Application of MABR in upgrading and reconstruction of a wastwater treatment station
WEI Aishu1,2,, NIU Xiaojun3,4,, 1.Beijing Capital Co. Ltd., Beijing 100144, China 2.Beijing Branch of Shouchuangaihua Tianjin Municipal & Environment Engineering Co. Ltd., Beijing 100144, China 3.College of Environment and Energy, South China University of Technology, Guangzhou 510006, China 4.Key Laboratory of Pollution Control and Ecosystem Restoration in Industry Clusters, Ministry of Education, Guangzhou 510006, China
Abstract:MABR membrane aeration biofilm reactor process was adopted for the reconstruction of a sewage treatment station in North China. MABR membrane components were added to the original CAST process and a new secondary sedimentation tank was built to reconstruct the original biochemical system. In the meanwhile, an advanced treatment system with new high-density tanks and V-shaped filters were built to ensure the quality of the final effluent. In the establishment of the MABR membrane aeration biofilm reactor process, only new aeration membrane components were added and no new equipment and civil works were needed in the original biochemical tank. No new blowers were needed due to the high aeration efficiency and low energy consumption of the biofilm system. The one-off investment is about 850 yuan·m?3 and the reconstruction period was about 15 days, indicating its advantages of short reconstruction period and low operational cost. For the new membrane aeration biofilm reactor process, the mean value of ammonia nitrogen in the inflow was 39 mg·L?1 and its mean value in the effluent was 3 mg·L?1, i.e. the average removal rate was 92%. The mean value of total nitrogen (TN) in the inflow was 63 mg·L?1 and the mean value in the effluent was 11 mg·L?1, making an average removal rate of 83%. The mean value of total phosphorus (TP) in the inflow was 7.5 mg·L?1 and the mean value in the effluent was 0.9 mg·L?1, thus the average removal rate was 88%. The TP concentration in the effluent could be kept below 0.4 mg·L?1 by chemical phosphorus removal by the follow-up advanced treatment section. The mean value of COD in the inflow was 367 mg·L?1 and the mean value of effluent was 35 mg·L?1, i.e. the average removal rate was 90%. After the reconstruction of the treatment process, the effluent quality of the sewage treatment station stably reached the Class 1A level of tHe Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant (GB 18918-2002). Key words:MABR/ membrane aeration/ biofilm/ high ammonia nitrogen/ upgrade and reconstruction.
图1MABR主工艺单元改造示意图 Figure1.Schematic diagram of the MABR main process reconstruction
1.Beijing Capital Co. Ltd., Beijing 100144, China 2.Beijing Branch of Shouchuangaihua Tianjin Municipal & Environment Engineering Co. Ltd., Beijing 100144, China 3.College of Environment and Energy, South China University of Technology, Guangzhou 510006, China 4.Key Laboratory of Pollution Control and Ecosystem Restoration in Industry Clusters, Ministry of Education, Guangzhou 510006, China Received Date: 2020-08-11 Accepted Date: 2021-01-29 Available Online: 2021-06-25 Keywords:MABR/ membrane aeration/ biofilm/ high ammonia nitrogen/ upgrade and reconstruction Abstract:MABR membrane aeration biofilm reactor process was adopted for the reconstruction of a sewage treatment station in North China. MABR membrane components were added to the original CAST process and a new secondary sedimentation tank was built to reconstruct the original biochemical system. In the meanwhile, an advanced treatment system with new high-density tanks and V-shaped filters were built to ensure the quality of the final effluent. In the establishment of the MABR membrane aeration biofilm reactor process, only new aeration membrane components were added and no new equipment and civil works were needed in the original biochemical tank. No new blowers were needed due to the high aeration efficiency and low energy consumption of the biofilm system. The one-off investment is about 850 yuan·m?3 and the reconstruction period was about 15 days, indicating its advantages of short reconstruction period and low operational cost. For the new membrane aeration biofilm reactor process, the mean value of ammonia nitrogen in the inflow was 39 mg·L?1 and its mean value in the effluent was 3 mg·L?1, i.e. the average removal rate was 92%. The mean value of total nitrogen (TN) in the inflow was 63 mg·L?1 and the mean value in the effluent was 11 mg·L?1, making an average removal rate of 83%. The mean value of total phosphorus (TP) in the inflow was 7.5 mg·L?1 and the mean value in the effluent was 0.9 mg·L?1, thus the average removal rate was 88%. The TP concentration in the effluent could be kept below 0.4 mg·L?1 by chemical phosphorus removal by the follow-up advanced treatment section. The mean value of COD in the inflow was 367 mg·L?1 and the mean value of effluent was 35 mg·L?1, i.e. the average removal rate was 90%. After the reconstruction of the treatment process, the effluent quality of the sewage treatment station stably reached the Class 1A level of tHe Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant (GB 18918-2002).
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