A. Ouerghui et al. / Reactive and Functional Polymers 100 (2016) 191–197
195
Table 1
210 °C. This transition can be attributed to the decomposition of the
azido group of the polymer [20].
Loadings and DSC studies of synthesized polymers B and 2a–e.
Polymera
Loading (mmol·g−1
)
Texo (°C)
Tg (°C)
b
2a
2b
2c
2d
2e
B
4.48
3.97
3.25
3.50
4.38
7.92
–
–
–
–
–
210
132
131
126
123
119
90
3.3. Metal ion extraction
The results of extraction as determined by AAS, mean values of three
readings of each of three extraction experiments, were calculated as
percentages of extraction based on the initial concentration, and are
presented in Fig. 5.
As a first observation, the extraction of the metals by blanks A (PVC)
and B (PVC-N3) is low, the extraction yields do not go over a maximum
value of 10%; 10 4.06% and 8 1.54% respectively. Only the percent-
age of Cadmium extraction reached 15 0.18% with the polymer A. In a
second observation, the extraction of Nickel is very low with polymers
a
For structures, see Scheme 3.
mmol triazole for 2a–e and N3 for B.
b
synthesized using the corresponding acyl chlorides and coupling them
on propargylamine in the presence of a base and a catalyst (Scheme
2). The obtained yields were modest (66–79%) but the products were
pure enough to be used without further purification. The structure
of 1a–d was confirmed by characteristic signals in NMR (ca. δ = 2.25
(triplet, `C–H) ppm in 1H and 70, 80 (C`C), 170 (C_O) ppm in 13C)
and IR spectroscopy (ca. 3300 (ν`C–H), 2100 (νC`C), 1640 (νC_O) cm−1).
2c–e, the yield of extraction never exceeded 10
performance of extraction for this metal is obtained with polymers 2b
and 2a with yields of extraction of 22 5.95% and 19 1.84%
1.52%. The best
respectively. The extraction of Copper is better than the one of Nickel,
the extraction yields being of 63 8.72% (2a), 58 4.48% (2b), 54
8.83% (2c), and not exceeding 9 2.07% for the others polymers. The
average yield for this metal by polymers 2a–c is in the order 58
4.51%, this value being comparable with that found by Pellera et al.
using aqueous solutions using agricultural by-product for removal of
Copper [32]. The result of Lead extraction with polymers 2a–c reached
up to 74 7.87%, but only a maximum of 21 8.64% with the others.
Extraction yields of Pb by polymers 2a–c are a little better than those
obtained by Chaari et al., which have achieved an adsorption perfor-
mance around 65% using a Tunisian smectic clay [33].
The extraction of Cadmium is better than with the other metals, one
of the polymer-supported triazole 2a was found to extract Cadmium se-
lectively with a high efficiency of 92
comparable with those obtained by us using the same appendages
onto poly(styrene) [20]. The extraction yields for this metal by polymers
2d and 2e are good and similar around 83 0.75%, while polymer 2b
3.2. Characterization of polymer-supported triazoles (2f–j)
The reaction between alkynes 1a–d and azido-PVC (B) was
performed using a CuAAC procedure to obtain polymer-supported
1,2,3-triazoles 2a–d with various substituents onto the triazole in the
fourth position (Scheme 3). PVC-N3 (B) was treated with an excess of
the alkyne in the presence of a base (DIPEA) and cuprous iodide as a
catalyst, to increase both the reaction speed and yield. Another polymer
2e was synthesized using phenylacetylene which does not have an
amide bond in order to evaluate this influence of this link [26]. The
cycloadditions were followed by ATR/FTIR and considered as finished
when the azide vibration was not visible anymore. The yields of
the cycloadditions were difficult to evaluate using a mass increase on
the scale used. The reactions were considered as quantitative based on
the ATR/FTIR analysis and previous work.
Residual vibrations form the azido group of B or from the starting
alkynes 1a–e were not observed onto the IR spectra of polymers 2a–e
(Fig. 3). On these spectra, vibrations form amide bonds (NH, C_O),
with the exception of 2e, can be observed together with vibrations
coming from the triazole ring and its substituent, when compared to
the spectrum of the starting polymer B.
7.49%. These results are
(72
7.03%) and polymer 2c (52
7.86%) were a bit less efficient.
The results for Cadmium extraction found for those polymers (2a, 2b,
2d and 2e) are similar to those found by M'leyh et al. using natural
clays of Borj Chekir [34]. For the polymeric triazoles 2a–e, the average
extraction yields are in the following order: Cd2+ N Pb2+ N Cu2+ N Ni2+
.
These results are comparable to those obtained by Sprynskyy et al. with
the adsorption–diffusion column filled by the zeolite [35].
At the beginning of our work onto this set of alkynes, we became
interested on the possible chelations when the triazole formed was
bearing an amide function. Polymers described in the literature are
incorporating amine or pyridine sidearm's (“pendant” or “integrated
design”) or only “simple” triazoles (“triazole design”) in order to chelate
a metal ion before their reduction inside dendrimeric structures, as an
example. Catalysis was the ultimate goal for most of them [36–40].
For the study of our supported pendant amide triazole, we evaluated
the polymers 2a–e. The amino methyl substituent of the triazole ring
was linked under an amide form to alkyl chain, as well as a phenyl
ring, in order to evaluate the effect of steric hindrance and/or hydropho-
bicity. In this series, the polymer 2e was prepared to act as a blank, since
no amide function nor the amino methyl was included. From the results
The DSC curves of azido-PVC (B) and the polymers 2a–e are shown
in Fig. 4. The glass-transition temperatures (Tg) of the polymers were
determined from inflection points of DSC curves and are listed in
Table 1 [30,31]. The Tc and Tm temperatures are not easy to find. In
the case of PVC-N3 (B), an exothermic peak was also observed at
of Cadmium extraction by the polymers 2a (92
7.49%), 2b (72
7.03%) and 2c (52 7.86%), we can observe that the extraction yield
is dropping with the chain length increase. For the polymers 2d and
2e, they have the same extraction yield for Cadmium (around 83%),
suggesting that the amide function has no effect onto the chelation of
Cadmium, but a phenyl ring increases the extraction yield to almost
the level of the methyl substituant of the amide like in 2a. The extraction
yields of Cadmium by polymers A (15 0.18%) and B (7 2.69%) with
no amide neither triazole are low, which seems to confirm that the
triazole is responsible for the chelation of Cadmium by the polymers
studied.
Fig. 5. Percentages of metal cation extraction for the polymers 2a–e, in comparison to the
values found for PVC (A) and PVC-N3 (B) as blanks.