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13.3 Poly(Ethylene Terephthalate)-Based Nanocomposites 437
the cation, sodium - MMT, methyl, tallow, bis - 2 - hydroxyethyl, quaternary ammo-
nium - MMT (Cloisite 30B) (Table 13.5 , row b), dimethyl, benzyl, hydrogenated
tallow, quaternary ammonium - MMT (Cloisite 10A) (Table 13.5 , row g) and dime-
thyl, dehydrogenated tallow, quaternary ammonium - MMT (Cloisite 15A) (Table
13.5 , row i) were compared.
As revealed by both TEM and WAXD characterization, the shear in the extruder
favored the exfoliation process, which resulted in both intercalated and exfoliated
morphologies. PET nanocomposites obtained by using clay with polar modifi ers
showed intercalated and exfoliated morphologies, whereas tactoids were obtained
when only apolar modifi ers were present. The polymer – clay interactions and the
extrusion conditions were suffi cient to break the organized arrangement of the
natural MMT, so as to disperse it in the polymer matrix. The organic modifi er also
appeared to sustain the exfoliated clay sheets fl at since, in its absence, the intramo-
lecular interactions were stronger and the platelets tended to roll due to their high
fl exibility. A comparison of these two reports [121, 122] showed contradictory
results, however. As the recycled and virgin PET had practically identical structural
characteristics (although the recycled form usually had a lower viscosity in the
melt), the comparison mainly highlighted the strong effect of shear stresses on
the morphology. In fact, the stronger shear stresses developed in the twin - screw
extruder were most likely suffi cient to achieve an exfoliated/intercalated structure,
without using an organophilic modifi er. In the study of Pegoretti et al . [121] , the
lower shear stresses of the injection - molding machine produced the opposite
result, as in these conditions the main driving forces were the interactions of the
hydrophobic chains with the polymer matrix, which were capable of producing a
primary disaggregation of the fi ller.
The strong effects of processing conditions and rheological properties on mor-
phology were also reported by Krakalik et al . [123] , who prepared composites in a
co - rotating, twin - screw, microextruder by adding to recycled PET 5% (by weight)
of different modifi ed MMTs (Cloisite 6A, 15A, 20A, 25A, and 30B) (Table 13.5 ).
Subsequently, these authors observed the partial exfoliation of Cloisite 25A, 30B,
and 10A, which was in good agreement with the results observed by both Pegoretti
et al . [121] and Calcagno et al . [122] .
Davis et al . [125] investigated the effects of melt - processing conditions on the
quality of PET/MMT nanocomposites prepared in a mini twin - screw extruder
at 285 ° C, and identifi ed the need to use a highly stable ammonium salt in
modifi ed MMT. In fact, the use N , N - dimethyl - N , N - dioctadecylammonium - MMT
led to the production of black PET nanocomposites as a result of ammonium
salt degradation under the processing conditions. The most dispersed, exfoliated
PET nanocomposite was achieved by melt - mixing at 21 radians per second for
2 min in a nitrogen atmosphere, after drying the polymer at 120 ° C, and the
clay at 150 ° C. Alternative mixing conditions, longer residence times, and higher
screw speeds resulted in poorer - quality nanocomposites. The alternative use of
a hexadecyl imidazolium salt, which resulted in an intercalated/exfoliated mor-
phology, allowed improvements in stability, as the imidazolium salt (which has
a decomposition temperature of 350 ° C) is stable under the conditions of