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.
Abstract:
An expanded polyolefin resin particle is obtained by expanding a polyolefin resin particle using water and/or an inorganic gas as a foaming agent. The polyolefin resin particle includes a polyolefin resin, a product obtained by heating and kneading a mixture, and a water absorbing substance, wherein the mixture includes a first polypropylene resin, a polypropylene wax, a polyorganosiloxane including at least one silicon-atom-bound radical polymerizable functional group per molecule, and an organic peroxide.
Abstract:
An expanded polyolefin resin particle is obtained by expanding a polyolefin resin particle using water and/or an inorganic gas as a foaming agent. The polyolefin resin particle includes a polyolefin resin, a product obtained by heating and kneading a mixture, and a water absorbing substance, wherein the mixture includes a first polypropylene resin, a polypropylene wax, a polyorganosiloxane including at least one silicon-atom-bound radical polymerizable functional group per molecule, and an organic peroxide.
Abstract:
Expanded polypropylene resin particles include a polypropylene resin as a base material resin, wherein the polypropylene resin has a flexural modulus of 750 MPa to 1100 MPa. The flexural modulus and a melting point of the expanded polypropylene resin particles satisfy Expression (1): [Flexural modulus (MPa)]
Abstract:
Provided are expanded polypropylene resin particles from which a polypropylene resin-based in-mold expansion-molded product is obtainable, the polypropylene resin-based in-mold expansion-molded product being excellent in electrical conductivity and particularly having improved in flame retardancy with no use of a flame retardant. Expanded polypropylene resin particles obtainable by expanding polypropylene resin particles containing a polypropylene resin composition which contains electrically conductive carbon black in an amount in a range of not less than 11 parts by weight and not more than 25 parts by weight with respect to 100 parts by weight of polypropylene resin, the electrically conductive carbon black having a dibutyl phthalate absorption amount in a range of not less than 300 cm3/100 g and not more than 600 cm3/100 g, have an average cell diameter in a range of more than 0.16 mm and not more than 0.35 mm.
Abstract:
Expanded polypropylene resin particles include a polypropylene resin as a base material resin, wherein the polypropylene resin has a flexural modulus of 750 MPa to 1100 MPa. The flexural modulus and a melting point of the expanded polypropylene resin particles satisfy Expression (1): [Flexural modulus (MPa)]
Abstract:
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 haying 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.
Abstract:
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.
Abstract:
An expanded polypropylene resin particle includes a polypropylene resin (X) as a base resin, the polypropylene resin (X) containing a polypropylene resin (I) and a high density polyethylene resin (II). The polypropylene resin (I) has a melting point of 145 to 165° C., and the high density polyethylene resin (II) has a density of 0.93 to 0.97 g/cm3. The polypropylene resin (X) contains no or one foam nucleating agent.
Abstract:
An expanded polypropylene resin particle includes a polypropylene resin composition that serves as a base material resin. The polypropylene resin composition includes a first polypropylene resin having a melting point of 140° C. or less, a second polypropylene resin having a melting point of 145° C. or more, and a polyethylene resin having a melting point of 120° C. to 135° C. The first polypropylene resin accounts for 50 to 75 weight %, the second polypropylene resin accounts for 25 to 50 weight %, and the polyethylene resin accounts for 1 to 10 weight %, wherein the weight % is based on a total amount of the first polypropylene resin, the second polypropylene resin, and the polyethylene resin.