TY - JOUR
T1 - Comparison on molecular transformation of dissolved organic matter during Fenton and activated carbon adsorption processes for chemical cleaning wastewater treatment
AU - Zhao, Xiaodan
AU - Huang, Zhuojun
AU - Sun, Haosen
AU - Zhao, Qiqi
AU - Huang, Zhanghe
AU - Zhang, Chun
AU - Wang, Yang
AU - Yang, Chunyan
AU - Zhou, Zhen
N1 - Publisher Copyright:
© 2024 Elsevier B.V.
PY - 2024/9/20
Y1 - 2024/9/20
N2 - This study employed Fenton oxidation and powdered activated carbon (PAC) adsorption processes for the removal of recalcitrant dissolved organic matter (DOM) in chemical cleaning wastewater (CCW) to meet discharge standards. Fourier transform ion cyclotron resonance mass spectrometry (FT-ICR MS) was used to identify resistant compounds and investigate the transformation characteristics of DOM. CCW mainly contained surfactant exhibiting heteroatom-rich characteristics, and both processes exhibited effective DOM removal but distinct selectivity towards different subclasses of formulas. PAC adsorption significantly decreased the number of DOM compounds and more effective in aromatic compounds than Fenton oxidation. The aliphatic compounds (AImod ≤ 0.5, 1.5 ≤ H/C ≤ 2.0) predominantly with saturated and reduced states were resistant to PAC adsorption, and particularly a specific CHONSP formula was the predominant contributor to residual DOM in the effluent. In contrast, Fenton oxidation degraded most substances in the CCW except for a few saturated and reduced compounds primarily consisting of CHO, resulting in an increase in DOM number. Two unsaturated subclasses, carboxylic-rich alicyclic molecules/lignin-like structures (primarily CHON) and carbohydrates (primarily CHONP and CHONSP), were prominently produced after Fenton oxidation. The major mechanisms governing Fenton oxidation of surfactant in CCW primarily involved dealkylation (25.2 %), oxygen addition (21.2 %), and decarboxylation (19.8 %). Given the unique removal preferences and resistance observed in Fenton and PAC processes, a combination approach could be explored in the future to achieve advanced overall performance.
AB - This study employed Fenton oxidation and powdered activated carbon (PAC) adsorption processes for the removal of recalcitrant dissolved organic matter (DOM) in chemical cleaning wastewater (CCW) to meet discharge standards. Fourier transform ion cyclotron resonance mass spectrometry (FT-ICR MS) was used to identify resistant compounds and investigate the transformation characteristics of DOM. CCW mainly contained surfactant exhibiting heteroatom-rich characteristics, and both processes exhibited effective DOM removal but distinct selectivity towards different subclasses of formulas. PAC adsorption significantly decreased the number of DOM compounds and more effective in aromatic compounds than Fenton oxidation. The aliphatic compounds (AImod ≤ 0.5, 1.5 ≤ H/C ≤ 2.0) predominantly with saturated and reduced states were resistant to PAC adsorption, and particularly a specific CHONSP formula was the predominant contributor to residual DOM in the effluent. In contrast, Fenton oxidation degraded most substances in the CCW except for a few saturated and reduced compounds primarily consisting of CHO, resulting in an increase in DOM number. Two unsaturated subclasses, carboxylic-rich alicyclic molecules/lignin-like structures (primarily CHON) and carbohydrates (primarily CHONP and CHONSP), were prominently produced after Fenton oxidation. The major mechanisms governing Fenton oxidation of surfactant in CCW primarily involved dealkylation (25.2 %), oxygen addition (21.2 %), and decarboxylation (19.8 %). Given the unique removal preferences and resistance observed in Fenton and PAC processes, a combination approach could be explored in the future to achieve advanced overall performance.
KW - Activated carbon adsorption
KW - Chemical cleaning wastewater
KW - Dissolved organic matter
KW - FT-ICR MS
KW - Fenton oxidation
UR - https://www.scopus.com/pages/publications/85189355042
U2 - 10.1016/j.seppur.2024.127226
DO - 10.1016/j.seppur.2024.127226
M3 - 文章
AN - SCOPUS:85189355042
SN - 1383-5866
VL - 344
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 127226
ER -