Uranium
Mining, and Processing
Primary Uranium Minerals
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|
Uraninite
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UO2.x
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Pitchblende
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UO2.x (x =
0.2-0.6)
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Coffinite
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U(SiO4)1-x(OH)4x
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Brannerite
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(U,
CA, Y, CE)(Ti, Fe)2O6
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Davidite
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(REE)(Y,
U)(Ti, Fe3+)20O38
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Thucholite
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Thorium-
and uranium-bearing organic material
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Secondary Uranium Minerals
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Autunite
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Ca(UO2)2(PO4)2·8-12
H2O
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Carnotite
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K2(UO2)2(VO4)2·1-3 H2O
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Gummite
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A
mixture of uraninite and secondary uranium minerals of variable composition
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Seleeite
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Mg(UO2)2(PO4)2·10
H2O
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Torbernite
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Cu(UO2)2(PO4)2·12
H2O
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Tyuyamunite
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Ca(UO2)2(VO4)2·5-8
H2O
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Uranocircite
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Ba(UO2)2(PO4)2·8-10
H2O
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Uranophane
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Ca(UO2)2(HSiO4)2·5
H2O
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Zeunerite
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Cu(UO2)2(AsO4)2·8-10
H2O
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Conventional
Agitation Leach
Uranium is highly soluble as a
sulfate in sulfuric acid, and as a carbonate in alkaline solution in the U6+ valence state. If it occurs in the U4+ state it must oxidized before becoming
soluble; this is a two-step reaction, with a chemical oxidant first used to
oxidize iron, for example, from the ferrous Fe2+to the
ferric Fe3+ state, and in turn the oxidized iron causes
oxidation of the uranium from U4+ to U6+
The first step in the agitated
leaching process is to finely grind the ore (typically to about 300- to
500-micron size) in a water–slurry mixture. The ore slurry is thickened to a
higher density (about 50 percent solids), and then forwarded to a series of
stirred tanks where the leaching takes place. Acid and oxidants are added—for
acid leaching, temperatures of 50°C to 60°C are used, whereas alkaline leaching
requires a higher temperature of 90°C to 95°C. The tanks can be at normal
atmospheric pressure or pressurized. Acid and a suitable oxidant (e.g., oxygen,
hydrogen peroxide, sodium chlorate, or manganese dioxide) is added to oxidize U4+ to U6+. The acid is the
lixiviant—or liquid solution—that dissolves the metal in the U6+ sulfate form.
Alternatively, a mixture of
sodium carbonate and sodium bicarbonate can be used if the ore gangue has a
high acid consumption. The choice of a carbonate or acid leaching route is
based on the consumption of each chemical by the ore matrix or host rock, reagent
availability, and environmental and economic considerations. The choice of
oxidant is based on many of the same considerations as the choice of lixiviant.
In either acid or alkaline
leaching, the ore slurry—with the uranium in solution—requires the separation
of the solids from the uranium-containing liquid. This is commonly performed
using filters (horizontal belt, pressure, or drum filters) or a series of
thickeners or decanters. In both cases, the slurry is washed with acidified
water for the acid leach process, or water only in the case of the alkaline
leach option, in what is termed countercurrent decantation. The washed solids,
now referred to as tailings, are generally neutralized with lime or other
alkaline material if acid leaching of the ore was employed to extract the
uranium. The tailings are then forwarded to a tailings impoundment facility for
storage.
The clear liquid containing the
uranium in solution is further purified using a solvent extraction or ion
exchange technology. After uranium removal, the solution—known as “raffinate”
or “barren solution”—is recycled back to the filters or decantation process.
The concentrated, purified uranium solution (referred to as “pregnant solution”
or “eluate”) is advanced to a precipitation stage using hydrogen peroxide,
magnesium oxide, or sodium hydroxide. The resultant uranium precipitate is then
filtered or centrifuged, dried or calcined, and packaged into suitable drums
for shipping
Uranium Enrichment
Uranium when mined is in the form of a stable
oxide (U3O8) or peroxide. After initial purification to remove impurities,
which is done by heating strongly and subsequent agglomeration and crushing,
the purified uranium oxide is then reduced in a kiln by hydrogen to form
uranium dioxide by the following reaction.
U3O8 +
2H2 → 3UO2 + 2H2O
The reduced oxide of uranium is then reacted with
hydrogen fluoride to form uranium tetrafluoride which is further reacted with
gaseous fluorine to produce uranium hexafluoride which is then used as a
starting input material in an enrichment plant. The reactions by which the
above mentioned conversion takes place are given below.
UO2 + 4HF → UF4 + 2H2O
UF4 + F2 →
UF6
Enrichment Methods
Gaseous diffusion: Uranium
hexafluoride is first heated and converted from a solid to a gas. It is then
made to pass through a series of semi-permeable membranes which are a part of
compressors and converters. Since the U-235 isotope molecules are lighter than
the U-238 isotope molecules, they tend to diffuse faster through the pores of
the membranes and hence can be separated. The two streams of gas produced have
different U-235 concentrations and hence are separated. Several repetitions of
this process are required to obtain concentrations of U-235 isotope in the gas
are high enough to the extent that it can be used in a nuclear reactor. [3] The
enriched UF6 gas is then allowed to liquefy and subsequently solidify before
being transported to a nuclear power plant. This technology contributes to
about 27% of the world's enriched uranium.
Gas centrifuge: This
method of uranium enrichment also utilizes the difference in mass of the
uranium isotopes are an aid in their separation. A gas centrifuge system
consists of several cylinders which rotate at high speeds that create a strong
centrifugal force within. The U-238 molecules being heavier tend to line the
outer wall of the cylinder while the lighter U-235 molecules stay more towards
the center. The two streams are separated and the depleted stream is pumped
back for further U-235 extraction. This method of enrichment proves to be more
energy efficient as compared to the diffusion method by a factor of 50:1 and
hence is currently used to produce 50% of the world enriched uranium.
Grades of Enriched Uranium
Different
grades of uranium can be produced through enrichment which then has different
applications. These are broadly classified under the following categories.
Slightly Enriched Uranium (SEU): This
has a concentration of 0.9% to 2% of U-235 isotope and is most commonly used as
a substitute to natural uranium in heavy water reactors. One benefit of using
this instead of natural uranium is that lesser quantity of fuel is required to
produce the same amount of energy and as a result, the amount of nuclear waste
to manage at the end of the production is significantly reduced.
Low Enriched Uranium (LEU): This
has a concentration lower than 20% of U-235 isotope. It is commonly used in
light water reactors and research reactors.
Highly Enriched Uranium (HEU): This
has a concentration higher than 20% of U-235 isotope. When the concentration is
over 80%, it is termed as weapons grade uranium which is necessary for a
nuclear chain reaction to occur. Highly Enriched Uranium with concentrations
greater than 40% is used in naval reactors in powering submarines and in fast
neutron reactors.