Polymethyl methacrylate and preparation method thereof
A technology of polymethyl methacrylate and parts of methyl methacrylate is applied in the field of polymethyl methacrylate and its preparation, and can solve the problem of improving heat resistance, loss of fluidity, and disadvantage of injection molding of polymethyl methacrylate. Influence, heat resistance and fluidity are difficult to balance and other issues
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Embodiment 1
[0056] Add 95 parts by mass of methyl methacrylate, 2 parts by mass of isobornyl methacrylate, 3 parts by mass of dicyclopentyl methacrylate, 0.5 part of azobisisobutyronitrile, 0.35 part of n-dodecylsulfide in the batching tank Alcohol, stir evenly to prepare the oil phase. In addition, add 0.3 parts of polyvinyl alcohol 1788 and 200 parts of deionized water into the reactor, stir and dissolve to prepare the water phase evenly. Add the oil phase material in the batching tank to the water phase of the reaction kettle, fully replace it with nitrogen, and start stirring at the same time to prepare a suspension.
[0057] The reaction kettle was heated through an oil bath, and the temperature was gradually raised to 70° C. to start polymerization. After reacting at 70°C for 3h, the temperature was raised to 90-100°C for further reaction for 2h. End the reaction.
[0058] The obtained reaction product was filtered, washed with water, and dried at 80° C. for 24 hours to obtain a ...
Embodiment 2
[0060] Add 80 parts by mass of methyl methacrylate, 10 parts by mass of isobornyl methacrylate, 10 parts by mass of dicyclopentyl methacrylate, 0.5 parts of azobisisobutyronitrile, 0.35 parts of n-dodecylsulfide in the batching tank Alcohol, stir evenly to prepare the oil phase. In addition, add 0.3 parts of polyvinyl alcohol 1788 and 200 parts of deionized water into the reactor, stir and dissolve to prepare the water phase evenly. Add the oil phase material in the batching tank to the water phase of the reaction kettle, fully replace it with nitrogen, and start stirring at the same time to prepare a suspension.
[0061] The reaction kettle was heated through an oil bath, and the temperature was gradually raised to 70° C. to start polymerization. After reacting at 70°C for 3h, the temperature was raised to 90-100°C for further reaction for 2h. End the reaction.
[0062] The obtained reaction product was filtered, washed with water, and dried at 80° C. for 24 hours to obtai...
Embodiment 3
[0064] Add 70 parts by mass of methyl methacrylate, 10 parts by mass of isobornyl methacrylate, 20 parts by mass of dicyclopentyl methacrylate, 0.5 part of azobisisobutyronitrile, 0.35 part of n-dodecylsulfide in the batching tank Alcohol, stir evenly to prepare the oil phase. In addition, add 0.3 parts of polyvinyl alcohol 1788 and 200 parts of deionized water into the reactor, stir and dissolve to prepare the water phase evenly. Add the oil phase material in the batching tank to the water phase of the reaction kettle, fully replace it with nitrogen, and start stirring at the same time to prepare a suspension.
[0065] The reaction kettle was heated through an oil bath, and the temperature was gradually raised to 70° C. to start polymerization. After reacting at 70°C for 3h, the temperature was raised to 90-100°C for further reaction for 2h. End the reaction.
[0066] The obtained reaction product was filtered, washed with water, and dried at 80° C. for 24 hours to obtain ...
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