Degradation of sulfamethoxazole by super-hydrophilic MoS2 sponge co-catalytic Fenton: Enhancing Fe2+/Fe3+cycle and mass transfer

被引:30
|
作者
Xiao, Chun [1 ,2 ]
Hu, Yongyou [1 ,2 ]
Li, Qitian [1 ]
Liu, Jingyu [1 ,2 ]
Li, Xian [1 ,2 ]
Shi, Yueyue [1 ,2 ]
Chen, Yuancai [1 ,2 ]
Cheng, Jianhua [1 ,2 ]
Zhu, Xiaoqiang [3 ]
Wang, Guobin [3 ]
Xie, Jieyun [3 ]
机构
[1] South China Univ Technol, Guangzhou Higher Educ Mega Ctr, Sch Environm & Energy, Guangzhou 510006, Peoples R China
[2] South China Univ Technol, Guangzhou Higher Educ Mega Ctr, Key Lab Pollut Control & Eco Restorat Ind Clusters, Minist Educ, Guangzhou 510006, Peoples R China
[3] Guangzhou Pengkai Environm Technol Co Ltd, Guangzhou 511493, Peoples R China
基金
中国国家自然科学基金;
关键词
MoS2; Sponge; Co-catalytic Fenton; Hydrophilicity; Reactor; WATER; H2O2; ANTIBIOTICS; REDUCTION; ACID; IRON;
D O I
10.1016/j.jhazmat.2023.131878
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
To promote the cycle of Fe2+/Fe3+ in co-catalytic Fenton and enhance mass transfer in an external circulation sequencing batch packed bed reactor (ECSPBR), super-hydrophilicity MoS2 sponge (TMS) modified by tungstosilicic acid (TA) was prepared for efficiently degrading sulfamethoxazole (SMX) antibiotics in aqueous solution. The influence of hydrophilicity of co-catalyst on co-catalytic Fenton and the advantages of ECSPBR were systematically studied through comparative research methods. The results showed that the super hydrophilicity increased the contact between Fe2+ and Fe3+ with TMS, then accelerated Fe2+/Fe3+ cycle. The max Fe2+/Fe3+ ratio of TMS co-catalytic Fenton (TMS/Fe2+/H2O2) was 1.7 times that of hydrophobic MoS2 sponge (CMS) co catalytic Fenton. SMX degradation efficiency could reach over 90% under suitable conditions. The structure of TMS remained unchanged during the process, and the max dissolved concentration of Mo was lower than 0.06 mg/L. Additionally, the catalytic activity of TMS could be restored by a simple re-impregnation. The external circulation of the reactor was conducive to improving the mass transfer and the utilization rate of Fe2+ and H2O2 during the process. This study offered new insights to prepare a recyclable and hydrophilic co-catalyst and develop an efficient co-catalytic Fenton reactor for organic wastewater treatment.
引用
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页数:15
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