Ni-Cd sealed and vented cells have been widely used in the last few years. The environmental hazard related to the heavy metals contained in Ni-Cd batteries is well known. Therefore, a number of scientific studies and commercial processes have been implemented in order to recycle them. Since spent batteries are a heterogeneous and complex material, any kind of recovery process needs some preliminary treatments. The proposed process described in this paper has been tested in laboratory and further developed in a pilot plant. It consists of a combination of mechanical and hydrometallurgical treatment steps, and is able to treat all type of Ni-Cd batteries. In particular, the mechanical treatments have to be done separately on vented and sealed cells, while the hydrometallurgical step is performed on a mixture of the two products obtained from mechanical steps. A fully automated dismantling line would allow the separate recovery of the plastic or metallic casing, terminals, KOH electrolyte, and electrodes to be further processed for Ni and Cd recovery. The electrodes coming from dismantling line and sealed batteries are submitted separately to an original crushing and elutriation treatment to separate metallic and active paste in the first case and metallic, plastic and active paste in the second case. The hydrometallurgical treatment is carried out on active paste bearing product to produce Ni, Cd, and Fe commercial salts through acidic leaching followed by a multi-step solvent extraction operation to obtain pure solutions.

Laboratory and pilot plant processing of spent Ni-Cd batteries / Cavallini, Mauro; Lupi, Carla; Pilone, Daniela; P. P., Milella; A., Pescetelli; G., Cannavale. - STAMPA. - 1:(2000), pp. 471-478. (Intervento presentato al convegno 4th International Symposium on Recycling of Metals and Engineered Materials tenutosi a PITTSBURGH, PA nel OCT 22-25, 2000).

Laboratory and pilot plant processing of spent Ni-Cd batteries

CAVALLINI, Mauro;LUPI, Carla;PILONE, Daniela;
2000

Abstract

Ni-Cd sealed and vented cells have been widely used in the last few years. The environmental hazard related to the heavy metals contained in Ni-Cd batteries is well known. Therefore, a number of scientific studies and commercial processes have been implemented in order to recycle them. Since spent batteries are a heterogeneous and complex material, any kind of recovery process needs some preliminary treatments. The proposed process described in this paper has been tested in laboratory and further developed in a pilot plant. It consists of a combination of mechanical and hydrometallurgical treatment steps, and is able to treat all type of Ni-Cd batteries. In particular, the mechanical treatments have to be done separately on vented and sealed cells, while the hydrometallurgical step is performed on a mixture of the two products obtained from mechanical steps. A fully automated dismantling line would allow the separate recovery of the plastic or metallic casing, terminals, KOH electrolyte, and electrodes to be further processed for Ni and Cd recovery. The electrodes coming from dismantling line and sealed batteries are submitted separately to an original crushing and elutriation treatment to separate metallic and active paste in the first case and metallic, plastic and active paste in the second case. The hydrometallurgical treatment is carried out on active paste bearing product to produce Ni, Cd, and Fe commercial salts through acidic leaching followed by a multi-step solvent extraction operation to obtain pure solutions.
2000
4th International Symposium on Recycling of Metals and Engineered Materials
battery recycling
04 Pubblicazione in atti di convegno::04b Atto di convegno in volume
Laboratory and pilot plant processing of spent Ni-Cd batteries / Cavallini, Mauro; Lupi, Carla; Pilone, Daniela; P. P., Milella; A., Pescetelli; G., Cannavale. - STAMPA. - 1:(2000), pp. 471-478. (Intervento presentato al convegno 4th International Symposium on Recycling of Metals and Engineered Materials tenutosi a PITTSBURGH, PA nel OCT 22-25, 2000).
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11573/250438
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