268
S. Vezzosi et al. / Journal of Catalysis 257 (2008) 262–269
Table 3
under selected conditions (Table 3 and Scheme 8). Because EtOH
is a nucleophilic solvent, these oxidations were useful probes for
evaluating the stability of newly formed epoxides toward possible
solvolytic side processes. The results of the oxidations are reported
in Table 3 and Scheme 8. Again, the yields are referred to mmol
of product per mmol of starting material. The oxidation of 1 with
VI in EtOH proceeded with a quantitative conversion of substrate
(greater than that observed previously in CH2Cl2) to give a mix-
ture of 6a as the main reaction product (70%) and of the oxiranyl
ring-opened derivative 7a (28%) as a side product (Table 3, en-
try 2). Similar behavior was observed in the oxidation of 1 with
VII and VIII (Table 3, entries 5 and 8, respectively). Of note, the
yield of 6a with catalysts VI and VII was higher than that obtained
with MTO (see, e.g., Table 3, entry 2 vs entry 1), with VII being the
most efficient system. These data further confirm the capability of
aliphatic amines of tuning the reactivity of MTO. Irrespective of
experimental conditions, the oxidation of olefin 2 always afforded
the ring-opened derivative 7b in high or quantitative yield (Table 3,
entries 3, 6, and 9). In contrast, a quantitative conversion of 3 and
a quantitative yield of epoxide 6c was obtained with catalysts VI
and VII (Table 3, entries 4 and 7), with catalyst VIII showing a
slightly lower reactivity (Table 3, entry 10). Finally, when olefin 4
was treated with VII, a quantitative conversion of substrate and
quantitative yield of cis-stylbene oxide 6d was obtained (Table 3,
entry 11). It is interesting to note that the oxidation of 1 with
microencapsulated catalyst mVII afforded 6a in higher yield and
better selectivity than obtained with catalyst VII (Table 3, entry
12 vs entry 2), thus suggesting a role of the microcapsule envi-
ronment in the oxidation pathway. These data are in accordance
with our previous findings on the effect of the polymeric matrix
on the reactivity and selectivity of MTO [4]. Again, irrespective of
the catalyst used, the oxidation of 2 always afforded 7b as the
sole recovered product, with mVII being the most reactive system
(Table 3, entries 13 and 16). Of note, a quantitative conversion of
substrate and a quantitative yield of epoxide 6c were obtained in
the oxidation of 3 with both catalysts mVI and mVII (Table 3, en-
tries 14 and 17). The catalyst mVII also proved to be an efficient
system for the oxidation of 4 to give 6d in high yield (Table 3,
entry 18).
Oxidation of olefins 1–4 in EtOH with UHP and MTO/Ln adducts VI–VIII or microen-
capsulated PS/MTO/Ln adducts mVI and mVII
Entry
Olefin
Catalysta
Conv.
(%)
Product(s)b
Yield(s)
(%)c,d
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
1
1
2
3
1
2
3
1
2
3
4
1
2
3
1
2
3
4
MTO
VI
VI
VI
VII
99
99
99
99
99
99
99
72
87
88
97
82
78
99
85
88
99
85
6a, 7a
6a, 7a
7b
6c
6a, 7a
7b
6c
6a, 7a
7b
6c
6d
6a, 7a
7b
6c
6a, 7a
7b
6c
56 (44)
70 (28)
98
98
72 (27)
98
98
47 (25)
87
88
96
75 (7)
76
99
78 (6)
86
99
VII
VII
VIII
VIII
VIII
VII
mVI
mVI
mVI
mVII
mVII
mVII
mVII
6d
83
a
Catalysts: MTO/(1R,2R)-1,2-cyclohexyldiamine, VI; MTO/(1S,2S)-1,2 cyclo-
hexyldiamine, VII; MTO/cis-1,2-cyclohexyldiamine, VIII; microencapsulated MTO/
(1R,2R)-1,2-cyclohexyldiamine, mVI; microencapsulated MTO/(1S,2S)-1,2-cyclo-
hexyldiamine, mVII.
b
The reactions were performed in EtOH, UHP (3 equiv.), 5% w/w of catalyst, at
r.t., running for 24 h.
c
Yields in parentheses are referred to product 7a.
