Page 162 - Engineering Plastics Handbook
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Polybutylene Terephthalate (PBT)  135

        methanol or water during transesterification reaction, with 1,4-butanediol
        during second polycondensation stages. The catalyst is usually applied
        during reaction; the preferred catalysts  are organotitanium or organotin
        compounds. The most commonly used catalysts for PBT are tetra alkyl
        titanates. The by-product 1,4-butanediol is removed from the melt by
        mixing the melt and by using vacuum. Through the elimination of excess
        1,4-butanediol, a number-average molecular weight of up to 30,000 g/mol
        is attainable. Owing to the high temperatures during the second stage,
        oxidative thermal decomposition and yellowing occur. These decomposi-
        tion reactions place the upper limit on the molecular weight that can be
        realized by the normal melt condensation reaction. High-molecular-weight
        PBT grades for extrusion applications are typically produced by further
        polycondensation in an additional solid-state process at temperatures 15
        to 40°C below the melting temperature of PBT and under vacuum or in
        an inert gas atmosphere (see Fig. 7.4). The solid-state reaction is carried
        out separately, generally minimizing the degradation and discoloration of
        high- molecular-weight PBT [4, 5].


        Commercial process
        For commercial PBT polymerization, both batch process and continuous
        process can be used. When a variety of different grades of PBT are needed,
        a batch process is preferred; however, for large commercial production of
        PBT of more than 20,000 metric ton capacities, a continuous process is
        more economical.
          Due to different residence times needed for the reaction steps, the indus-
        trial batch processes are typically run in multiple reactors. Usually two
        reactors are involved, an ester interchange (EI) reactor designed to extract
        methanol or water and a polycondensation (PC) reactor designed to drive
        the polymerization and build molecular weight by removing excess
        1,4-butanediol as well as volatile by-products. During EI reaction the

        Melt polymerization
             Direct/Transesterification
                                         O
                 TPA + 2 Butanediol = BHBT + 2H 2
                 DMT + 2 Butanediol = BHBT + 2CH OH
                                          3
             Polycondensation
                                  + Butanediol
                 BHBT + BHBT = PBT 2
                      + PBT  = PBT   + Butanediol
                 PBT n   m     n+m
                                                Figure 7.4 Reaction equations for
        Solid-state polymerization              the polymerization of PBT.
                 PBT  + PBT  = PBT n+m  + Butanediol
                    n
                         m
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