Saternus M., European metallurgical conference: EMC 2017 Leipzig, Germany 25-Jun-1728-Jun-17, Fornalczyk A., Lisinska M., Willner J., Saternus M., European metallurgical conference: EMC 2017 Leipzig, Germany 25-Jun-1728-Jun-17, Fornalczyk A., Lisinska M., and Willner J.
LEDs are made from semiconductor materials which combine Ga, Al and In with As, P and N, and other components contain metals such as Fe, Cu, Ni, Pb, Zn, Ag, Au and rare earth elements (REE). The recovery of critical and rare earth elements from spent LEDs is discussed in relation to future demand for these materials, in particular Ga, In, Ce, Eu, Gd and Y. There are three different approaches: direct re-use of lamp phosphors in new lamps, although this is only applicable to one type of fluorescent lamp; recycling of individual phosphor components, using physicochemical separation methods to pre-treat the phosphor mixture to separate the halophosphate phosphor fraction from the rare earth phosphors before recycling of its REE content; and chemical treatment of the phosphors with recovery of REE from solution by precipitation or solvent extraction. Separation of lamp phosphors by flotation is not easy because the components have similar hydrophobicity. The efficiency of the collectors dodecyl ammonium acetate, sodium dodecyl sulphate and sodium oleate has been tested at different pH values and the effect of sodium metasilicate as dispersant has also been investigated, with the results depending on the type of collector and pH. Two-liquid flotation using immiscible liquids consisting of water as a polar solvent and hexane, heptane or octane as non-polar solvent is more suitable for the separation of fine, less than 10 mm particles, and the wettability of the particles can be adjusted using a surfactant. Pneumatic separation in an air stream gave only moderate results. Separation of phosphor particles has been achieved using heavy medium separation, and the process was accelerated by centrifugation and particle pre-treatment with sodium oleate. Processes for the recovery of REEs from phosphors include leaching with HCl/H2O2, heating with sodium carbonate at 1000 degrees C, pressure leaching with H2SO4/HNO3, and extraction with supercritical CO2 containing tri-n-butyl ph, LEDs are made from semiconductor materials which combine Ga, Al and In with As, P and N, and other components contain metals such as Fe, Cu, Ni, Pb, Zn, Ag, Au and rare earth elements (REE). The recovery of critical and rare earth elements from spent LEDs is discussed in relation to future demand for these materials, in particular Ga, In, Ce, Eu, Gd and Y. There are three different approaches: direct re-use of lamp phosphors in new lamps, although this is only applicable to one type of fluorescent lamp; recycling of individual phosphor components, using physicochemical separation methods to pre-treat the phosphor mixture to separate the halophosphate phosphor fraction from the rare earth phosphors before recycling of its REE content; and chemical treatment of the phosphors with recovery of REE from solution by precipitation or solvent extraction. Separation of lamp phosphors by flotation is not easy because the components have similar hydrophobicity. The efficiency of the collectors dodecyl ammonium acetate, sodium dodecyl sulphate and sodium oleate has been tested at different pH values and the effect of sodium metasilicate as dispersant has also been investigated, with the results depending on the type of collector and pH. Two-liquid flotation using immiscible liquids consisting of water as a polar solvent and hexane, heptane or octane as non-polar solvent is more suitable for the separation of fine, less than 10 mm particles, and the wettability of the particles can be adjusted using a surfactant. Pneumatic separation in an air stream gave only moderate results. Separation of phosphor particles has been achieved using heavy medium separation, and the process was accelerated by centrifugation and particle pre-treatment with sodium oleate. Processes for the recovery of REEs from phosphors include leaching with HCl/H2O2, heating with sodium carbonate at 1000 degrees C, pressure leaching with H2SO4/HNO3, and extraction with supercritical CO2 containing tri-n-butyl ph