TSX-V: RES
VANCOUVER, Aug. 18 /PRNewswire-FirstCall/ - Rare Element
Resources Ltd. (TSX-V: RES) is pleased to announce progress toward
defining a commercial process for rare-earth-element (REE)
concentration from oxide samples collected on the Company's
100%-owned Bear Lodge property, Wyoming,
USA. The favorable metallurgical test results on a large
sample of near-surface high-grade oxide mineralization indicate the
following:
1. With scrubbing/attritioning in water, a preconcentrate is produced
with a recovery of approximately 90% and a grade up to 20% rare-earth
oxide (REO); the REO resides in the finer fractions (-100 to- 500
mesh).
2. Hydrochloric acid leaching of the preconcentrates in an agitation
leach system gives a recovery of about 80 to 85% of the total REO
from the original mineralized material in the same general
proportions as the original REO distribution.
3. Additional testing is being conducted to optimize the processing
methods.
Metallurgical testwork is being conducted at Mountain States
R&D International, Inc. (MSRDI) of Vail, Arizona. Additional tests of REE
extraction and separation are underway at Intellimet LLC of
Missoula, Montana. Plans for
confirmatory testing by NAGROM of Perth,
Australia and by ANSTO of Sydney,
Australia are being formulated. Bulk sampling of oxide
mineralization from large diameter drill core and from surface
trenches will take place this fall. The bulk sample will be
processed in a pilot plant test in 2011 as part of a planned
prefeasibility study.
The metallurgical testing is ongoing on oxide samples from an NI
43-101-compliant inferred resource of oxide mineralization
consisting of 8.0 million tons averaging 3.6% REO. Nearly all of
this material is sufficiently close to the surface for projected
mining by open pit methods. The oxide resource is part of a larger
total inferred resource estimated at 17.5 million tons averaging
3.5% REO, using a 1.5% REO cutoff grade (see news release dated
May 26, 2010). The oxide zone
mineralization extends from surface to depths of 400 to 500 feet.
Excellent exploration potential for expansion of the oxide zone is
being tested currently by a program of step-out drilling, while
in-fill drilling is directed at an upgrade of the resource
category.
The current testing program conducted on this oxide
mineralization is designed to take advantage of the unique mode of
mineral occurrence of the REE mineralization. The mineralization is
characterized by fine-grained REE minerals that variably adhere to
the surfaces of the coarser gangue (non-REE-bearing) minerals. The
REE minerals in oxide mineralization from the resource area are
nearly all from the bastnasite group-listed in decreasing order of
abundance: synchysite, parisite, and bastnasite, with generally
minor monazite.
Most of this news release is derived directly from an MSRDI
progress report received in late July
2010.
Summary
In early 2010, MSRDI initiated confirmatory preconcentration and
leaching tests on a large oxide sample that was collected near
surface in the fall of 2009 from a drill site (location of
drill-holes RES 09-3, 3A, and 6) on the Bear Lodge project. The
head grade of this sample ranges from 8 to 9% REO. The primary
objective of this investigation was to confirm the potential for
upgrading (preconcentration) and leaching that was previously
demonstrated on the 2008 drill core samples of oxide mineralization
averaging about 4.4% REO (see news releases dated July 15, 2009 and September 29, 2009).
The current study was conducted on a series of 50-lb oxide
samples. Results indicate clearly that the proposed upgrading
technique, consisting of mild scrubbing/attritioning and size
separation, is effective. Some crushing may be required, but much
of the mineralized material disaggregates easily and will not
require a crushing step. Using this process it is technically
feasible to obtain preconcentrate grades of 15 to 21% REO in the
fine fraction, with an REO recovery ranging from 60 to 90%.
Recovery percentage is dependent on the size of the fine product
(-48 mesh to -500 mesh), which amounted to 26 to 43 wt.% of the
original sample. In practice, the best size fraction of the fines
(-48 mesh to -500 mesh) to be retained will be determined by a
cost/benefit analysis.
The subsequent hydrometallurgical step conducted on the
preconcentrated (upgraded) product indicates that leaching with
hydrochloric acid (HCl) is more effective than sulfuric acid
(H(2)SO(4)) and gives REO extractions that range from 80 to 90%.
