September 2002
New Route for the Extraction of Crude Zirconia from Zircon
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annealing conditions, the extent of ilmenite reduction under
identical conditions increased with the stoichiometric excess of the
carbon; the same phenomenon may well hold true here, also, with
the excess of MgO.
to occur. Increasing the milling time resulted in an increased extent
of reaction. Thermal analysis of the powders showed a change
from a net endothermic to a net exothermic state after milling for
10 h. Zircon recrystallization was evident as an exothermic peak at
400°–550°C for all samples except that milled for 100 h. The mass
loss associated with the small amount of Mg(OH)2 present shifted
to higher temperature as the milling time increased, indicating that
the reaction was increasing the binding strength of the water. For
50 and 100 h milling, two exothermic peaks also occurred at
800°–900°C, both apparently associated with the emergence of
ZrO2.
Leaching of the as-milled powders showed increasing dissolu-
tion with milling time, although the soluble phase could not be
positively identified because of a lack of crystallinity. However,
the only phase remaining after leaching was zircon, and the
silicon:zirconium ratio was the same as that of the feed powder,
implying that a complex nanostructured phase composed of
zirconium, silicon, and magnesium formed during milling and was
congruently soluble.
XRD of this powder heated at 800°C showed peaks for zircon
and MgO and a broad, weak peak for ZrO2 (essentially identical to
that in the sample heated to 840°C in Fig. 2). Clearly, although the
MgO content was greater, the reaction during milling was not
complete. Heating the powder to 1000°C showed the presence of
t-ZrO2 as the major phase, with somewhat weaker peaks evident
for Mg2SiO4. No evidence supported the presence of either zircon
or MgO. Clearly, a thermal reaction must have occurred between
zircon and MgO, between 800°C and 1000°C, to form ZrO2 and
Mg2SiO4. This reaction correlates with that observed for the
exothermic events in the 50 and 100 h milled powders in Fig. 1,
implying that the increase in the MgO content did not alter the
progress or the extent of the reaction; thus, chemical control must
have been the rate-determining step.
The percentage of each element reporting to the solids after
leaching is presented in Table I, along with the silicon:zirconium
molar ratios. For the unleached powder, the ratio is slightly greater
than the unity expected for zircon; this result is probably attribut-
able to the presence of small amounts of silica in the feed powder.
When the as-milled powder was heated, the total solubility
decreased to 50%–54%. However, the percentage of the various
elements remaining in the insoluble solid changed dramatically.
After the powder was heated at 800°C, the percentage of zirconium
increased from 40% to ϳ81%, whereas the silicon increased from
40% to 61%. This result suggests that heating the powder did not
substantially change the soluble percentage, although some sepa-
ration did occur, with the silicon:zirconium molar ratio decreasing
from 1.05:1 to 0.79:1. Heating to 1000°C caused the most dramatic
changes, with almost 97% of the zirconium reporting to the solid,
along with only 9.5% of the silicon. After 1 h at 1200°C, a similar
result occurred, with 95% of zirconium in the solid; however, more
silicon and magnesium were present in the solid than after heating
to 1000°C. Clearly, heating at or above 1000°C caused substantial
separation of zirconium and silicon, although heating to 1200°C
increased the percentage of both silicon and magnesium in
insoluble phases. The powder obtained after heating to 1000°C
contained ϳ90 wt% ZrO2, 4.5% SiO2, and 5.5% MgO, clearly a
more appropriate starting material for chlorination than pure
zircon.
Thermal processing of the as-milled powders induced crystal-
lization of ZrO2 and Mg2SiO4, of which the latter was soluble,
resulting in separation of the zirconium and silicon. Using a greater
fraction of MgO led to a greater extent of reaction and improved
separation, with Ͼ90% of silicon and magnesium solubilized,
while Ͻ5% zirconium went into solution. The final powder was
ϳ90% ZrO2, 4.5% SiO2, and 5.5% MgO.
References
1F. Farnworth, S. L. Jones, and I. McAlpine, “The Production, Properties and Uses
of Zirconium Chemicals”; pp. 248–79 in Speciality Inorganic Chemicals. Edited by
R. Thompson. Royal Society of Chemistry, London, U.K., 1981.
2T. Puclin, W. A. Kaczmarek, and B. W. Ninham, “Mechanochemical Processing
of ZrSiO4,” Mater. Chem. Phys., 40, 73–81 (1995).
3N. J. Welham, “Investigation of Mechanochemical Reactions between Zircon
(ZrSiO4) and Alkaline Earth Metal Oxides,” Metall. Mater. Trans. B, B29, 603–10
(1998).
4N. J. Welham, “Enhancing Zircon (ZrSiO4) Dissolution by Ambient Temperature
Processing,” AusIMM Proc., 305, 1–3 (2000).
5N. J. Welham and L. Walmsley, “Solubilisation of Zircon by Mechanically-
Induced Solid-State Cation Exchange with Alkaline Earth Oxides,” Trans. Inst. Min.
Metall., Sect. C, 109, C57–C60 (2000).
6N. J. Welham, “Ambient-Temperature Formation of Metal Titanates from Ilmenite
(FeTiO3),” J. Mater. Sci., 33, 1795–99 (1998).
7N. J. Welham, “Mechanically Induced Reaction between Alkaline Earth Metal
Oxides and TiO2,” J. Mater. Res., 13, 1607–13 (1998).
8B. E. Warren, X-Ray Diffraction; pp. 251–314. Dover Press, New York, 1990.
9N. J. Welham, “Mechanical Activation of the Solid-State Reaction between Al and
TiO2,” Mater. Sci. Eng. A, A255, 81–89 (1998).
10N. J. Welham and D. J. Llewellyn, “Mechanical Enhancement of the Dissolution
of Ilmenite,” Min. Eng., 11, 827–41 (1998).
IV. Conclusions
11T. Puclin, W. A. Kaczmarek, and B. W. Ninham, “Dissolution of ZrSiO4 after
Mechanical Milling with Al2O3,” Mater. Chem. Phys., 40, 105–109 (1995).
12N. J. Welham, “A Parametric Study of the Mechanically Activated Carbothermic
Zircon was milled with MgO for up to 100 h, which resulted in
a solid-state reaction. No apparent reaction occurred during the
initial 2 h of milling, during which time size reduction was thought
Reduction of Ilmenite,” Min. Eng., 9, 1189–200 (1996).
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