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2.4. Syntheses
and different amounts of 1-hexadecyl-3-(6-hydroxyhexyl)imi-
dazolium salt depending on the ionic concentration to be obtained.
Titanium tetrabutoxide (TBT) (0.106 g, 0.312 mmol, 175 ppm as
titanium with respect to the final polymer weight) was introduced
into the reactor that was closed with a three-neck flat flange lid
equipped with a mechanical stirrer, a torque meter and a heating
band at 90 °C. The system was then connected to a water-cooled
condenser and immersed in a thermostatic salt bath at 215 °C
and the stirrer switched on at 140 rpm. After 2 h, the temperature
was increased to 245 °C, the lid was heated at a temperature of
120 °C and the reactor connected to a liquid nitrogen cooled con-
denser. Dynamic vacuum was then applied to reduce the pressure
down to 0.2 mbar in 60 min. After 75 min the very viscous and
transparent melt was discharged from the reactor.
2.4.1. 1-Hexadecylimidazole
Potassium hydroxide (16.83 g, 0.300 mol) was added to a
dimethyl sulfoxide (DMSO) solution (500 mL) containing imidazole
(13.60 g, 0.200 mol). The mixture was then stirred for 30 min at
70 °C and 1-bromohexadecane (64.12 g, 0.210 mol) was added
dropwise under vigorous stirring. After 6 h, the mixture was cooled
at room temperature and 100 mL of water were added in order to
allow the precipitation of the N-alkylimidazole. The precipitate
was filtered and washed with distilled water (2 L). The washing
procedure was repeated twice.
The final product was dried in an oven under reduced pressure
(yield 95%). 1H NMR (400 MHz, CDCl3, d, ppm from TMS): 0.88 (t,
J = 6.9 Hz, 3H, CH3), 1.20–1.35 (m, 26H, CH2), 1.77 (quintet, 2H,
J = 7.0 Hz, 2H, CH2–C14 chain), 3.92 (t, J = 7.1 Hz, 2H, N–CH2–C15
chain), 6.90 (s, 1H, CH in imidazolium ring), 7.05 (s, 1H, CH in imi-
dazolium ring), 7.46 (s, 1H, N–CH–N in imidazolium ring).
2.4.5. Telechelic PBT ionomers bearing imidazolium end-groups scale-
up polymerization
Micro-pilot plant polymerizations were carried out by using a
two-stage process in a 1.8 L stainless steel batch reactor equipped
with a paddle stirrer (driven at 60 rpm) and a strain-gauge sensor
mounted on the stirrer shaft in order to monitor the viscosity of the
reaction melt (and indirectly the increase of PBT molecular weight)
during the polymerization. Two condensers in series (the first
water-cooled and the second liquid nitrogen-cooled) were con-
nected to the reactor to collect volatile products during the first
and second stages. A typical polymerization procedure is described
below.
2.4.2. 1-Hexadecyl -3-(6-hydroxyhexyl)imidazolium chloride
6-chlorohexanol (16.59 g, 0.121 mol) was added dropwise un-
der vigorous stirring to a solution containing 1-hexadecylimidaz-
ole (32.25 g, 0.100 mol) dissolved in 25 mL of anhydrous toluene.
The solution was stirred for 64 h at reflux temperature. The solvent
was then distilled under reduced pressure. The residue was
washed twice with 500 mL of ethyl acetate and dried under re-
duced pressure (yield 95%). 1H NMR (400 MHz, CDCl3, d, ppm from
TMS): 0.88 (t, J = 6.9 Hz, 3H, CH3), 1.20–1.62 (m, 32H, CH2), 1.72–
2.00 (m, 4H, CH2), 3.58 (t, J = 6.0 Hz, 2H, CH2–OH), 4.32 (dd,
J1 = 7.3 Hz, J2 = 7.5 Hz, 2H, N–CH2–C5 chain), 4.39 (t, J = 7.3 Hz,
2H, N–CH2–C15 chain), 7.40 (s, 1H, CH in imidazolium ring), 7.62
(s, 1H, CH in imidazolium ring), 10.39 (s, 1H, N–CH–N in imidazo-
lium ring).