However, HCl is more expensive than H(2)SO(4) and potentially has
associated inherent transportation, storage, and environmental
considerations. Thus, economic factors dictate the necessity to
regenerate HCl from the spent solution. The testing by MSRDI
indicates that it is feasible to regenerate HCl in a process that
uses H(2)SO(4), a less costly and environmentally accepted reagent.
The result of the REO extraction would be precipitation of the REO
values into a marketable bulk oxalate product. A conceptual
flowsheet was prepared, based on the upgrading, leaching, and
precipitation steps described above. Preliminary capital and
operating costs are being estimated for the proposed processing
plant as part of a Scoping Study (PEA) in progress.
The next phase of testwork will evaluate additional upgrading
and leaching studies on 250 to 500-lb oxide samples from throughout
the deposit to obtain process engineering data for the forthcoming
proposed pilot plant test and prefeasibility study.
Mineralogy & REO Distribution
An initial mineralogy study of unprocessed -6 mesh material from
the large oxide sample shows a mineral assemblage that is
summarized in Table 1. The study was conducted by the Colorado
School of Mines Advanced Mineralogy Research Center in Golden, Colorado.
Table 1. Mineralogy of Large Sample Collected from Surface in Fall 2009
----------------------------------------------------
Mineral Phase Abundance
----------------------------------------------------
Biotite 26
----------------------------------------------------
K feldspar 21
----------------------------------------------------
Fe-Mn oxides 16
----------------------------------------------------
Barite 2
----------------------------------------------------
Apatite 1
----------------------------------------------------
Ilmenite and rutile 1
----------------------------------------------------
Other minor silicates and oxides 7
----------------------------------------------------
Bastnasite-group minerals 20
----------------------------------------------------
Monazite 2
----------------------------------------------------
Mn+Fe(REE) 3
----------------------------------------------------
REE-nano 2
----------------------------------------------------
The phases identified as Mn+Fe(REE) and REE-nano are Mn and Fe
oxides that contain sub-micron REE phases that are inextricably
associated with the Mn-Fe oxides. These phases are likely to be
Ce-dominant (cerite and cerianite) and contain Ce in the 4+ valence
state.
Table 2. REO distribution of the various rare earths in the
average grade (3.62% REO) oxide zone mineralization
-------------------------------------------------------------------------
Parameter REO Oxide Distribution %
-------------------------------------------------------------------------
Cutoff (%REO) 1.5
Million Tons Resource 8.0
Tonnage Factor (ft(3)/ton) 13.7
%REO 3.62
Million lbs REO 582
-------------------------------------------------------------------------
%Cerium Oxide Ce(2)O(3) 1.66 45.9
%Lanthanum Oxide La(2)O(3) 1.06 29.3
%Neodymium Oxide Nd(2)O(3) 0.52 14.4
%Praseodymium Oxide Pr(2)O(3) 0.16 4.4
%Samarium Oxide Sm(2)O(3) 0.088 2.4
%Gadolinium Oxide Gd(2)O(3) 0.045 1.2
%Yttrium Y(2)O(3) 0.032 0.9
%Europium Oxide Eu(2)O(3) 0.021 0.6
%Dysprosium Oxide Dy(2)O(3) 0.018 0.5
%Terbium Oxide Tb(2)O(3) 0.0075 0.2
%Erbium Oxide Er(2)O(3) 0.0020 0.1
%Ytterbium Oxide Yb(2)O(3) 0.0012 (less than) 0.1
%Lutetium Oxide Lu(2)O(3) 0.00016 (less than) 0.1
%Holmium Oxide Ho(2)O(3) 0.00100 (less than) 0.1
%Thulium Oxide Tm(2)O(3) 0.00015 (less than) 0.1
-------------------------------------------------------------------------
Results of Scrubbing/Attrition Tests
Screening of the raw run-of-mine (ROM) material produced the
results displayed in Table 3, and show that the minus 1/4 inch
material contains over 93% of the REO. Scrubbing/attrition
optimization tests were run on -1/4 inch Bear Lodge project
mineralization with a 1.0 liter Lightnin Attrition Scrubber test
unit.
Table 3. Distribution of REO in the +1/4 inch and -1/4 inch
Fractions
-------------------------------------------------------------------------
% REO % REO
Grams % Weight Assay Distribution
-------------------------------------------------------------------------
+1/4" 9100 46.96 1.12 6.52
-------------------------------------------------------------------------
-1/4" 10280 53.04 14.22 93.48
-------------------------------------------------------------------------
Total Ore 19380 100 8.07 100
-------------------------------------------------------------------------
The favorable results shown in Table 4 included 60-minutes
retention time, 38% solids, and 1000 rpm attrition speed on the
minus 1/4 inch fraction of ROM mineralization.
