Tan Hong-Xin, Liu Yan-Hong, Zhou Qi, Yang Dian-Hai
College of Life Science and Technology, Shanghai Fisheries University, Shanghai 200090, China.
Huan Jing Ke Xue. 2007 Jun;28(6):1209-15.
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 (NO2(-) + NO3(-))/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 x d)(-1), respectively, as directly treating effluent of A/O reactor in wetland (working condition I). COD/TN and (NO2(-) + NO3(-))/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 x d)(-1), respectively, as adding municipal wastewater in effluent of A/O reactor as external carbon source in wetland (working condition II). Compared with working condition I, 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 (NO2(-) + NO3(-))/TN, respectively, when ranges of influent load rates are 3.8 - 38.7 g x (m2 x d)(-1) for COD, 5.07 - 13.08 g x (m2 x d)(-1) for TN and 0.57 - 1.92 g x (m2 x 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 (NO2(-) + NO3(-))/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.
通过在缺氧-好氧(A/O)反应器出水中添加城市污水作为外部碳源,在中试规模下研究了外部碳源对潜流和自由水面复合人工湿地脱氮除磷效果的影响。结果表明,在湿地直接处理A/O反应器出水时(工况I),湿地进水的COD/TN和(NO2- + NO3-)/TN分别为1.00和0.48,COD、TN和TP的负荷去除率分别为1.82、1.59和0.14 g/(m2·d)-1。在湿地中向A/O反应器出水中添加城市污水作为外部碳源时(工况II),湿地进水的COD/TN和(NO2- + NO3-)/TN分别为3.55和0.44,COD、TN和TP的负荷去除率分别为19.03、5.42和0.29 g/(m2·d)-1。与工况I相比,工况II的TN和TP负荷去除率分别提高了3.4倍和2.1倍。当进水负荷率范围分别为:COD为3.8 - 38.7 g/(m2·d)、TN为5.07 - 13.08 g/(m2·d)、TP为0.57 - 1.92 g/(m2·d),水力停留时间(HRT)范围为0.5 - 1.0 d时,TN负荷去除率的影响因素分别是水温、HRT、COD/TN和(NO2- + NO3-)/TN。TN负荷去除率随HRT的增加呈指数函数下降,随水温及(NO2- + NO3-)/TN的增加呈线性增加,随COD/TN的增加呈幂函数增加。TP负荷去除率也随COD/TN的增加呈幂函数增加。