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as follows. To a calculated amount of EGM or PGM,
dissolved in excess toluene in the presence of triethylamine
(TEA) as acid acceptor, we added dropwise with stirring
a toluene solution of DFA DC at the molar ratio glycol
monomethacrylate : DFA DC : TEA = 2.2 : 1 : 2.8.
The mixture was vigorously stirred for 1 h at 20°С,
after which it was heated at 40°С for an additional 2 h.
After cooling, the mixture was filtered to remove TEA
hydrochloride, and the filtrate was transferred into
a separation funnel in which it was washed 5–6 times
with water to neutral reaction. To the washed solution,
we added 0.01–0.04 wt % p-methoxyphenol, after which
the toluene was distilled off.
τ, h
High reactivity of DFA dichloride allowed the con-
densation to be performed at a lower temperature and in
a shorter time, compared to azeotropic esterification, and
the DFA dimethacrylates to be obtained in high yield.
Fig. 2. Total acid numberAN of the reaction mixture in synthesis
of dimethacrylates as a function of time τ.
The data we obtained show that it is appropriate to
prepare DFA dimethacrylates using compounds IX and
X, because introduction of a ready glycol monomethac-
rylate into the reaction system considerably simplifies the
condensation process.
All the synthesized dimethacrylates are viscous trans-
parent liquids with the color from yellow to dark brown
and with a weak methacrylate odor. The physicochemical
and chemical properties of V–VIII and XI–XIV and the
IR and NMR data for them are given in Table 1.
Dimethacrylates XI and XII were prepared at the
molar ratio DFA : glycol monomethacrylate = 1 : 2.4 in
toluene in the presence of a catalyst, p-TSA.
It seems also important to study the molecular-weight
characteristics of the DFA dimethacrylates prepared and
their dependence on the synthesis conditions.
The reaction of DFA with EGM completes in 4.5–5 h
on reaching 95–96% conversion. Thus, in esterification
of the dimerized acid with glycol monomethacrylate the
reaction time is considerably shorter (by a factor of 2)
than in the system with EG and methacrylic acid, the yield
of dimethacrylate XI is approximately 10% higher than
that of V, and the product is washed with faster phase
separation.
It is known [15–17] that the structure of the
oligoester acrylates formed does not always meet the
expectations, despite agreement between the calculated
and experimentally determined characetristics. Probably,
deeper condensation of the bifunctional components
(glycol, DFA) leads to the formation of a wide range of
mono- and oligomeric products, and the dimethacrylates
formed are actually polydisperse multicomponent
mixtures.
At the same time, dimethacrylate XII in the reaction
with PGM is formed slowly. The reaction completes in
10–11 h on reaching 95.6% conversion. In this case, the
decreased reaction rate is due to specific features of the
structure and reactivity of PGM containing a secondary
hydroxy group.
In this connection, we examined the molecular-weight
characteristics of the DFA methacrylates prepared from
different starting compounds. Depending on the synthesis
conditions, the products can be subdivided into three
groups: V–VIII; XI and XII; and XIII and XIV.
The formation of DFA dimethacrylates occurs at
elevated temperatures (108–120°С) and therefore is
accompanied by formation of certain amounts of by-
products and tars. Therefore, it was of interest to examine
the possibility of preparing FDA dimethacrylates under
milder conditions, e.g., by nonequilibrium condensation
with DFA dichloride [10].
The molecular-weight characteristics of the
compounds prepared were studied by gel permeation
chromatography. The GPC data show that FDA
dimethacrylates V–VIII are not monodisperse. The
gel chromatogram of dimethacrylate VIII, shown in
Fig. 3a, reflects its complex oligomer composition:
Along with the expected main compound, it contains
compounds of lower and higher molecular weights, which
Synthesis of dimethacrylates XIII and XIV from
DFA DC and glycol monomethacrylates was performed
RUSSIAN JOURNAL OF APPLIED CHEMISTRY Vol. 85 No. 8 2012