Preparation method of high-strength specially shaped PMI (polymethacrylimide) foam
A technology of polymethacrylimide and acrylimide, which is applied in the field of preparation of high-strength special-shaped polyacrylimide foam materials, can solve the problems of low bonding strength between boundaries, increased cost of special-shaped foam, and low particle yield and other problems, to achieve the effect of saving the time of foaming in the mold, fast preparation speed and good performance
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Embodiment 1
[0052] (1) Prepolymerization: 50 parts by weight of (meth)acrylic acid, 50 parts by weight of (meth)acrylonitrile, 20 parts by weight of acrylamide, 8.5 parts by weight of polyether siloxane, 1 part by weight of foaming agent, medium and high temperature Add 0.6 parts by weight of initiator, 7.5 parts by weight of ricinoleol sodium salt of sulfonation, 8 parts by weight of crosslinking agent, and 8 parts by weight of styrene into the dispersion kettle, vacuumize, fill with nitrogen, remove the air in the kettle, and then continue Nitrogen flow, nitrogen flow rate 13mL / min, disperse the mixed solution evenly, and then stir while heating, the reaction temperature is 85°C, the stirring speed is 20r / min, and the reaction is 105min. The viscosity of the prepolymerized solution is 63mpa.s; reduce the temperature of the reaction solution to At 7°C, add 1 part by weight of a low-temperature initiator and stir to dissolve;
[0053] (2) Foaming: transfer the material liquid into the aut...
Embodiment 2
[0060] (1) Prepolymerization: 40 parts by weight of (meth)acrylic acid, 60 parts by weight of (meth)acrylonitrile, 10 parts by weight of methyl acrylate, 10 parts by weight of polyacrylamide, 2.5 parts by weight of foaming agent, and medium-high temperature initiation Add 0.7 parts by weight of agent, 8 parts by weight of sodium lauryl sulfate, 4 parts by weight of crosslinking agent, and 7.6 parts by weight of 4-acetoxystyrene into the dispersion kettle, vacuumize, fill with nitrogen, and get rid of the air in the kettle. Then continue to flow nitrogen, the nitrogen flow rate is 12mL / min, disperse the mixed solution evenly, and then stir while heating, the reaction temperature is 85°C, the stirring speed is 18r / min, and the reaction is 100min. The viscosity of the pre-polymerization liquid is 61mpa.s; reduce the reaction liquid When the temperature reaches 9°C, add 0.73 parts by weight of a low-temperature initiator and stir to dissolve;
[0061] (2) Foaming: add 7.5 parts by...
Embodiment 3
[0068] (1) Prepolymerization: 65 parts by weight of (meth)acrylic acid, 35 parts by weight of (meth)acrylonitrile, 15 parts by weight of maleimide, 8 parts by weight of polyvinyl alcohol, 3 parts by weight of foaming agent, Add 0.9 parts by weight of high-temperature initiator, 7 parts by weight of fatty alcohol polyoxyethylene ether sodium sulfate, 2 parts by weight of crosslinking agent, and 5 parts by weight of α-methylstyrene into the dispersion kettle, vacuumize, fill with nitrogen, and remove the Then continue to pass nitrogen, the nitrogen flow rate is 14mL / min, disperse the mixture evenly, and then stir while heating, the reaction temperature is 78°C, the stirring speed is 20r / min, the reaction is 120min, and the viscosity of the pre-polymerization liquid is 70mpa.s; Lower the temperature of the reaction solution to 8°C, add 0.4 parts by weight of a low-temperature initiator, and stir to dissolve;
[0069] (2) Foaming: add 5 parts by weight of magnesium carbonate in th...
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