CHEN Z D,SONG H Y,JIANG J Y,et al.Metal recovery and hydrogen production from acid mine drainage by acid-base imbalance electrolytic cell[J].Journal of Environmental Engineering Technology,2025,15(6):1928-1937. DOI: 10.12153/j.issn.1674-991X.20250206
Citation: CHEN Z D,SONG H Y,JIANG J Y,et al.Metal recovery and hydrogen production from acid mine drainage by acid-base imbalance electrolytic cell[J].Journal of Environmental Engineering Technology,2025,15(6):1928-1937. DOI: 10.12153/j.issn.1674-991X.20250206

Metal recovery and hydrogen production from acid mine drainage by acid-base imbalance electrolytic cell

  • An acid-base unbalanced electrolytic cell (AB-EC) was designed to overcome the limitations of slow reaction rate and low hydrogen (H2) production in the treatment of acid mine drainage (AMD) by microbial electrolysis and photoelectrochemical technology. Taking the coal mine type AMD with a single Fe2+ as the model system, the key parameters such as electrode spacing, voltage, urea concentration and pH were systematically optimized to establish the basic operating conditions of AB-EC. Furthermore, the optimization system was extended to the AMD treatment of freeze-thaw pyrite containing Fe2+, Al3+, Mn2+ and Ni2+, and the reaction mechanism under the competition of polymetallic ions was deeply explored. Finally, a strategy of two-stage AB-EC collaborative hydrogen production and staged metal recovery is proposed.The results showed that the optimal operating conditions of AB-EC were determined by system optimization tests as follows: electrode spacing of 2.5 cm, applied voltage of 8 V, and 0.5 mol/L urea solution with pH 13 for the anode electrolyte. After treating 230 mL of coal-type AMD for 50 min under these conditions, the Fe2+ removal rate reached 70.10%±3.87% and the H2 production was (54±2)mL, which was significantly better than microbial electrolysis and photoelectrochemical technology in terms of metal removal and H2 production. For the 230 mL freeze-thawed sulfuric iron pyrite AMD, the average concentrations of Fe2+, Al3+, Mn2+, Ni2+ in the effluent were 0.71, 0.01, 2.81, 0.23 mg/L, respectively, and the removal rate was more than 97% after the AB-EC was operated for 100 min. Simultaneously, the H2 production amounted to (116±3)mL, and the anode urea and NaOH average consumption were measured at 0.21 and 0.18 g, respectively. Further results showed that the construction of sequential batch two-stage AB-EC process could simultaneously achieve the H2 production and the selective separation and recovery of Al(OH)3 and Fe3O4.
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