Method for continuously producing thermoplastic resin from conjugated diene and thermoplastic resin produced by the same
A method for continuously producing a thermoplastic resin from a conjugated diene includes: primarily polymerizing a conjugated diene monomer with an aromatic vinyl monomer in a first solvent in a first reactor, and feeding a hydroxyl group-containing polymerization inhibitor and a polar hydrocarbon to the first reactor to prepare a rubber solution; and adding an aromatic vinyl monomer and a monomer copolymerizable with the aromatic vinyl monomer to the rubber solution, and subjecting the mixture to secondary polymerization in a second solvent of the same kind as the first solvent in a second reactor. The method can provide a thermoplastic resin that can have excellent color and low gloss characteristics.
1. A method for continuously producing a thermoplastic resin from a conjugated diene, the method comprising:
primarily polymerizing a conjugated diene monomer with an aromatic vinyl monomer in a first solvent in a first reactor, and feeding a hydroxyl group-containing polymerization inhibitor and a polar hydrocarbon to the first reactor to prepare a rubber solution; and
adding an aromatic vinyl monomer and a monomer copolymerizable with the aromatic vinyl monomer to the rubber solution, and subjecting the mixture to secondary polymerization in a second solvent of the same kind as the first solvent in a second reactor,
wherein the polar hydrocarbon is a hydrophilic organic solvent comprising low molecular weight ether-based solvent, ketone-based solvent, sulfoxide, or a combination thereof.
2. The method as claimed in claim 1 , wherein the conjugated diene monomer is butadiene, isoprene or a combination thereof.
3. The method as claimed in claim 1 , wherein the polymerization in the first reactor is carried out using an organometallic catalyst.
4. The method as claimed in claim 1 , wherein a vinyl modifier is added for the polymerization in the first reactor.
5. The method as claimed in claim 1 , wherein the rubber solution prepared by the polymerization in the first reactor is concentrated by extrusion before being fed into the second reactor.
6. The method as claimed in claim 1 , wherein the first and second solvents are aromatic solvents.
7. The method as claimed in claim 1 , wherein the hydroxyl group-containing polymerization inhibitor comprises water, low molecular weight monohydric alcohol, low molecular weight dihydric alcohol, or a combination thereof.
8. The method as claimed in claim 1 , wherein the hydroxyl group-containing polymerization inhibitor and the polar hydrocarbon are in a weight ratio of about 1:1 to about 1:3.5.
9. The method as claimed in claim 1 , wherein no rubber bale is formed.
10. A thermoplastic resin which is produced by the method of claim 1 , having a yellow index (YI) of about 5 or less, as measured in accordance with ASTM E313, and a ⅛″ notched impact strength of about 10 to about 60 kgf·cm/cm, as measured in accordance with ASTM D256.
11. A method for continuously producing a thermoplastic resin from a conjugated diene, the method comprising:
primarily polymerizing a conjugated diene monomer with an aromatic vinyl monomer in a first solvent in a first reactor, and feeding a hydroxyl group-containing polymerization inhibitor and a polar hydrocarbon to the first reactor to prepare a rubber solution; and
adding an aromatic vinyl monomer and a monomer copolymerizable with the aromatic vinyl monomer to the rubber solution, and subjecting the mixture to secondary polymerization in a second solvent of the same kind as the first solvent in a second reactor,
wherein a vinyl modifier is added for the polymerization in the first reactor.
12. A method for continuously producing a thermoplastic resin from a conjugated diene, the method comprising:
primarily polymerizing a conjugated diene monomer with an aromatic vinyl monomer in a first solvent in a first reactor, and feeding a hydroxyl group-containing polymerization inhibitor and a polar hydrocarbon to the first reactor to prepare a rubber solution; and
adding an aromatic vinyl monomer and a monomer copolymerizable with the aromatic vinyl monomer to the rubber solution, and subjecting the mixture to secondary polymerization in a second solvent of the same kind as the first solvent in a second reactor,
wherein the rubber solution prepared by the polymerization in the first reactor is concentrated by extrusion before being fed into the second reactor.