Engineering Research Center of Beijing, Beijing University of Technology, Beijing, China.
Bioresour Technol. 2013 Apr;134:212-8. doi: 10.1016/j.biortech.2013.02.017. Epub 2013 Feb 11.
In order to achieve advanced nitrogen removal from landfill leachate without the addition of external carbon sources, a novel system coupling an anaerobic sequencing batch reactor (ASBR) and sequencing batch reactor (SBR) was proposed for the treatment of real landfill leachate with NH4+-N and chemical oxygen demand (COD) concentrations of 1100 mg/L and 6000 mg/L, respectively. ASBR could remove 80% of the influent COD under a volumetric loading rate of 5 kg COD/(m3d). Denitritation and simultaneous nitritation-denitritation were responsible for 50% of the TN removal in SBR under alternate anoxic/aerobic modes. Furthermore, advanced nitrogen removal was realized with a total inorganic nitrogen (TIN) removal efficiency of 99% at the expense of endogenous denitritation during a 26 h period, which led to effluent COD and TN values of 550-650 mg/L and 15-25 mgN/L, respectively. For the combined system, removal efficiencies of COD and total nitrogen (TN) were above 90% and 95%, respectively.
为了在不添加外部碳源的情况下实现高级的垃圾渗滤液脱氮,提出了一种新型的厌氧序批式反应器(ASBR)和序批式反应器(SBR)耦合系统,用于处理实际的垃圾渗滤液,其 NH4+-N 和化学需氧量(COD)浓度分别为 1100mg/L 和 6000mg/L。ASBR 在容积负荷为 5kgCOD/(m3d)下可以去除 80%的进水 COD。在交替缺氧/好氧模式下,SBR 中的反硝化和同时硝化-反硝化分别承担了 50%的 TN 去除。此外,通过 26 小时的内源反硝化作用,实现了总无机氮(TIN)去除效率达 99%的高级脱氮,导致出水 COD 和 TN 值分别为 550-650mg/L 和 15-25mgN/L。对于组合系统,COD 和总氮(TN)的去除效率均高于 90%和 95%。