造纸
废水
制浆造纸工业
流出物
曝气
化学需氧量
序批式反应器
移动床生物膜反应器
化学
水力停留时间
污水处理
间歇式反应器
生物量(生态学)
旋转生物接触器
氮气
生物反应器
环境科学
废物管理
响应面法
批处理
生物膜
动力学
生化需氧量
氨
污水
化学工程
厌氧氨氧化菌
环境工程
降级(电信)
作者
J. Peng,Yi Hou,Xiaoming Liu,Lirong Lei
标识
DOI:10.1515/npprj-2024-0069
摘要
Abstract This study evaluated the use of three Sequencing Batch Moving Bed Biofilm Reactors (SBMBBR) with Mutag biochip 30™ (MB) carriers for treating regenerated papermaking wastewater. The reactors operated at filling ratios of 15 % (MB15), 30 % (MB30), and 45 % (MB45). Biomass stabilized after 30 days, reaching 2.26 g/L, 4.01 g/L, and 5.58 g/L, respectively. The process parameters of the reactors were optimized using Response Surface Methodology (RSM). Under conditions of a C/N ratio of 21:1, an aeration rate (AR) of 2.65 L/min, a hydraulic retention time (HRT) of 9 h, and a 45 % filling ratio, the chemical oxygen demand (COD) removal efficiency of the wastewater achieved the highest value of 68.28 ± 2.03 %, with the average effluent COD reduced to approximately 170 mg/L while ammonia nitrogen and total nitrogen were below 10 mg/L and 15 mg/L, meeting the discharge standards for recycled paper mill wastewater in China. Kinetic analysis using an improved Stover-Kincannon model showed good fitting (R 2 > 0.93) and the highest degradation rate (U max ) of 2.6413 g/Lday in the MB45 reactor. These results support SBMBBR’s potential for treating papermaking wastewater and addressing challenges in other industrial wastewater treatments.
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