Page 127 - Biodegradable Polyesters
P. 127

4.5  Conclusions  105

               k and k , which means faster transesterification and esterification rates and, as a
                     2
                1
               result, lower carboxyl concentrations at all temperatures and higher amounts of
               hydroxyl consumption. As a result, the polyesters produced exhibit higher intrin-
               sic viscosities and average molecular weights. Accordingly, use of a larger glycol
               (i.e., PG and consequently BG) leads to lower esterification kinetic rate constant,
               following the number of methylene units. However, the transesterfication reaction
               rate constant of PPSu is much lower compared to that of PBSu, leading to higher
               number of carboxyl and hydroxyl end groups and therefore eventually lower IV
               values, meaning lower average molecular weights.
                In addition, the values of the esterification rate constant, k , estimated are
                                                                 2
               always much larger compared to the corresponding value of k in all three
                                                                   1
               poly(alkylene succinate)s. This signifies esterification proceeding in a much
               faster rate compared to transesterification. Since carboxyl end groups are only
               consumed through the esterification reaction, this explains the very low values
               of COOH end groups measured and as a result, the cessation of their reaction
               after a point and the continuation of the reaction only through transesterification
               (consumption of OH end groups).
                Finally, the activation energies for the transesterification and esterification reac-
               tions were determined. Results showed that the esterification reaction decreases
               with increasing methylene units in glycols (i.e., PESu > PPSu > PBSu), although
               the activation energy of the transesterification reaction was larger in PESu fol-
               lowed by PBSu and significantly lower in PPSu [45]. Results on the estimated val-
               ues of the inactive end group concentration, [OH] and [COOH] of PESu, PPSu,
                                                                 i
                                                      i
               and PBSu can be found in Ref. [45].

               4.5
               Conclusions

               Production of 1,3-PD in high quality and quantity during the last 15–20 years
               has led to the synthesis of several aliphatic polyesters with biodegradable prop-
               erties. Poly(propylene alkylanedicarboxylate) polyesters can be prepared by the
               two-stage melt polycondensation method (esterification and polycondensation)
               using proper amounts of aliphatic acids and 1,3-PD and a procedure similar to
               that used for aromatic polyesters.
                PPSu presents lower crystallinity, crystallization rates, and melting point com-
               pared to its homologs PESu and PBSu This in turn results in a polymer with higher
               enzymatic hydrolysis rates and hence greater biodegradability. On the other hand,
               retardation in PPSu crystallization is due to its reduced symmetry caused by the
               propylene units.
                Esterification and polycondensation kinetics of PPSu synthesis can be well
               described on the basis of rather simple simulation models, taking into account
               the reaction kinetics and the functional group modeling approach. The latter is
               a very beneficial technique which includes aspects of the reaction mechanism
               although with the minimum computational effort.
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