4.7 Article

Treatment of organic wastewater by a synergic electrocatalysis process with Ti3+ self-doped TiO2 nanotube arrays electrode as both cathode and anode

Journal

JOURNAL OF HAZARDOUS MATERIALS
Volume 424, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.jhazmat.2021.127747

Keywords

Ti 3+self-doped TiO 2 nanotube arrays; Electrochemical anodic oxidation; Electro-Fenton; Hydroxyl radical; Direct oxidation

Funding

  1. National Natural Science Foundation of China [21936002]
  2. Liaoning Revitalization Talents Program [XLYC1801003]
  3. Program of Introducing Talents of Discipline to Universities [B13012]

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The combination of electro-Fenton (EF) and electrochemical anodic oxidation (AO) using Ti3+/TNTAs electrode is an effective method for refractory pollutants degradation in wastewater treatment, showing enhanced removal efficiency due to the coexistence of ·OH oxidation and direct oxidation on the Ti3+/TNTAs surface.
Electrochemical anodic oxidation (AO) is a promising technology for wastewater treatment due to its strong oxidation property and environmental compatibility. However, it suffers from high energy consumption for pollutants removal due to the side-reactions of hydrogen evolution reaction on cathode and oxygen evolution reaction on anode. Combining electro-Fenton (EF) with AO not only generated center dot OH for pollutants degradation but also increased current efficiency. This work investigated a synergic electrocatalysis process between EF and AO with Ti3+ self-doped TiO2 nanotube arrays (Ti3+/TNTAs) electrode as both cathode and anode for wastewater treatment. The pseudo-first-order kinetic rate constant of phenol degradation by EF+AO (0.107 min- 1) was 9.7 or 6.3 times as much as that of only EF (0.011 min- 1) or AO (0.017 min- 1) process, respectively. Enhanced pollutants removal of EF+AO could be attributed to the coexistence of center dot OH oxidation and direct oxidation on Ti3+/TNTAs surface. The COD of secondary effluent of coking wastewater decreased from 159.3 mg L-1 to 47.0 mg L-1 by EF+AO within 120 min with low specific energy consumption (9.5 kWh kg-1 COD-1). This work provided a new insight into design of the energy-efficient synergic electrocatalysis process for refractory pollutants degradation.

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