9322
J. Melis et al. / Polymer 42 62001) 9319±9327
Table 2
Transesteri®cation of PAAꢀDL)G-2 with alcohols
c
Polymer
t ꢀmin)a
C ꢀ%)b
Yield ꢀ%)
h ꢀdl g21
)
Mvd
d/le
Tm
DMSO
DCA
PAAꢀDL)G-2
PAAꢀDL)G-1
PAAꢀDL)G-3
PAAꢀDL)G-4
PAAꢀDL)G-4f
PAAꢀDL)G-6f
PAAꢀDL)G-8f
PAAꢀDL)G-10f
±
85
70
20
25
40
45
50
±
100
100
100
100
100
.98
.98
±
85
91
59
84
88
78
73
0.81
0.39
0.26
0.43
0.37
±
1.41
0.9
0.65
0.94
0.81
±
96,000
50,000
38,000
55,000
45,000
±
58:42
261
228
±
60:40
±
236
260
230
168
±
58:42
±
±
±
±
±
±
±
±
55:45
a
Reaction time at 1808C.
Conversion degree measured by H-NMR.
b
c
d
1
Intrinsic viscosity measured at 25 ^ 0:18C measured in dimethyl sulfoxide ꢀDMSO) or dichloroacetic acid ꢀDCA).
Viscosity-average molecular weight estimated by using the Mark±Howink±Sakurada equation [24] h 2:9 £ 1024 Mv0:74 established for polyꢀg-methyl
a,l-glutamate) in dichloroacetic acid ꢀDCA).
e
Determined by HPLC.
f
Non-soluble in the solvents used for viscosity measurements.
Thermogravimetric analyses were performed with a Perkin±
Elmer TGA-6 thermobalance under ¯owing nitrogen.
The transesteri®cation reaction was carried out at 1808C
with PAAG-2 suspended in a large excess of the alcohol of
choice and in the presence of TiꢀBuO)4 as catalyst. The
advance of the reaction was followed by 1H-NMR by
comparing the areas of the CH2 signal of the ethyl leaving
group with a conveniently selected signal of the replacing
alkyl side group. The evolution of transesteri®cation of
PAAG-2 with isobutanol is shown in Fig. 1. The conversion
was considered to reach 100% when the ethyl CH2 signal
completely disappeared. A good advantage offered by this
reaction is that the polymer passes into solution as transes-
teri®cation proceeds. Thus, the reaction mixture becomes
homogenized when a certain degree of conversion is
reached making easier the subsequent attack by the
replacing alcohol ꢀwhich is the reaction solvent) and possi-
ble to attain almost total conversion. The results obtained in
the transesteri®cation step are shown in Table 2 for the
whole set of alcohols examined in this work. Conversions
attained between 98 and 100%, the larger alcohols being
less ef®cient as substituting reagents. Puri®cation of the
products was feasible by simple precipitation from the reac-
tion mixture by addition of methanol. The purity of PAAG-n
thus obtained was assessed by IR, 1H and 13C-NMR spectro-
scopy, as illustrated in Fig. 2 for the case of PAAG-6. Simi-
larly to what happened in the esteri®cation stage, a certain
decreasing in viscosity was found to accompany the trans-
esteri®cation reaction whereas no appreciable change in the
enantiomeric composition was detected.
3. Results and discussion
3.1. Preparation and characterization of poly6a-alkyl
g-glutamate)s
Esteri®cation of PGGA to PAAG-n was performed in two
stages, as indicated in Scheme 1 ꢀreaction scheme for the
preparation of PAAG-n by esteri®cation in two steps). The
ethyl ester of PGGA ꢀPAAG-2) was obtained in ®rst place
by treating the polyacid with ethyl bromide using the two
methods available in the literature for the synthesis of this
compound. These methods essentially differ to each other in
the solvent and temperature used for reaction: DMSO at
458C in method A and NMP at 608C in method B. Two
PGGA, one almost racemic, PGꢀDL)GA, and the other
highly enriched in d-units, PGꢀD)GA, were used for ester-
i®cation. Reaction conditions and characteristics of the
resulting PAAG-2 are compared in Table 1. In both meth-
ods, results were found to be essentially independent of both
molecular weight and enantiomeric composition of the
polymer and no signi®cant alteration of the d/l ratio was
observed to occur. Although the conversion attained by the
two methods was nearly complete, PAAG-2 obtained in
NMP distinguished in showing no traces of unreacted
carboxilic groups. Comparison of viscosities for PGGA
and PAAG-2 ꢀno strictly comparable) revealed that a
considerable reduction in molecular weight took place
upon esteri®cation. Such a reduction is though to be due
to uncontrolled hydrolysis of the polyamide chain, a process
that appears to take place much easier for high molecular
weight species and, according to expectations, to increase
considerably with reaction time and temperature.
It can be concluded from these results that the character-
istics of the ®nal polyꢀa-alkyl g-glutamate)s obtained by
transesteri®cation do not differ signi®cantly from those
obtained by the single-step esteri®cation methods described
in the literature. The same can be said about yields, as far as
short alkyl groups are concerned. Since the solubility of the
polymer increases with the advancement of transesteri®ca-
tion, almost complete conversions are attained regardless