Dawei Liang
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Dawei Liang has a total of 186 co-authors. Here are the top co-authors by number of shared publications:
- Shanfu Lu
Beijing Key Laboratory of Bio-inspired Energy Materials and Devices, School of Energy and Power Engineering, Beihang University, Beijing, 102206, China
17 shared publications Yan Xiang
Beijing Key Laboratory of Bio-Inspired Energy Materials and Devices, School of Space & Environment, Beihang University, Shahe Campus, Beijing 102206, China
13 shared publications- Yan Xiang
Beijing Key Laboratory of Bio-inspired Energy Materials and Devices, School of Energy and Power Engineering, Beihang University, Beijing, 102206, China
12 shared publications - Haining Wang
Beijing Key Laboratory of Bio‐inspired Energy Materials and Devices School of Energy and Power Engineering Beihang University Beijing People's Republic of China
7 shared publications Chao Qu
Department of Environmental Science, College of Environmental Science and Engineering, Beijing University of Technology, Beijing 100124, China
6 shared publicationsShujuan Meng
6 shared publications
Latest Publications
- 13 August 2026
- Published by Elsevier in Journal of Membrane Science
- Vol. 758
Sub-nanoconfined MXene membrane electrodes for monovalent cation-selective separation with an electrochemical ion pumping
- 13 August 2026
- Published by Elsevier in Journal of Membrane Science
- Vol. 758
Sub-nanoconfined MXene membrane electrodes for monovalent cation-selective separation with an electrochemical ion pumping
- 8 December 2025
- Published by Elsevier in Journal of Hazardous Materials
- Vol. 501, 140755
Dual-functional Mn-single atom catalysts for synergistic H2O2 generation and activation: Toward efficient refractory organic wastewater treatment
- 8 December 2025
- Published by Elsevier in Journal of Hazardous Materials
- Vol. 501, 140755
Dual-functional Mn-single atom catalysts for synergistic H2O2 generation and activation: Toward efficient refractory organic wastewater treatment
- 16 July 2025
- Published by Royal Society of Chemistry (RSC) in Journal of Materials Chemistry A
- Vol. 13 (35) , 29092-29100
A triboelectric-electromagnetic hybrid nanogenerator enhancing electrochemical oxidation for organic pollutant degradation
The hybrid electrooxidation system driven by a wind-powered TE-HNG nanogenerator achieves high energy efficiency and more than 90% degradation of pollutants, providing a practical strategy for sustainable wastewater treatment.
- 16 July 2025
- Published by Royal Society of Chemistry (RSC) in Journal of Materials Chemistry A
- Vol. 13 (35) , 29092-29100
A triboelectric-electromagnetic hybrid nanogenerator enhancing electrochemical oxidation for organic pollutant degradation
The hybrid electrooxidation system driven by a wind-powered TE-HNG nanogenerator achieves high energy efficiency and more than 90% degradation of pollutants, providing a practical strategy for sustainable wastewater treatment.
- 11 December 2024
- Published by American Chemical Society (ACS) in Environmental Science & Technology
- Vol. 58 (51) , 22829-22839
Multistage Generation Mechanisms of Reactive Oxygen Species and Reactive Chlorine Species in a Synergistic System of Anodic Oxidation Coupled with in Situ Free Chlorine and H2O2 Production
Electro-oxidation (EO) is an efficient approach to removing refractory organics in wastewater. However, the interference from chlorine ions (Cl-) can generate reactive chlorine species (RCS), potentially leading to the production of undesirable chlorinated byproducts. A novel approach involving the cathodic oxygen reduction reaction (ORR) for in situ H2O2 production has emerged as a promising strategy to counteract this issue. This study systematically investigated the dynamics and transformation of RCS and reactive oxygen species (ROS) in an ORR/chloride-containing EO (EO-Cl) system, elucidating their respective roles in organic removal and chlorinated byproduct minimization. Distinct generation rates and patterns were observed for free chlorine and H2O2 in the ORR/EO-Cl system. The rapid generation of free chlorine at the anode quickly reached a dynamic equilibrium, which contrasted with the moderate, continuous cathodic production of H2O2, resulting in considerable H2O2 accumulation over time. This difference established kinetics-driven ROS and RCS formation and distribution, influencing the subsequent organic degradation process. Three distinct stages were identified in the degradation process. In stage I, free chlorine was the primary species, along with reactive species including Cl2•-, 1O2, ClO•, HO•, and Cl•. In stage II, the gradual accumulation of H2O2 consumed free chlorine, favoring the formation of 1O2 and HO•. In stage III, excessive H2O2 quenched the free radicals. Insights into these multistage mechanisms reveal that the rapid degradation of chlorinated byproducts by 1O2 and HO• occurs in stage II of the ORR/EO-Cl system.
