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Co-treatment performance of pollutants and per- and polyfluoroalkyl substances (PFAS) in centralized industrial wastewater using a membrane bioreactor (MBR)

Phan Ta Hoang Nhi 1, 2
Phuong Thao Nguyen 3, *
Nguyen Huu Viet 4
Dao Thi Viet Huong 4
Du My Le 4
To Thi Hien 1
Le Van Thang 5
Bui Xuan Thanh 4
  1. Trường Đại học Khoa học Tự nhiên, ĐHQG-HCM, 227 Nguyễn Văn Cừ, phường Chợ Quán, Thành phố Hồ Chí Minh 700000, Việt Nam
  2. Ho Chi Minh City University of Science
  3. Ho Chi Minh City University of Technology
  4. Trường Đại học Bách Khoa, ĐHQG-HCM, 268 Lý Thường Kiệt, phường Diên Hồng, Thành phố Hồ Chí Minh 700000, Việt Nam
  5. Trường Đại học Quốc tế, ĐHQG-HCM, Phường Linh Trung, Thành phố Hồ Chí Minh 700000, Việt Nam
Correspondence to: Phuong Thao Nguyen, Ho Chi Minh City University of Technology. Email: [email protected].
Volume & Issue: Vol. 10 No. 1 (2026) | Page No.: 1225-1236 | DOI: 10.32508/vnuhcmj-ees.v10i1.833
Published: 2026-06-17

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Copyright The Author(s) 2018. This article is published with open access by Vietnam National University, Ho Chi Minh city, Vietnam. This article is distributed under the terms of the Creative Commons Attribution License (CC-BY 4.0) which permits any use, distribution, and reproduction in any medium, provided the original author(s) and the source are credited. 

Abstract

Centralized industrial wastewater presents a major challenge due to its high pollutant loads and the presence of persistent micropollutants such as per- and polyfluoroalkyl substances (PFAS), which pose significant risks to human health and the environment. Membrane bioreactor (MBR) technology is highly regarded for its high organic removal efficiency, environmental friendliness, and cost-effectiveness. Although PFAS removal by MBR remains limited, it has been reported that a fraction of PFAS can be transferred from the aqueous phase to the biomass through adsorption. Therefore, this study was conducted to evaluate the co-treatment performance of COD, NH4⁺-N, and PFAS in centralized industrial wastewater. The lab-scale MBR system was operated at a flux of 6 L/m2.h (LMH). The results showed that the COD and NH4⁺-N removal rates reached 258 ± 103 mg COD/g VSS.day and 31.6 ± 7.6 mg NH4⁺-N/g VSS.day, respectively. For PFAS, the concentrations of 9 out of 11 compounds, including PFHxA, PFHpA, PFOA, PFBS, PFHxS, PFHpS, PFOS, PFDoA, and PFTrA, increased after treatment, likely because PFAS precursors were degraded and transformed into terminal PFAS compounds. In particular, PFOS concentrations markedly increased from 97.5 ng/L to 142.0 ng/L. In contrast, PFUnA and PFDA concentrations decreased, but only to a very limited extent. These results indicate that the MBR system is effective for organic pollutant removal. However, to remove trace-level, poorly biodegradable pollutants such as PFAS, the MBR needs to be coupled with additional physico-chemical treatment processes.

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