Polypropylene foaming material, production and preparation method of product
A foamed material and polypropylene technology, which is applied in the field of polymer foamed material production, can solve problems such as unfavorable pressure control in the melt extrusion process, and achieve the effects of avoiding easy cross-linking, reducing production costs and being easy to control.
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Embodiment 1
[0038] Raw material components: component (A) is 100 parts of homopolymerized PP powder, produced by Shandong Kairi Chemical Co., Ltd., the brand is 045, MFR 3.0g / 10min; component (B) is 10 parts of ethylene acrylic acid copolymer, acrylic acid Content 11%; Component (C) is 1 part of superfine zinc oxide; Component (D) is 0.08 part of dicumyl peroxide; Component (E) is 0.15 part of four [β-(3,5-di tert-Butyl-4-hydroxyphenyl) propionate] pentaerythritol, dilaurate thiodipropionate 0.3 part; component (F) is 0.5 part glyceryl monostearate; component (G) is 0.4 part blowing agent AC.
[0039]Leather material: polypropylene copolymer, produced by Qilu Petrochemical Company, grade EPS30R, MFR 2.0g / 10min.
[0040] The structure and function of the single-screw extruder: The single-screw extruder B used has a screw diameter of 90mm, a length-to-diameter ratio of 33:1, frequency conversion speed regulation, and 5-stage heating and temperature control. Single screw A, C screw diamete...
Embodiment 2
[0051] Raw material components: component (A) is 100 parts of homopolymerized PP powder, produced by Shandong Kairi Chemical Co., Ltd., brand is 045, MFR 3.0g / 10min; component (B) is 10 parts of ethylene acrylic acid copolymer, acrylic acid content 11%; component (C) is 1 part of superfine zinc oxide; component (D) is 0.12 part of dicumyl peroxide; component (E) is 0.15 part of four [β-(3,5- tert-Butyl-4-hydroxyphenyl) propionate] pentaerythritol, 0.3 part dilaurate thiodipropionate; component (F) is 0.5 part glyceryl monostearate; component (G) is 0.4 part blowing agent AC.
[0052] Extruder B temperature setting: 170°C, 192°C, 197°C, 205°C, 195°C
[0053] Mold temperature, 180°C, 178°C, 178°C, 178°C, 178°C, 178°C, 180°C
[0054] The mode of operation is the same as in Example 1.
Embodiment 3
[0056] Raw material components: component (A) is 100 parts of homopolymerized PP powder, produced by Shandong Kairi Chemical Co., Ltd., the brand is 045, MFR 3.0g / 10min; component (B) is 15 parts of ethylene acrylic acid copolymer, acrylic acid content 11%; component (C) is 1 part of superfine zinc oxide; component (D) is 0.15 part of dicumyl peroxide; component (E) is 0.15 part of four [β-(3,5- tert-Butyl-4-hydroxyphenyl) propionate] pentaerythritol, 0.3 part dilaurate thiodipropionate; component (F) is 0.5 part glyceryl monostearate; component (G) is 0.4 part blowing agent AC.
[0057] Extruder B temperature setting: 170°C, 188°C, 195°C, 198°C, 190°C
[0058] Mold temperature, 177°C, 175°C, 175°C, 175°C, 175°C, 175°C, 177°C
[0059] All the other operating modes are the same as in Example 1.
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