- 11 December 2024
- Published by American Chemical Society (ACS) in Environmental Science & Technology
- Vol. 58 (51) , 22829-22839
Multistage Generation Mechanisms of Reactive Oxygen Species and Reactive Chlorine Species in a Synergistic System of Anodic Oxidation Coupled with in Situ Free Chlorine and H2O2 Production
Electro-oxidation (EO) is an efficient approach to removing refractory organics in wastewater. However, the interference from chlorine ions (Cl-) can generate reactive chlorine species (RCS), potentially leading to the production of undesirable chlorinated byproducts. A novel approach involving the cathodic oxygen reduction reaction (ORR) for in situ H2O2 production has emerged as a promising strategy to counteract this issue. This study systematically investigated the dynamics and transformation of RCS and reactive oxygen species (ROS) in an ORR/chloride-containing EO (EO-Cl) system, elucidating their respective roles in organic removal and chlorinated byproduct minimization. Distinct generation rates and patterns were observed for free chlorine and H2O2 in the ORR/EO-Cl system. The rapid generation of free chlorine at the anode quickly reached a dynamic equilibrium, which contrasted with the moderate, continuous cathodic production of H2O2, resulting in considerable H2O2 accumulation over time. This difference established kinetics-driven ROS and RCS formation and distribution, influencing the subsequent organic degradation process. Three distinct stages were identified in the degradation process. In stage I, free chlorine was the primary species, along with reactive species including Cl2•-, 1O2, ClO•, HO•, and Cl•. In stage II, the gradual accumulation of H2O2 consumed free chlorine, favoring the formation of 1O2 and HO•. In stage III, excessive H2O2 quenched the free radicals. Insights into these multistage mechanisms reveal that the rapid degradation of chlorinated byproducts by 1O2 and HO• occurs in stage II of the ORR/EO-Cl system.
- 5 November 2024
- Published by Elsevier in Renewable Energy
- Vol. 237
Reduction short-chain volatile fatty acids and CO2 into alcohols in microbial electrosynthesis system
- 5 November 2024
- Published by Elsevier in Renewable Energy
- Vol. 237
Reduction short-chain volatile fatty acids and CO2 into alcohols in microbial electrosynthesis system
- Open Access
Recent Advances in the Reactor Design for Industrial Wastewater Treatment by Electro-Oxidation Process
Refractory organic wastewater mainly includes wastewater from papermaking, textile, printing and dyeing, petrochemical, coking, pharmaceutical and other industries, as well as landfill leachate and its membrane-treated concentrate. The traditional biochemical method is difficult to adapt to its harsh conditions such as high toxicity, high organic load and high salinity. Compared to other methods, the electro-oxidation (EO) process owns the attractive characteristics of being clean and eco-friendly, highly efficient and producing no secondary pollution. EO systems mainly include electrodes, a reactor, a power supply and other basic units. The design of reactors with different electrodes was the key link in the application of EO technology. This paper mainly reported the different configurations of electrochemical reactors (ECRs) for refractory organic wastewater treatment, and summarized the advantages and disadvantages of them, including reactor structure, flow mode, operation mode and electrode construction. Compared with traditional reactors, the improved reactors such as 3D-ECR achieve higher mass transfer efficiency by increasing the contact area between the electrode and the fluid. Additionally, it has a higher removal rate of organics and a lower energy consumption. Finally, the future perspectives of the treatment of refractory organic wastewater by ECRs is discussed. This paper is expected to provide a reliable scientific basis for the real application of EO technology in refractory organic wastewater treatment.
Open AccessRecent Advances in the Reactor Design for Industrial Wastewater Treatment by Electro-Oxidation Process
Refractory organic wastewater mainly includes wastewater from papermaking, textile, printing and dyeing, petrochemical, coking, pharmaceutical and other industries, as well as landfill leachate and its membrane-treated concentrate. The traditional biochemical method is difficult to adapt to its harsh conditions such as high toxicity, high organic load and high salinity. Compared to other methods, the electro-oxidation (EO) process owns the attractive characteristics of being clean and eco-friendly, highly efficient and producing no secondary pollution. EO systems mainly include electrodes, a reactor, a power supply and other basic units. The design of reactors with different electrodes was the key link in the application of EO technology. This paper mainly reported the different configurations of electrochemical reactors (ECRs) for refractory organic wastewater treatment, and summarized the advantages and disadvantages of them, including reactor structure, flow mode, operation mode and electrode construction. Compared with traditional reactors, the improved reactors such as 3D-ECR achieve higher mass transfer efficiency by increasing the contact area between the electrode and the fluid. Additionally, it has a higher removal rate of organics and a lower energy consumption. Finally, the future perspectives of the treatment of refractory organic wastewater by ECRs is discussed. This paper is expected to provide a reliable scientific basis for the real application of EO technology in refractory organic wastewater treatment.
- 14 April 2022
- Published by Elsevier in Journal of Hazardous Materials
- Vol. 434, 128923
Enhanced refractory organics removal by •OH and 1O2 generated in an electro-oxidation system with cathodic Fenton-like reaction
- 14 April 2022
- Published by Elsevier in Journal of Hazardous Materials
- Vol. 434, 128923
Enhanced refractory organics removal by •OH and 1O2 generated in an electro-oxidation system with cathodic Fenton-like reaction