Article
Figure 3. Kinetic plots for hydrosilylation of silsesquioxanes 1−4, and 7 with dimethylphenylsilane (a), in the presence of Karstedt’s catalyst, measured
by in situ FT-IR (the formation of products 1a−4a and 7a). Reaction conditions: toluene; 95 °C; m /V = 100 mg/mL; Pt (dvs) catalyst; [POSS]:
POSS
tol
2
3
−
4
[
silane]:[platinum] = 1:3:(3 × 10 ).
the predominant formation of β products (1b, 4b, and 7b over
4%) and a greater number of dehydrogenative coupling
required for total hydrosilylation of CC bonds in the reactions
between phenyldimethylsilane and POSS derivatives (1−3)
reached 397, 1197, and 897 min, respectively. So, for the POSSs
with alkyl inert groups, the reaction was faster than that for the
aromatic (phenyl) group, although, at the beginning of the
process, the reaction of 2 was faster than that of 3. However,
eventually more time was needed to complete the addition of
Si−H to CC bonds. Additionally, the smaller the alkyl
substituent, the shorter the reaction (time < time ). The
reason for such a reactivity could be the different electronic
effects and steric hindrances of the alkyl and aryl groups. In the
case of IC-POSSs with the same iBu inert cage groups and
different moieties protruding from the cage dimethylvinylsilyl
(1), phenylmethylvinylsilyl (4), and diphenylvinylsilyl (7), the
reaction time increased with increasing steric hindrance of the
functional groups. The reaction time was 397 min for 1, 867 min
for 4, and 2522 min for 7, and differences in the reactivity and
reaction times were quite significant.
9
products and α products. The conducted experiments showed
that the rhodium catalyst was the least selective in hydro-
silylation of IC-POSS with phenylsilanes. All catalysts showed
less selectivity in the reactions with the more sterically crowded
−
2
silane b. Although in the initial tests with 10 mol of C1−C4
−
3
and 10 mol of C5 of metal loading per 1 mol of Si−H group we
obtained products with similar conversion of the reagents and
selectivity, we decided to reduce the catalyst loadings. It turned
out that C5 proved to be in all cases the most selective catalyst
with the lowest metal loading (10− mol of platinum per Si−H
group). On the basis of the preliminary results, we decided to use
Karstedt’s catalyst, as the most efficient hydrosilylation
promoter, in our further study.
iBu
octyl
4
In Situ FT-IR Experiments. On the basis of earlier results,
we decided to perform several additional experiments using in
situ FT-IR spectroscopy to more precisely explore the effect of
the silsesquioxane structure on the reaction time. The applied
methodology allowed precise monitoring of the experiments by
measurement of the reaction trends and profiles in real time,
providing highly specific information, e.g., about the kinetics,
reaction initiation, and conversion of the reagents in the course
of the reaction. For this purpose, we chose simple
dimethylphenylsilane (a) and two groups of silsesquioxanes:
the first of 1−3 with the same dimethylvinylsilyl opening moiety
and different inert groups in the POSS cage and the second of 1,
Figure 4 shows 2D and 3D illustrations of the disappearance
of the characteristic Si−H signal in the course of an exemplary
hydrosilylation reaction of 7 with dimethylphenylsilane, which
leads to complete conversion of the substrates, selective
functionalization of all functional groups, and formation of 7a.
Hydrosilylation of Open-Cage Silsesquioxanes with
Phenylsilanes. The positive results achieved in the catalytic
tests of hydrosilylation of selected IC-POSSs with silanes a and b
prompted us to extend the range of POSSs and silanes. We
decided to extend the described method to functionalization of
all obtained IC-POSSs (1−9). Our choice of silanes was based
on the tests with silanes with different steric hindrances (Tables
2 and 3). Therefore, we decided to perform the next experiments
with silanes containing a dimethylsilylhydride moiety. In the
earlier selected reaction conditions, new trisubstituted deriva-
tives were obtained in the stoichiometric reaction of IC-POSSs
(1−9) with phenylsilanes (Scheme 4). The molar ratio was as
follows: [IC-POSS]:[silane a/b/c/d]:[platinum] = 1:3:(3 ×
4, and 7 with the same inert group and different types of
vinyldiorganosilyl moieties. In these experiments, 1 equiv of
silsesquioxane (1−4 or 7), 3 equiv of dimethylphenylsilane, and
1
mL of toluene were added to a glass reactor equipped with an
in situ FT-IR probe and placed in an oil bath at 95 °C, and then
−
4
1
0
mol of platinum (per each Si−H group) of Karstedt’s
catalyst was added. The progress of hydrosilylation of selected
silsesquioxanes with PhSiMe H in the presence of Karstedt’s
2
complex was possible to control by monitoring of the high
−
1
−4
absorption bands assigned to Si−H units (v = 822 cm ), which
10 ). For 1−6, we conducted the reaction for 24 h, and for 7−9,
decreased over time. All results are shown in Figure 3.
the reaction was for 48 h. Using silane e in the stoichiometric
reactions with silsesquioxanes, various types of cross-linked
structures were obtained, which is related to the presence of two
The rate of hydrosilylation of the CC bond was found to
strongly depend on the silsesquioxane structure. The time
F
Inorg. Chem. XXXX, XXX, XXX−XXX