Ma Cui, Ma Panfeng, He Zhengguang, Mi Xiao
School of Environmental and Municipal Engineering, North China University of Water Resources and Electric Power, Zhengzhou 450046, China.
School of Ecology and Environment, Zhengzhou University, Zhengzhou 450001, China.
Toxics. 2022 Aug 28;10(9):505. doi: 10.3390/toxics10090505.
The mature landfill leachate (MLL) is characterized by a large number of fulvic acids and humic acids, which is refractory organic matter and can be cleaned by ozone oxidation. However, the poor property of mass transfer prohibits the widespread use of ozone oxidation in actual leachate treatment. Meanwhile, some combined processes are adopted to treat the mature landfill leachate, which places catalytic ozonation before the membrane bioreactor (MBR) process to enhance the biodegradability of MLL. Thus, this research is conducted to investigate the practicability of applying nano-FeO loaded cow-dung ash (FeO@CDA) and biological post-treatment with MBR for the effective removal of pollutants from MLL and puts forward the variation of organics in leachate between catalytic ozonation and MBR. The addition of catalytic ozonation not only improved the removal of hazardous organics but also enhanced the biodegradability of the leachate and favored the subsequent MBR process. Chemical oxygen demand (COD) removal in the catalytic ozonation step was optimized, and 53% removal was obtained at pH = 7, catalyst dosage = 1.0 g/L, and O dosage = 3.0 g/L. After the MBR process, COD in effluent stabilized in the range of 57.85-65.38 mg/L, and the variation range of the ammonia nitrogen (NH-N) concentration was 5.98-10.24 mg/L. The catalytic ozonation-MBR integrated process showed strong feasibility in dealing with the biologically pre-treated leachate.
成熟垃圾渗滤液(MLL)的特点是含有大量富里酸和腐殖酸,这些都是难降解有机物,可通过臭氧氧化进行净化。然而,传质性能较差阻碍了臭氧氧化在实际渗滤液处理中的广泛应用。同时,一些联合工艺被用于处理成熟垃圾渗滤液,即将催化臭氧化置于膜生物反应器(MBR)工艺之前,以提高MLL的生物降解性。因此,本研究旨在探讨应用负载纳米FeO的牛粪灰(FeO@CDA)和MBR进行生物后处理以有效去除MLL中污染物的可行性,并提出催化臭氧化和MBR之间渗滤液中有机物的变化情况。催化臭氧化的加入不仅提高了有害有机物的去除率,还增强了渗滤液的生物降解性,有利于后续的MBR工艺。优化了催化臭氧化步骤中化学需氧量(COD)的去除效果,在pH = 7、催化剂用量 = 1.0 g/L和臭氧用量 = 3.0 g/L时,去除率达到53%。经过MBR工艺后,出水COD稳定在57.85 - 65.38 mg/L范围内,氨氮(NH-N)浓度的变化范围为5.98 - 10.24 mg/L。催化臭氧化 - MBR集成工艺在处理经过生物预处理的渗滤液方面显示出很强的可行性。