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238  10  Highly Toughened Polylactide-Based Materials through Melt-Blending Techniques

                                  O                   O
                            HO                  HO
                                    OH                  OH
                               CH 3                 CH 3
                             L-Lactic acid       D-Lactic acid



                                                            O
                           O               O
                               CH 3             CH 3             CH 3
                        O                O                O
                             O               O        H C     O
                    H 3 C            H 3 C             3
                           O               O                O
                       L,L-Lactide     D,L-Lactide       D,D-Lactide

                    Figure 10.2 Stereoforms of lactides.

                    backbiting reaction [21]. Because of the chiral nature of lactic acid, LA exists in
                    three different forms, that is, L,L-LA, D,D-LA, and D,L-LA (meso lactide) as well as
                    a 50/50 mixture of L,L-LA and D,D-LA referred to as racemic lactide (Figure 10.2).
                    In this regard, the extent of racemization of LA depends on different factors such
                    as the reaction conditions and the type of catalyst used in the backbiting reaction
                    of the lactic acid oligomer [22].
                      The first attempt to prepare PLA was ascribed to Pelouze in 1845. The
                    condensation of L-lactic acid and the continuous removal of water leads to
                    low-molecular-weight PLA (usually lower than 30 000 g mol −1  with a molecular
                    weight dispersity close to 2) [23]. However, the polycondensation method suffers
                    from several drawbacks such as the need for high temperature, continuous
                    removal of by-products (most often water), and long reaction time [24]. In con-
                    trast, high-molecular-weight PLA can be obtained in a straightforward manner
                    via ROP of LA. In this respect, ROP of LA promoted by protic compounds
                    (water, alcohol, and amine) as initiators and tin(II) octoate (Sn(Oct) ) as catalyst
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                    is industrially preferred to obtain high-molecular-weight PLA in bulk (absence of
                    solvent) (Figure 10.3).
                      Upon the choice of polymerization conditions (temperature, solvent, initiator,
                    and catalyst), ROP can be a “living” process, that is, without any irreversible
                    transfer and termination reactions, affording a good control over the molecular
                    parameters of polymeric chains (predetermination of the molecular weight by the
                    monomer-to-initiator molar ratio and a narrow molecular weight distribution)
                    and the topology of the as-synthesized polymer. Depending on the nature of
                    catalysts and initiators, ROP can proceed through different mechanisms: cationic,
                    anionic (nucleophilic), or coordination type [20]. For industrial implementation,
                    Sn(Oct) is preferentially used on the approval of FDA (US Food and Drug
                           2
                    Administration); it has good efficiency toward the synthesis of high molecular
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