/Fe2+/TCE, SPC/Fe2+/CA/TCE and HAH/SPC/Fe2+/CA/TCE systems. The results indicated that HAH alleviated HCO3- inhibitory effect on the degradation of TCE. Scavengers tests were also conducted to understand the roles of ·OH and O2-· on TCE degradation. The results showed that ·OH and O2-· contributed 79.2% and 21.9% to TCE removal, respectively. The consistency of Cl- concentration both experimentally and theoretically suggested the complete dechlorination of TCE in HAH/SPC/Fe2+/CA/TCE system. The intermediate products were formic acid, NO2- and NO3-. The concentration of formic acid increased to 5.8 mg/L within 60 min and then decreased to 1.4 mg/L within 120 min, meaning that the addition of HAH favors further degradation of formic acid and therefore complete mineralization of TCE. The overall results strongly confirmed the benefits of HAH amendment to TCE degradation in the SPC/Fe2+/CA system which provided a technical basis for practical applications in TCE contaminated groundwater remediation.

       

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