China Architecture Design and Research Group, Beijing 100044, PR China; National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Engineering Research Center of Beijing, Beijing University of Technology, Beijing 100124, PR China.
National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Engineering Research Center of Beijing, Beijing University of Technology, Beijing 100124, PR China.
Water Res. 2021 Sep 15;203:117540. doi: 10.1016/j.watres.2021.117540. Epub 2021 Aug 11.
Introducing fermentation technology into sewage treatment is a sustainable development concept, but future application still faces many challenges. A novel partial nitrification, fermentation-based double denitrification bioprocess (PN-F-Double/DN) was achieved in three separated SBR type reactors, simultaneously treating high ammonia (1766.6 mg/L) mature landfill leachate and external waste activated sludge (WAS, MLSS = 20.6 g/L). Firstly, NH-N was oxidized to NO-N in partial nitrification reactor (PN-SBR), with nitrite accumulation ratio (NAR) of 96.5%. Next, the PN-SBR effluent (NO-N = 1529.8 mg/L) coupled with the WAS were introduced to an anoxic reactor for integrated fermentation-denitrification (IFD-SBR). The occurrence of fermentation was mainly attributed to free nitrous acid (FNA, nitrite protonate form) promoting the splitting decomposition of sludge spatial configuration and interfacial forces. The released volatile fatty acids (VFAs) were utilized in situ during the denitrification process (NO-N→N), obtaining 0.6 kg/m•d nitrogen removal rate and 3.3 kg/m•d sludge reduction rate. Finally, undesirable fermentation by-products from IFD-SBR (NH-N = 119.2 mg/L) were further removed in the endogenous post-denitrification reactor (EPD-SBR) through operational strategy of anaerobic/aerobic/anoxic by residual VFAs as the carbon source. In the EPD-SBR, Defluviicoccus (0.9%) and Candidatus Competibacter (5.8%) dominated carbon source storage and nitrogen removal, acting as a typical denitrifying glycogen-accumulating organism (DGAO), with an intracellular carbon storage efficiency of 83.1% and nitrogen removal contribution of 93.7%. After 200 days of operation, the PN-F-Double/DN process provided effluent containing, on average, 1.86 mg/L NH-N and 5.5 mg/L NO-N, with 98.5% TN removal. Compared with traditional bioprocesses, PN-F-Double/DN allowed up to 25% saving in aeration energy consumption, 100% decrease in carbon source demand, and achieve 46.1% external WAS reduction.
将发酵技术引入污水处理是一种可持续发展的理念,但未来的应用仍面临许多挑战。一种新型的部分硝化、基于发酵的双反硝化生物工艺(PN-F-Double/DN)在三个独立的 SBR 型反应器中实现,同时处理高氨(1766.6mg/L)成熟垃圾渗滤液和外部废活性污泥(WAS,MLSS=20.6g/L)。首先,在部分硝化反应器(PN-SBR)中,NH-N 被氧化为 NO-N,亚硝酸盐积累率(NAR)为 96.5%。接下来,PN-SBR 出水(NO-N=1529.8mg/L)与 WAS 一起引入缺氧反应器进行集成发酵-反硝化(IFD-SBR)。发酵的发生主要归因于游离亚硝酸(FNA,亚硝酸盐质子化形式)促进污泥空间结构和界面力的分裂分解。释放的挥发性脂肪酸(VFAs)在反硝化过程中就地利用(NO-N→N),获得 0.6kg/m•d 的氮去除率和 3.3kg/m•d 的污泥减少率。最后,IFD-SBR 中的不良发酵副产物(NH-N=119.2mg/L)通过剩余 VFAs 作为碳源的厌氧/好氧/缺氧操作策略在内源反硝化反应器(EPD-SBR)中进一步去除。在 EPD-SBR 中,脱铁杆菌(0.9%)和候选 Competibacter(5.8%)主导碳源储存和氮去除,作为典型的反硝化糖原积累菌(DGAO),细胞内碳储存效率为 83.1%,氮去除贡献为 93.7%。经过 200 天的运行,PN-F-Double/DN 工艺提供的出水平均含有 1.86mg/L 的 NH-N 和 5.5mg/L 的 NO-N,TN 去除率为 98.5%。与传统生物工艺相比,PN-F-Double/DN 可节省高达 25%的曝气能耗,100%减少碳源需求,并实现 46.1%的外部 WAS 减少。