Zinc separation from brass dust by the Fenton process

被引:0
作者
Phuong, Nguyen Van [1 ]
Tong, Nguyen Xuan [1 ]
机构
[1] Ind Univ Ho Chi Minh City, Inst Sci Engn & Environm Management, Ho Chi Minh 700000, Vietnam
关键词
brass dust; current density; electrolysis; Fenton process; zinc recovery; COPPER; RECOVERY;
D O I
10.1002/vjch.202300352
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Brass polishing facilities generate waste dust rich in zinc and copper, presenting both an economic opportunity for resource recovery and an environmental challenge. The Fenton process, a promising hydrometallurgical solution, offers a way to separate zinc from this waste dust. Researchers employed an experimental design method to identify optimal parameters for zinc dissolution, including pH, ferrous iron (Fe2+) content, stirring speed, and hydrogen peroxide (H2O2) concentration. Kinetic modeling identified the optimal parameters for zinc dissolution: pH 1, 0.1 M Fe2+, 60 rpm stirring speed, 1.0% H2O2 concentration (flow rate 1 mL min-1), and a reaction time of 2 h. The kinetic data suggested a first-order kinetic model, indicating a chemically controlled surface reaction mechanism. These findings demonstrate the Fenton process's effectiveness in zinc dissolution from brass dust. This paves the way for further research on zinc recovery methods, such as electrolysis for metallic zinc production or integration into chemical manufacturing processes. image
引用
收藏
页码:138 / 145
页数:8
相关论文
共 15 条
[1]  
Abooalfazl A, 2015, Journal of health sciences and surveillance system, V3, P153
[2]   Kinetics and mechanisms of reactions between H2O2 and copper and copper oxides [J].
Bjorkbacka, Asa ;
Yang, Miao ;
Gasparrini, Claudia ;
Leygraf, Christofer ;
Jonsson, Mats .
DALTON TRANSACTIONS, 2015, 44 (36) :16045-16051
[3]  
Brandt M. J., 2016, TWORTS WATER SUPPLY, P444
[4]  
Dickinson CF, 1999, THERMOCHIM ACTA, V341, P89
[5]   Development of a reaction-limited model of dissolution: Application to official dissolution tests experiments [J].
Dokoumetzidis, A. ;
Papadopoulou, V. ;
Valsami, G. ;
Macheras, P. .
INTERNATIONAL JOURNAL OF PHARMACEUTICS, 2008, 355 (1-2) :114-125
[6]   Recovery of zinc and copper from copper smelter flue dust. Optimisation of sulphuric acid leaching [J].
Gonzalez-Montero, Pablo ;
Iglesias-Gonzalez, Nieves ;
Romero, Rafael ;
Mazuelos, Alfonso ;
Carranza, Francisco .
ENVIRONMENTAL TECHNOLOGY, 2020, 41 (09) :1093-1100
[7]   Review of hydrometallurgical recovery of zinc from industrial wastes [J].
Jha, MK ;
Kumar, V ;
Singh, RJ .
RESOURCES CONSERVATION AND RECYCLING, 2001, 33 (01) :1-22
[8]  
Laubertova M, 2019, ACTA MONTAN SLOVACA, V24, P223
[9]   Leaching kinetics of low-grade copper ore containing calcium-magnesium carbonate in ammonia-ammonium sulfate solution with persulfate [J].
Liu Zhi-xiong ;
Yin Zhou-lan ;
Hu Hui-ping ;
Chen Qi-yuan .
TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA, 2012, 22 (11) :2822-2830
[10]   Metal sulfide precipitation coupled with membrane filtration process for recovering copper from acid mine drainage [J].
Menzel, Katherine ;
Barros, Lorena ;
Garcia, Andreina ;
Ruby-Figueroa, Rene ;
Estay, Humberto .
SEPARATION AND PURIFICATION TECHNOLOGY, 2021, 270