Synthesis of nickel powder with good hydrogen evolution performance from spent Fluid Catalytic Cracking catalysts

被引:10
作者
Cheng, Wenbo [1 ,2 ]
Wu, Mingshuai [1 ,2 ]
Yu, Fengshan [1 ,2 ]
Tian, Maolin [1 ,2 ]
Wen, Jiawei [1 ,2 ]
Wang, Chunxia [1 ,2 ]
Huang, Guoyong [1 ,2 ]
Xu, Shengming [3 ,4 ]
机构
[1] China Univ Petr, Coll New Energy & Mat, Beijing 102249, Peoples R China
[2] China Univ Petr, Coll Chem Engn, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[3] Tsinghua Univ, Inst Nucl & New Energy Technol, Beijing 100084, Peoples R China
[4] Tsinghua Univ, Beijing Key Lab Fine Ceram, Beijing 100084, Peoples R China
关键词
Spent Fluid Catalytic Cracking catalysts; Recycling; Value-added utilization; Electrocatalysis; Hydrogen evolution reaction; NANOPARTICLES; RECOVERY;
D O I
10.1016/j.jclepro.2022.135540
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The strategic metals in spent Fluid Catalytic Cracking (FCC) catalysts have attracted worldwide attention. In this work, the recovery of rare earths (lanthanum and cerium), nickel and vanadium have been achieved by acid leaching, extraction and precipitation, while the high-purity nickel powder with pretty hydrogen evolution performance has been synthesized for value-added utilization. Secondary leaching has been used for insoluble Ni power, and the total leaching rates of Ce, La, V and Ni are 96.17%, 85.86%, 99.99% and 74.62%, respectively. Rare earths have been recovered by the precipitation in primary leaching solution. The recovery rate of La is 97.11% and Ce is 99.96%. In secondary leaching solution, the impurity removal has been conducted, and the removal rate of Al and Fe is above 99.9%. Then the V and Ni are separated by solvent extraction, the extraction rate of V by N235 is 97.57%, the separation factor of Ni and V is 634.61. Finally, the high-purity NiSO4 solution (99.62%)is reduced to nickel power by the reducing agent N2H4 center dot H2O, which was made for the hydrogen evo-lution reaction catalyst. When the current density is 10 mA/cm(2), the overpotential is 308 mV, and the slope of Tafel is 128 mV.dec(-1). This process provides a comprehensive recovery route of valuable metals from spent FCC catalysts for new energy industry.
引用
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页数:11
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