Copolymer preparation method, copolymer prepared thereby, and thermoplastic resin composition comprising same
A technology of copolymer and polymerization initiator, applied in the field of copolymer preparation, can solve the problems of deterioration of physical properties of copolymer, poor thermal stability, increase in yellowness, etc., achieve uniform distribution of thermal stability, excellent thermal stability, prevent effect of gas
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[0036] The present invention provides a method for preparing a copolymer in which the heterogeneity of monomer units in the copolymer is reduced and has excellent thermal stability.
[0037] The production method of the copolymer according to the present invention may be a production method of a styrenic copolymer, and as a specific example, may be a production method of a heat-resistant styrenic copolymer.
[0038] The preparation method of the copolymer according to the present invention is characterized in that it includes the step of adding an alkyl-substituted aromatic vinyl-based monomer and a vinyl cyano-based monomer to polymerize in the presence of a polymerization initiator (S10), wherein In the step (S10), the vinyl cyano monomer is added at one time before the polymerization is initiated, and the monomer droplets are continuously and separately added during the polymerization in the step (S10), and the monomer droplets contain part or all of the Alkyl substituted a...
Embodiment 1
[0093]
[0094] In a mixing device equipped with a stirrer, add 22.8 parts by weight of ion-exchanged water, 20 parts by weight of α-methylstyrene, 0.26 parts by weight of tricalcium phosphate and 0.001 parts by weight of polyoxyethylene alkyl ether phosphate and stirring to prepare a monomer dispersion for addition of monomer droplets.
[0095]
[0096] Into the reactor, 91.2 parts by weight of ion-exchanged water, 48 parts by weight of α-methylstyrene, 32 parts by weight of acrylonitrile, 0.5 parts by weight of 1,1-bis(tert- Butyl peroxide) cyclohexane, 0.1 parts by weight of t-butyl peroxybenzoate as the second polymerization initiator, 0.004 parts by weight of polyoxyethylene alkyl ether phosphate, and 1.04 parts by weight of tricalcium phosphate, And polymerization was initiated at 100°C. Upon initiation of polymerization, monomer droplets from a prepared monomer dispersion containing 20 parts by weight of α-methylstyrene were continuously added for 8 hours while mai...
Embodiment 2
[0099] Except in Example 1, during the preparation of the copolymer, when the polymerization was initiated, monomer droplets from the prepared monomer dispersion containing 20 parts by weight of α-methylstyrene were continuously added for 6 hours, while A rate of 3.33 parts by weight / hour (based on α-methylstyrene monomer) was maintained, and after completion of the addition of monomer droplets (polymerization conversion 70%), the polymerization was allowed to proceed for an additional 6 hours, in accordance with the implementation Example 2 was carried out in the same manner as Example 1.
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