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Volume 44 Issue 9
Sep.  2026
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Article Contents
YU Jifang, CHI Mingzhe, BAI Feifei, SUN Gang, WANG Jianbing. Preparation of ordered nano-porous Ti4O7 REM and its performance in treatment of coking wastewater[J]. ENVIRONMENTAL ENGINEERING , 2026, 44(9): 18-29. doi: 10.13205/j.hjgc.202609003
Citation: YU Jifang, CHI Mingzhe, BAI Feifei, SUN Gang, WANG Jianbing. Preparation of ordered nano-porous Ti4O7 REM and its performance in treatment of coking wastewater[J]. ENVIRONMENTAL ENGINEERING , 2026, 44(9): 18-29. doi: 10.13205/j.hjgc.202609003

Preparation of ordered nano-porous Ti4O7 REM and its performance in treatment of coking wastewater

doi: 10.13205/j.hjgc.202609003
  • Received Date: 2025-11-02
    Available Online: 2026-11-05
  • In recent years, the existing secondary biochemical process has been difficult to achieve the standard COD discharge of coking wastewater. Although the electrochemical oxidation technology with Ti4O7 REM as the anode can effectively remove organic matter in the secondary biochemical effluent, there is a problem of high energy consumption. Enhancing the catalytic activity of the electrodes is the key to reducing the energy consumption. To enhance the catalytic activity of Ti4O7 REM, ordered nano-porous Ti4O7 particles were synthesized by self-assembly in this research. These particles were then loaded onto a porous titanium substrate, to obtain a Ti-based ordered nano-porous Ti4O7 electroactive membrane (named ordered nano-porous Ti4O7 REM). Using ordered nano-porous Ti4O7 REM as the anode, the Ti4O7 REM superimposed reactor was constructed to deeply remove the organic substances in the biochemical effluent of coking wastewater. The result showed that the ordered nanoporous structure compressed the width of the charge layer (dsc = 0.97 nm), increasing the probability of electron tunneling and shortening the electron transmission path, which enhanced the excitation activity of ·OH. Under the oxidative conditions of a current density of 15 mA/cm2 and the electrolysis time of 120 minutes, the energy consumption was 96.7 kW·h/kg COD, the TOC removal rate was 62.7%, the COD removal rate was 88.5%, and the effluent COD met the limit requirements of the Pollutant Discharge Standard for Coking Chemical Industry(GB 16171—2012).
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