9
the reaction of carboxylic acids with 1,2-epoxypropane or
-chloro-2,3-epoxypropane.10 Steric conditions, however,
1
may distort this order. A reduced rate was observed for large
2
cations in the case 2-methylpyridine or 2-methylquinoline.
The differences in the observed reaction order of the
addition of carboxylic acids to glycidyl phenyl ethers
catalyzed by tertiary amines is probably the result of the
equilibrium which is established between the amine and
carboxylic acid. The latter strongly depends on the other
conditions of the reaction.
The basic catalysts, although quite widely used, have
certain disadvantages, the main one being the ability to
1
1
initiate cationic polymerization of epoxy compounds. In a
dilute solution this reaction may be neglected, but in the
systems without a solvent, such as in the commercial
synthesis of hydroxyalkyl esters, the side polymerization
reaction in the alkaline medium may reduce considerably
the reaction selectivity.
Figure 1. The concentration of 1,2-epoxy-3-phenoxypropane
GPE) and of acetic acid (AcOH) versus time in the reaction
(
carried out in the presence of chromium(III) ethanoate cata-
The chromium(III) catalysts, which are effective in the
reactions of carboxylic acids with oxirane, 1,2-epoxypropane,
or 1-chloro-2,3-epoxypropane, are free of this disadvantage.
They exhibit not only a high selectivity, but are usually
more active than basic catalysts.1
-3
lyst (cat); CAcOH,0 ≈ CGPE,0; Ccat ) 0.008 mol‚dm ; temperature
70 °C.
chromatograph with an FFAP capillary column, 10 m/0.53
mm/1 µm).
2-17
The kinetic relationships observed in the addition of
selected carboxylic acids to 1,2-epoxy-3-phenoxypropane in
the presence of such a homogeneous chromium(III) catalyst
in the system without a solvent are presented in this work.
Results and Discussion
Among the products of reaction in the system containing
a carboxylic acid (CA), asymmetric epoxy compound and
catalyst one may expect beside the two isomeric esters with
alcoholic hydroxy groups also the products of dispropor-
tionation of hydroxyesters, subsequent addition of oxirane
to hydroxyesters, polymerization of oxirane or its isomer-
ization to ketone or aldehyde, or even esterification of
carboxylic acid with the addition product. The extent of either
of these reactions depends on the conditions applied and,
primarily, on the kind of catalyst used. Among two isomeric
hydroxyester products, usually the so-called normal product
is formed in excess, i.e., the product of addition to the carbon
atom in epoxy ring which has a lower substitution degree.
In our previous papers on the reactions of carboxylic acids
with 1-chloro-2,3-epoxypropane carried out in the presence
Experimental Section
Materials. Commercially available acetic, acrylic, and
methacrylic acids and 1,2-epoxy-3-phenoxypropane were
purified in the standard manner and distilled prior to use.
Chromic ethanoate was of p.a. grade and used without further
purification.
Procedures. The kinetics of addition were studied in
3
purpose designed glass reactors (50 cm ) equipped with a
heating jacket, reflux condenser, thermometer, and magnetic
stirrer. The content of reactor was brought to desired
temperature with an external thermostat. The equimolar ratio
of carboxylic acid to epichlorohydrin was used. The con-
centration of chromium(III) ethanoate was changed in the
1
7,19,20
of chromium(III) ethanoate
we have shown that in the
-
3
systems without a solvent, most of the above-mentioned side
reactions involving oxiranes do not take place, or their
contribution among products is negligible.
range 2.0-17.0 mmol‚dm and temperature from 60 to 90
°
C at 10° intervals.
The content of unreacted acid in the samples withdrawn
The typical kinetic curves obtained for the reaction of
acetic (1), acrylic (2), and methacrylic acid (3) with 1,2-
epoxy-3-phenoxypropane in the presence of chromium(III)
ethanoate in temperature range 60-90 °C are shown in
Figures 1-3.
from the reactor at predetermined reaction times was
determined by titration. The concentration of 1,2-epoxy-3-
phenoxypropane was determined by Jay’s method. The final
reaction mixtures were carefully analyzed by GLC (HP 5890
18
(
9) Szak a´ cs, S.; G o¨ b o¨ l o¨ s, S.; Nagy, F. J. Chem. Soc., Perkin Trans. 2 1983, 4,
For all systems, the shape of kinetic curves indicates that
the changes of both substrate concentrations are simulta-
neous. This confirms the small contribution of side reactions
in the conditions applied. The same conclusion follows from
results of GLC analysis of the crude reaction products. In
the crude products of reaction two isomeric esters, 2-hy-
droxy-3-phenoxypropyl (n-PHPC) and 1-(hydroxymethyl)-
4
17.
(
10) Bukowska, A.; Guskov, A. K.; Makarov, M. G.; Rokaszewski, E.; Svets,
V. F.. J. Chem. Technol. Biotechnol. 1995, 63, 374.
11) Ellis, B. Chemistry and Technology of Epoxy Resins; Blackie Academic &
Professional: London, 1993.
12) German Patent 1,911,447, 1970.
13) U.S. Patent 3,875,211, 1975.
14) German Patent 2,801,422, 1979.
15) Russian Patent 505,627, 1976.
16) European Patent 1904, 1978.
17) Bukowska, A.; Bukowski, W. J. Chem. Technol. Biotechnol. 1996, 67, 176.
18) Jay, R. Anal. Chim. 1964, 36, 667.
(
(
(
(
(
(
(
(
(19) Bukowska, A.; Bukowski, W. J. Chem. Technol. Biotechnol. 1998, 73, 341.
(20) Bukowska, A.; Bukowski, W. J. Chem. Technol. Biotechnol. 1999, 74, 675.
Vol. 3, No. 6, 1999 / Organic Process Research & Development
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