Tenements
EL 24987, EL25080, EL28205, EL28272, EL28273 (RUM 50% - RWD 50%)
Resource Drilling
Eight experimental vibracore holes were completed with drilling depths between 1 m and 3.5 m during September 2011. Fifty-five sonic drill holes were satisfactorily completed during October 2011. These holes averaged 3.2 m deep and penetrated through the soft lake sediment aquifer, the stiff clay aquiclude of the basal lake sediments and into the fractured Devonian siltstone aquifer beneath. Logging, sampling and geochemical asssaying should be complete in the first quarter of 2012. It is hoped to post a maiden potash resource estimate shortly thereafter.
Drilling was successful and confirm the following:
Highlight Brine Samples From Selected Lakes
|
Sample |
K (mg/L) |
Mg (mg/L) |
SO4 (mg/L) |
LAKE |
|
122248 |
12000 |
20372 |
57581 |
Curtin Island |
|
122249 |
11000 |
18232 |
47334 |
Curtin Island |
|
122259 |
8400 |
7694 |
42956 |
Mallee Well |
|
122229 |
11000 |
4302 |
42735 |
Miningere |
|
122289 |
8000 |
9392 |
30842 |
Mallee Well East |
|
122286 |
7700 |
11786 |
40872 |
Mallee Well East |
|
122293 |
7500 |
8785 |
41803 |
Curtin West |
|
122281 |
7700 |
17989 |
39008 |
Island lake 5 |
|
122277 |
7100 |
10161 |
37766 |
Island Lake 3 |
Conclusions from the trials are as follows:
1. The Karinga Lakes system brines comprise primarily sodium chloride, minor sodium sulfate and sulfate salts of potassium and magnesium. The brines collected to date appear to have potential as a source of Schoenite/Leonite (K2SO4 MgSO4 6H2O/4H2O) from which Potassium Sulfate can be recovered by established technology.
2. In the two trials conducted to date the Potassium loss to the sodium chloride (halite) harvest was approximately 20% of the feed, i.e. 80% of the potassium input progressed to the crude Potash salt crystallization phase. The loss is incurred via the brine entrained in the crude halite as it is harvested and not as crystalline potassium salt contamination.
3. Phase 1 trial was cut short due to technical difficulties but indicated a Potassium recovery of 56.5% to a mixed salt grading 3.8% K. The residual Potassium content representing 24.1% of input reported to the end brine hence was not recovered in the Phase 1 study. Results from Phase 2 trial confirm that a substantial portion of this Potassium can be recovered in a crystalline mixed salt at a considerably higher Potassium grade.
4. Phase 2 trial indicated a combined Potassium recovery of 76% to a mixed salt grading 6.1% K. This product comprised two fractions – Product A representing a K yield of 55.8% in a product grading 5.2% K and Product B representing an additional yield of 20.2% in a product grading 10.6% K.
5. All evaporate products have significant sodium chloride (halite) content as the process brine is saturated in sodium chloride at all stages of the evaporation cycle.
6. The combined A+B product from the Phase 2 trial contains approximately 44% sodium chloride. The Potassium Magnesium Sulfate salts Schoenite and Leonite, which crystallized, can be effectively separated from sodium chloride by flotation.