Table 4. Preconcentrate upgrading at varying sizes gives the
following results on the total ROM mineralization (Note: REO
Distribution equals % recovery of the ROM material.)
-------------------------------------------------------------------------
REO
Product W t. (%) REO (%) Distribution
-------------------------------------------------------------------------
-500 Mesh 28.60 21.68 79.10
-325 Mesh 32.30 20.60 84.80
-200 Mesh 35.60 19.49 88.60
-100 Mesh 38.10 18.54 90.20
-48 Mesh 40.10 17.83 91.10
-------------------------------------------------------------------------
The minus 500 mesh material produced the highest grade and
lowest weight retained of product that would be sent to the
chemical treatment plant. Further testing should establish the
optimal size fraction for use in hydrometallurgical processing, and
whether recycling of coarser fractions will prove to be beneficial
for enhanced recovery.
Flotation and other tests are being run on the minus 500 mesh
product to see if further upgrading above 21% REO can be
accomplished.
Discussion on Scrubbing/Attritioning Test Results
The results of scrubbing and attritioning tests conducted on the
large oxide ROM sample clearly confirm that upgrading of the
contained REO values (from 8.4% REO) in this sample can be
accomplished by simple scrubbing/attritioning of the ROM material
and/or the minus 1/4-inch crushed product. The grade of the
preconcentrate (upgraded product) varies from higher grade REO (16
to 21% REO) in about 26 to 45 wt.%, with REO recoveries ranging
from 60 to 90% depending on the size fraction (-48 mesh to -500
mesh).
The results show conclusively that nearly 47% of the total feed,
containing only 6.5% of the total REO, can be discarded (rejected)
after simple scrubbing of ROM ore and screening at 1/4-inch. In
this case the minus 1/4-inch product assays 14.2% REO in about 53
wt.% of the original sample, and contains about 93% of the total
REO content.
The best scrubbing and attritioning techniques allow an upgraded
preconcentrate product with REO values up to 21.7%, with a recovery
of 79.1% from the finest fraction (-500 mesh) in 28.6% wt.% of the
original sample. On the other hand, higher recoveries (up to 90%)
are obtained from minus 48 mesh or minus 100 mesh product with a
grade of 18.5 to 17.8% REO. Preliminary tests indicate that all
rare earths are recovered in the same general proportions as their
original distributions (Table 2).
Results of Leaching Tests
Early tests showed that leaching with hydrochloric acid produces
consistent extractions in the range of 93 to 96%. Tests using
sulfuric acid consistently produced about 80% recovery. It was
initially thought that the high cost of hydrochloric acid and
environmental considerations would make the process prohibitively
expensive unless a regeneration process could be developed.
Literature reviews show that processes are available to
recover/regenerate HCL at a concentration of 20% using H(2)SO4.
Subsequently, leach tests were performed using 20% HCL instead of
the 36% HCl used in early tests. Results indicate that extractions
up to 96% REO can be achieved using 20% HCL. Further optimization
tests are planned to determine the best acid concentration for the
leaching.
Several attempts were made to produce a pure oxalate
precipitate, but the presence of other dissolved elements can cause
problems with either purity or the percent of REO precipitated.
However, the dissolved REO from the pregnant leach solution (PLS)
can be precipitated as an REO - oxalate compound, which is similar
to a rare-earth carbonate concentrate.
Development of Conceptual Flowsheet
There are many possible processing scenarios that can be used to
concentrate and recover REO from Bear Lodge mineralization. All
start with preconcentration by size or gravity methods. The
preconcentrates can be leached with either H(2)SO4 or HCL. Testwork
at MSRDI indicates that leaching with HCL at a concentration of 20%
or less may be economically viable.
HCL leaching becomes feasible if acid regeneration techniques
are utilized. HCL regeneration is achieved by adding H(2)SO4 to a
solution stripped of REO in a distillation apparatus. The
acid-consuming elements, calcium, etc., remain in the still bottoms
as sulfate sludge, while the HCl is condensed and returned to the
process.
