High-strength EPP packaging bottom mat for refrigerator transportation and preparation method of high-strength EPP packaging bottom mat
A high-strength, bottom-cushion technology, applied in the polymer field, can solve the problems of being unenvironmental, non-recyclable, easy to break, etc., and achieve the effects of improving performance, increasing the degree of entanglement, and extending branched chains
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[0041] The above-mentioned preparation method of the high-strength EPP packaging bottom pad used for refrigerator transportation comprises the following steps:
[0042] Dry the ternary random copolymer polypropylene and add initiator, graft monomer, nucleating agent, toughening agent, anti-aging agent, etc. into the high-speed mixer according to the proportion and mix evenly, and feed it into the extruder through the feeder In the process, after melting, extruding, cooling, pelletizing, and drying procedures, high-strength and high-toughness melt-grafted modified polypropylene particles are obtained;
[0043] Add the above-mentioned high-strength and high-toughness melt-grafted modified EPP particles and water into the high-pressure reactor, and pass in the physical blowing agent CO 2 , the temperature of the equipment is set to 120-150°C, the pressure is set to 3.0-8.0MPa, after maintaining the pressure and stirring for 30-60min, adjust the pressure valve to reduce the pressu...
Embodiment 1
[0051] The raw materials are weighed in the following parts by weight: 90 parts of ternary copolymerized polypropylene resin, 1.5 parts of methacrylic acid, 7 parts of polyetheramine with a molecular weight of 3000, 0.05 part of dibenzoyl peroxide, 0.5 part of nano calcium carbonate, β- 0.5 parts of (3,5-di-tert-butyl-4-hydroxyphenyl) n-octadecyl propionate, 0.5 parts of ethoxylated octadecylamine;
[0052] Dry the terpolymer polypropylene resin at 50°C for 6 hours, put it into a high-speed mixer and mix it evenly with other raw materials, feed it into the extruder through a feeder, and go through the procedures of melting, extrusion, cooling, pelletizing and drying Finally, the modified polypropylene particles are obtained;
[0053] Add the above-mentioned modified polypropylene particles and water into the autoclave, and pass in the physical blowing agent CO 2 , the temperature of the equipment is set to 135°C, the pressure is set to 5.0MPa, after maintaining the pressure a...
Embodiment 2
[0059] The raw materials are weighed in the following parts by weight: 91 parts of ternary copolymerized polypropylene resin, 2 parts of methacrylic acid, 5 parts of polyetheramine with molecular weight of 3000, 0.1 part of benzoyl tert-butyl peroxide, 0.5 part of nano talcum powder, 0.5 parts of n-octadecyl β-(3,5-di-tert-butyl-4-hydroxyphenyl) propionate, 0.5 parts of ethoxylated octadecylamine;
[0060] The difference from Example 1 is that in the preparation step of Example 2, the speed of the main machine in the processing conditions of the melt extrusion of the extruder is 300 rpm; the pressure is set to 6.0 MPa when preparing a round of beads.
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