3
970 J . Org. Chem., Vol. 61, No. 12, 1996
Al-Ajlouni and Espenson
Sch em e 1
fied, neat acetonitrile. The more water present, however,
particularly in the acidic medium, the greater the yield
of the ring-opened diol originating from the primary
epoxide product. From the kinetic data we can now
present a detailed picture of the reactions, including a
description of their steric and electronic requirements.
Exp er im en ta l Section
Ma ter ia ls. The solvents used for quantitative kinetic
studies were 1:1 CH
3
CN-H
2 3
O at pH 1 and CD OD. Methanol-
d
4
(Cambridge Isotopes) and HPLC-grade acetonitrile (Fisher)
were used. Water was purified by a Millipore-Q water
purification system. When required, 0.1 M perchloric acid,
diluted from the 70% reagent (Fisher), was used to maintain
3 3
pH. Occasional experiments were done in CH OH or CD CN.
within a Parr Model 1455 precision calorimeter, equipped with
a thermistor in a platinum resistance probe. The solutions
were separately allowed to reach temperature equilibration
for 20-30 min. The two solutions were then mixed and stirred
for 1-2 min. The stirrer was then stopped, and the temper-
ature was recorded at 5-10 s intervals by a computer with
Lotus 1-2-3 software. For each alkene, experiments were done
1
7
Methylrhenium trioxide was purified first by sublimation,
then by recrystallization from methylene chloride-hexane, and
finally by a second sublimation. Stock solutions of MTO in
methanol-d
or 2 weeks. The concentration was determined spectropho-
tometrically after dilution into a large volume of water: 239
4
or acetonitrile were stored at 5 °C and used within
1
-
1
-1
-1
-1 18
nm (ꢀ 1900 L mol cm ), 270 nm (ꢀ 1300 L mol cm ).
with 1.0 M H
2 2 T
O , with [Re] (which is essentially equal to [B]
at this high a peroxide concentration) being varied in the range
We purchased the alkenes (Aldrich); those which proved to
1
be pure by H NMR were used as such. trans-4-Octene,
0
.5-5.0 mM, and with [alkene] 10-50 mM. The reaction
1
-octene, and 1-hexene were purified by distillation. Aqueous
followed first-order kinetics, with temperature-time curves
independent of the reaction stoichiometry; in these systems
solutions of hydrogen peroxide were prepared from the 30%,
or occasionally the 3%, reagent. The concentrated reagent,
which proved quite stable over time, was standardized by
iodometric titration; the diluted peroxide solutions were much
less stable and were made up daily by dilution.
∆
T was within the range 0.2-0.8 °C. The temperature profile
is in addition affected by a slow thermal leakage in the
adiabatic calorimeter. With the thermal leakage expressed
as a first-order function with a constant k
cooling), the expression for the temperature at a given time
T
, (Newton’s law of
Kin etics. Three methods were applied, as required by the
range of alkenes and solvents. In every case the temperature
was controlled at 25 °C. (a) The reactions studied in methanol
20
(
T
t
) is given by eq 1, where the constants m
1
, m
2
, and m
3
are
(1)
related to the temperature factors of the experiment.
1
were followed by H NMR in a total volume of 0.6 mL. These
experiments used 0.50 M H
2 2
O , 1-50 mM MTO, and 0.05-
-kψt
-kTt
T ) m + m e
+ m e
3
0
.1 M alkene, added last. The relative amounts of peroxide
t
1
2
and alkene were chosen with a concern for the requirements
of the kinetic analysis which was carried out by a first-order
kinetic equation. The proton spectrum was recorded at 2-20
min increments over the 2-5 h reaction time. The changes
in intensity (Y) of the alkene signal(s) were fit to a single-
Resu lts
Ca ta lytic In ter m ed ia tes. As cited in the Introduc-
tion, quantitative kinetic data have already been reported
for oxygen-transfer reactions in the MTO/H O system.
2 2
exponential decay: Y
b) A spectrophotometric method was used for some of the
reactions carried out in 1:1 CH O, in which the acid
t
) Y
∞
+ (Y
0
- Y
∞
) × exp(-k
ψ
t).
(
Because of that, we shall rely on the established course
of these systems to provide the initial guidance for the
kinetic scheme that might apply to epoxidation reactions
of the alkyl-substituted alkenes. In this scheme, either
or both of the previously-depicted rhenium peroxides, A
or B, may transfer an oxygen atom to the alkene.
In the event that the monoperoxide A is reactive, then
MTO is immediately recovered along with the epoxide.
Similarly, if an oxygen atom is transferred from the bis-
peroxide B, then A is generated along with the epoxide.
This sequence of events in shown in Scheme 1.
Prior research has established that the conversion of
MTO to A upon reaction with hydrogen peroxide consti-
tutes a reversible equilibrium, likewise the conversion of
A to B. With the notation in Scheme 1, these are the
applicable equilibrium constants at 25.0 °C:
3
CN-H
2
concentration and the ionic strength was maintained at 0.100
M unless specified otherwise. The acid concentration needs
2 2
to be fairly high, because MTO-H O solutions otherwise
1
9
decompose fairly rapidly, unlike MTO itself. The cuvettes
had short optical paths, 0.01-0.2 cm, because the alkenes to
which the method was applicable had high molar absorptivities
and the other reagents contributed a large absorbance back-
ground at the wavelengths used. The reaction mixtures were
prepared in the reaction cuvette which was held in a thermo-
statted water bath, with the last component added being the
alkene. Air was not excluded, since controls showed there was
no need. Hydrogen peroxide was used in large excess over
the alkene, such that the bis-peroxide B was maintained at
constant concentration throughout. The data were obtained
by following the loss of the alkene absorption in the range
2
00-225 nm. The absorbance-time data were fitted by
nonlinear least-squares to a first-order kinetic equation: A
+ (A - A t).
) × exp(-k
c) A number of the reactions of the alkyl-substituted
t
K1/L mol-
1
K2/L mol-1
)
A
(
∞
0
∞
ψ
medium
13
1
2
1
:1 CH3CN-H2O, pH 1
1.3 × 10
1.36 × 10
alkenes were not accompanied by a useful absorbance change
at an accessible wavelength (>200 nm). These reactions, along
with several known systems that we used as controls, were
studied in the aqueous acetonitrile medium by a thermometric
21
2
2
CH3OH
2.61 × 10
8.14 × 10
Kin etic Design . The fact that the peroxo complex
formation reactions are reversible certainly does not
mean that the concentrations of the three species are
necessarily sustained at equilibrium under all circum-
stances in which the catalytic cycles are in operation. In
many of the cases already considered, especially those
2
0
method. The components were placed inside two reservoirs
(
17) Herrmann, W. A.; K u¨ hn, F. E.; Fischer, R. W.; Thiel, W. R.;
Ramao, C. C. Inorg. Chem. 1992, 31, 4431.
18) Yamazaki, S.; Espenson, J . H.; Huston, P. Inorg. Chem. 1993,
2, 4683.
19) Abu-Omar, M. M.; Hansen, P. J .; Espenson, J . H. J . Am. Chem.
Soc. 1996, 118, 4966.
20) Kustin, K.; Ross, E. W. J . Chem. Educ. 1993, 70, 454.
(
3
13
with reactive substrates such as phosphines and sul-
(
(
(21) Zhu, Z.; Espenson, J . H. J . Org. Chem. 1995, 60, 1326.