检索规则说明:AND代表“并且”;OR代表“或者”;NOT代表“不包含”;(注意必须大写,运算符两边需空一格)
检 索 范 例 :范例一: (K=图书馆学 OR K=情报学) AND A=范并思 范例二:J=计算机应用与软件 AND (U=C++ OR U=Basic) NOT M=Visual
作 者:周元[1,2] 金腊华[1,2] 张一凡[1,2] 黄志伟[1,2]
机构地区:[1]暨南大学环境学院,广州510632 [2]广东省高校水土环境毒害性污染物防治与生物修复重点实验室,广州510632
出 处:《环境工程学报》2015年第8期3739-3744,共6页Chinese Journal of Environmental Engineering
基 金:东莞市高校科研机构科技计划项目(2012108101002)
摘 要:为了提高污水脱氮效果,在传统A2O工艺的基础上,增加后置缺氧段并与膜生物反应器相结合,构建了AAOA-MBR污水处理中试装置,进行了中试实验.实验结果表明,在进水COD浓度为100.00 ~ 280.00 mg/L、TN浓度为18.32 ~31.86 mg/L、NH4+-N浓度为12.78~24.44 mg/L时,COD、TN和NH4+-N的平均去除率分别达到了90.0%、72.1%和99.0%,出水水质达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)中的一级A标准;通过多点进水优化了内源配置,节约了碳源,强化了脱氮效果;采用膜池回流供氧,可在节能的同时保证缺氧池1的缺氧环境,提高了反硝化效果.本文的研究成果为实际污水处理工程市场提供了一套高效脱氮的新工艺.In order to improve the effect of nitrogen removal from sewage, a rear anoxic pond was added af- ter a traditional A20 process, and followed by MBR, which constructed a pilot sewage treatment device with AAOA-MBR technology. Pilot experiments was accomplished with the device. The experimental results showed that when the influent concentrations of COD, TN, NH4+ -N were 100.00 to 280.00 mg/L , 18.32 to 31.86 mg/ L, 12.78 to 24.44 mg/L, respectively, the average removal rates of COD, TN and NH4-N were 90.0% , 72.1% and 99.0% , the effluent quality met the first level A criteria specified in Discharge Standard of Pollu- tants for Municipal Wastewater Treatment Plant (GB 18918-2002 ). Through step feeding, inner carbon configu- ration can be optimized, and carbon source can be partially saved, and the effect of nitrogen removal can be im- proved. By backflow from MBR, oxygen can be provided to oxidation pond, which can decrease aeration quantity for saving energy and ensure anoxic pond in hypoxia environment for increasing denitrifieation effect. The experi- ment results may provide a new technology for nitrogen removal in actual practice.
关 键 词:AAOA-MBR 工艺 脱氮 多点进水 膜池回流供氧
分 类 号:X703.1[环境科学与工程—环境工程]
正在载入数据...
正在载入数据...
正在载入数据...
正在载入数据...
正在载入数据...
正在载入数据...
正在载入数据...
正在链接到云南高校图书馆文献保障联盟下载...
云南高校图书馆联盟文献共享服务平台 版权所有©
您的IP:216.73.216.118