Integrated Electrochemical–Electrolytic Conversion of Oilfield-Produced Water into Hydrogen

This study tackles the challenge of treating high-oil (≥90 mg/L) and high-salinity (Cl− ≥ 6900 mg/L) oilfield-produced water for green hydrogen production. An integrated technology combining electrochemical cascade purification (EDCF: electro-demulsification–coagulation–flotation) with alkaline water electrolysis is developed. The EDCF process effectively reduces oil, suspended solids, and turbidity to <10 mg/L, <20 mg/L, and <20 NTU, respectively, meeting stringent feedwater criteria for electrolysis. An asymmetric electrolysis strategy employing a nickel felt anode/Raney nickel cathode system achieves a low cell voltage of 1.856 V at 1 A/cm2 in 6 M KOH at 85 °C, with 96.58% H2 purity. Crucially, separate anolyte/catholyte (0.5/6 M KOH) mitigates Cl− corrosion, enabling stable 240 h operation (96.66% ± 0.5% H2 purity) in a duplex steel electrolyzer. The work establishes comprehensive boundary conditions for scalable hydrogen production from treated produced water.

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Publication Details

Journal
Processes
Published
2026-01-05
DOI
https://doi.org/10.3390/pr14010173
Primary Topic
Microbial Fuel Cells and Bioremediation
Type
article
Field-Weighted Citation Impact
0.00

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article

Integrated Electrochemical–Electrolytic Conversion of Oilfield-Produced Water into Hydrogen

Weikang Han, Bin Dong, Gen-Sheng Zha, Chao Zhang et al.
Processes
Microbial Fuel Cells and Bioremediation
article

Integrated Electrochemical–Electrolytic Conversion of Oilfield-Produced Water into Hydrogen

Weikang Han, Bin Dong, Gen-Sheng Zha, Chao Zhang, Fuli Wang, Wenming Jiang, Pengjun Fan
article en

Abstract

This study tackles the challenge of treating high-oil (≥90 mg/L) and high-salinity (Cl− ≥ 6900 mg/L) oilfield-produced water for green hydrogen production. An integrated technology combining electrochemical cascade purification (EDCF: electro-demulsification–coagulation–flotation) with alkaline water electrolysis is developed. The EDCF process effectively reduces oil, suspended solids, and turbidity to <10 mg/L, <20 mg/L, and <20 NTU, respectively, meeting stringent feedwater criteria for electrolysis. An asymmetric electrolysis strategy employing a nickel felt anode/Raney nickel cathode system achieves a low cell voltage of 1.856 V at 1 A/cm2 in 6 M KOH at 85 °C, with 96.58% H2 purity. Crucially, separate anolyte/catholyte (0.5/6 M KOH) mitigates Cl− corrosion, enabling stable 240 h operation (96.66% ± 0.5% H2 purity) in a duplex steel electrolyzer. The work establishes comprehensive boundary conditions for scalable hydrogen production from treated produced water.

ProcessesVol. 14(1)
Xi'an City Planning&Design Institute (China) (CN), China University of Petroleum, East China (CN)
National Natural Science Foundation of China
Openalex Percentile: Top 97%
Microbial Fuel Cells and Bioremediation
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