Key Laboratory of Beijing for Water Quality Science and Water Environmental Recovery Engineering, Beijing University of Technology, Beijing 100124, China.
Bioresour Technol. 2011 Mar;102(5):4091-7. doi: 10.1016/j.biortech.2010.12.051. Epub 2010 Dec 22.
To enhance nutrient removal performance and reduce disposal amount of waste activated sludge (WAS), a pilot-scale continuous system consisting of a 2-step sludge alkaline fermentation process and an A(2)O reactor was proposed. The feasibility of WAS reducing and resourcing by alkaline fermentation was investigated. Volatile fatty acids (VFA) yield was higher under alkaline condition than that under acidic condition. Through 2-step alkaline fermentation, substantial VFA was accumulated, and then elutriated out continuously from an up-flow column by domestic wastewater. The results showed that 38.2% of sludge was hydrolyzed, 19.7% was finally acidified into VFA, and as high as 42.1% of WAS was reduced. Moreover, after introducing the fermentation liquids with higher proportion of acetic acid and propionic acid into the A(2)O reactor, the total nitrogen and phosphorus removal efficiencies reached to 80.1% and 90.0%, respectively. Sludge reduction and enhanced nutrient removal could be achieved simultaneously in the proposed system.
为了提高营养物质去除性能并减少剩余污泥(WAS)的处置量,提出了一种由两步污泥碱性发酵过程和 A(2)O 反应器组成的中试规模连续系统。考察了碱性发酵使 WAS 还原和资源化的可行性。在碱性条件下,挥发性脂肪酸(VFA)的产率高于酸性条件下的产率。通过两步碱性发酵,大量 VFA 被积累,并通过生活污水从升流式柱中连续洗脱出来。结果表明,38.2%的污泥被水解,19.7%最终酸化成 VFA,高达 42.1%的 WAS 被还原。此外,在将具有更高比例乙酸和丙酸的发酵液引入 A(2)O 反应器后,总氮和总磷的去除效率分别达到 80.1%和 90.0%。在提出的系统中可以同时实现污泥减量和强化营养物去除。