The leaching process can be conducted in a one-stage process at
ambient conditions using 20% HCL, or possibly in a three-stage
countercurrent leach using weaker acid. The weak acid leach has the
advantage of producing a leach solution containing fewer
impurities. The weak acid leach must be conducted at elevated
temperatures to give high dissolution, while the 20% leach can be
conducted at ambient temperature. Additional equipment is required
to conduct the countercurrent leach.
Figure 1. Conceptual Flowsheet of Preconcentration Process:
http://files.newswire.ca/675/Rare_Element_Fig1.pdf
Figure 2. Conceptual Flowsheet of Leaching and Concentration Process:
http://files.newswire.ca/675/Rare_Element_Fig2.pdf
Conclusions and Recommendations
The results of the metallurgical test program conducted on the
large oxide sample from the Bear Lodge rare-earth deposit are as
follows.
- The initial wet screening and light scrubbing at +3-inch size would
provide a throw away product amounting to about 10 wt.% of the
original sample, and containing about 1.0% of the total REO value.
- After proper scrubbing and screening at 1/4-inch, it appears
technically feasible to discard an additional 35 wt % of oversize
material with a loss of less than 1.0% of the total REO content.
- Simple wet scrubbing in autogenous or tube milling or log washing of
the ROM mineralization, followed by screening at 1/4-inch, allows
discard of more than 45 wt % oversize material with a loss of less
than 6% of the total REO content. Accordingly, initial scrubbing and
screening is an integral and important step in the development of the
overall flowsheet for treating the oxide mineralization.
- Additional attritioning of the minus 1/4-inch product assaying 14.2%
REO in a Lightning Attrition Scrubber allows further upgrading of the
preconcentrate as shown in Table 3.
- It appears technically feasible to obtain an 18 to 20% REO product
(preconcentrate) in about 40 wt % of the original sample, with a
total REO recovery of about 90%. This light attritioning step would
be an important and integral step in the overall flowsheet for
treating the oxide mineralization. The selection of the best size for
upgrading (preconcentrates) should be based on a cost-benefit
analysis after projecting the capital and operating costs of the
proposed flowsheet (including scrubbing, attritioning and leaching
steps).
- Although both H(2)SO4 and HCl leaching agents are applicable for
dissolving REO from preconcentrates, HCl is found to be a more
effective reagent. More than 90% of the contained REO values from the
preconcentrate are recovered using HCl as the leaching agent.
However, cost and environmental considerations dictate that HCl be
regenerated and recycled in this hydrometallurgical process.
- The dissolved REO values from the pregnant leach solution can be
precipitated as an REO-oxalate compound, which is similar to a rare-
earth carbonate concentrate. Preliminary tests indicate that all rare
earths are recovered in the same general proportions as their
original distributions (Table 2).
- The HCl remaining in the spent leach solution can be recovered upon
the addition of H(2)SO(4), which drives off HCl acid vapor to obtain
HCl concentration of 20.2% for recycle.
Rare Element Resources Ltd (TSX-V:RES) is a publicly traded
mineral resource company focused on exploration and development of
rare-earth elements and gold on the Bear Lodge property.
Rare-earth elements are key components of the green energy
technologies and other high-technology applications. Some of the
major applications include hybrid automobiles, plug-in electric
automobiles, advanced wind turbines, computer hard drives, compact
fluorescent light bulbs, metal alloys, additives in ceramics and
glass, petroleum cracking catalysts, and a number of critical
military applications. China
currently produces more than 95% of the 130,000 metric tonnes of
rare-earths consumed annually worldwide, and China has been reducing its exports of rare
earths each year. The rare-earth market is growing rapidly, and is
projected to accelerate if the green technologies are implemented
on a broad scale.
ON BEHALF OF THE BOARD
Donald E. Ranta, PhD, PGeo,
President & CEO
Donald E. Ranta, PhD, PGeo,
serves the Board of Directors of the Company as an internal,
technically Qualified Person. Technical information in this news
release has been reviewed by Dr. Ranta and has been prepared in
accordance with Canadian regulatory requirements that are set out
in National Instrument 43-101. This news release was prepared by
Company management, who take full responsibility for content.
Neither TSX Venture Exchange nor its Regulation Services Provider
(as that term is defined in the policies of the TSX Venture
Exchange) accepts responsibility for the adequacy or accuracy of
this release.
SOURCE Rare Element Resources Ltd.
Copyright . 18 PR Newswire