University of Michigan, Department of Environmental Engineering, 1351 Beal Avenue, Ann Arbor, MI, United States.
University of Michigan, Department of Environmental Engineering, 1351 Beal Avenue, Ann Arbor, MI, United States.
Water Res. 2024 Apr 1;253:121261. doi: 10.1016/j.watres.2024.121261. Epub 2024 Feb 7.
Fully anoxic suspended growth treatment of domestic wastewater is rarely performed in practice at large scale. However, recent advances in membrane aerated biofilm reactor (MABR) technology can enable the "hybrid" concept that couples nitrification in the MABR with anoxic suspended growth for biological nitrogen removal. Small scale sequencing batch reactors were constructed to compare high-rate anoxic metabolization of influent carbon and biological phosphorus removal side-by-side with a conventional aerated system in a low-strength domestic wastewater (COD/TN ratio of approximately 6). Little differences existed in the oxidation of soluble readily biodegradable organic material between the two systems, but hydrolysis of particulate and colloidal organic matter in the anoxic reactor over a range of solid retention times was 60 % of the aerobic reactor. Reduced hydrolysis limited the amount of carbon available to ferment to volatile fatty acid (VFA), adversely impacting anoxic biological phosphorus removal (bio-P) process rates, and ortho-P removal performance was diminished by more than half at equivalent SRTs. At optimal growth conditions, i.e., an SRT of approximately 8 days and with supplementary VFA, ortho-P removal from the influent averaged roughly 75 %. Experimentation with supplemented acetic acid showed reduced anoxic metabolic efficiency, quantified via a P/O ratio of 0.90 versus 1.7 for the aerobic system, although overall anoxic bio-P removal demonstrably increased with external carbon.
完全缺氧悬浮生长处理的生活污水在大规模实践中很少进行。然而,膜曝气生物膜反应器(MABR)技术的最新进展可以实现“混合”概念,即将 MABR 中的硝化作用与缺氧悬浮生长相结合,用于生物脱氮。构建了小型序批式反应器,以比较在低强度生活污水(COD/TN 比约为 6)中,与传统曝气系统相比,高负荷缺氧代谢进水碳和生物除磷的情况。两个系统之间在可溶性易生物降解有机物质的氧化方面几乎没有差异,但在一系列固体停留时间内,缺氧反应器中颗粒状和胶体有机物的水解率为好氧反应器的 60%。水解减少限制了可用于发酵生成挥发性脂肪酸(VFA)的碳量,对缺氧生物除磷(bio-P)过程速率产生不利影响,并且在相同 SRT 下,正磷酸盐去除性能降低了一半以上。在最佳生长条件下,即 SRT 约为 8 天,并补充 VFA,进水的正磷酸盐去除率平均约为 75%。通过补充乙酸的实验表明,缺氧代谢效率降低,通过 P/O 比为 0.90 对比如好氧系统的 1.7,尽管通过外加碳明显增加了缺氧生物除磷。