L. Marchese et al.
ent in the reference titanocene-derived catalysts with respect
to the anchored ones.
A similar behaviour is observed in carveol (2-methyl-5-
(prop-1-en-2-yl)cyclohex-2-enol) epoxidation. Anchored Ti–
POSS-derived catalysts show TON values almost identical
to reference Ti/SBA-15 catalyst (47, 52 and 48, for 2/SBA-
15, 2/SiO2 and Ti/SBA-15, respectively), but they display a
remarkably higher selectivity to endocyclic epoxide than ti-
tanocene-derived systems (ca. 80% vs. 60%, respectively;
see Supporting Information).
Scheme 2. Limonene (1-methyl-4-(prop-1-en-2-yl)cyclohex-1-ene) epoxi-
dation with TBHP.
similar (Table 2). Furthermore, the heterogeneous character
of both catalysts was checked by removing the solid catalyst
by centrifugation and testing the residual liquid mixture for
further reaction. No significant loss of active species was de-
In conclusion, a novel approach for the preparation of
heterogeneous catalysts based on an innovative and versatile
functional titanosilsesquioxane (Ti–POSS-TSIPI; 2) and
mesoporous silicas (SBA-15 and non-ordered silica) is pro-
posed. The spectroscopic characterisation showed that 2 was
effectively anchored with good dispersion on the surface of
both ordered and non-ordered silica supports. Preliminary
catalytic tests in the epoxidation reaction of limonene and
carveol showed that both hybrid materials (2/SBA-15 and 2/
SiO2-Dav) display interesting catalytic activity that was not
sensitive to the morphology of the support. Anchored cata-
lysts showed, in terms of selectivity, good results comparable
to those obtained over the reference titanocene-derived ma-
terials (Ti/SBA-15 and Ti/SiO2-Dav). Finally, this new ap-
proach of functionalisation and immobilisation of Ti–POSS
species may generate a wider interest, especially for mecha-
nistic studies for which a thorough tuning and control of the
chemical surroundings of the Ti active sites is crucial.
Table 2. Catalytic performance of limonene epoxidation over Ti-contain-
ing catalysts.[a]
Catalyst
Ti content[b] C[c]
TON[d]
S[e]
ACHTREUNG
2/SBA-15
2/SiO2-Dav
Ti/SBA-15
Ti/SiO2-Dav 0.29
no catalyst
SiO2
0.23
0.33
0.24
25
39
48
60
4
95
108
192
198
–
88
85
78
82
–
–
n.d.[f]
n.d.
5
–
[a] Reaction conditions: glass batch reactor; 10 mL AcOEt solvent;
358 K; 24 h; 50 mg catalyst; 1.2 mmol TBHP; 1.0 mmol limonene; mesi-
tylene internal standard. [b] Obtained by ICP-AES. [c] Limonene con-
version after 24 h. [d] Turn-over Numbers after 24 h (mol converted sub-
strate/mol Ti). [e] Selectivity to endocyclic limonene monoepoxide after
24 h. [f] Not detected.
Experimental Section
tected (see Supporting Information). Thus, the immobilisa-
tion technique by covalent anchoring does not hinder the
oxidising activity of the TiIV sites and, more significantly, it
is not sensitive to the morphology of the support. When the
epoxidation of limonene is considered, in fact, the choice of
an ordered mesoporous silica with a marked confinement
effect is not essential (this is not the case when simple im-
mobilisation by impregnation is employed[10]) and non-or-
dered commercial silica with large mesopores can be used
successfully.
Anchored catalysts show lower conversions with respect
to reference materials (Ti/SBA-15 or Ti/SiO2-Dav) simply
prepared by direct grafting of titanocene on the same silica
supports. This is likely due to the optimal site isolation ach-
ieved by grafting modest amount of titanocene over high-
surface-area silica supports. However, in terms of selectivity,
the anchored materials display slightly better results than
those obtained over reference titanium–silica catalysts with
comparable metal loading. In all cases, the major product is
the endocyclic limonene epoxide (80–88%). Virtually the
only other product is the exocyclic epoxide (10–12%) when
anchored Ti–POSS-derived catalysts are used, whereas acid-
derived by-products (9–14%) are found when reference tita-
nium catalysts are employed. This behaviour suggests that a
similar reactivity takes place at the TiIV sites for the epoxi-
dation reaction, but a more marked acidic character is pres-
Preparation of Ti–POSS-TSIPI (2): Ti-NH2POSS (1 g, 1.110À3 mol)[15]
was dissolved in chloroform (40 mL). An equimolar amount of 3-isocya-
natopropyl triethoxysilane and triethylamine was added to the solution.
The reaction was performed under inert conditions, using nitrogen flow,
at room temperature for 20 h. Finally, the solvent was evaporated until a
white powder was obtained. 1H NMR(400 MHz CDCl 3): d=3.9 (t, 2H;
NH, ureic group), 3.7 (q, 6H; CH2, OEt) ,3.6 (m, 1H; CH, OiPr), 2.9 (m,
4H; CH2 of ureic group), 1.85 (m, 6H; CH), 1.20 (m, 15H; CH3 of OEt
and OiPr groups), 0.93 (d, 36H; CH3 of isobutyl groups), 0.59 ppm (m,
20H; CH2).
Preparation of SBA-15: Pluronic P123 (4.0 g, Sigma–Aldrich) was dis-
solved in water (30 g) and HCl (2n, 120 g) with stirring at 308 K. Tetra-
ethoxysilane (8.5 g, Sigma–Aldrich) was added to the solution and stirred
at 308 K for 24 h. The mixture was aged at 373 K in an autoclave for
24 h. The solid product was filtered and washed several times by water.
Calcination was carried out increasing the temperature at 18CminÀ1
under air flow from room temperature to 823 K and heating the material
at 823 K for 5 h.
Preparation of 2/SBA-15: SBA-15 (1 g) was evacuated at 773 K for 4 h in
order to remove the adsorbed water and to activate the surface. Then the
powder was dispersed in anhydrous THF (by Sigma–Aldrich) under
vacuum. Compound 2 (20 wt% respect to the support) was added to the
suspension. The reaction was stirred at 323 K for 24 h. The final product
was filtered through a fine sintered glass funnel and washed several times
by THF.
Preparation of 2/SiO2: SiO2-Dav (1 g, commercial silica, obtained from
Grace) was treated at 773 K for 4 h in order to remove the adsorbed
water and to activate the surface. Then, SiO2 was dispersed in anhydrous
THF (by Sigma–Aldrich) under vacuum. Compound 2 (20 wt% respect
to the support) was added to the suspension. The reaction was stirred at
8100
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Chem. Eur. J. 2008, 14, 8098 – 8101