SELECTIVE ACYLATION OF STERICALLY HINDERED OH GROUPS
Table 2. Competitive acetylation of mono-olsa
357
area of the SiO2 used is 371 m2 gÀ1 by BET measure-
ment. Hence the saturation amount of 1,5-hexanediol
gives an estimation of E? of 3.9 mmol gÀ1 SiO2, whereas
E? is estimated as 2.9 mmol gÀ1 SiO2 in the case of the
compact adsorption of the alcohol in a bidentate fashion.
The good agreement between the isotherm and the
molecular modeling indicates that 1,5-hexanediol ad-
sorbs on the surface via a single OH group. The results of
a series of investigations imply that unsymmetrical diols
adsorb on the surface of SiO2 preferentially via a primary
OH group, leaving the non-adsorbed OH group available
for reaction. In addition, adsorption of the group on the
surface would create a sterically congested environment
which shields it from added reagents as suggested in
recent papers.1–3,7a,16d,17a,19 These would allow selective
monoacylation at the more sterically hindered, non-
adsorbed, site to give sterically hindered secondary and
tertiary monoacetates.
Methodb
Substratec
Relative reactivityd
primary: secondary: tertiary
Homogeneous 1° 2°
Homogeneous 1° 3°
1e:
1f:
1g:
1h:
0.75
1.69
0.67
1.38
Adsorption
Adsorption
1° 2°
1° 3°
a
Each experiment was carried out under reflux for 2 h with AcCl (1 equiv.)
in the absence of pyridine.
b
Homogeneous: homogeneous reaction (0.03 mol lÀ1 solution of each
alcohol in 1,4-dioxane). Adsorption: adsorption method (3.0 mmol gÀ1
SiO2 of each alcohol, ꢀ = 0.8).
c
1°, 1-hexanol; 2°, 2-hexanol; 3°, 3-methyl-3-pentanol.
d
Relative reactivity of each alcohol based on a yield of primary acetate.
e–h
Yields of 1-hexyl acetate correspond to
62.8%,
62.7%,
43.6% and
e
f
g
h
41.1%.
acetylation of 1-phenyl-1,2-ethanediol in homogeneous
reaction conditions, as shown in entry 6 in Table 1 at a
temperature 0°C, showed values 55.3% for Shind, and the
value of Shind was changed slightly by refluxing to 51.0%;
the transfer would occur under homogeneous reaction
conditions. Acetylation of 1-phenyl-1,2-ethanediol in a
homogeneous reaction under the same reaction condi-
tions as in entry 6 in Table 1 gave values of Smono and
Shind of 50.8% and 51.4%, respectively, and moreover the
reaction mixture was used in a reaction by the adsorption
method in the absence of AcCl. The composition of the
mixture did not change. This indicates that the transfer
does not proceed by an adsorption method.
The adsorption isotherm of 1,5-hexandiol on SiO2 in
1,4-dioxane showed Langmuir-type adsorption and
reached a saturation E? of 3.9 mmol gÀ1 SiO2 with an
adsorption constant Kad = 38 l molÀ1. Table 3 sum-
marizes the relative Kad for appropriate monofunctional
alcohols in addition to that for 1,5-hexanediol. A primary
alcohol interacts more easily with the surface of SiO2 and
adsorbs more preferentially than secondary and tertiary
alcohols. From molecular modeling, one molecule of 1,5-
hexanediol, adsorbed on the surface via a single OH
group with the free counterpart of the residue remote
from the surface, occupies 0.16 nm2. The specific surface
REFERENCES
1. (a) Laszlo P (ed). Preparative Chemistry Using Supported
Reagents. Academic Press: San Diego, 1987; (b) Clark JH, Kybett
AP, Macquarrie DJ. Supported Reagents: Preparation, Analysis,
and Applications. VCH: New York, 1992; (c) Smith K (ed). Solid
Supports and Catalysis in Organic Synthesis. Prentice Hall:
Chichester, 1992.
2. (a) McKillop A, Young DW. Synthesis 1979; 401; (b) Posner GH.
