Department of Civil and Environmental Engineering, University of Maryland, College Park, Maryland, USA.
WSSC Water, Laurel, Maryland, USA.
Water Environ Res. 2024 Jan;96(1):e10961. doi: 10.1002/wer.10961.
Phosphorous (P) removal in wastewater treatment is essential to prevent eutrophication in water bodies. Side-stream enhanced biological phosphorous removal (S2EBPR) is utilized to improve biological P removal by recirculating internal streams within a side-stream reactor to generate biodegradable carbon (C) for polyphosphate accumulating organisms (PAOs). In this study, a full-scale S2EBPR system in a water resource recovery facility (WRRF) was evaluated for 5 months. Batch experiments revealed a strong positive correlation (r = 0.91) between temperature and C consumption rate (3.56-8.18 mg-COD/g-VSS/h) in the system, with temperature ranging from 14°C to 18°C. The anaerobic P-release to COD-uptake ratio decreased from 0.93 to 0.25 mg-P/mg-COD as the temperature increased, suggesting competition between PAOs and other C-consumers, such as heterotrophic microorganisms, to uptake bioavailable C. Microbial community analysis did not show a strong relationship between abundance and activity of PAO in the tested WRRF. An assessment of the economic feasibility was performed to compare the costs and benefits of a full scale WRRF with and without implementation of the S2EBPR technology. The results showed the higher capital costs required for S2EBPR were estimated to be compensated after 5 and 11 years of operation, respectively, compared to chemical precipitation and conventional EBPR. The results from this study can assist in the decision-making process for upgrading a conventional EBPR or chemical P removal process to S2EBPR. PRACTITIONER POINTS: Implementation of S2EBPR presents adaptable configurations, exhibiting advantages over conventional setups in addressing prevalent challenges associated with phosphorous removal. A full-scale S2EBPR WRRF was monitored over 5 months, and activity tests were used to measure the kinetic parameters. The seasonal changes impact the kinetic parameters of PAOs in the S2EBPR process, with elevated temperatures raising the carbon demand. PAOs abundance showed no strong correlation with their activity in the full-scale S2EBPR process in the tested WRRF. Feasibility assessment shows that the benefits from S2EBPR operation can offset upgrading costs from conventional BPR or chemical precipitation.
污水中磷的去除对于防止水体富营养化至关重要。侧流强化生物除磷(S2EBPR)通过在侧流反应器内循环内部流来提高生物除磷,从而产生可生物降解的碳(C)用于聚磷菌(PAO)。在本研究中,对一个水资源回收厂(WRRF)中的全尺寸 S2EBPR 系统进行了 5 个月的评估。批处理实验表明,系统中温度与 C 消耗率(3.56-8.18mg-COD/g-VSS/h)之间存在很强的正相关(r=0.91),温度范围为 14°C 至 18°C。随着温度的升高,厌氧释磷与 COD 吸收比从 0.93 降至 0.25mg-P/mg-COD,表明 PAO 与其他 C 消费者(如异养微生物)之间存在竞争,争夺可利用的 C。微生物群落分析并未显示测试的 WRRF 中 PAO 的丰度与活性之间存在很强的关系。进行了经济可行性评估,以比较实施 S2EBPR 前后全尺寸 WRRF 的成本和收益。结果表明,S2EBPR 所需的较高资本成本预计分别在运行 5 年和 11 年后得到补偿,与化学沉淀和传统 EBPR 相比。本研究的结果可以帮助决策过程,将传统的 EBPR 或化学除磷工艺升级为 S2EBPR。