Ann: 2024 AGM Chair address and presentation, page-63

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TrayonRanger

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28/11/24

11:14

Post #: 76818526
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Originally posted by Scarpa: ↑

As I thought with that earlier discussion, losses in the magnetic and slurry can be sorted out upstream at the SAG/ball mill and crushing units via increasing particle size (as means to deal with the fines issue).

Interesting comments around iron, meaning whether the magnetic separator's use is reduced significantly given would appear that the ore they are using has low iron content by the time it gets to that stage, meaning also it would appear the upstream elements of the process flowsheet are working well. I guess the proof in the pudding will be when they increase particle size and how that flows through to increased recovery, which I believe it will.

. It will be also be interesting whether the increase in particle size will make magnetic separator more effective at that stage but if the iron at that stage still remains low then suspect they will significantly reduce its application at this time (i.e. I suspect the higher grade sections of the deposit may also have lower iron levels that the lower grade aspects of the deposit, despite iron been low throughout the deposit overall itself compared to some of its peers.)

As to SP performance, long term as we all know it does depend on the rebound in the spodumene price, whilst keeping costs competitrve/low

All IMO

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"...if the iron at that stage still remains low then suspect they will significantly reduce its application ..."

Or even turn off resulting in further savings of wear-n-tear and power.

Win win.

LTR Price at posting: 78.3¢ Sentiment: Buy Disclosure: Held
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