Angew. Chem., Int. Ed. Engl. 1978; 17: 487; (c) Cornelis A, Laszlo
P. Synthesis 1985; 909.
3. (a) Hojo S, Masuda R. Yukigosei Kagaku Kyoukaishi 1979; 37:
689; (b) Hojo S. Yukigosei Kagaku Kyoukaishi 1984; 42: 635; (c)
Ando T, Ichihara J, Hanahusa A. Kagaku Sosetsu 1985; 47: 166;
(d) Onaka A, Izumi Y. Shokubai 1992; 34: 159; (e) Okuhara T,
Misono M. Yukigosei Kagaku Kyoukaishi 1993; 51: 128; (f)
Nishiguti T. Yukigosei Kagaku Kyoukaishi 1993; 51: 308; (g)
Hattori H, Tsuji H. Shokubai 1995; 37: 2; (h) Ogawa H. Hyomen
Kagaku 1990; 11: 124; (i) Ogawa H, Kodomari M, Chihara T.
PETROTECH 1996; 19: 404.
4. (a) Cohen Z, Keinan E, Mazur Y, Varkony TH. J. Org. Chem.
1975; 40: 2141; (b) Keinan E, Mazur Y. J. Org. Chem. 1977; 42:
844; and references cited therein.
5. Bram G, Fillebeen-Khan T. J. Chem. Soc., Chem. Commun. 1979;
522.
6. (a) Keinan E, Mazur Y. J. Am. Chem. Soc. 1977; 99: 3861; (b)
Muzard J. Synthesis 1982; 60.
7. (a) Ogawa H, Chihara T, Taya K. J. Am. Chem. Soc. 1985; 107:
1365; (b) Ogawa H. J. Phys. Org. Chem. 1991; 4: 346; (c) Ogawa
H, Chihara T, Teratani S, Taya K. J. Chem. Soc., Chem. Commun.
1986; 1337.
8. (a) Chihara T, Teratani S, Ogawa H. J. Chem. Soc., Chem.
Commun. 1981; 1120; (b) Chihara T, Takagi Y, Teratani S, Ogawa
H. Chem. Lett. 1982; 1451.
9. (a) Wilkinson SG. In Comprehensive Organic Chemistry, vol. 1,
Stoddart JF (ed). Pergamon Press: New York, 1979; 681; (b)
Greene TW, Wuts PGM. Protective Groups in Organic Synthesis.
Wiley: New York, 1991; 88; (c) Furhop J, Penzlin G. Organic
Synthesis. Verlag Chemie: Weinheim, 1983; 143.
10. Babler JH, Coghlan MJ. Tetrahedron Lett. 1979; 22: 1971.
11. (a) Nishiguchi T, Kawamine K. J. Chem. Soc., Chem. Commun.
1990; 1766; (b) Nishiguchi T, Kawamine K, Ohtsuka T. J. Org.
Chem. 1992; 57: 312; (c) Ogawa H, Amano M, Chihara T. J.
Chem. Soc., Chem. Commun. 1998; 495.
12. Ogawa H, Ichimura Y, Chihara T, Teratani S, Taya K. Bull. Chem.
Soc. Jpn. 1986; 59: 2481.
Table 3. SiO2 adsorption equilibria for alcoholsa
Alcoholb
Kad(alcohol)/Kad(1-hexanol)
1,5-Hexanediol
1.2
1°
2°
3°
1c
0.78
0.63
a
Langmuir adsorption isotherms on SiO2 (Wakogel C-200, surface area
371 m2 gÀ1) in 1,4-dioxane suspension at 25 Æ 0.2°C.
b
1°, 1-hexanol; 2°, 2-hexanol; 3°, 3-methyl-3-pentanol.
13. Zerda JDL, Barak G, Sasson Y. Tetrahedron 1989; 29: 1533.
14. Lezonoff CC. Acc. Chem. Res. 1978; 11: 327.
c
Adsorption constant Kad equals 32 l molÀ1
.
Copyright 2003 John Wiley & Sons, Ltd.
J. Phys. Org. Chem. 2003; 16: 355–358