The yields are referred to mmol of product per mmol of starting material.
d
6a in acceptable conversion of substrate and high yield (Table 2,
entry 2). Catalyst VI was more selective than MTO; in fact, byprod-
ucts, such as phenylacetaldehyde, previously observed during the
oxidation with MTO (Table 2, note d), were not recovered in the
reaction mixture (Table 2, entry 2 versus entry 1). The position
of the methyl group on the isomeric olefins 2 and 3 (i.e., the
α- vs β-position on the vinyl moiety) played a relevant role in
the efficiency of the oxidation. Thus, although a low conversion of
substrate and a low yield of epoxide 6b were recovered from the
oxidation of 2, the oxidation of 3 afforded the epoxide 6c in high
conversion and yield (Table 2, entry 4 vs entry 3). Similar results
were obtained in the oxidations with VII, with epoxides 6a and
6c isolated at yields (72% and 76%, respectively) greater than that
of 6b (Table 2, entries 5–7). As a general reaction pattern, catalyst
VIII exhibited poorer performance compared with catalysts VI and
VII (Table 2, entries 8–10).
The oxidations with microencapsulated PS/MTO/Ln were succes-
sively performed with the most reactive catalysts, mVI and mVII,
and olefins 1 and 3. It is interesting to note that both catalysts af-
forded epoxides 6a and 6c in yields comparable to that of their
homogeneous counterpart, with olefin 3 being the most reactive
substrate (see, e.g., Table 2, entries 11 and 12 vs 2 and 4). Thus,
specific kinetic barriers to the approach of substrate to heteroge-
neous systems were not observed. To the best of our knowledge,
this is the first report dealing with the high efficacy of aliphatic
amines in tuning the reactivity of MTO, both in homogeneous and
heterogeneous conditions. This reactivity is comparable to that re-
ported previously for aromatic amines [12].
3.5. Evaluation of stereoselectivity for the epoxidation of prochiral
olefins
Despite the high reactivity and versatility of MTO in the epoxi-
dation of olefins, up to now, no relevant results in terms of stereos-
electivity have been obtained. To date, efforts have focused mainly
on using MTO in the presence of a large excess of chiral amines
added to the reaction mixture; for example, Corma et al. [14] re-
ported moderate stereoinduction values (accompanied by low con-
version values) during the epoxidation of prochiral olefins at low
◦
◦
temperature (from −5 C to −55 C), with MTO and added chiral
amines. Similar results have been reported by Herrmann and Kühn
et al. [1b,15] in the MTO-catalyzed epoxidation of prochiral olefins
in the presence of a large excess of chiral pyrazole based ligands.
In this latter case, the fluxionality property of MTO nitrogen-based
adducts (i.e., the rapid equilibrium between the coordinated and
the noncoordinated species) was suggested to explain the effect
of the temperature on the values of stereoinduction [1b,15]. With
the aim of evaluating the values of stereoselectivity induced by
our chiral MTO complexes, the epoxidation of 1 with VI and mVI,
performed in both CH2Cl2 and EtOH, was analyzed by GC in a chi-
ral capillary column (30 m × 0.25 mm × 0.25 μm film thickness
BETA-DEX-325 fused silica) as selected representative examples.
The results, collected in Table 4, show rather low ee in the oxi-
dation of 1 with VI in both reaction solvents (Table 4, entries 1
and 2). In contrast, the use of mVI as the catalyst led to a signif-
3.4. Effect of solvent on epoxidation
It is well known from the literature that the reactivity of MTO
can be increased by the use of polar protic solvents, such as alco-
hols [1a,13]. Based on these data, and with the aim of increasing
the conversion of substrate, we repeated the oxidation of olefins
1–3 with MTO/Ln adducts VI–VIII and PS/MTO/Ln adducts mVI and
mVII in ethanol (EtOH) under similar experimental conditions. In
this latter case, the cis-stylbene 4 also was evaluated as a substrate