Zhou Shuyan, Gong Hui, Xu Enhui, Chen Xiang, Wang Xiankai, Wang Hang, Zhu Danyang, Zhang Yanyan, Yang Jing, Gu Guowei, Dai Xiaohu
College of Environmental Science and Engineering, State Key Laboratory of Pollution Control and Resources Reuse, Tongji University, Shanghai 200092, China.
YANGTZE Eco-Environment Engineering Research Center, China Three Gorges Corporation, Wuhan 430010, China.
Water Res X. 2024 Sep 23;25:100259. doi: 10.1016/j.wroa.2024.100259. eCollection 2024 Dec 1.
High solid anaerobic digestion (HSAD) achieves the benefits of high volumetric loading rates and lower reject water production, which, however, results in much more concentrated reject water with a remarkable increase in organics and nitrogen compared with that from conventional AD with low solid content. The high concentrations of ammonium (2000-3500 mg/L) and COD (3000-4000 mg/L) were reported to exert inhibition on anammox bacteria (AnAOB), posing challenges to the application of the partial nitritation/anammox (PN/A). To date, no cases of PN/A process start-up for sludge HSAD reject water were reported. This study demonstrated the start-up process of a 480 m/d PN/A project without anammox sludge inoculation and treating HSAD reject water from a centralized dewatered sludge treatment plant. The project did not construct new infrastructures but utilized previously constructed tanks to upgrade the process from existing short-cut nitrification-denitrification to a two-stage PN/A process. Although no external anammox sludge inoculation was performed to save seeding sludge cost, the start-up was successfully achieved in about 9 months (273 days) based on a three-step method of "AnAOB enrichment - sludge acclimation - capacity doubling". During start-up, the relative abundance of AnAOB (Candidatus_) increased from near zero to 12.0%. After start-up, the total inorganic nitrogen (TIN) removal load reached 0.74 kgN/(m•d), with a total nitrogen removal efficiency of over 90%. Compared to the traditional nitrification-denitrification process, the PN/A process remarkably reduces the addition of organic chemicals and aeration energy consumption, saving approximately 4.2 million yuan (RMB) in operational costs annually. In summary, this research provides a full-scale reference for the start-up of the PN/A process treating sludge HSAD reject water.
高固体厌氧消化(HSAD)具有容积负荷率高和产水量低的优点,然而,与低固体含量的传统厌氧消化相比,这会产生浓度更高的剩余水,其中有机物和氮的含量显著增加。据报道,高浓度的铵(2000 - 3500毫克/升)和化学需氧量(3000 - 4000毫克/升)会对厌氧氨氧化细菌(AnAOB)产生抑制作用,这给部分亚硝化/厌氧氨氧化(PN/A)工艺的应用带来了挑战。迄今为止,尚未有关于污泥HSAD剩余水PN/A工艺启动的案例报道。本研究展示了一个日处理量为480立方米的PN/A项目的启动过程,该项目未接种厌氧氨氧化污泥,处理的是来自集中脱水污泥处理厂的HSAD剩余水。该项目没有建设新的基础设施,而是利用先前建造的罐体将现有短程硝化反硝化工艺升级为两级PN/A工艺。尽管为节省接种污泥成本未进行外部厌氧氨氧化污泥接种,但基于“厌氧氨氧化细菌富集 - 污泥驯化 - 能力翻倍”的三步法,在约9个月(273天)内成功实现了启动。启动期间,厌氧氨氧化细菌(“Candidatus_”)的相对丰度从接近零增加到12.0%。启动后,总无机氮(TIN)去除负荷达到0.74千克氮/(立方米·天),总氮去除效率超过90%。与传统的硝化反硝化工艺相比,PN/A工艺显著减少了有机化学药剂的添加量和曝气能耗,每年节省运营成本约420万元人民币。总之,本研究为处理污泥HSAD剩余水的PN/A工艺启动提供了一个全尺寸参考。