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3DBER-S-Fe同步脱氮除磷及去除邻苯二甲酸酯的工艺特性
摘要点击 2004  全文点击 677  投稿时间:2016-04-09  修订日期:2016-05-28
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中文关键词  再生水  三维电极生物膜  水力停留时间  邻苯二甲酸酯  脱氮除磷
英文关键词  reclaimed water  three-dimensional biofilm-electrode  hydraulic retention time  phthalate esters (PAEs)  nitrogen and phosphorus removal
作者单位E-mail
张娅 北京工业大学北京市水质科学与水环境恢复工程重点实验室, 北京 100124 amyzhang_1990@163.com 
郝瑞霞 北京工业大学北京市水质科学与水环境恢复工程重点实验室, 北京 100124 haoruixia@bjut.edu.cn 
徐鹏程 北京工业大学北京市水质科学与水环境恢复工程重点实验室, 北京 100124  
徐忠强 北京工业大学北京市水质科学与水环境恢复工程重点实验室, 北京 100124  
中文摘要
      为探究三维电极生物膜耦合硫铁新工艺(3DBER-S-Fe)脱氮除磷并同步去除邻苯二甲酸酯(PAEs)的工艺特性,在水力停留时间(HRT)分别为8、6、4 h条件下,研究分析了系统内总氮(TN)、总磷(TP)、邻苯二甲酸二丁酯(DBP)、邻苯二甲酸二(2-乙基)己酯(DEHP)、NO3--N、SO42-及pH的变化情况.结果表明,3DBER-S-Fe系统具有较好的脱氮除磷及PAEs去除效果.当水力停留时间为8、6、4 h时,TN去除率分别为80.99%、78.85%、64.76%;TP去除率分别为65.18%、67.17%、43.44%;DBP去除率分别为96.72%、97.32%、96.53%;DEHP去除率分别为91.89%、81.57%、74.30%.在3DBER-S-Fe系统内,存在异养、氢自养、硫自养反硝化脱氮过程,当HRT由8h缩短到4h时,单质硫可以弥补进水NO3--N负荷增加所导致的反硝化电子供体相对不足问题,维持系统高效的脱氮效率;系统中海绵铁填料腐蚀产生的铁离子能够高效持续沉淀除磷;3DBER-S-Fe工艺结合了物理吸附、生物降解及电化学作用,使其在不同HRT条件下具有较高的DBP与DEHP去除率.
英文摘要
      In order to explore the technological characteristics of the simultaneous removal of phthalate esters (PAEs) as well as nitrogen and phosphorus by the novel technology of three-dimensional biofilm-electrode coupled with iron/sulfur reactor (3DBER-S-Fe), the changes of the total nitrogen (TN),total phosphorus (TP),DBP,DEHP,NO3--N, SO42- and pH value were analyzed under the hydraulic retention time (HRT) of 8 h, 6 h and 4 h respectively. The results showed that 3DBER-S-Fe could remove nitrogen, phosphorus and PAEs effectively. Under the HRT of 8 h, 6 h and 4 h, the removal rates of TN were 80.99%, 78.85% and 64.76%; TP were 65.18%, 67.17% and 43.44%; DBP were 96.72%, 97.32% and 96.53%; DEHP were 91.89%, 81.57% and 74.30%, respectively. There were heterotrophic denitrification, hydrogen autotrophic denitrification and sulfur autotrophic denitrification processes in the 3DBER-S-Fe, the elemental sulfur could compensate for the relative shortage of denitrification electron donor caused by the increase of NO3--N load in the influent as a result of maintaining a high efficiency of the denitrification system when the HRT was shortened from 8h to 4h; the iron ions produced by the corrosion of the sponge iron filler in the system had a sustainable and efficient function of removing phosphorus by precipitation; the 3DBER-S-Fe process combined the interactions of physical adsorption, biological degradation and electrochemical processes which supported its high removal rates of DBP and DEHP under the different HRT conditions.

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