3210 XXXI International Mineral Processing Congress 2024 Proceedings/Washington, DC/Sep 29–Oct 3
CONCLUSION
The LFP black mass flotation poses distinct challenges com-
pared to NMC or LCO black mass types, primarily due to
the ultrafine nature of LFP particles. Addressing these chal-
lenges, this study explored a novel reagent scheme integrat-
ing graphite promoter ESCAID110 and a frother MIBC
alongside a flocculant, polyacrylamide (PAM). First, the
bubble loading experiments show that adding PAM into
LFP conditioned with MIBC and ESCAID decreases the
attachment of LFP particles from 10.9±3.0 to 6.1±0.9 due
to the agglomeration of the LFP particles. In addition, it
was shown that when PAM was used in conjunction with
MIBC and ESCAID, the bubble loading decreased from
100% to 85.0±3% for graphite particles. This suggests
that the presence of PAM in the mixture affects the sur-
face properties of the graphite particles, potentially altering
their hydrophobicity or changing the dynamics of bubble-
particle interactions.
The findings of the flotation tests with MBM demon-
strate that PAM notably enhances the grade and recovery
of graphite, where particles are fully liberated without bind-
ers. The addition of 100g/t PAM significantly improved
the graphite grade in the overflow product from 45.5% to
71.1%, and recovery from 38.9% to 90.6%.
Better grade where obtained with 50g/t, 82%C but the
recovery dropped to 72.2%C. Therefore, 100 g/t of PAM
was selected for IBM flotation test work. However, the result
of test with only MIBC and ESCAID were better compared
to with addition of PAM, with grade of 88%C and recov-
ery of 81.4% compared to grade of 66.8%C and recovery
of 70.9%C. Additionally, attrition pre-treatment for IBM
unexpectedly resulted in a lower carbon grade, likely due to
the liberation and subsequent entrainment of ultrafine LFP
particles into the overflow product. These outcomes under-
score the delicate balance required in reagent selection and
process optimization for LFP black mass flotation.
ACKNOWLEDGMENT
The authors gratefully acknowledge the EU Horizon
Europe-EIT Raw Materials for funding the ReLiFe
(Recycling Lithium Ferro phosphate in the RIS area)
Project, KAVA reference: 22020.
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