Organotin-Mediated Monoacylation of Diols
J . Org. Chem., Vol. 61, No. 16, 1996 5263
Sch em e 8
over a three-step pathway in which the dibutylstannylene
acetal of the starting diol plays the double role of reagent
and catalyst. The initially formed primary stannyl
monoester isomerizes to the secondary regioisomer,
thermodynamically more stable regioisomer, by over 4
kcal mol-1, through a fast intramolecular transesterifi-
cation equilibrium. Subsequent treatment with a quench-
ing reagent affords increasing amounts of a secondary
monoester the slower the quench. It has been shown that
selectivity can be optimized up to complete formation of
the secondary monoester by appropriately tuning the
reactivity difference between the acylating and the
quenching reagents. Thus, reversal of chemoselectivity
has been explained on the basis of the Curtin-Hammett
principle. It has been ascertained that the stannylation
procedure highly chemoselectively activates hydroxyl
groups toward acyl reagents, particularly acyl halides.
The reactivity of the Sn-O bond has been found to follow
the electronegativity order of ligands on tin, while halide
ligands have been found essential for reversal of chemo-
selectivity. A structure has been proposed for the
catalytic species that accounts for steric effects and the
observed reactivity.
stannyl ester A, while the reactivity of the latter de-
creases with decreasing electronegativity of ligands.
Scheme 6 can thus be expanded to include the equilibria
reported in Scheme 8.
This model also accounts for the relevance of steric
effects in this reaction. It can be seen in fact that the
bulk of the stannyl group increases dramatically in the
adduct. Such a conspicuous steric hindrance is reason-
ably the cause that biases the equilibrium toward the
secondary monoester in order to relieve strain. Having
the concentration ratios of the two regioisomers available
with reasonable accuracy in a significantly large tem-
perature range, an estimate of the stability gap between
the interconverting monoesters 3a and 4a can be at-
tempted. A plot of the ln K values vs 1/T for the
equilibrium constants measured from NMR data in the
investigated range of temperature gives van’t Hoff plot
of good linearity (r ) 0.981), with ∆H° ) 4.2 kcal mol-1
and ∆S° ) 12.8 eu. The enthalpy difference provides a
quantitative estimate of the preference for the most
stable secondary monoester, while the unexpectedly large
entropy difference that favors the primary monoester
accounts for the efficient compensation of contributions,
which level off at ca. 50 °C to afford equally abundant
regioisomers.19
Exp er im en ta l Section
Ma ter ia ls. 4-Phenyl-2,2-dibutyl-1,3,2-dioxastannolane (1)
was prepared and purified as previously described.17b Acetyl
chloride (Carlo Erba RPE, 99+%), benzoyl bromide (Aldrich,
97%), bromoacetyl chloride (Aldrich, 98%), 4-nitrophenyl
acetate (Fluka, >99%), p-anisoyl chloride (Aldrich, 99%), and
methyl trifluoromethanesulfonate (Aldrich, 99+%) were used
without further purification. 4-Nitrobenzoyl chloride (Aldrich,
98%) was used as such or purified by filtering off the insoluble
fraction of a concentrated solution in toluene and subsequently
evaporating the solvent. Chlorotrimethylsilane (Carlo Erba
RPE) was used as such or distilled over quinoline. Methane-
sulfonyl chloride (Aldrich, 99+%) was purified by distillation.
Gen er a l. Standard acylation and quench procedures, isola-
tion, and characterization of products have been described
elsewhere.6 All reactions were run in CDCl3 (Merck, 99.8%)
stored on activated 13 X molecular sieves and Ag foil. Room
temperature 1H NMR spectra were run at 200 MHz. Variable
temperature experiments and kinetic measurements were
carried out at 300 MHz. Reactions were performed in 5 mm
screw-capped NMR tubes, mixing the reactants with syringes
through a septum cap. Variable temperature experiments
were carried out under an inert atmosphere; this was not
necessary for room temperature experiments. For all the
experiments, mixing of reactants was carried out batchwise
by injecting the solution of one reagent onto the other, neat
or in solution depending on the reactivity of the substrate, so
as to achieve a 0.3 ( 0.1 M concentration in each of the two
reagents. Subsequent quench was carried out quantitatively
by transferring with a syringe the mixture into a second screw-
capped tube containing the appropriate amount of quenching
reagent. Reproducibility of the results was checked by per-
forming each experiment at least in duplicate and using
different lots of reagents when possible. Taking into account
variable extent of adventitious hydrolysis and diester forma-
tion due to reactants unbalance, results were satisfactorily
reproducible.
In conclusion, the structure proposed for the catalytic
adduct is consistent with the observed reactivity, explains
steric effects, and adequately represents the key inter-
mediate responsible for the reversal of chemoselectivity.
Con clu sion s. The investigation of the mechanism of
the organotin-mediated monoacylation of diols has re-
vealed that product distribution is determined by an
interplay between kinetic and thermodynamic control
(19) It must be emphasized, however, that the reaction scheme
consists of a system of multiple equilibria that, besides intramolecular
transesterification, involve association processes with 1. According to
this scheme, the measured concentration ratios are not directly
amenable to a “true” equilibrium constant, but only to an “apparent”
global constant. Thus, thermodynamic parameters may appear anoma-
lous in value, being the net result of a complex situation. The entropy
difference, in particular, exhibits an unexpectedly large value for an
isomerization reaction; this might be due to contributions from
dissociation equilibria, reasonably unbalanced between the two iso-
mers. Clearly, the multiple equilibria system is too complex for a
quantitative treatment. Analytical relationships show however that
concentration ratios are dependent, inter alia, on the equilibrium
concentration of 1; the estimated thermodynamic parameters are
therefore meaningful for the set of conditions used, but may vary with
the concentration of 1. Fortunately, such does not seem to be the case,
as shown by the experiment described in Figure 3, so that the overall
thermodynamic analysis is correct.
Ack n ow led gm en t. The author is grateful to Profes-
sor L. Mandolini at the University of Roma “La Sapi-
enza” for discussion and helpful suggestions in the
preparation of the manuscript.
J O960453F