US2017218158A1PendingUtilityA1
Polypropylene resin foamed particles, in-mold foam molded body of polypropylene resin, and method for manufacturing same
Est. expiryOct 15, 2034(~8.2 yrs left)· nominal 20-yr term from priority
C08J 2323/14C08J 2203/06C08J 9/232B29C 44/02C08J 2201/03C08J 9/18C08J 2423/14B29C 44/3426C08L 2314/02C08L 23/16C08L 23/14C08J 2423/16C08J 2205/04C08J 9/224C08J 9/0061B29K 2105/048B29C 44/445B29C 44/3461B29K 2105/041B29K 2105/0014B29K 2995/0063B29K 2023/12
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Claims
Abstract
An expanded polypropylene resin particle is obtained from a base material resin having a melting point of 140° C. to 150° C., wherein the base material resin includes a polypropylene resin A including 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 expanded polypropylene resin particle has an average cell diameter of 100 μm to 340 μm.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . An expanded polypropylene resin particle, obtained from a base material resin having a melting point of 140° C. to 150° C., wherein the base material resin comprises:
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 expanded polypropylene resin particle has an average cell diameter of 100 μm to 340 μm.
2 . The expanded polypropylene resin particle according to claim 1 , wherein the polypropylene resin A further comprises 2 weight % to 10 weight % of ethylene.
3 . The expanded polypropylene resin particle according to claim 1 , wherein the base material resin comprises:
50 weight % to 70 weight % of the polypropylene resin A; and 30 weight % to 50 weight % of the polypropylene resin B, wherein the polypropylene resin A and the polypropylene resin B together account for 100 weight %.
4 . The expanded polypropylene resin particle according to claim 1 , wherein the average cell diameter is 120 μm to 250 μm.
5 . The expanded polypropylene resin particle according to claim 1 , wherein the melting point of the base material resin is 145° C. to 150° C.
6 . The expanded polypropylene resin particle according to claim 1 , wherein the melting point of the base material resin is 146° C. to 148° C.
7 . The expanded polypropylene resin particle according to claim 1 , wherein the polypropylene resin B is a propylene-ethylene random copolymer or a propylene-ethylene-1-butene random copolymer.
8 . The expanded polypropylene resin particle according to claim 1 , wherein the polypropylene resin A is obtained using a Ziegler catalyst.
9 . The expanded polypropylene resin particle according to claim 1 , wherein
the expanded polypropylene resin particle is an expanded composite particle comprising an expanded polypropylene resin core layer covered with a polypropylene resin covering layer, the expanded polypropylene resin core layer is obtained from a base material resin comprising the polypropylene resin A and the polypropylene resin B; and the polypropylene resin covering layer comprises the polypropylene resin A.
10 . A polypropylene resin in-mold expanded molded product formed by subjecting the expanded polypropylene resin particles according to claim 1 to in-mold foaming molding.
11 . The polypropylene resin in-mold expanded molded product according to claim 10 , 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.
12 . The polypropylene resin in-mold expanded molded product according to claim 10 , wherein the polypropylene resin in-mold expanded molded product has a density of 20 g/L to 40 g/L.
13 . 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 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., 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; 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.
14 . The method according to claim 13 , wherein the polypropylene resin A comprises 2 weight % to 10 weight % of ethylene.
15 . The method according to claim 13 , further comprising:
melting and kneading the polypropylene resin A and the polypropylene resin B in an extruder and obtaining the polypropylene resin particles.
16 . The method according to claim 13 , further comprising:
obtaining the polypropylene resin A by polymerization using a Ziegler catalyst.
17 . The method according to claim 13 , wherein
the expanded polypropylene resin particles are each an expanded composite particle comprising an expanded polypropylene resin core layer covered with a polypropylene resin covering layer, the expanded polypropylene resin core layer is obtained from a base material resin comprising the polypropylene resin A and the polypropylene resin B; and the polypropylene resin covering layer comprises the polypropylene resin A.
18 . The method according to claim 13 , wherein
the expanded polypropylene resin particles are heated with steam having a pressure of 0.22 MPa (gauge pressure) or less, and 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.Join the waitlist — get patent alerts
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