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苯胺污染场地修复技术研究进展

刘元生,  王颖,  王月,  李雅君,  闫国凯

刘元生,王颖,王月,等. 苯胺污染场地修复技术研究进展[J]. 地质科技通报,2026,45(5):271-284 doi: 10.19509/j.cnki.dzkq.tb202606030
引用本文: 刘元生,王颖,王月,等. 苯胺污染场地修复技术研究进展[J]. 地质科技通报,2026,45(5):271-284 doi: 10.19509/j.cnki.dzkq.tb202606030
LIU Yuansheng,WANG Ying,WANG Yue,et al. Research progress on remediation technologies for aniline-contaminated sites[J]. Bulletin of Geological Science and Technology,2026,45(5):271-284 doi: 10.19509/j.cnki.dzkq.tb202606030
Citation: LIU Yuansheng,WANG Ying,WANG Yue,et al. Research progress on remediation technologies for aniline-contaminated sites[J]. Bulletin of Geological Science and Technology,2026,45(5):271-284 doi: 10.19509/j.cnki.dzkq.tb202606030

苯胺污染场地修复技术研究进展

doi: 10.19509/j.cnki.dzkq.tb202606030
基金项目: 京津冀环境综合治理国家科技重大专项(2026ZD1210201-03)
详细信息
    作者简介:

    刘元生:E-mail:13051127797@163.com

    通讯作者:

    E-mail: yuewanggg@126.com

  • 中图分类号: X53

Research progress on remediation technologies for aniline-contaminated sites

More Information
  • 摘要:

    苯胺是一类高毒性、难降解、性质稳定的半挥发性有机污染物,主要来自染料、医药、农药、橡胶助剂等化工生产活动泄漏与排放,部分农业活动也会造成环境苯胺累积。由于其环境稳定性强、多介质迁移转化过程复杂,苯胺污染场地高效修复已成为当前环境修复领域的突出难点。基于 Web of Science 数据库文献计量分析结果,系统梳理苯胺污染的来源、污染场地环境特征及检测分析技术发展现状,归纳各类修复技术的适用边界。在此基础上,依据场地污染程度提出差异化修复思路:对于高浓度污染区(土壤苯胺质量分数>1500 mg/kg、地下水苯胺质量浓度>1000 mg/L),应以污染源削减和污染羽控制为核心,优先采用热脱附、化学氧化 / 还原、土壤淋洗、土壤气相抽提、地下水抽出处理等物理−化学协同修复技术,快速削减污染负荷,降低污染物持续释放风险;对于中浓度污染区(土壤苯胺质量分数(260, 1500] mg/kg、地下水苯胺质量浓度(100, 1000] mg/L),宜采用阻隔墙、可渗透反应墙(PRB)等技术实现污染羽管控;对于低浓度污染区(土壤苯胺质量分数≤260 mg/kg、地下水苯胺质量浓度≤100 mg/L),可选用微生物修复、植物修复、监测自然衰减(MNA)等低干预技术实现长效风险管控。在此基础上,总结现有修复技术工程应用存在成本高、部分技术修复效率受限、实验室结果与现场工程脱节等现实瓶颈,并从新型修复材料开发、多技术耦合体系优化、绿色可持续修复体系构建等方面提出研究展望,以期为苯胺污染场地科学精准治理提供理论参考与技术支撑。

     

  • 图 1  2005—2024年间苯胺研究领域的文献计量学特征分析

    a.苯胺及其环境介质(废水、土壤和地下水)年度发文量变化趋势;b.基于聚类分析的国家/地区科研合作网络图谱,节点颜色代表不同国家/地区,大小代表发文量,连线代表合作关系;c.基于聚类分析的作者关键词的共现网络图谱,不同颜色代表不同的研究热点聚类,连线粗细代表词汇间共现强度;DFT. density functional theory;GC-MS. gas chromatography-mass spectrometry

    Figure 1.  Bibliometric characteristics of aniline-related research (2005—2024)

    图 2  苯胺在地下介质中的多相迁移转化示意图(NAPL为非水相液体)

    Figure 2.  Schematic diagram of multiphase migration and transformation of aniline in subsurface media

    图 3  受污染场地中人类接触苯胺的途径

    Figure 3.  Human exposure pathways to aniline at contaminated sites

    图 4  不同浓度分区修复技术示意图

    Figure 4.  Schematic diagram of remediation technologies for different concentration zones

    图 5  原位热脱附工艺示意图

    Figure 5.  Schematic diagram of in-situ thermal desorption process

    图 6  典型原位土壤淋洗系统的设置与工作原理

    Figure 6.  Layout and working principle of a typical in-situ soil-washing system

    表  1  场地修复技术对苯胺污染场地适用性分析

    Table  1.   Applicability analysis of remediation technologies for aniline-contaminated sites

