Ecology and Environment ›› 2025, Vol. 34 ›› Issue (4): 653-664.DOI: 10.16258/j.cnki.1674-5906.2025.04.014
• Review • Previous Articles
WANG Longfei1,2(), ZHANG Jiaojiao1,2, WANG Ziyi1,2, CHEN Yudong3, LI Yi1,2,*(
)
Received:
2024-09-30
Online:
2025-04-18
Published:
2025-04-24
Contact:
LI Yi
王龙飞1,2(), 张皎皎1,2, 王子怡1,2, 陈玉东3, 李轶1,2,*(
)
通讯作者:
李轶
作者简介:
王龙飞(1988年生),男,副教授,博士,主要从事水污染控制和水生态修复方面的研究。E-mail: lfwang@hhu.edu.cn
基金资助:
CLC Number:
WANG Longfei, ZHANG Jiaojiao, WANG Ziyi, CHEN Yudong, LI Yi. Innovation and Practice of Biofilm-based Technology in the Ecological Restoration of Aquatic Systems[J]. Ecology and Environment, 2025, 34(4): 653-664.
王龙飞, 张皎皎, 王子怡, 陈玉东, 李轶. 生物膜技术在河湖生态修复中的创新与实践[J]. 生态环境学报, 2025, 34(4): 653-664.
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URL: https://www.jeesci.com/EN/10.16258/j.cnki.1674-5906.2025.04.014
水环境类型 | 适用技术 | 处理方式 | 重点关注污染物 | 修复机理 | 存在问题 | 文献 | |
---|---|---|---|---|---|---|---|
不同 水质条件水体 | 富营养化水体 | 生态水草,如阿科蔓生态基 | 原位处理 | BOD、TSS、氮磷 | 比表面积大有利于大量微生物附着,纤维孔状结构使得它能够创造较理想的好氧、兼性和厌氧环境 | 成本较高,只适合微污染水体,优势微生物菌群不明显 | Tang et al., |
污染程度较高、自净能力不足的河道 | 人工填料接触氧化法 | 原位处理 | 氨氮、铁、锰和有机物 | 以人工合成材料为填料,通过填料上生物膜中微生物生化过程实现污染水体净化 | 填料及支架成本较高、负荷过高时会导致生物膜过厚引起填料堵塞 | 杨林, | |
微污染水体 | 砾间接触氧化法 | 原位处理 | BOD、SS | 以填充砾石作为载体,砾石表面带电吸附有机物从而被生物膜上的微生物分解 | 需要预处理大的悬浮物,对TN、TP去除率不高 | 李应辉, | |
污染较轻、对人工干预较为敏感的水体 | 伏流净化法 | 原位处理 | 有机污染物、悬浮颗粒物 | 利用河床向地下的渗透作用和伏流水的稀释作用来净化河流 | 考虑采用伏流净化法时,需要对必要取水量、河床伏流量充分调查和论证 | 郭芳等, | |
低碳氮比水体 | 菌藻生物膜 | 原位处理 | 氮磷、矿物质、脂质 | 通过微生物与藻类之间的协同作用实现污染物的去除 | 菌藻生物量易流失、污染物降解速率低、微藻光能利用率低 | Wei et al., | |
不同水动力条件水体 | 完全截污河湖的水质净化、不完全截污黑臭水体修复 | 膜曝气生物膜反应器(MABR) | 流速缓慢时适合于原位处理;流速过快时可采用旁路处理 | 氮磷、COD | 以中空纤维曝气膜作为载体并同步曝气,污染物在浓差驱动和微生物吸附等作用下被生物膜上微生物利用 | 实验条件要求严苛;对气相压力、液相流速要求很高 | Zhong et al., |
富营养化缓流水体 | 太阳能悬浮曝气生物膜反应器 | 原位处理 | COD、氨氮、TN、TP | 依靠填料的吸附、拦截、生物膜表面净化作用,辅以强化曝气及人工推流净化水体,太阳能供能 | 对溶解氧的提高作用效果不显著、夏季净化效果好但冬季净化效果一般 | Zhang et al., |
Table 1 Overview of applicable biofilm-based techniques in representative river and lake water bodies
水环境类型 | 适用技术 | 处理方式 | 重点关注污染物 | 修复机理 | 存在问题 | 文献 | |
---|---|---|---|---|---|---|---|
不同 水质条件水体 | 富营养化水体 | 生态水草,如阿科蔓生态基 | 原位处理 | BOD、TSS、氮磷 | 比表面积大有利于大量微生物附着,纤维孔状结构使得它能够创造较理想的好氧、兼性和厌氧环境 | 成本较高,只适合微污染水体,优势微生物菌群不明显 | Tang et al., |
污染程度较高、自净能力不足的河道 | 人工填料接触氧化法 | 原位处理 | 氨氮、铁、锰和有机物 | 以人工合成材料为填料,通过填料上生物膜中微生物生化过程实现污染水体净化 | 填料及支架成本较高、负荷过高时会导致生物膜过厚引起填料堵塞 | 杨林, | |
微污染水体 | 砾间接触氧化法 | 原位处理 | BOD、SS | 以填充砾石作为载体,砾石表面带电吸附有机物从而被生物膜上的微生物分解 | 需要预处理大的悬浮物,对TN、TP去除率不高 | 李应辉, | |
