Recovery of Valuable Materials from a Spent Nickel-Metal Hydride Battery: Selective Chlorination Roasting of an Anodic Active Material with CCl4 Gas
Recovery of Valuable Materials from a Spent Nickel-Metal Hydride Battery: Selective Chlorination Roasting of an Anodic Active Material with CCl4 Gas
复制标题
从废镍氢电池中回收有价值的材料:用 CCl4 气体选择性氯化焙烧阳极活性材料
DOI:
10.1016/j.seppur.2013.08.008
复制
发表时间:
2013
影响因子:
8.6
通讯作者:
S.Hirai and V.Sokolov
中科院分区:
文献类型:
--
作者:
T.Kuzuya;S.Hirai and V.Sokolov
A method for recovery of valuable metals from a spent nickel–metal hydride battery has been investigated. Mischmetal–nickel alloy (MmNi5), which acts as an anode active material, was separated from an electrode scrap mixture using a sedimentation process. The separated MmNi5contains rare earth metals (14.5 mass% Ce, 10.8 mass% La, 4.5 mass% Nd) and transition metals (49.2 mass% Ni, 9.8 mass% Co, 4.7 mass% Mn). CCl4gas was employed as a chlorination roasting agent to prevent the formation of rare earth oxychlorides. When MmNi5was chlorinated at 673 K, it was decomposed into rare earth chlorides and nickel alloy. The chlorinated sample was subsequently leached with distilled water to recover these materials. The leaching yields of La, Ce, and Nd reached 96.3, 77.4, and 80.1 mass%, respectively, and 85.7 mass% of the Ni and 87.1 mass% of the Co could be recovered as Ni–Co alloy. The relatively lower recovery ratios of Ce and Nd can be attributed to the stability of Ce and Nd oxychlorides. When the chlorination temperature reached 773 K, MmNi5was completely chlorinated. At 973 K and higher, a greenish precipitate was also observed in the low-temperature zone of the reaction tube. Because the vapor pressures of rare earth and transition metal chlorides differ from each other, the transition metal chlorides can be separated by vaporization. Their yields reached 94.6% (La), 95.3% (Ce), and 94.9% (Nd) in the chlorinated residue.