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Preferably, the metal cation is selected from the group comprised of:
— rhodium;
— ruthenium;
— rhenium;
— palladium; — platinum;
— nickel;
— copper;
— iridium;
— iron; — gold.
In particular, the employed alcoholic medium can have a molecular weight
below 100.
Advantageously, the alcoholic solvent or co-solvent is selected from the
group comprised of: — methanol;
— ethanol;
— n-propanol;
— n-butanol; — n-pentanol and their isomers.
Preferably, the alcoholic medium is selected from the group comprised of:
— methanol — ethanol;
— propanol;
— isopropanol.
Nanosized metal catalysts can be employed in many catalytic reactions
such as the selective hydrogenation of organic molecules.
In particular, the up to now known catalysts employed in the selective
hydrogenation of benzene to cyclohexene and of phenol to cyclohexanone
are not able to perform in high yield the target product and imply high
costs, as when palladium based catalysts are required.
In particular, the above described reduction reaction of the or each
metal precursor is carried out at a pressure in the range from 10 and
150 bar, produced by an inert gas, such as, for instance, nitrogen.
In particular, the nanosized catalyst, mono- or poly- metallic, can be
deposited on an inert support, such as — © ?" alumina, silica, magnesia,
zirconia, ceria and other metal oxides.
Also this type of process appears not suitable for large scale
applications. This procedure, in fact, employs as precursors
organometallic derivatives which are very difficult to be synthesized
and very expensive. Moreover, this process does not often enable to
reach a good control of the particles sizes and their morphology.
Moreover, frequently, this method is scarcely reproducible.
These and other features are accomplished with one exemplary process,
according to the present invention, for the preparation of nanosized
metal catalysts through the reduction reaction of at least one metal
precursor carried out by heating in an alcoholic solvent or co- solvent,
whose main characteristic is that the above reduction is carried out
under an overpressure. In this way it is possible to employ a low
molecular weight alcoholic solvent which is easily removable from the
target product.
Summary of the invention It is therefore a first feature of the present
invention to realize a simple and cheap process for the preparation of
nanosized metal catalysts on a large scale resolving the drawbacks of
the conventional methods.
In particular, the or each metal precursor has the formula: MnXy or
HxMnXy, used as that or solvated, where M is a metal cation and X is an
anion selected from the group comprised of:
-
— a halogenide
-
— a carboxylate — a substituted carboxylate
-
— a hydroxide
-
— a carbamate
-
— an aldiminate
In particular, the electrochemical reduction of metal salts is extremely
expensive for large scale applications and frequently does not allow to
control the particles size. Moreover, this process is scarcely suitable
for important transition metals such as Pt, Rh, Ru and Mo, due to low
solubility of their cations when employed as an anode.
It is another feature of the present invention to give a process for the
preparation of nanosized metal catalysts which allows to easily separate
any by-products present in the reaction mixture from the final product.
The main known methods concern processes of electrochemical reduction of
metal salts, chemical reduction of metal salts, the "metal vapors
technique" and the reduction, or decomposition, of organometallic
precursors.
Preferably, the said reduction reaction of the or each metal precursor
is carried out at a pressure from 20 and 100 bar. In particular, the
reduction of one or more metal precursors together at the same time can
be carried out at a temperature from 50 to 400 0C and preferably from 50
to 250 0C.
Otherwise, the nanosized catalyst can be employed as not supported
catalyst . Advantageously, the support can be directly introduced in the
reactor where the reduction of the metal precursor or precursors is
carried out or, otherwise, at room temperature in a successive step
after the reduction reaction. The process of synthesis of metal
nanostructured catalysts as above described allows to avoid on the one
hand the use of expensive and difficult to be synthesized organometallic
precursors and on the other hand the employment of high boiling solvents
such as glycols and polyglycols, in particular diethylene- and
triethylene- glycol, hardly removable from the final product after the
reduction of the starting metal precursor.
The method of the chemical reduction of the metal salts is based on the
use of reducing agents such as metal hydrides or hydrogen itself, and of
a stabilizing agent, generally a polymer. Otherwise, in order to avoid
the eventual poisoning of the product by the reducing agent and to
perform the reduction under higher control, a method of reduction in an
alcohol has been proposed. Because the reduction in the presence of an
alcohol generally needs high temperature to be efficient and complete,
the reduction in the presence of polyols such as ethylene glycol, but
mainly diethylene glycol and triethylene glycol, has been preferred.
In particular, nanostructured metal catalysts offer excellent catalytic
properties and many advantages in comparison with corresponding
catalysts based on metal particles with larger dimensions. Their main advantage is represented by a significant increase of the surface
activity which allows to greatly improve the performances of catalytic
processes where they are employed. As a consequence, different synthetic methods have been studied in order to produce Nanostructured metal
catalysts.
Otherwise, not very often, high boiling alcohols such as n-octanol are
employed, as described in WO 9604088. Both polyols and high molecular
weight alcohols present the obvious drawback of a difficult removal from
the final product and thus are not suitable for a large scale production
of nanocatalysts. Another method for the production of Nanostructured
metal catalysts is based on the "metal vapors technology" . For this
approach very expensive and rarely available reactors are necessary,
thus appearing not suitable for large scale preparations. Finally, a
further method for the production of Nanostructured metal catalysts
involves the reduction, or decomposition, of organometallic precursors.
According to another aspect of the present invention, the nanosized
metal catalyst as above described can be advantageously employed in
hydrogenation, dehydrogenation, oxidation, hydroxylation,
cis-dihydroxylation and in C-C bond formation reactions.
In particular, the nanosized metal catalyst as above described can be
advantageously employed in the selective hydrogenation of organic
substrates, in particular in the reaction of selective hydrogenation of
benzene to cyclohexene, of phenol to cyclohexanone and of benzaldehyde
to benzyl alcohol.
Advantageously, a stabilizing agent can be also employed, such as a
polymer or a copolymer, for instance poly-N-vinyl-2-pyrrolidone (PVP) ,
polyethylenoxide, polypropylenoxide, polyacrylates, or their copolymers.
Moreover, a base and/or an inorganic or organic salt, such as alkali or
alkali earth hydroxides and/or their salts as acetates, oxalates,
formates, amines etc. can be employed as a stabilizer. In this case the
use of the polymer as stabilizing agent is not necessary.
It is a particular feature of the present invention to produce a
nanosized metal catalyst that is particularly efficient, in terms of
activity and selectivity for specific catalytic reactions.
It is a further feature of the present invention to give a process for
the preparation of nanosized metal catalysts which allows to obtain a
final product with improved characteristics, in terms of average
diameter and size distribution of the metal particles, with respect to
the known Nanostructured catalysts.
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