Conjugated diene and monovinylarene random copolymer, and preparation method thereof
A technology of monovinyl arene and conjugated diene, which is applied in the field of preparation of conjugated diene and monovinyl arene random copolymer, can solve the problems of increasing vinyl structure content, high production cost, butadiene and benzene The problems of incomplete conversion of ethylene monomers, etc., can achieve the effect of increasing the polymerization temperature of the system, increasing the Mw/Mn, and increasing the monomer conversion rate.
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[0018] The preparation method of the random copolymer of conjugated diene and monovinylarene provided by the present invention is to carry out continuous copolymerization reaction in a continuous polymerization reaction device comprising a plurality of series reactors, the method comprising: under anionic polymerization conditions, The reaction materials containing the first part of conjugated diene, monovinylarene, solvent, gel inhibitor and monoorganolithium initiator are continuously introduced from the first tank of the continuous polymerization reaction device, and successively introduced in the continuous polymerization The continuous copolymerization reaction is carried out in each reactor of the reaction device, wherein the second part of conjugated diene is respectively introduced into each reactor, and the polymerization temperature is controlled at 90-140°C.
[0019] In the present invention, the continuous copolymerization reaction is carried out in a continuous pol...
Embodiment 1
[0058] This example illustrates the preparation of the random copolymer of conjugated diene and monovinylarene of the present invention.
[0059] Three 5-liter polymerization reactors connected in series are used as continuous polymerization reaction devices.
[0060] In the continuous polymerization reaction device, under the protective atmosphere of high-purity nitrogen, the total residence time of the reaction materials in the three tanks is 50 minutes, and the polymerization reaction pressure is controlled at 0.7±0.05MPa:
[0061] (1) Add reaction materials from the bottom of the first kettle: hexane fraction 9180g / h, styrene 1224g / h, 1,3-butadiene 1101.6g / h, n-butyl lithium 20.4mmol / h and 1,2- Butadiene 5.97g / h, carry out first kettle continuous polymerization reaction;
[0062] (2) Add 1,3-butadiene 367.2g / h at the bottom of the second kettle;
[0063] (3) Add 1,3-butadiene 367.2g / h at the bottom of the three-pot;
[0064] (4) Add 0.37 g / h terminator water at the outl...
Embodiment 2
[0074] This example illustrates the preparation of the random copolymer of conjugated diene and monovinylarene of the present invention.
[0075] Three 5-liter polymerization reactors connected in series are used as continuous polymerization reaction devices.
[0076] In the continuous polymerization reaction device, under the protective atmosphere of high-purity nitrogen, the total residence time of the reaction materials in the three tanks is 60 minutes, and the polymerization reaction pressure is controlled at 0.8±0.05MPa:
[0077] (1) Add reaction materials from the bottom of the first kettle: cyclohexane 7956g / h, styrene 448g / h, 1,3-butadiene 538.56g / h, n-butyllithium 10.2mmol / h and 1,2- Butadiene 4.38g / h, carry out first kettle continuous polymerization reaction;
[0078] (2) Add 1,3-butadiene 718.08g / h at the bottom of the second kettle;
[0079] (3) Add 1,3-butadiene 538.56g / h at the bottom of the three-pot;
[0080] (4) Add 0.15 mg / h terminator water at the outlet ...
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