低碳源条件下改良双污泥系统脱氮除磷优化研究

在低碳源废水条件下,通过对改良后的双污泥处理工艺与传统厌氧-好氧-缺氧工艺效果进行比较分析,探究解决城市生活污水碳源不足的方法.实验组反应器为改良型双污泥系统,即在原双污泥系统缺氧段增加两个阶段的微曝气(曝气量0.5 L·min~(-1)),对照组反应器为多级厌氧-好氧-缺氧SBR.结果表明,进水COD、氨氮、SOP浓度分别为200、35、10 mg·L-1时,实验组比对照组脱氮除磷效果好(去除率分别为:TN 94.8%与60.9%;TP 96.5%与75%),出水SOP浓度0.35 mg·L-1,NH+4-N浓度0.50 mg·L-1,TN浓度1.82 mg·L-1,完全满足《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级A标准.采用优化后的工艺,单位碳源(以COD计)可实现的最大的氮、磷的去除量分别为0.17 g·g-1和0.048 g·g-1,可以最大程度地解决当前城市废水碳源浓度较低的问题.

Optimization Study on the Nitrogen and Phosphorus Removal of Modified Two-sludge System Under the Condition of Low Carbon Source

This paper explored the method of resolving insufficient carbon source in urban sewage by comparing and analyzing denitrification and phosphorus removal (NPR) effect between modified two-sludge system and traditional anaerobic-aerobic-anoxic process under the condition of low carbon source wastewater. The modified two-sludge system was the experimental reactor, which was optimized by adding two stages of micro-aeration (aeration rate 0.5 L ·min^-1) in the anoxic period of the original two-sludge system, and multi-stage anaerobic-aerobic-anoxic SBR was the control reactor. When the influent COD, ammonia nitrogen, SOP concentration were respectively 200, 35, 10 mg ·L^-1, the NPR effect of the experimental reactor was better than that of thecontrol reactor with the removal efficiency of TN being 94.8% vs 60.9%, and TP removal being 96.5% vs 75%, respectively. The effluent SOP, ammonia, TN concentration of the experimental reactor were 0.35, 0.50, 1.82 mg ·L^-1, respectively, which could fully meet the first class of A standard of the Pollutants Emission Standard of Urban Wastewater Treatment Firm (GB 18918-2002). Using the optimized treatment process, the largest amounts of nitrogen and phosphorus removal per unit carbon source (as COD) were 0.17 g ·g^-1 and 0.048 g ·g^-1 respectively, which could furthest solve the lower carbon concentration in current municipal wastewater.