Non-glossy rubber modified aromatic vinyl-vinyl cyanide copolymer and method for continuously preparing the same
A technology for aromatic vinyl and vinyl cyanide, applied in the field of continuous preparation of the copolymer and rubber-modified aromatic vinyl-vinyl cyanide copolymer, can solve undesired problems
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Embodiment 1
[0081] In the mixed solution comprising 53.4 parts by weight of styrene, 17.8 parts by weight of acrylonitrile and 20 parts by weight of ethylbenzene, a butadiene rubber (BR-1: ASADENE 55AE with a solution viscosity of 170 cps in a 5% styrene solution was added. ), and make it dissolve, then add 0.015 parts by weight of 1,1-bis(tert-butylperoxy)cyclohexane and 0.07 parts by weight of tert-dodecyl mercaptan as molecular weight control agent to prepare reaction solution . The prepared reaction solution was fed into the reactor at a rate of 25 kg / hr. During the polymerization, the first reactor was controlled to a stirring rate of 120 rpm and a conversion of 35%, while the second reactor was controlled to a stirring rate of 70 rpm and a conversion of 75%. Then, the reactants discharged from the reactor are continuously sent to a devolatilization device to remove unreacted monomers, and then the polymerized product is pelletized to obtain an ABS resin. The average rubber particl...
Embodiment 2
[0084] Example 2 was implemented in the same manner as Example 1 except that the stirring rate of the first reactor was 100 rpm. The average rubber particle diameter of the ABS resin prepared in Example 2 was about 8.58 μm. TEM image of rubber particles figure 2 shown.
Embodiment 3
[0086] Example 3 was implemented in the same manner as in Example 1 except that the stirring rate of the first reactor was 80 rpm. The average rubber particle diameter of the ABS resin prepared in Example 3 was about 14.11 μm. TEM image of rubber particles image 3 shown.
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