Morales-Rico Pablo, Ramos-Díaz Jessica, Thalasso Frédéric
Biotecnología y Bioingeniería, Centro de Investigación y de Estudios Avanzados del Instituto Politécnico Nacional (Cinvestav), Av. IPN 2508 San Pedro Zacatenco, 07360 Ciudad de México, Mexico.
ACS Omega. 2025 Feb 6;10(6):5574-5581. doi: 10.1021/acsomega.4c08289. eCollection 2025 Feb 18.
While numerous studies report methane emissions from wastewater treatment plants (WWTPs) in developed countries, few address emissions from plants in developing countries, where outdated technologies, such as the lack of enhanced primary and sludge treatment, are common. Moreover, these studies often rely on indirect calculations rather than direct measurements. Our study fills this gap by providing unit-process-level direct measurements of methane emissions in a conventional WWTP in Mexico, serving as a case study for developing countries. A standard plant was selected and visited on five occasions. It includes a primary settler, an aerated reactor, and a secondary settler, with no sludge treatment in place. Our findings revealed a CH emission factor of 0.396 ± 0.218 g CH m of treated water, with the primary settler accounting for 72.3 ± 15.9% of emissions, and the aerated reactor contributing 27.7 ± 15.9%. Notably, the emission factors are comparable to those reported for plants with more advanced treatment technologies, suggesting that technological obsolescence may not significantly enhance CH emissions. Methanotrophy in the aerated reactor was a key process, oxidizing 91-98% of the CH transported from the primary settler. Additionally, a carbon dioxide (CO) emission factor of 97.4 ± 34.4 g CO m was measured, primarily from the aerated reactor, consistent with the plant's overall treatment efficiency. These findings provide crucial data for understanding greenhouse gas emissions from WWTPs in developing regions and highlight the need for targeted mitigation strategies.
虽然众多研究报告了发达国家污水处理厂(WWTPs)的甲烷排放情况,但很少有研究涉及发展中国家污水处理厂的排放,在这些国家,诸如缺乏强化初级处理和污泥处理等过时技术很常见。此外,这些研究往往依赖间接计算而非直接测量。我们的研究通过对墨西哥一座传统污水处理厂的甲烷排放进行单元过程级别的直接测量填补了这一空白,为发展中国家提供了一个案例研究。我们选取了一座标准工厂并进行了五次实地考察。它包括一个初级沉淀池、一个曝气反应器和一个二级沉淀池,没有污泥处理设施。我们的研究结果显示,处理后水的CH排放因子为0.396±0.218克CH/立方米,其中初级沉淀池的排放量占72.3±15.9%,曝气反应器的排放量占27.7±15.9%。值得注意的是,这些排放因子与采用更先进处理技术的工厂所报告的排放因子相当,这表明技术过时可能不会显著增加CH排放。曝气反应器中的甲烷氧化作用是一个关键过程,氧化了从初级沉淀池输送来的91 - 98%的CH。此外,还测量到二氧化碳(CO)排放因子为97.4±34.4克CO/立方米,主要来自曝气反应器,这与该工厂的整体处理效率一致。这些研究结果为了解发展中地区污水处理厂的温室气体排放提供了关键数据,并突出了制定针对性减排策略的必要性。