Micro-cross-linked thermoplastic polyether ester elastomer and its preparing process
A thermoplastic polyether ester and elastomer technology, which is applied in the field of micro-crosslinked thermoplastic polyether ester elastomer and its preparation, can solve the problem of difficult to generate block copolymers, difficult to control the fluidity and product performance of polyether ester elastomer Unfavorable and other issues
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Embodiment 1
[0029] According to the prior art, 1018.2 parts of dimethyl terephthalate, 708.5 parts of 1,4-butanediol, 1407.1 parts of polyethylene glycol with a molecular weight of 2000, 5 parts of 1010 antioxidant, titanium 4.5 parts of tetrabutyl esters. Start stirring, the temperature of the kettle gradually rises to 160-220°C, the temperature of the fractionating column is set at 65°C, and methanol starts to distill out. When the amount of methanol distilled reaches 95% of the theoretical amount, the transesterification reaction can be considered complete. Gradually raise the temperature of the kettle to 240-280°C, and reduce the pressure in the kettle to below 1mmHg within 1 hour, and discharge the material when the stirring power reaches the maximum value. And the preparation method of the polyether ester elastomer of the embodiment of the present invention 1 is to add 140.7 parts of molecular weight to be the polyoxypropylene triol replacement part polyethylene glycol (accounting f...
Embodiment 2
[0033]According to the prior art, 1316.5 parts of dimethyl terephthalate, 916.1 parts of 1,4-butanediol, 1104.2 parts of polypropylene oxide diol with a molecular weight of 1000, 5 parts of antioxidant 1010, and 4.5 parts of titanic acid Tetrabutyl ester was added into a 10L polymerization kettle, and polymerized according to the steps in Example 1 above. Embodiment 2 of the present invention is to get 1024.7 parts of dimethyl terephthalate, 713.1 parts of 1,4-butanediol, 626.2 parts of molecular weight is 1000 polypropylene oxide glycol, 268.3 parts of molecular weight is 3000 polyepoxide Propane triol, 4 parts of antioxidant 1010, and 3.6 parts of tetrabutyl titanate were added to a 10L polymerization kettle, and polymerized according to the procedure in Example 1 above. Embodiment 2B of the present invention is to get 1276.5 parts of dimethyl terephthalate, 888.3 parts of 1,4-butanediol, 791.9 parts of molecular weight is the polypropylene oxide diol of 1000, 339.3 parts of...
Embodiment 3
[0037] According to the prior art, 1664.5 parts of dimethyl terephthalate, 1159.3 parts of 1,4-butanediol, 660.0 parts of polypropylene oxide diol with a molecular weight of 1000, 5.94 parts of trimethylolpropane, 5 parts of anti- Oxygen agent 1010 and 4.5 parts of tetrabutyl titanate were put into a 10L polymerization kettle, and the polymerization was carried out according to the above-mentioned steps of Example 1. And embodiment 3A of the present invention is to get 1660.3 parts of dimethyl terephthalates, 1155.4 parts of 1,4-butanediol, 533.3 parts of molecular weight is the polypropylene oxide diol of 1000, 133.3 parts of molecular weight is the polycyclic ring of 3000 Oxypropanetriol, 5 parts of antioxidant 1010, and 4.5 parts of tetrabutyl titanate were added to a 10L polymerization kettle, and polymerized according to the above-mentioned step 1 of Example 1.
[0038] Embodiment 3B of the present invention is to get 1666.0 parts of dimethyl terephthalate, 1159.3 parts o...
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