Naoya KanekoMsaharu OHNOTasuma SuzukiMasakazu NIINAE
Spent hydrodesulphurization (HDS) catalysts are treated with hydrometallurgical leaching processes such as caustic leaching and acid leaching with roasting as a pre-treatment step. In the alkaline leaching processes such as sodium carbonate roasting followed by water leaching, most of the molybdenum and vanadium are selectively leached and most of nickel is left in the residue after the alkaline leaching of spent HDS catalysts. Therefore, it is important to recover nickel from the alkaline leaching residue. The main form of nickel in the alkaline leaching residue is spinel, therefore, it is difficult to extract nickel from the residue using mineral acids.
Kota MANABETasuma SuzukiMasakazu NIINAEJunji Shibata
Kota MANABENaoya KanekoTasuma SuzukiMasakazu NIINAE
Kota MANABEAkiko FujiTasuma SuzukiMasakazu NIINAEJunji Shibata
Qiming FengYanhai ShaoLeming OuGuofan ZhangYiping Lu
A. OgnyanovaAyşe ÖztürkIda De MichelisFrancesco FerellaGiuliana TaglieriAta AkçılFrancesco Vegliò