Antwort auf Beitrag Nr.:
40.018.614 von Harry0978 am 20.08.10
09:55:31NEW DIRECTOR APPOINTED FOR MARENICA
International uranium company Marenica Energy Limited (ASX: MEY) is
pleased to
announce the appointment of Mr Gavin Becker, ARSM, BSc(Eng)
(London), MBA (Bond),
FAusIMM, CP (Met) as a non‐executive director.
Mr Becker is a metallurgist with over 35 years industry experience,
during that time he has
worked in senior operational, R&D, feasibility study and
consulting roles on lead / zinc, gold,
uranium, copper and nickel mines and / or projects. Earlier in his
career he lived and
worked in Southern Africa (Zambia 2 years, South Africa 4
years).
Mr Becker is currently an executive in a Services Company in the
mining sector.
Mr Becker has had a successful track record in capital raisings and
completion of a number
of significant feasibility studies. Also of direct relevance to
Marenica Energy Limited , Mr
Becker has uranium experience from his time in South Africa
(including Mintek) as well as in
Australia (Yeelirrie Project). He also managed WMC Resources'
initial heap leach projects at
St.Ives near Kambalda in WA, followed by Dominion Mining's Cosmo
Howley operations in
the Northern Territory, which produced Dominion's first gold using
heap leach methods.
MARENICA PROJECT UPDATE
The Marenica Uranium project comprises the Marenica Deposit and
surrounding exploration area
totalling 527 square kilomteres. The Marenica deposits mineral
resource estimate totals 227 million
tonnes at 170ppm U3O8 U3O8comprising an Indicated Mineral Resource
of 31Mt grading 175ppm
U3O8 and an Inferred Mineral Resource of 196Mt grading 169ppm U3O8
for a combined total of 85
million pounds (39,000 tonnes) of contained U3O8.
The Marenica deposit is a large low grade secondary uranium deposit
(carnotite) that is made up of
two significant ore types, paleo‐channel sedimentary and oxidised
bedrock. Testwork has been
completed on these types of ore to determine mineralogy and
beneficiation by radiometric sorting
or srubbing through to final product recovery. The scope of work by
ANSTO focused the preferred
process route of agitated slurry leaching on upgraded ore. The
uranium was readily leached from
the ores using alkaline leach solution, in both bottle roll tests
and slurry leaches recoveries ranged
from 75 to 90%.
Significantly the metallurgical testwork showed that the material
was easily broken down requiring
little crushing. As a consequence of this beneficiation by
screening and scrubbing indicated that the
uranium is concentrated in the fine material and that 90% of the
U3O8 concentrated in 30% to 37%
of the material in the minus 150 micron fraction while in the minus
38 micron fraction 83% of the
U3O8 concentrated in 15% to 23% of the mass.
The results from Preliminary scoping work conducted by SRK
Consulting (UK) during the first half of
2010, clearly demonstrated that a large heap leach operation shows
positive economics. The
beneficiation process is the key driver in the next round of
testwork, beneficiation prior to
agglomeration and leaching will significantly enhance the project
economics.
This change in the preferred process route will involve additional
metallurgical test work across a
broad selection of samples to confirm the use of the heap leach
technology. The metallurgical work
will involve a series of upgrade, agglomeration and column leach
tests that will take several months;
these tests are planned to commence in early September 2010.
This work is to be supervised Kappes‐Cassiday & Associates, who
are specialists in the development,
engineering and implementation of extractive metallurgical
processes for the mining industry and
have particular expertise in heap leaching.
A sample matrix for selection of ore types has been generated and
samples have been collected for
shipment for testwork at AMMTEC in Perth. The initial part of the
study will involve 10 subcomposites,
made up from a combination of basement and palaeo‐channel ores, and
classified
according to depth and grade.
Portions of sub‐composite will be subject to a series of screening
and scrubbing tests, and resulting
re‐combining screened and scrubbed material into an upgraded,
blended product. The blended
materials will be split and employed in agglomeration testing as
well as a 30‐day intermittent bottleroll
testwork.
Two master composites will be made by combining basement material
into a single composite and
channel material into a second composite. Each master composite
will be treated separately and
screen / crush sizes will depend on the results of the
sub‐composite screening / scrubbing work.
The aim is to produce an upgraded dry (screened) product that is
combined with upgraded
(scrubbed) slurry that will be agglomerated as preparation for
column leaching.
Results from this work will be fed back into a technical economic
model and are expected to
significantly enhance the project economics.
For further information contact Marenica Energy Limited; PH: +61 8
93217355
Notes