Composite molded body and method for producing same
A composite molded body and molded body technology, applied in the field of molding, can solve the problems of damage to its physical properties, insufficient heat resistance of foamed bodies, etc., and achieve the effect of high degree of design freedom
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[0110] Hereinafter, specific examples and comparative examples of the present invention will be described together, but the present invention is not limited to the following examples.
[0111] In addition, in the following Examples, the ultraviolet irradiation apparatus used the Fusion UV system Japan Co., Ltd. Light Hanma 6 and H Ball. For the measurement of peak illuminance and integrated light intensity, the UV integrated light meter UIT-150-A (sensitivity wavelength range 310-390nm, calibration wavelength 365nm) was used. For the measurement of the hardness, an E-type durometer according to JIS K6253 was used.
[0112] (Preparation of sheet-like foamed resin moldings)
[0113] Synthesis of Allyl-terminated Polypropylene Oxide Polymers
[0114] Polyoxypropylene diol with a molecular weight of about 10,000 was used as an initiator to polymerize propylene oxide with a zinc hexacyanocobaltate gram complex catalyst, and a number average molecular weight of about 28,500 was ...
manufacture example 1)
[0124] Production method of poly(n-butyl acrylate) having acryloyl groups at both ends
[0125] 100 parts of n-butyl acrylate were deoxidized. Deoxygenate the inside of the reaction vessel, add 0.42 parts of cuprous bromide, 20 parts of deoxygenated n-butyl acrylate, 4.4 parts of acetonitrile, and 1.8 parts of diethyl 2,5-dibromoadipate, and mix at 80°C. 0.018 part of pentamethyldiethylenetriamine (hereinafter abbreviated as triamine) was added to start the polymerization reaction. The remaining 80 parts of n-butyl acrylate were gradually added to perform a polymerization reaction. During the polymerization, triamine was appropriately added to adjust the polymerization rate, and the polymerization was carried out while adjusting the internal temperature to about 80°C to about 90°C. When the monomer conversion rate (polymerization reaction rate) is about 95% or more, introduce oxygen-nitrogen mixed gas into the gas phase part of the reaction vessel, and heat and stir while ...
manufacture example 2)
[0127] Production method of poly(n-butyl acrylate) having acryloyl group at one end
[0128] 100 parts of n-butyl acrylate were deoxidized. Deoxygenate the inside of the reaction vessel, add 0.42 parts of cuprous bromide, 20 parts of deoxygenated n-butyl acrylate, 4.4 parts of acetonitrile, 1.9 parts of ethyl α-bromobutyrate, mix at 80°C, add pentamethyldi 0.018 parts of ethylenetriamine (hereinafter referred to as triamine) to start the polymerization reaction. The remaining 80 parts of n-butyl acrylate were gradually added to perform a polymerization reaction. During the polymerization, triamine was appropriately added to adjust the polymerization rate, and the polymerization was carried out while adjusting the internal temperature to about 80°C to about 90°C. When the monomer conversion rate (polymerization reaction rate) is about 95% or more, introduce oxygen-nitrogen mixed gas into the gas phase part of the reaction vessel, and heat and stir while maintaining the inte...
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