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Treatment of landfill leachate by a pilot-scale modified Ludzack-Ettinger and sulfur-utilizing denitrification process

机译:中试改良的Ludzack-Ettinger和利用硫的反硝化工艺处理垃圾渗滤液

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摘要

Nitrogen removal efficiency of a pilot-scale system consisted of Modified Ludzack-Ettinger (MILE) followed by sulfur-utilizing denitrification (SUDNR) process was evaluated with a landfill leachate. For SUDNR, a down-flow mode sulfur packed bed reactor (SPBR) filled with sulfur and limestone particles was used. Although total nitrogen removal efficiency of the MLE process was about 80% at the recycle ratio of 4, effluent contained 350-450 mg/L NO3--N. Up to a loading rate of 1.2 kg NO3--N/m(3)-day, the SPBR could achieve complete removal of nitrate, and nitrate removal rate was kept to that level even at higher loading rate. When a COD/N ratio of MLE process was maintained at 2 instead of 4, more organics with molecular weight less than 500 were utilized for heterotrophic denitrification although denitrification was not complete with the lack of electron donors. Clogging in the SPBR, mainly by the accumulation of nitrogen gas in the pores, could easily be removed by introducing the effluent in an upward direction for 1 min at 1 hr intervals. The proposed treatment system could achieve nitrate free effluent with a slight increase in chemical cost. Furthermore, depending on further COD removal requirement after biological treatment, the proposed treatment system can be an economical solution.
机译:用垃圾渗滤液评估了中试规模的系统的脱氮效率,该系统由改性Ludzack-Ettinger(MILE),随后的利用硫的反硝化(SUDNR)工艺组成。对于SUDNR,使用填充有硫和石灰石颗粒的下流模式硫填充床反应器(SPBR)。尽管MLE工艺的总氮去除效率在4的循环比下约为80%,但废水中的NO3--N含量为350-450 mg / L。高达1.2 kg NO3--N / m(3)-day的装载量,SPBR可以完全去除硝酸盐,即使在更高的装载量下,硝酸盐去除率也可以保持在该水平。当MLE工艺的COD / N比率保持为2而不是4时,尽管缺乏电子给体,但反硝化未完成,但更多的分子量小于500的有机物被用于异养反硝化。 SPBR的堵塞主要是由于氮气在孔中的积聚,可以通过以1小时为间隔将废水向上方向引入1分钟来轻松消除。拟议的处理系统可实现无硝酸盐排放,而化学成本略有增加。此外,根据生物处理后进一步去除COD的要求,建议的处理系统可能是一种经济的解决方案。

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