4.7 Article

Treatment of reverse osmosis concentrate from industrial coal wastewater using an electro-peroxone process with a natural air diffusion electrode

Journal

SEPARATION AND PURIFICATION TECHNOLOGY
Volume 279, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.seppur.2021.119667

Keywords

Reverse osmosis concentrate; Industrial coal wastewater; Natural air diffusion electrode; Electro-peroxone; Electrochemical advanced oxidation processes

Funding

  1. National Natural Science Foundation of China [21976096, 21773129, 21806081, 21811530274, 51208267]
  2. Tianjin Science and Technology Program [19PTZWHZ00050]
  3. National Key Research and Development Program [2016YFC0400706]
  4. Natural Science Foundation of Tianjin [19JCQNJC07900]
  5. Tianjin Development Program for Innovation and Entrepreneurship
  6. Fundamental Research Funds for the Central Universities

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The study demonstrates that the EP process is the most efficient in treating ROC wastewater, and the combination of PC and EP processes significantly reduces energy consumption while achieving complete decolouration.
Reverse osmosis concentrate (ROC) produced in the RO treatment of coal chemical wastewater is highly toxic and difficult to degrade. In this study, an electro-peroxone (EP) process was applied to treat ROC with a natural air diffusion electrode (NADE), which was used as the cathode to efficiently generate H2O2. The treatment efficiency of EP, electro-Fenton, electro-oxidation (EO), peroxi-coagulation (PC) and ozonation for the removal of total organic carbon, colour and UV254 in ROC were studied and compared, confirming that EP was the most efficient process. The EP process as well as electric energy consumption (EEC) were optimized, and an optimum reaction conditions (current of 200 mA, pH of 4 and O-3 dose of 6 mg/min) were selected. The production of (OH)-O-center dot in EP was much higher than that in ozonation and EO, as indicated by the EPR measurement. Excitation-emission matrix spectra of ROC after EP treatment verified that all the fluorescent contaminants in ROC was removed within 2 h. Further, the combination of PC and EP processes (2 h + 3 h) significantly reduced EEC by 58% as compared with EP (6 h), realizing complete decolouration. This study declared the potential of using EP and the combined PC-EP process to effectively treat the real ROC wastewater.

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