2.4.5.1. First stage. BD (742.0 g, 8.25 mol), DMT (800.0 g, 4.12 mol)
and 1-hexadecyl-3-(6-hydroxyhexyl) imidazolium tosylate salt
(in different amounts in order to insert ionic groups at a content
0.6, 1 and 2 mol% respect to DMT) were loaded into the reactor
and then heated at atmospheric pressure under stirring to
180 °C. At this temperature, titanium butoxide (1.13 g, 3.31 mmol,
175 ppm as titanium with respect to the final polymer weight) was
introduced into the reactor. The reaction temperature was in-
creased from 180 to 215 °C. Volatile products (methanol and
THF) were distilled off from the reactor, condensed in the water-
cooled condenser and collected in a graduated cylinder. The start
of the first stage was taken when the first drop of liquid was col-
lected in the water-cooled condenser. The temperature was then
kept at 215 °C until 95% of the theoretical amount of methanol
was distilled off. The distilled volume was recorded versus time
as an indicator of the catalytic activity during the first stage and
distillate samples were analyzed by 1H NMR in order to measure
the methanol/THF ratio and thus the rate of THF formation.
2.4.3. 1-Hexadecyl-3-(6-hydroxyhexyl)imidazolium tosylate salt
1-hexadecyl-3-(6-hydroxyhexyl)imidazolium chloride (23.60 g,
0.0550 mol) was dissolved in dichloromethane (DCM) (350 mL)
and added to a solution of sodium p-toluenesulfonate (11.21 g,
0.0578 mol) dissolved in water (190 mL) in a separating funnel.
The content of the funnel was vigorously shaken for 5 min until
no further precipitate was present in the resulting two-phase mix-
ture. This procedure was repeated several times (usually twice) un-
til a silver nitrate test was negative confirming the complete
exchange of the chloride counter-ion. The organic layer was sepa-
rated and the solvent removed under reduced pressure. The yellow
solid was washed twice with ethyl acetate. The product was dried
under vacuum (yield 95%).
1H NMR (400 MHz, CDCl3, d, ppm from TMS): 0.87 (t, J = 6.9 Hz,
3H, CH3), 1.12–1.60 (m, 32H, CH2), 1.79 (m, 2H, CH2), 1.89 (tt,
J1 = 7.1 Hz, J2 = 7.3 Hz, 2H, CH2) 2.33 (s, 3H, CH3 in tosylate ion),
3.57 (t, J = 6.0 Hz, 2H, CH2–OH), 4.18 (dd, J1 = 7.3 Hz, J2 = 7.7 Hz,
2H, N–CH2–C5chain), 4.28 (dd, J1 = 7.1 Hz, J2 = 7.5 Hz, 2H, N–CH2–
C15 chain), 7.16 (d, J = 7.9 Hz, 2H, aromatic CH in tosylate ion),
7.22 (d, J = 1.6 Hz, 1H, CH in imidazolium ring), 7.38 (d, J = 1.6 Hz,
1H, CH in imidazolium ring), 7.77 (d, J = 8.0 Hz, 2H, aromatic CH
in tosylate ion), 9.92 (s, 1H, N–CH–N in imidazolium ring).
The synthesis of the imidazolium salts with other counter-ions
was performed with the same procedure using ammonium tetra-
fluoroborate, ammonium hexafluorophosphate, potassium perfluo-
robutanesulfonate and potassium trifluoromethanesulfonate.
2.4.5.2. Second stage. The internal pressure was slowly reduced,
first from atmospheric pressure down to 10 mbar in 30 min, then
from 10 mbar to 1 mbar in 20 min. At the same time the tempera-
ture of the reaction melt was increased to 240 °C and kept at this
temperature until the end of the polymerization. The start of sec-
ond stage was taken when the minimum pressure was reached.
The second stage was stopped when no further significant increase
in strain gauge signal was detected.
3. Results and discussion
3.1. Monomers synthesis and small scale polymerization
2.4.4. Telechelic PBT ionomers bearing imidazolium end-groups.
Synthesis in glass reactor
A round bottom wide-neck glass reactor (250 mL capacity) was
charged with 1,4-butanediol (BD) (48.88 g, 0.543 mol), dimethyl
terephthalate (DMT) (75.30 g, 0.388 mol) (BD/DMT ratio 1.4/1)
Imidazolium salts need to be modified in order to be inserted at
the end of the polyester chain. The approach we have followed
consists in the derivatization of the imidazolium ring with an alkyl
chain bearing an OH group that can react with the methyl ester
group of DMT and of the growing polymer chain during the poly-