NEW CLUSTER-TYPE RHODIUM SELENOCHLORIDES
199
shows how the output capacity of the catalysts for
methanol, ethanol, and acetic acid depends on
the process temperature and support pore size. As
can be seen in Fig. 3a, the highest output capacity
on its texture characteristics. This makes it possible
to regard nanovoids in porous silicas and carbon ma-
terials as nanoreactors whose size affects the selec-
tivity of oxidative carbonylation of methane on rho-
dium selenochlorides [13]. It should be noted that
none of the catalyst samples containing rhodium sele-
no-chlorides was carbonized in the tests, in contrast
to the catalyst prepared by impregnation with rhodium
trichloride and ammonium metavanadate.
1
1
for methanol (1.5 mol g h ) is observed on the
cat
Rh Se Cl/KSS-3 sample with a support pore size of
3
3
3
nm. Acetic acid is mostly formed on Rh Se Cl/KSS-4
3 3
and Rh Se Cl/KSS-5 samples with a pore size of 7
3
3
8
nm. As the support pore size increases to 12 nm,
ethanol becomes the main liquid product of the pro-
cess.
CONCLUSIONS
It was shown in [12] that single-stage synthesis
from methane and carbon monoxide yields methanol
in the presence of nitrogen(II) oxide as oxidizing
agent and iron(III) phosphate as catalyst, and methyl
acetate upon addition of highly dispersed Rh O to
(
1) New cluster-type cubane-like rhodium seleno-
chlorides Rh Se Cl and Rh Se Cl were syn-
4
16 10
4
18 10
thesized and products of their thermal transformations,
Rh Se Cl and Rh Se Cl, were obtained. An analysis
3
3
3
5
2
3
of the vibrational (IR, Raman) and Rh3d , Se3d,
5
/2
the catalyst. A conclusion was made on the basis of
these data that presence of a single active center
and Cl2p3/2 XPS spectra of these compounds sug-
gested the following structure of the rhodium seleno-
chlorides obtained: Rh ( -Se) ( -Se ) Cl (Se Cl )
and Rh ( -Se) ( -Se ) Cl (Se Cl ) , based on the
cubane core [Rh ( -Se) ].
(
FePO ) on the catalyst surface leads to activation of
4
4
3
4
2 3
4
2
2 3
methane to give a methyl radical and, subsequently,
4
3
4
2 4
4
2
2 3
C -oxygenate. Presence of a second closely lying
1
4
3
4
active center (Rh O ) enables carbonylation and
2
3
makes it possible to obtain longer-chain C C -oxy-
(2) The catalytic properties of Rh Se Cl and
4 18 10
2
3
genates.
a product of its thermal destruction, Rh Se Cl, depos-
3 5
ited on various carbon supports were studied in the re-
action of oxidative carbonylation of methane. It was
shown that, in contrast to samples prepared by im-
pregnation of supports with rhodium trichloride, rho-
dium selenochlorides exhibit catalytic activity in car-
bonylation of methane. The output capacity of the pro-
cess for methanol, ethanol, and acetic acid depends on
the method of catalyst preparation and type of a car-
bon support.
It was experimentally demonstrated that oxygen-
containing products are formed in oxidative carbon-
ylation of methane either on a rhodium selenochloride
or in the joint presence of rhodium and vanadium
oxides. The formation of acetic acid on the rhodi-
um-vanadium catalyst can be attributed, by analogy
with [12], to presence of two active centers respon-
sible for activation of methane and its subsequent
carbonylation into acetic acid. Use of rhodium seleno-
chloride instead of rhodium and vanadium oxides can
improve the output capacity for acetic acid by more
than an order of magnitude. In addition, the reaction
of oxidative carbonylation of methane yields ethanol
and ethanol.
(3) A study of the catalytic properties of a mech-
anical mixture of rhodium selenochloride Rh Se Cl
3
3
and silicas with various texture characteristics dem-
onstrated that support nanopores can be regarded as
nanoreactors whose size affects the output capacity
and selectivity of oxidative carbonylation of meth-
ane.
A detailed study of the structure of active centers
of the reaction of oxidative carbonylation of methane
on rhodium selenochlorides is beyond the scope of this
study. The suggested structure of both the starting rho-
dium selenochlorides, Rh ( -Se) ( -Se ) Cl (Se Cl )
REFERENCES
1. Kosmambetova, G.R., Gritsenko, V.I., Strizhak, P.E.,
et al. The Eur. Catalysis Forum EuropaCat-VI ,
31.08 4.09, 2003, Austria, Innsbruck, CD: Abstracts,
2003, Poster 1546.
4
3
4
2 3
4
2
2 3
and Rh ( -Se) ( -Se ) Cl (Se Cl ) , and products of
4
3
4
2 4
4
2
2 3
their thermal transformations, Rh ( -Se)( -Se) Cl
3
3
2
and Rh ( -Se)( -Se) ( -Se )Cl, leads to a conclusion
3
3
2
2
that the starting reagents are activated not only on
rhodium atoms, but on selenium as well. The sub-
sequent transformations of the activated complex and
the qualitative composition of the reaction products
strongly depend both on the nature of a support and
2. Kosmambetova, G.R., Gritsenko, V.I., Strizhak, P.E.,
et al., Ukr. Khim. Zh., 2004, vol. 70, no. 2, pp. 75 80.
3. Sheldon, R.A., Chemicals from Synthesis Gas: Cata-
lytic Reactions of CO and H , Dordrecht: Reidel,
2
1983.
RUSSIAN JOURNAL OF APPLIED CHEMISTRY Vol. 80 No. 2 2007