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A pilot-scale study on iron-driven autotrophic denitrification enhanced by CF-Fe-CS cathode for low C/N wastewater treatment

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中国科学数据2026-05-05 更新2026-04-25 收录
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https://www.sciengine.com/AA/doi/10.13205/j.hjgc.202604008
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The effluent from municipal wastewater treatment plants (WWTPs) is characterized by a low carbon-to-nitrogen (C/N) ratio in China. Achieving deep nitrogen removal using traditional heterotrophic denitrification processes requires substantial external carbon source addition, leading to high operational costs and potential secondary pollution. Nitrate-dependent ferrous oxidation (NDFO) presents a promising alternative denitrification technology. However, it faces bottlenecks such as unsustainable iron sources and surface passivation. In this study, a pilot-scale electrochemical-biological coupled system (CF-Fe-CS/NAFO) was constructed, featuring a built-in composite cathode (5% apparent filling rate of carbon felt-iron-chitosan, CF-Fe-CS), an effective volume of 200 L, and a treatment capacity of 100 L/d. A constant potential of -1.0 V (vs. Ag/AgCl) was applied to the cathode to achieve the in-situ electrochemical reduction of Fe(Ⅲ). In the test reactor, during stable operation from day 16 to 60 with a hydraulic retention time (HRT) of 48 h and synthetic wastewater containing 15 mg/L NO3--N, the effluent NO3--N concentration remained consistently below 6.5 mg/L, with a total nitrogen (TN) removal efficiency of 50% to 60%. In contrast, the control reactor (without an applied potential) showed an effluent NO3--N concentration above 12 mg/L and a TN removal efficiency below 20%. During continuous operation from day 61 to 74 using real secondary sedimentation tank effluent from a WWTP (influent NO3--N: 15.29 mg/L), the system reduced the effluent NO3--N to 6.06 mg/L, maintaining a TN removal efficiency above 50%. From day 74 to 98, as the HRT was sequentially reduced from 48 h to 24 h, 12 h, 6 h, and 3 h, the corresponding effluent NO3--N concentrations increased to 9.5 mg/L, 11.9 mg/L, 13.6 mg/L, and 14.6 mg/L, with TN removal efficiencies of 32.6%, 19.9%, 10.9%, and 5.8%, respectively. These results demonstrate that the CF-Fe-CS/NAFO electrochemical system can achieve long-term, stable, and advanced nitrogen removal from WWTP secondary effluent without the need for an external organic carbon source.
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2026-03-10
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