TY - JOUR
T1 - Life Cycle Assessment of Tantalum and Niobium Recycling from Hard Metal Scrap
AU - Aromaa, Riina
AU - Rinne, Marja
AU - Lundström, Mari
N1 - This research was conducted with the funding of Business Finland-financed TOCANEM project (grant number 41778/31/2020). The authors also gratefully acknowledge the support of the School of Chemical Engineering in Aalto University as well as the Academy of Finland-funded RawMatTERS Finland Infrastructure (RAMI). Authors would also like to thank Jervois Finland Oy for discussions and ideas.
PY - 2023/10/16
Y1 - 2023/10/16
N2 - Secondary hard metal contains valuable tantalum and niobium, which could be recovered after chemical recycling of the scrap; however, the environmental impacts of their recycling have not been earlier quantified. This study provides gate-to-gate life cycle inventory data on tantalum and niobium recovery from the Ta–Nb-rich residue after the leaching of cobalt in the chemical recycling of hard metal and first assessment of the environmental impacts of tantalum and niobium coproduction. The environmental impacts were quantified using life cycle assessment (LCA) based on data acquired by process simulation. Two processes were evaluated: one based on conventional HF leaching used in the primary production of tantalum and niobium and one prospective HF-free process using NaOH. The results show that environmental impacts of Ta–Nb recycling can outperform primary production environmentally if the Ta and Nb content in the raw material is high enough. At the process level, a benefit is gained even with a lower content, but at the product level, higher contents are required for tantalum recovery to be worthwhile. In HF-based recycling, increasing the Ta and Nb contents each from 2.5 to 5 wt % decreases the value of global warming potential (GWP) of Ta recycling from 1.24 times the GWP of primary tantalum production to 0.72 times the GWP of primary tantalum production. The environmental impacts of the recycling processes mostly originate from the background processes. The most burdening process hot spots of recycling included the leaching and effluent treatment stages for the HF-based process in which HF and lime were the largest contributors. For the HF-free process, the largest contributions were due to NaOH used in the caustic conversion as well as oxalic acid in the solvent extraction.
AB - Secondary hard metal contains valuable tantalum and niobium, which could be recovered after chemical recycling of the scrap; however, the environmental impacts of their recycling have not been earlier quantified. This study provides gate-to-gate life cycle inventory data on tantalum and niobium recovery from the Ta–Nb-rich residue after the leaching of cobalt in the chemical recycling of hard metal and first assessment of the environmental impacts of tantalum and niobium coproduction. The environmental impacts were quantified using life cycle assessment (LCA) based on data acquired by process simulation. Two processes were evaluated: one based on conventional HF leaching used in the primary production of tantalum and niobium and one prospective HF-free process using NaOH. The results show that environmental impacts of Ta–Nb recycling can outperform primary production environmentally if the Ta and Nb content in the raw material is high enough. At the process level, a benefit is gained even with a lower content, but at the product level, higher contents are required for tantalum recovery to be worthwhile. In HF-based recycling, increasing the Ta and Nb contents each from 2.5 to 5 wt % decreases the value of global warming potential (GWP) of Ta recycling from 1.24 times the GWP of primary tantalum production to 0.72 times the GWP of primary tantalum production. The environmental impacts of the recycling processes mostly originate from the background processes. The most burdening process hot spots of recycling included the leaching and effluent treatment stages for the HF-based process in which HF and lime were the largest contributors. For the HF-free process, the largest contributions were due to NaOH used in the caustic conversion as well as oxalic acid in the solvent extraction.
KW - LCA
KW - Environmental impacts
KW - Niobium
KW - Process simulation
KW - Recycling
KW - Tantalum
UR - https://www.webofscience.com/api/gateway?GWVersion=2&SrcApp=aalto_pure&SrcAuth=WosAPI&KeyUT=WOS:001079411600001&DestLinkType=FullRecord&DestApp=WOS
UR - https://www.scopus.com/pages/publications/85176151989
U2 - 10.1021/acssuschemeng.3c03540
DO - 10.1021/acssuschemeng.3c03540
M3 - Article
SN - 2168-0485
VL - 11
SP - 14997
EP - 15005
JO - ACS Sustainable Chemistry & Engineering
JF - ACS Sustainable Chemistry & Engineering
IS - 41
ER -