Process for producing expanded polyolefin resin particles and expanded polyolefin resin particles
US-9216525-B2 · Dec 22, 2015 · US
US10221292B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10221292-B2 |
| Application number | US-201815910652-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 2, 2018 |
| Priority date | Oct 15, 2014 |
| Publication date | Mar 5, 2019 |
| Grant date | Mar 5, 2019 |
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A method of producing a polypropylene resin in-mold expanded product, includes: placing polypropylene resin particles obtained from a base material resin having a melting point of 140° C. to 150° C., the base material resin comprising: a polypropylene resin A comprising 3 weight % to 15 weight % of 1-butene and having a melting point of 130° C. to 140° C.; and a polypropylene resin B having a melting point of 145° C. to 165° C., water, and an inorganic gas foaming agent in a pressure-resistant container, forming a mixture, dispersing the polypropylene resin particles while stirring the mixture, obtaining a dispersion liquid, increasing a temperature and a pressure in the pressure-resistant container, releasing the dispersion liquid from the pressure-resistant container into a region having a pressure lower than the pressure in the pressure-resistant container, producing expanded polypropylene resin particles; and filling a mold with the expanded polypropylene resin particles, and then heating the expanded polypropylene resin particles.
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What is claimed is: 1. A method of producing a polypropylene resin in-mold expanded molded product, comprising: placing polypropylene resin particles, water, and an inorganic gas foaming agent in a pressure-resistant container, forming a mixture, wherein the polypropylene resin particles comprise a core layer and a covering layer, wherein the core layer is obtained from a base material resin having a melting point of 140° C. to 150° C., the base material resin comprising: a polypropylene resin A comprising 3 weight % to 15 weight % of 1-butene and having a melting point of 130° C. to 140° C.; and a polypropylene resin B having a melting point of 145° C. to 165° C., and wherein the covering layer consists of the polypropylene resin A, dispersing the polypropylene resin particles while stirring the mixture, obtaining a dispersion liquid, increasing a temperature and a pressure in the pressure-resistant container, releasing the dispersion liquid from the pressure-resistant container into a region having a pressure lower than the pressure in the pressure-resistant container, producing expanded polypropylene resin particles each having an average cell diameter of 100 μm to 340 μm wherein the expanded polypropylene resin particles are each an expanded composite particle comprising the core layer and the covering layer, the core layer being covered with the covering layer; and obtaining the polypropylene resin in-mold expanded molded product by filling a mold with the expanded polypropylene resin particles, and then heating the expanded polypropylene resin particles, wherein the polypropylene resin in-mold expanded molded product has a density and a 50%-strained compressive strength satisfying the following: [50%-strained compressive strength (MPa)]≥0.0069×[Molded product density (g/L)]+0.018. 2. The method according to claim 1 , wherein the polypropylene resin A comprises 2 weight % to 10 weight % of ethylene. 3. The method according to claim 1 , wherein the inorganic gas foaming agent contains carbon dioxide. 4. The method according to claim 1 , further comprising: melting and kneading the polypropylene resin A and the polypropylene resin B in an extruder and obtaining the polypropylene resin particles. 5. The method according to claim 1 , further comprising: obtaining the polypropylene resin A by polymerization using a Ziegler catalyst. 6. The method according to claim 1 , wherein the expanded polypropylene resin particles are heated with steam having a pressure of 0.22 MPa (gauge pressure) or less.
Ethene-propene or ethene-propene-diene copolymers · CPC title
by impregnating polymer particles with the blowing agent · CPC title
Copolymers of propene (C08J2423/16 takes precedence) · CPC title
Extrusion of the foamable blend · CPC title
for articles of definite length, i.e. discrete articles · CPC title
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