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Leaching and Extraction of Uranium from
the Red Silica Veins Intruding the
Younger Granites of Gabal Al-Aglab,
North Eastern Desert, Egypt.
By
Gamal S. Awadalla,
Nuclear Materials Authority
Sample
No. 9 10 11 12 13 14 Average
Trace elements (ppm)
Ba 215 199 320 405 212 202 258.83
Ce 12 25 54 27 11 26 25.83
Cr 86 78 93 49 67 99 78.67
Ga 62 79 57 77 51 71 66.17
Hf 12 10 15 16 17 22 15.33
La 19 32 48 37 30 27 32.17
Nb 10 22 16 19 32 24 20.50
Pb 99 109 121 138 154 114 122.50
Rb 72 55 74 63 53 51 61.33
Sr 81 86 93 96 101 89 91.00
Ta 23 26 29 19 24 27 24.67
Y 19 30 35 41 39 26 31.67
Cu 10 12 13 14 10 11 11.67
W 56 99 89 84 26 68 70.33
Zn 161 135 166 214 189 146 168.50
Zr 263 215 240 199 206 228 225.17
Th 112 183 169 206 159 168 166.17
U 512 830 644 590 811 843 705.00
Th/U 0.22 0.22 0.26 0.35 0.20 0.20 0.24
XRD pattern of separated heavy mineral fraction in jasper
(A) Alunogen, synthetic Al2(SO4)3, 17H2O
(P) Pahasapaite, synthetic (Ca, Li) 11 Li 8 Be 24 (PO4)24, 38H2O
(S) Scheelite, synthetic CaWO4
(H) Hematite, synthetic Fe2O3
-Jasper is the ultimate product of silicification of this granite in
which the minerals are progressively replaced by jasper.
-The silicified granite zone is surrounded by a zone of
kaolinized granite, which grades outwards into the fresh
granite.
-Jasper is commonly developed as fracture fillings associated
by hematitization in presence of both shearing and faulting
-The uranium content in jasper reaches to 843 ppm and
thorium content reaches to 206 ppm
-Geochemically, XRF and ESEM (Environmental Scanning
Electron Microscope) analyses show that the Gabal Al-Aglab
jasperoid rocks are enriched in Th, U, Zr, W and LREEs (Ce
and La)
Chemical Analyses of major oxides and trace elements
of jasper working samples
Trace elements,
ppm
Major oxides,
wt%
199 Ba 91.2 SiO2
9 Li 0.03 TiO2
22 Nb 2.42 Al2O3
109 Pb 4.86 Fe2O3
86 Sr 0.06 MnO
196 Th 0.61 CaO
830 U 0.11 Na2O
135 Zn 1 K2O
215 Zr 1.05 H2O+
0.03 CO2
0.02 SO2
101.39 Total
Grinding the ore to -60 mesh size (250 µm
•Sulfuric acid under proper leaching conditions was applied
•uranium was then extracted using the synergistic solvent mixture
of D2EHPA and TOPO in kerosene -
From the studied leaching parameters,
it can be concluded that for 90 % U leaching efficiency of G. Al
glab jasper veins,
the optimum conditions would include only 30 g/L H2SO4 in a S/L
ratio of 1:1 for 3 hours at room temperature.
-Iron and some other impurities were removed from the leach
liquor by precipitation at pH 3.5 using lime water
- Al Aglab leach liquor (1.5 gU/L)
Equilibrium data of uranium in D2EHPA (0.25M) in absence
and presence of TOPO from Al Aglab leach liquor.
TOPO,
M
Uranium, g/L Doa
Organic
phase
Aqueous
phase
0.00
0.02
0.04
0.06
0.08
1.11
1.14
1.35
1.43
1.41
0.39
0.36
0.15
0.07
0. 09
2.82
3.17
9.00
20.43
15.67
The molar ratio at synergism of about 4D2EHPA : 1TOPO in
kerosene would be considered optimum.
{0.25M D2EHPA: 0.06M TOPO}
Conclusion
Petrographical and mineralogical studies upon some
mineralized samples from Gabal Al-Aglab red silica veins
(jasper) indicated the presence of the secondary uranium
minerals uranophane and beta-uranophane besides zircon,
epidote and allanite and iron oxide minerals that play an
important role in uranium enrichment. Leaching studies of a
representative mineralized sample assaying 830 ppm U
resulted a leaching efficiency of 90 % under the determined
optimum conditions.
The latter involved 30 kg/t sulfuric acid in a S/L ratio of 1/1
for 3 hr at room temperature upon an ore material of grain size
of -60 mesh (250 µm). These conditions are more mild than
those used for comparable El Missikat and El Erediya
mineralized silica veins; a matter which might be due to the
partial presence of primay minerals.
The remaining unleached 10 % of input uranium in the
studied ore Al Aglab material might be due to their presence in
some refractory mineral (allanite and/ or thorite)
The leached uranium was recovered by the synergistic
mixture D2EHPA/ TOPO in kerosene after a prior purification
steps of the leach liquor through precipitation of impurities at
pH of about 3.5. Application of the McCabe- Thiele diagram
resulted in 3 extraction stages at a flow rate (O/A) of about 0.3.
For stripping, 1M sodium carbonate solution was used and
application of the corresponding McCabe- Thiele diagram
resulted in only 2 stripping stage at a flow rate (O/A) of about
2.15.