4.8 Article

Optimization of a Hierarchical Porous-Structured Reactor to Mitigate Mass Transport Limitations for Efficient Electrocatalytic Ammonia Oxidation through a Three-Electron-Transfer Pathway

Journal

ENVIRONMENTAL SCIENCE & TECHNOLOGY
Volume 55, Issue 18, Pages 12596-12606

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acs.est.1c02825

Keywords

hierarchical porous structure; mass transport intensification; electrocatalytic ammonia oxidation; three-electron-transfer; transition-metal phosphide

Funding

  1. National Natural Science Foundation of China [22022606, 51738013]
  2. Guangxi Bagui Scholar Construction Project [2016A10]
  3. Excellent Innovation Project of Research Center for Eco-Environmental Sciences [CAS RCEES-EEI-2019-02]

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By developing a novel ammonia oxidation reactor with hierarchical porous-structured Ni foam electrodes, high-efficiency three-electron-transfer ammonia conversion was achieved, with approximately 70% ammonia removal efficiency and around 4% byproduct production, significantly superior to conventional ammonia oxidation configurations. After 20 days of continuous operation, the reactor achieved over 90% ammonia degradation performance with an energy consumption of 25.42 kW h kg(-1) N.
Regulation of fast three-electron-transfer processes for electrocatalytic oxidation of ammonia to nitrogen by achieving efficient generation and utilization of active sites is the optimal strategy in ammonia-containing wastewater treatment. However, the limited number of accessible active sites and sluggish interfacial mass transfer are two main bottlenecks restricting conventional ammonia oxidation configurations. Herein, we develop a macroporous Ni foam electrode integrated with vertically aligned two-dimensional mesoporous Ni2P nanosheets to create sufficient exposure of active centers. A novel ammonia oxidation reactor with the developed hierarchical porous-structured electrodes was assembled to construct an intensified microfluidic process with flow-through operation to mitigate macroscopic mass transport limitations. The confined microreaction space in the hierarchical porous reactor further promotes spontaneous nanoscale diffusion/convection of the target contaminant to high-valence Ni sites and enhances the microscopic mass transfer. The combined results of electrochemical measurements and in situ Raman spectra showed that the ammonia degradation mechanism results from direct oxidation by the high-valence Ni, significantly different from the conventional indirect active-chlorine-species-mediated oxidation. The optimized reactor achieves high-efficiency three-electron-transfer ammonia conversion with an ammonia removal efficiency of similar to 70% from an initial concentration of similar to 1400 mg/L and byproduct production of similar to 4%, significantly superior to a conversion unit comprising a featureless Ni-based electrode in the immersed configuration, which had >50% byproduct yield. 20 days of continuous operation under variable conditions achieved >90% ammonia degradation performance and an energy consumption of 25.42 kW h kg(-1) N (1 order of magnitude lower than the active-chlorine-mediated process), showing the potential of the reactor in medium-concentration ammonia-containing wastewater treatment.

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