    修复技术 适用性分析 优点 缺点
    热脱附 适用于黏粒含量低、渗透性好的砂质土壤;当苯胺浓度较高或土壤黏粒含量较高时,宜加热到370 ℃以上,采用高温热脱附,使苯胺在挥发的同时发生热分解,以增强脱附效率 处理效率高,可同时去除多种有机污染物;设备成熟,工程应用广泛 能耗较高,设备投资大;高温处理可能产生次生污染物,需配套尾气净化系统
    化学氧化/
    还原
    该技术对土壤类型适应性强,适用于各类水文地质条件的污染区域。从药剂选择方面,氧化剂对苯胺的去除效果总体优于还原剂,其中活化过硫酸盐、高锰酸钾及H2O2药剂去除率可达99%以上[34] 反应速率快;可在常温常压下进行;药剂投加方式灵活 氧化剂消耗量大,成本较高;可能影响土壤理化性质;部分氧化剂(如过硫酸盐)可能产生硫酸盐残留等二次污染风险
    土壤淋洗 适用于渗透性较好的砂质、粉砂质土壤;当土壤砂粒含量低、有机质含量高时,淋洗去除率会降低。常选择表面活性剂作为淋洗药剂,其中阴离子表面活性剂(如十二烷基苯磺酸钠)效果优于非离子表面活性剂,阴−非离子复配体系可进一步提升去除效率[50] 可大幅削减污染土方量,将污染物转移至液相集中处理;处理周期短 淋洗液需进一步处理,可能产生二次污染;对黏性土壤效果较差;大规模应用成本较高
    土壤气相
    抽提
    适用于渗透性较好的非饱和带苯胺污染场地。由于苯胺蒸汽压相对较低,单独使用时处理效率有限,常与化学氧化(如臭氧)联用以增强降解效果[51] 操作简单,成本较低;可在原位或异位条件下实施;对土壤结构破坏小 对低渗透性土壤效果有限;苯胺蒸汽压相对较低,单独使用时处理效率有限;需配合尾气处理
    地下水
    抽出处理
    适用于地下水丰富、苯胺浓度较高、污染羽扩散明显的场地。通过抽出处理将高浓度污染地下水转移至地面,再结合化学氧化、生物处理等组合工艺进行达标处理。适用于污染源区快速水力控制及长期地下水修复 可有效控制高浓度污染羽扩散;操作成熟,技术可靠;可将污染物转移至地面集中处理 处理周期长;需配套水处理设施;对吸附态污染物去除有限
    下载: 导出CSV

    表  2  常用氧化剂与还原剂对苯胺污染场地修复适用性

    Table  2.   Applicability of common oxidants and reducing agents for remediation of aniline-contaminated sites

    氧化剂
    名称 优点 缺点 对苯胺污染场地的适用性
    高锰酸钾
    (KMnO4)
    ①氧化能力强,反应速率快
    ②成本较低,易于获取
    ③对多种有机污染物有效
    ①可能产生副产物(如MnO2沉淀),影响土壤渗透性
    ②对某些饱和烃类污染物氧化效率较低
    ③过量使用可能导致土壤酸化
    可有效氧化苯胺,反应速率与苯胺浓度呈正相关,研究表明,pH为5~6时反应速率最高[61]。酸性条件下原位生成的MnO2具有催化作用,反应遵循中间体络合物电子转移机制
    过氧化氢
    (H2O2)
    ①反应产物为水和氧气,环
    境友好
    ②反应条件温和,易于控制
    ①单独使用时氧化能力较弱,需配合催化剂
    ②高浓度H2O2存在安全隐患,运输和储存要求高
    ③对土壤有机质有一定破坏作用
    单独使用氧化能力弱,需与Fe2+或过硫酸盐联用。Fenton反应产生的羟基自由基无选择性攻击苯胺
    苯环,引发羟基化与开环反应[62]。H2O2活化过硫
    酸盐时,自由基协同效应可显著增强降解效果
    臭氧(O3) ①氧化能力强,反应速率快
    ②无二次污染,产物为氧气
    ①设备成本高,操作复杂
    ②臭氧易分解,需现场生成
    ③对土壤渗透性要求高,可能影响微生物活性
    苯胺属高臭氧反应活性物质,反应速率常数达
    106 L/(mol·s)量级[51]。臭氧通过直接氧化与间接
    氧化(羟基自由基)2条途径降解苯胺,初始产
    物为亚硝基苯和硝基苯,进一步可矿化为CO2
    过硫酸盐(如过硫酸钠,Na2S2O8) ①氧化能力强,稳定性好
    ②适用pH范围广,可在中性
    或弱碱性条件下使用
    ①活化过程可能增加成本
    ②过量使用可能导致土壤酸化或盐分积累
    过硫酸盐经活化后产生的硫酸根自由基可高效降解苯胺[62]
    还原剂
    名称 优点 缺点 对苯胺污染场地的适用性
    零价铁
    (Fe0)
    ①还原能力强,反应速率快
    ②成本低,材料易得
    ③对多种污染物有效,尤其
    是氯代有机物
    ①表面易钝化,降低长期反应效率
    ②可能产生铁氧化物沉淀,影响渗透性
    ③对某些污染物(如芳香族化合物)还原效率
    较低
    零价铁对苯胺的还原脱胺效率较低,主要适用于氯代有机物,对苯胺的去除以吸附作用为主
    亚硫酸盐
    (如Na2SO3)
    ①还原能力强,反应速率快
    ②成本较低,易于操作
    ①过量使用可能导致土壤酸化
    ②对有机污染物还原效率有限
    亚硫酸盐体系可通过活化溶解氧产生硫酸根自由基(SO4•−),有效氧化降解苯胺[63]
    硫化物
    (如Na2S)
    ①对重金属还原效果好,可
    形成难溶性硫化物沉淀
    ②对某些氯代有机物有还原
    脱氯作用
    ①可能产生硫化氢等有毒气体,需严格控制操作条件
    ②对土壤微生物活性有影响
    硫化物对苯胺无显著还原效果。相反,高浓度硫化氢对苯胺降解菌具有显著抑制作用,20 mmol/L硫化氢可完全抑制该菌的生长和苯胺降解活性[64]
    氢气
    (H2)
    ①还原产物为水,环境友好
    ②对某些污染物(如硝酸盐)
    还原效率高
    ①氢气易燃易爆,安全风险高
    ②需催化剂(如Pd、Pt),成本较高
    氢气适用于卤代苯胺类污染物的预处理[65],但对非卤代苯胺的直接还原效果有限
    下载: 导出CSV
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出版历程
  • 收稿日期:  2026-06-17
  • 录用日期:  2026-06-26
  • 修回日期:  2026-06-18
  • 网络出版日期:  2026-06-30

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