ISSN 0020-1685, Inorganic Materials, 2006, Vol. 42, No. 3, pp. 310–315. © Pleiades Publishing, Inc., 2006.
Original Russian Text © N.V. Lebukhova, N.F. Karpovich, 2006, published in Neorganicheskie Materialy, 2006, Vol. 42, No. 3, pp. 357–362.
Carbothermic Reduction of Cobalt and Nickel Tungstates
N. V. Lebukhova and N. F. Karpovich
Institute of Materials Science, Khabarovsk Scientific Center, Far East Division, Russian Academy of Sciences,
Tikhookeanskaya ul. 153, Khabarovsk, 680042 Russia
e-mail: LNV1@yandex.ru
Received September 26, 2005
Abstract—Data are presented on the formation sequence of metallic, carbide, and intermediate oxide phases
in the carbon reduction of CoWO and NiWO . The surface reaction between CoWO particles and solid car-
4
4
4
bon yields the mixed carbide Co W C, while the reaction with the CO originating from carbon vaporization
6
6
yields the intermetallic phase Co W . The initial stage of the solid-state and gas-phase reduction of NiWO
7
6
4
yields a solid solution of tungsten in nickel (~10 at % W), Ni W, and, presumably, the NiWO –WO eutectic.
4
4
3
The solid solution reacts with carbon to form Ni W C and with CO to form filamentary tungsten crystals.
2
4
DOI: 10.1134/S0020168506030174
INTRODUCTION
oxide phases in the carbothermic reduction of cobalt
and nickel tungstates at different temperatures.
Coreduction of mixtures of oxides, oxide solid solu-
tions, and chemical compounds is used in the extraction
of elements from slags and mineral associations, syn-
thesis of intermetallics, processing of slime waste, and
production of cermets [1–3]. In recent years, intense
scientific and technological interest has been centered
on the application of tungstate systems in the prepara-
tion of composite powders of hard tungsten alloys,
which are known to combine nanostructure with a
highly homogeneous distribution of tungsten carbide
and the metallic binder.
EXPERIMENTAL
CoWO and NiWO were prepared via coprecipita-
4
4
tion from equimolar solutions of divalent-metal nitrates
and ammonium paratungstate. The precipitates were
calcined in air, first at 600 and then at 1000°C for 2 h.
The resultant powders were investigated in the as-pre-
pared state or after grinding in a Petsch PM-400 plane-
tary ball mill. The particle size distribution was evalu-
The known processes for the synthesis of such com- ated using a Biolam M optical microscope (1000×) and
posites [4, 5] involve two consecutive steps: hydrogen Analyzette 22 Comfort laser analyzer. The average par-
reduction of mechanically activated oxide mixtures to ticle diameter was determined as
metals and carbonizing of tungsten with carbon or car-
bon-containing gases. One promising way to ensure
d =
d n / ni,
i i
structural homogeneity of such mixed-phase materials
∑
∑
is to use tungsten oxide compounds, e.g., CoWO and
i
i
4
NiWO , as starting reagents. The preparation process
4
can be reduced to one heat-treatment step by using car- where n is the number of particles examined and i is the
bon as both a reductant and carbonizing agent.
number of size ranges. The reductants used were car-
bon black (RF Standard GOST 12222-78) and CO. In
our preparations, we used stoichiometric (1 : 1) mix-
tures to obtain metals and also mixtures containing up
to 50% excess carbon. Reduction was carried out in
flowing argon during heating at a rate of 5°C/min or
under quasi-isothermal conditions in the furnace of a
MOM Q-1000 Paulik–Paulik–Erdey thermoanalytical
system and also in an SNOL 0.2/1250 programmed
tubular furnace in flowing CO. The gas flow rate was
Despite the wide use and practical importance of
reactions between metal oxides and solid carbon, such
reactions have been studied in less detail than reduction
with gases. There is only limited information regarding
the phase formation sequence in the reduction of cobalt
and nickel tungstates with carbon or natural gases [6–8].
Hydrogen reduction processes have not yet been inves-
tigated in detail. Data on the conditions of carbothermic
reactions, the role of CO, and the distribution of metals
over intermediate oxide phases during the reaction are
missing.
1
5 l/h in both cases. The extent of reduction, α, was
evaluated from thermogravimetric (TG) curves as the
ratio of the weight loss from the sample to the maxi-
The purpose of this work was to establish the forma- mum possible gas release, corresponding to the com-
tion sequence of metallic, carbide, and intermediate pletion of the reaction and formation of the metal.
3
10