Hi guys,
Can anyone comment on the impurity levels of Al203, Fe203, Si02, Th and U and what processing methods would be needed to remove them to get to a saleable rutile concentrate?
The high Al203 suggests flotation may be required? And the Th+U may need acid leaching?
Just trying to get an idea of capex.
Below is snapshot from SVM's PFS on Rutile Product Spec:
Chat GPT response for Typical Rutile Con spec:
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