Good old fireside chat, page-13788

After a year of frustration, some thoughts on the year ahead.

The Preliminary Economic Assessment to begin this quarter.
If the Bromine plant is proved up I wouldn't think it would be running before the end of the year. With the Lithium PP maybe a year after that.

As for the brine feed for the Bromine plant, why use LC2 which has the highest Li grades? The brine with Br removed will be pumped into an old oil well, where it will possibly be contaminated.
It makes sense to use CC32 for the Br plant. The assays for Br are much higher .
CC zone 29.....12894 ppm Br.....143 ppm Li.
CC zone 31.....8439 ppm Br...….48 ppm L1.
LC2 zone 31...3978 ppm Br...….253 ppm Li.
Skyline zone 31....4427 ppm Li.....194 ppm Li.

The flow rates are quite a bit lower for CC but the other 2 wells improved by 320% and 100% respectively with a well clean up. Als0 pumping from CC would be required anyway if the plant was by LC2.

I have used the assay results for CC32 from 11/4/18 Ann these results were used through 2018, then for some reason the assays changed in 2019 zone 29..5041ppm Br and zone 31...4450 ppm Br . I have not contacted BBB regarding this as he doesn't answer my emails.

The object of the Bromine plant is to make money and I think CC32 will do this.