Curious what part of the $50M would be required for the detailed engineering of an 8ktpa plant. Anyone got a comparator?
Also seems the scaling factor from 1ktpa to 8ktpa means a lot less surface area per volume HPA reaction and that would seem an upside risk to the achievable purity on the thinking that at least some of the contaminants are contributed by those surfaces. In the pharmaceutical industry, this is established fact, but I’m just guessing as regards the mining/refining process being piloted here. But as a chemist thinking about how aggressive HCl is, I have my suspicions. Upside risk only, but maybe that fifth nine is there?
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