The Journal of Organic Chemistry
Brief Communication
azide anion catalysis of the direct addition of water to substrate
[kB (M−1 s−1), Scheme 3]. The solid line shows the theoretical
fit of data from Figure 1 to eq 2 derived for Scheme 3 (the
the transition state for nucleophile addition, that results in a
weakening in the bonding to the reacting nucleophile.20
A
similar shift in transition state structure has been proposed to
rationalize the smaller selectivity of methyl perchlorate
compared to methyl iodide toward reaction with nucleophilic
anions.19
derivation is given as Supporting Information) using [(kNu
kB)/ksolv] = (3.64 × 10−6 M−1 s−1)/(1.95 × 10−6 s−1) = 1.9 M−1
determined above and values of kaz/ks = 83 M−1 and kB/kNu
+
=
0.016 for the variable parameters obtained from the nonlinear
least-squares fit of these data. There is good agreement between
EXPERIMENTAL SECTION
■
the total observed yields of MeO-1-N3 (f RN3
)
and the
T
Potassium [13C]-cyanide (99% enriched) was purchased from a
commercial supplier. All other organic and inorganic chemicals were
reagent grade from commercial sources and were used without further
purification. 2-(4-Methoxyphenyl)[1-13C]ethanol [MeO-1-
[α-13C]OH] was synthesized according to a published procedure.21
Carbon-13 NMR Analyses. Proton-decoupled 13C NMR spectra
were recorded at 100.4 MHz. Chemical shifts were measured in ppm,
relative to a value of δ = 77.0 ppm for CDCl3. A pulse angle of 45° was
employed to obtain spectra centered at 55.0 ppm, which spanned
7042.25 Hz and contained 65000K data points (0.107 Hz/pt). Several
delay times between FT pulses, ranging from 8 to 70 s, were examined.
Identical ratios of the peak areas for carbon-1 and carbon-2 of 2-(4-
methoxyphenyl)ethyl derivatives were observed at 35 and 70 s delay
times, and the longer relaxation time of 70 s was used for these spectra.
Generally >1000 FT transients were averaged before the final spectra
were determined.
theoretical yields calculated from eq 3 using the above three
rate constant ratios.
(1)
Kinetic and Product Studies. The progress of the reactions of
MeO-1-[α-13C]Ts in 50/50 (v/v) TFE/H2O (I = 0.5, NaClO4) and at
−
25 °C in the absence or in the presence of N3 was monitored by
HPLC analyses as described in previous work.6,18 The reactions were
initiated by making a 100-fold dilution of 2-(4-methoxyphenyl)ethyl
tosylate dissolved in acetonitrile into 20 mL of 50/50 (v/v) TFE/H2O
(I = 0.5 (NaClO4). The final substrate concentration was 2 mM for
reactions in the presence of 0, 0.1, 0.2, and 0.3 M azide anion and 0.3
mM for reactions in the presence of 0.01 and 0.03 M azide anion. At
specified times, aliquots of 100 μL were applied directly onto an
HPLC column for analysis. The reactant and products were separated
by gradient elution using a mixed MeOH/H2O solvent.22 The peaks
for the substrate and product were monitored at 276 nm, which is λmax
for 2-(4-methoxyphenyl)ethyl alcohol and 2-(4-methoxyphenyl)ethyl
azide. A value of εROTs/εR‑Nu = 1.17 for the ratio of extinction
coefficients of MeO-1-Ts and MeO-1-OH at 276 nm was determined
by comparing the HPLC peak areas at 276 nm of known
concentrations of MeO-1-Ts and MeO-1-OH. The sum of the peak
areas from HPLC analyses at 276 nm for MeO-1-OH and MeO-1-N3
The azide ion selectivity of kaz/ks = 83 M−1 requires that the
lifetime of 2+ in water is sufficiently long to allow for its
diffusion through the nucleophilic solvent and selection for
reaction with strongly nucleophilic azide anion.13,14 The upper
limit for kaz is kd ≈ 5 × 109 M−1 s−1 for a diffusion-controlled
reaction of 2+.15 Combining this and kaz/ks = 83 M−1 gives an
upper limit of ks ≤ 6 × 107 s−1 for addition of solvent. We
expect that ks for addition of solvent to 2+ is smaller than 2 ×
108 s−1 observed for the 4-methoxybenzyl carbocation because
ks = 3.4 × 10−3 s−1 for addition of solvent to the neutral
spiro[2,5]octa-1,4-diene-3-one16 is 1000-fold smaller than ks =
3.3 s−1 for addition of solvent to the unsubsituted p-quinone
methide 4,17 while O-methylation of 4 causes a 108-fold
increase in electrophile reactivity.18 We suggest that the rate
constants for addition of nucleophiles to 2+ lie closer to ks = 105
s−1 and kaz = 107 M−1 s−1 for the addition of azide ion and
solvent, that are estimated from kaz/ks = 83 M−1, and assuming
that O-methylation causes similar ∼108-fold increases in ks for
addition of solvent to 3 and 4.
−
remained constant as [N3 ] was increased from 0.00 [100% yield of
MeO-1-OSolv] to 0.30 M [97% yield of MeO-1-N3]. This shows that
these products have the same extinction coefficient at λmax = 276 nm.
The decrease in the HPLC peak area (AROTs) for the reactant MeO-
1-Ts was monitored for ca. 2-reaction halftimes, and first-order
reaction rate constants were determined as the slopes of semi-
logarithmic plots of reaction progress f S (eq 1) against time, where
ΣARNu is the sum of the peak areas for the products MeO-1-OH
(AROH) MeO-1-OCH2CF3 (AROTFE), and MeO-1-N3 (ARN3). The
ratio of the yields of the products of the reactions of MeO-1-Ts in 50/
50 (v/v) TFE/H2O at I = 0.5 (NaClO4) was determined directly from
the ratio of the HPLC peak areas for the products using eq 5 because
MeO-1-OSolv and MeO-1-N3 have the same extinction coefficient at
λmax = 276 nm (see above).
The value of log(kaz/ks) = 1.9 for the reaction of 2+ is smaller
than the Swain−Scott nucleophilicity parameter of n = 3.9
determined for the reaction of azide anion with methyl
bromide.19 This decrease in selectivity for nucleophile addition
to the more reactive electrophile might reflect the different
diffusion-limited (kd = kaz = 5 × 109 M−1 s−1) and activation-
limited rate constants for addition of azide ion and solvent to
2+, if ks = 6 × 107 s−1 for addition of solvent to 2+. However, we
suggest that this decrease in selectivity with increasing
electrophile reactivity is due to a change in the structure of
(4)
(5)
At ca. 2 half-times for the reaction of MeO-1-[α-13C]Ts the
remaining substrate and the products were extracted into either ether
or toluene. The organic layer was washed with water, dried over
MgSO4, and then removed using a rotary evaporator. The resulting
9570
dx.doi.org/10.1021/jo202118s|J. Org. Chem. 2011, 76, 9568−9571