Since September 2011,A 2/O-MBR wastewater treatment plant in Xi'an Siyuan University has been successfully running without replacing any of membrane modules.A total of 6.661 million m^3 of campus wastewater has be...Since September 2011,A 2/O-MBR wastewater treatment plant in Xi'an Siyuan University has been successfully running without replacing any of membrane modules.A total of 6.661 million m^3 of campus wastewater has been treated,and 4.405 million m^3 of water reaching the national urban miscellaneous water standard has been reclaimed and reused.A total of 25 km pipeline,5 pits,scenery fountains,lakes,and 12 pump stations have been constructed for flushing toilets,irrigating green grass lawn and afforest,and cleaning hardened pavement.The design and construction of 5 pits,scenery fountains,and lakes are important to meet the national urban miscellaneous water standard under occasional phosphorus and/or nitrogen exceed concentration.The unit water cost is 4.19 yuan/m^3,including membrane modules depreciation and amortization.After the A 2/O-MBR system passes the membrane modules depreciation and amortization period,the unit water cost is 2.82 yuan/m^3.The water productivity of the membrane stack rises first at the beginning of operation,reaches the maximum value,and then decreases.The average annual transmembrane pressure difference increases by 1.12 kPa.The average VMD of industrial permeability decreases annually by 0.45 m^3.展开更多
能耗是再生水厂运行主要的考核指标.采用比能耗分析法、单元能耗分析法以及冗余分析法等探讨了清河再生水厂不同污水处理工艺(倒置A2/O、A2/O和A2/O-MBR)的能耗构成和时空分布特征.重点考察了A2/O-MBR工艺的主要能耗环节和原因,探讨了A2...能耗是再生水厂运行主要的考核指标.采用比能耗分析法、单元能耗分析法以及冗余分析法等探讨了清河再生水厂不同污水处理工艺(倒置A2/O、A2/O和A2/O-MBR)的能耗构成和时空分布特征.重点考察了A2/O-MBR工艺的主要能耗环节和原因,探讨了A2/O-MBR工艺的节能改造方法,并比较了其改造前后的能耗.结果表明,曝气是清河再生水厂污水处理的常规工艺和A2/O-MBR工艺的主要耗能需求,分别占总能耗的42.97%和50.65%.在保证A2/O-MBR工艺出水水质的同时,采用脉冲曝气改造后节能效果明显.改造后的膜运行通量增大约20%,吨水能耗为0.53 k W·h·t-1,降幅达42.39%,去除单位COD能耗为1.29 k W·h·kg-1,降幅达54.74%.该厂A2/O-MBR工艺回流量大,但与出水水质相关性较弱.在一定范围内降低回流比不会造成出水水质恶化,因此可作为进一步节能的方向之一.展开更多
文摘Since September 2011,A 2/O-MBR wastewater treatment plant in Xi'an Siyuan University has been successfully running without replacing any of membrane modules.A total of 6.661 million m^3 of campus wastewater has been treated,and 4.405 million m^3 of water reaching the national urban miscellaneous water standard has been reclaimed and reused.A total of 25 km pipeline,5 pits,scenery fountains,lakes,and 12 pump stations have been constructed for flushing toilets,irrigating green grass lawn and afforest,and cleaning hardened pavement.The design and construction of 5 pits,scenery fountains,and lakes are important to meet the national urban miscellaneous water standard under occasional phosphorus and/or nitrogen exceed concentration.The unit water cost is 4.19 yuan/m^3,including membrane modules depreciation and amortization.After the A 2/O-MBR system passes the membrane modules depreciation and amortization period,the unit water cost is 2.82 yuan/m^3.The water productivity of the membrane stack rises first at the beginning of operation,reaches the maximum value,and then decreases.The average annual transmembrane pressure difference increases by 1.12 kPa.The average VMD of industrial permeability decreases annually by 0.45 m^3.
文摘能耗是再生水厂运行主要的考核指标.采用比能耗分析法、单元能耗分析法以及冗余分析法等探讨了清河再生水厂不同污水处理工艺(倒置A2/O、A2/O和A2/O-MBR)的能耗构成和时空分布特征.重点考察了A2/O-MBR工艺的主要能耗环节和原因,探讨了A2/O-MBR工艺的节能改造方法,并比较了其改造前后的能耗.结果表明,曝气是清河再生水厂污水处理的常规工艺和A2/O-MBR工艺的主要耗能需求,分别占总能耗的42.97%和50.65%.在保证A2/O-MBR工艺出水水质的同时,采用脉冲曝气改造后节能效果明显.改造后的膜运行通量增大约20%,吨水能耗为0.53 k W·h·t-1,降幅达42.39%,去除单位COD能耗为1.29 k W·h·kg-1,降幅达54.74%.该厂A2/O-MBR工艺回流量大,但与出水水质相关性较弱.在一定范围内降低回流比不会造成出水水质恶化,因此可作为进一步节能的方向之一.
