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添加碳源对潜流+表面流组合湿地脱氮除磷的影响
摘要点击 1910  全文点击 1528  投稿时间:2006-06-12  修订日期:2006-09-21
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中文关键词  表面流湿地  潜流湿地  脱氮除磷  碳源
英文关键词  free water surface wetland  subsurface flow wetland  nitrogen and phosphorus removal  carbon source
作者单位
谭洪新 上海水产大学生命科学与技术学院,上海200090 
刘艳红 上海水产大学生命科学与技术学院,上海200090 
周琪 同济大学环境科学与工程学院,上海200092 
杨殿海 同济大学环境科学与工程学院,上海200092 
中文摘要
      采用向ANOXIC-OXIC(A/O)工艺出水中添加城市污水的方法,在中试规模上研究了外加碳源对潜流+表面流组合湿地脱氮除磷的影响.结果表明,直接处理A/O工艺出水时(工况Ⅰ),湿地进水COD/TN仅为1.00,(NO-2+NO-3)/TN为0.48,COD、TN和TP的面积负荷去除率分别为1.82、1.59、0.14 g·(m2·d)-1.A/O工艺出水中添加少量城市污水后(工况Ⅱ),湿地进水COD/TN为3.55,(NO-2+NO-3)/TN为0.44,COD、TN和TP的面积负荷去除率分别为19.03、5.42、0.29 g·(m2·d)-1.工况Ⅱ的TN和TP面积负荷去除率分别比工况Ⅰ提高了3.4倍和2.1倍.HRT、水温、(NO-2+NO-3)/TN和COD/TN对湿地脱氮除磷效能有显著影响,在HRT为0.5~1.0d, COD、TN和TP的面积负荷率分别为3.8~38.7、5.07~13.08、0.57~1.92 g·(m2·d)-1时, TN面积负荷去除率随HRT增加而指数下降,随水温和(NO-2+NO-3)/TN的升高而线性增加,随COD/TN的增加呈幂函数增加.TP面积负荷去除率随COD/TN的增加呈幂函数增加.
英文摘要
      By adding municipal wastewater in effluent of ANOXIC-OXIC (A/O) reactor as external carbon source, effects of external carbon source on nitrogen and phosphorus removal in subsurface flow and free water surface integrated constructed wetland were studied in pilot-scale. Results indicate that, COD/TN and (NO-2+NO-3)/TN in influent of wetland are 1.00 and 0.48, respectively, and load removal rates of COD, TN and TP are 1.82, 1.59 and 0.14 g·(m2·d)-1, respectively, as directly treating effluent of A/O reactor in wetland (working conditionⅠ). COD/TN and (NO-2+NO-3)/TN in influent of wetland are 3.55 and 0.44, respectively, and load removal rates of COD, TN and TP are 19.03, 5.42 and 0.29 g·(m2·d)-1, respectively, as adding municipal wastewater in effluent of A/O reactor as external carbon source in wetland (working conditionⅡ). Compared with working conditionⅠ, load removal rates of TN and TP for working condition Ⅱ increase 3.4 times and 2.1 times, respectively. Impact factors of load removal rate of TN and TP are water temperature, HRT, COD/TN and (NO-2+NO-3)/TN, respectively, when ranges of influent load rates are 3.8~38.7 g·(m2·d)-1 for COD, 5.07~13.08 g·(m2·d)-1 for TN and 0.57~1.92 g·(m2·d)-1 for TP, respectively, and range of HRT is 0.5~1.0 d. TN load removal rate decreases by exponent function along with increase of HRT, linearly increases along with increase of water temperature and (NO-2+NO-3)/TN, and increases by power function along with increase of COD/TN. TP load removal rate also increases by power function along with increase of COD/TN.

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