Styrene block copolymer reaction extruding polymerizing method
A block copolymer and styrenic technology, applied in the field of preparation of styrenic block copolymers, can solve the problems of restricting the application of styrenic block copolymers, increasing equipment investment and energy consumption, heavy pollution and the like
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Embodiment 1
[0073] 3 feed inlets are set on the twin-screw extruder, followed by styrene monomer feed inlet, n-butyllithium initiator feed inlet, and isoprene monomer feed inlet; under the delivery of metering pump, The refined monomer and initiator were input into a twin-screw extruder for staged feeding reaction extrusion polymerization to obtain a diblock styrene-isoprene copolymer product A with a number average molecular weight of 230,000. The process conditions are set as follows:
[0074] The temperature of each section of the screw: 40 / 60 / 150 / 200°C
[0075] Monomer mass flow rate (kg / hour): styrene / isoprene=1.0 / 4.0
[0076] Initiator mass flow rate 1.5g / hour
[0077] Screw speed: 50rpm
[0078] product
Embodiment 2
[0080] There are 4 feed ports on the twin-screw extruder, which are styrene monomer feed port, n-butyllithium initiator feed port, isoprene monomer feed port, styrene monomer feed port ; Under the delivery of the metering pump, the refined monomer and initiator are input into the twin-screw extruder for staged feeding reaction extrusion polymerization to obtain a triblock styrene-isoprene with a number average molecular weight of 330,000 Ethylene-styrene copolymer product B. The process conditions are set as follows:
[0081] The temperature of each section of the screw: 20 / 45 / 140 / 180 / 200°C
[0082] Monomer mass flow rate (kg / hour): styrene / isoprene / styrene=0.75 / 3.5 / 0.75
[0083] Initiator mass flow rate 1.1g / hour
[0084] Screw speed: 50rpm
[0085] Product B performance test results
[0086] product
Embodiment 3
[0088] product
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