电极-SBBR对集中型沼液的脱氮除铜研究

    Synchronous removal of nitrogen and copper from biogas slurry by electrode-SBBR

    • 摘要: 为了处理集中型沼液中过高的氨氮和由饲料添加剂带入的铜,将电极生物膜法与序批式生物膜反应器(SBBR)工艺的优势进行互补,构建电极-SBBR耦合新工艺,以同时去除氮与铜。通过实验室配水与沼液试验,探讨了电极-SBBR体系同步脱氮除铜的工艺参数及其效果。结果表明,集中型沼液电极-SBBR体系的操作工序为:进水→厌氧→曝气→缺氧/厌氧→出水→闲置,运行参数为:水力停留时间7.0 h,厌氧0.5 h、曝气4.0 h、缺氧/厌氧2.5 h;电流30~60 mA,溶解氧(DO)4.0~5.0 mg/L,碳氮比(C/N)>10.0。电极-SBBR体系对沼液中全氮(TN)、Cu2+、化学耗氧量(COD)的去除率分别达到45.79%、86.53%和84.86%,可以作为沼液脱氮除铜的新工艺。

       

      Abstract: For consideration of excessive ammonia nitrogen (NH4+-N) in concentrated biogas slurry, and copper (Cu2+) caused by additions of feed additives, a new system of electrode-sequencing batch biofilm reactor (SBBR) technique was constructed for simultaneously removing the NH4+-N and copper in concentrated biogas slurry, through integrating the advantages of two methods including electrode-biofilm and SBBR. Meanwhile, through simulated wastewater and biogas slurry, the both of pertinent parameters and effects of electrode-SBBR were also investigated. The results showed that the operating process of this technique was: adding water → anaerobic processing → aeration → anoxic or anaerobic processing → effluent dewatering → idle. The optimal conditions were suggested as follows: hydraulic retention time (HRT) was 7.0 h, anaerobic and aeration time was 0.5 h and 4.0 h respectively, and anoxia / anaerobic time was 2.5 h, furthermore, electric current ranged 30-60 mA, DO was 4.0-5.0 mg/L and C/N ratio was greater than 10.0. In summary, the removing efficiencies of total nitrogen, Cu2+ and COD from the biogas slurry could reach to 45.79%, 86.53% and 84.86% respectively by the electrode-SBBR system. The results indicate that the electrode-SBBR system can be considered as a new technique for removal of nitrogen and copper from the biogas slurry simultaneously.

       

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