罗丹, 郭丽潇, 郝全爱, 黄淑龙, 石亮. 芬顿氧化法处理氧化性泡沫去污废液中的有机物[J]. 核化学与放射化学, 2024, 46(2): 170-176. DOI: 10.7538/hhx.2024.YX.2023095
    引用本文: 罗丹, 郭丽潇, 郝全爱, 黄淑龙, 石亮. 芬顿氧化法处理氧化性泡沫去污废液中的有机物[J]. 核化学与放射化学, 2024, 46(2): 170-176. DOI: 10.7538/hhx.2024.YX.2023095
    LUO Dan, GUO Li-xiao, HAO Quan-ai, HUANG Shu-long, SHI Liang. Treatment of Organic Compounds in Oxidative Foam Decontamination Waste Liquid by Fenton Oxidation Method[J]. Journal of Nuclear and Radiochemistry, 2024, 46(2): 170-176. DOI: 10.7538/hhx.2024.YX.2023095
    Citation: LUO Dan, GUO Li-xiao, HAO Quan-ai, HUANG Shu-long, SHI Liang. Treatment of Organic Compounds in Oxidative Foam Decontamination Waste Liquid by Fenton Oxidation Method[J]. Journal of Nuclear and Radiochemistry, 2024, 46(2): 170-176. DOI: 10.7538/hhx.2024.YX.2023095

    芬顿氧化法处理氧化性泡沫去污废液中的有机物

    Treatment of Organic Compounds in Oxidative Foam Decontamination Waste Liquid by Fenton Oxidation Method

    • 摘要: 氧化性泡沫去污废液因含有大量有机物而无法被直接处理。针对该问题,将芬顿氧化法用于降解泡沫去污废液中的有机物,为泡沫去污废液的预处理提供了一种新思路。采用芬顿氧化法以及两步联合降解工艺对氧化性泡沫去污废液进行了预处理,探索了过氧化氢用量、亚铁离子用量、反应时间、反应温度、紫外光照等工艺参数对氧化性泡沫去污废液化学需氧量去污率的影响规律,以及每步降解实验的适宜操作条件。结果表明:在初次降解的最佳工艺条件下,芬顿氧化法可将废液的化学需氧量从(37 000±1 850) mg/L降至(2 064±95) mg/L (n=3),化学需氧量去除率高达(94.40±0.54)%(n=3),但化学需氧量为(2 064±95) mg/L的残液仍不符合既有废液处理方法的条件;在二次降解的最佳工艺条件下,芬顿联合紫外法可继续将残液的化学需氧量从(2 064±95) mg/L降至(478±12) mg/L,满足了既有废液处理方法的条件。结果说明,芬顿氧化法以及两步联合降解工艺适宜作为氧化性泡沫去污废液的预处理方法。

       

      Abstract: Oxidative foam decontamination waste liquid could not be treated directly due to high levels of organic compounds. In order to solve this problem, Fenton oxidation method was applied for the first time to degrade organic compounds in foam decontamination waste liquid, which provided a new idea for the pretreatment. Fenton oxidation method and two-step combined degradation process were adopted. The effects of various process parameters on COD removal rate of foam decontamination waste liquid and the suitable operating conditions of each degradation process were explored in this study. The results show that under the suitable operating conditions of initial degradation, Fenton oxidation method can reduce the COD of waste liquid from (37 000±1 850) mg/L to (2 064±95) mg/L(n=3), with a COD removal rate of up to (94.40±0.54) %(n=3). However, the residual liquid with COD of (2 064±95) mg/L still do not meet the conditions of existing methods of waste liquid treatment. Under the suitable operating conditions of second degradation, Fenton-UV combined method can continue to reduce the COD of residual liquid from (2 064±95) mg/L to (478±12) mg/L, which meets the conditions of existing methods of waste liquid treatment. In conclusion, Fenton oxidation method and two-step combined degradation process are suitable for the pretreatment of oxidative foam decontamination waste liquid.

       

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