污染较轻、对人工干预较为敏感的水体 | 伏流净化法 | 原位处理 | 有机污染物、悬浮颗粒物 | 利用河床向地下的渗透作用和伏流水的稀释作用来净化河流 | 考虑采用伏流净化法时,需要对必要取水量、河床伏流量充分调查和论证 | 郭芳等, | |
低碳氮比水体 | 菌藻生物膜 | 原位处理 | 氮磷、矿物质、脂质 | 通过微生物与藻类之间的协同作用实现污染物的去除 | 菌藻生物量易流失、污染物降解速率低、微藻光能利用率低 | Wei et al., | |
不同水动力条件水体 | 完全截污河湖的水质净化、不完全截污黑臭水体修复 | 膜曝气生物膜反应器(MABR) | 流速缓慢时适合于原位处理;流速过快时可采用旁路处理 | 氮磷、COD | 以中空纤维曝气膜作为载体并同步曝气,污染物在浓差驱动和微生物吸附等作用下被生物膜上微生物利用 | 实验条件要求严苛;对气相压力、液相流速要求很高 | Zhong et al., |
富营养化缓流水体 | 太阳能悬浮曝气生物膜反应器 | 原位处理 | COD、氨氮、TN、TP | 依靠填料的吸附、拦截、生物膜表面净化作用,辅以强化曝气及人工推流净化水体,太阳能供能 | 对溶解氧的提高作用效果不显著、夏季净化效果好但冬季净化效果一般 | Zhang et al., |
时间 | 治理对象 | 治理方法 | 治理成果 | 文献 |
---|---|---|---|---|
2002 | 上海苏州河支流 木渎港河段 | 原位悬浮填料移动床生物膜反应器 | 经过1个月治理,CODCr、BOD5的去除率分别达到52.3%和58.3% | 王学江等, |
2005 | 宁波月湖 | 基于人工水草的菌藻生物膜技术 | 经6个月治理,水体透明度提高,CODMn、TP、TN和NH4+-N的削减率分别达到93%、49%、95%和70% | 吴永红等, |
2006 | 太湖入湖河道宜兴市 大浦镇林庄港 | 基于轮藻仿生填料的生物接触氧化法 | 经过6个月治理,进水水质均在地表水环境质量标准中的Ⅲ类以内,氨氮净去除率的范围在5%-40%之间 | 田伟君等, |
2015 | 南宁市朝阳溪 黑臭河水 | 基于碳素纤维载体的生态基技术 | 24 h内,浊度由原来的47.32 NTU降低为13.78 NTU;10 d后无曝气情况下,COD、TP、NH3-N和TN去除率分别达到76%、54%、91%和55% | 梁益聪等, |
2020 | 合肥市匡河 | 原位强化耦合生物膜反应器EHBR | 经过1个月治理,出水水质基本达到Ⅳ类水体指标,出水COD、氨氮平均去除率分别为15%、46% | 李曼等, |
2022 | 天津马厂减河 | 原位膜曝气生物反应器(Membrane -Aerated Biofilm Reactor,简称MABR)与微纳米曝气技术组合技术 | 24周后,COD、NH3-N、TP的去除率分别达到47%、44%、14%,DO增加32%;水质达到地表水环境质量Ⅴ类标准 | 梁静波等, |
2023 | 苏州科技大学石湖 校区九曲桥 | 原位生物蜡技术 | COD、氨氮、TN、TP、叶绿素a均值分别降低24%、42%、47%、23%、18%,透明度提高24% | 吕凌霄等, |
Table 2 A brief introduction to the application of biofilm-based technology in river-lake restoration in China
时间 | 治理对象 | 治理方法 | 治理成果 | 文献 |
---|---|---|---|---|
2002 | 上海苏州河支流 木渎港河段 | 原位悬浮填料移动床生物膜反应器 | 经过1个月治理,CODCr、BOD5的去除率分别达到52.3%和58.3% | 王学江等, |
2005 | 宁波月湖 | 基于人工水草的菌藻生物膜技术 | 经6个月治理,水体透明度提高,CODMn、TP、TN和NH4+-N的削减率分别达到93%、49%、95%和70% | 吴永红等, |
2006 | 太湖入湖河道宜兴市 大浦镇林庄港 | 基于轮藻仿生填料的生物接触氧化法 | 经过6个月治理,进水水质均在地表水环境质量标准中的Ⅲ类以内,氨氮净去除率的范围在5%-40%之间 | 田伟君等, |
2015 | 南宁市朝阳溪 黑臭河水 | 基于碳素纤维载体的生态基技术 | 24 h内,浊度由原来的47.32 NTU降低为13.78 NTU;10 d后无曝气情况下,COD、TP、NH3-N和TN去除率分别达到76%、54%、91%和55% | 梁益聪等, |
2020 | 合肥市匡河 | 原位强化耦合生物膜反应器EHBR | 经过1个月治理,出水水质基本达到Ⅳ类水体指标,出水COD、氨氮平均去除率分别为15%、46% | 李曼等, |
2022 | 天津马厂减河 | 原位膜曝气生物反应器(Membrane -Aerated Biofilm Reactor,简称MABR)与微纳米曝气技术组合技术 | 24周后,COD、NH3-N、TP的去除率分别达到47%、44%、14%,DO增加32%;水质达到地表水环境质量Ⅴ类标准 | 梁静波等, |
2023 | 苏州科技大学石湖 校区九曲桥 | 原位生物蜡技术 | COD、氨氮、TN、TP、叶绿素a均值分别降低24%、42%、47%、23%、18%,透明度提高24% | 吕凌霄等, |
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