Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/16—Making expandable particles
  • C08J9/18—Making expandable particles by impregnating polymer particles with the blowing agent
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
  • B29C44/34—Auxiliary operations
  • B29C44/3415—Heating or cooling
  • B29C44/3426—Heating by introducing steam in the mould
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
  • B29C44/34—Auxiliary operations
  • B29C44/3461—Making or treating expandable particles
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/0061—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/22—After-treatment of expandable particles; Forming foamed products
  • C08J9/228—Forming foamed products
  • C08J9/232—Forming foamed products by sintering expandable particles
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2203/00—Foams characterized by the expanding agent
  • C08J2203/06—CO2, N2 or noble gases
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2323/10—Homopolymers or copolymers of propene
  • C08J2323/14—Copolymers of propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2400/00—Characterised by the use of unspecified polymers
  • C08J2400/30—Polymeric waste or recycled polymer
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
  • C08J2423/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
  • C08J2423/10—Homopolymers or copolymers of propene
  • C08J2423/14—Copolymers of propene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J2453/00—Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
  • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
  • C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
  • C08J9/122—Hydrogen, oxygen, CO2, nitrogen or noble gases

Definitions

• the present invention relates to foamed polypropylene resin particles, foamed polypropylene resin molded articles, and methods for producing foamed polypropylene resin particles. Regarding.
• Polypropylene resin foam moldings are used for various purposes such as automobile interior parts, core materials for automobile bumpers, insulation materials, cushioning packaging materials, and returnable boxes (Patent Document 1).
• An embodiment of the present invention has been made in view of the above-mentioned problems, and its purpose is to provide foamed polypropylene resin particles with excellent productivity of polypropylene resin foam moldings, and to mold the foamed polypropylene resin particles.
• An object of the present invention is to provide a polypropylene resin foam molded article.
• the present inventors have completed the present invention as a result of intensive studies to solve the above problems.
• the polypropylene resin foam particles according to one embodiment of the present invention include the following configuration. Including a base resin containing a propylene-based random copolymer and a propylene-based block copolymer, where the content ratio of the block copolymer is X (%), and the foaming pressure during production is Y (MPa), The above X and Y satisfy the following formula (1): polypropylene resin foam particles: Y ⁇ -0.07X+3.6 (1).
• polypropylene resin foam particles include the following configuration. Contains a base resin containing a propylene random copolymer and a propylene block copolymer, has a peak intensity ratio I 720 /I 810 of 0.45 to 0.67, and has a shrinkage rate of 20% or less.
• polypropylene resin foam particles Here, the peak intensity ratio I 720 /I 810 is the intensity of the peak at wavelength 720 cm -1 to I 810 which is the intensity of the peak at wavelength 810 cm -1 obtained in the spectrum obtained by infrared spectroscopy.
• the ratio is 720
• the shrinkage rate (%) is a value determined by the following formula (2);
• the shrinkage rate (%) (BD-VBD) ⁇ 100/VBD...(2)
• the BD is the bulk density of polypropylene resin foam particles obtained by measurement at a temperature of 23° C. and a pressure of 0.1 MPa
• the VBD is the bulk density of the expanded polypropylene resin particles obtained when the temperature is 23° C. This is the bulk density of polypropylene resin foam particles obtained by measuring at 23° C. and under a pressure of ⁇ 0.09 MPa.
• a method for producing expanded polypropylene resin particles includes the following configuration.
• Polypropylene resin particles containing a base resin containing a propylene random copolymer and a propylene block copolymer are depressurized at a foaming temperature of 163.5°C or lower and a foaming pressure of 2.80 MPa or lower.
• the base resin contains 73% to 95% by weight of the propylene random copolymer when the total amount of the propylene random copolymer and the propylene block copolymer is 100% by weight.
• a method for producing foamed polypropylene resin particles containing 5% to 27% by weight of the propylene block copolymer is a method for producing foamed polypropylene resin particles containing 5% to 27% by weight of the propylene block copolymer.
• a method for producing expanded polypropylene resin particles includes the following configuration.
• Polypropylene resin particles containing a base resin containing a propylene random copolymer and a propylene block copolymer are depressurized at a foaming temperature of 163.5°C or lower and a foaming pressure of 2.80 MPa or lower.
• foamed polypropylene resin particles that are excellent in the productivity of foamed polypropylene resin molded products, and a foamed polypropylene resin molded product obtained by molding the foamed polypropylene resin particles. It has the effect of saying that it can be done.
• X unit a structural unit derived from an X monomer and contained in a polymer, copolymer, or resin.
• a copolymer containing as structural units X 1 unit, X 2 unit, ... and X n unit (n is an integer of 2 or more) is referred to as "X 1 /X 2 /.../X n copolymer".
• the polymerization mode of the X 1 /X 2 /.../X n copolymer is not particularly limited unless otherwise specified, and it may be a random copolymer or an alternating copolymer. It may be a block copolymer, or a graft copolymer.
• a propylene random copolymer can generally be used as a raw material for a polypropylene resin foam molded article.
• a propylene block copolymer may be used as a raw material for a polypropylene resin foam molded article. For example, this is the case when improving the impact resistance of a polypropylene resin foam molded article, or when using recycled resin from the viewpoint of reducing environmental load.
• the amount of propylene block copolymers in circulation is much larger than that of propylene random copolymers.
• the present inventors used a propylene random copolymer and a propylene block copolymer in combination to provide polypropylene resin foam particles, which are raw materials for polypropylene resin foam moldings. We have carefully considered what to do.
• the present inventors manufactured expanded polypropylene resin particles using a combination of a propylene random copolymer and a propylene block copolymer, and the resulting expanded polypropylene resin particles.
• the productivity of the polypropylene resin foam moldings may be poor.
• the productivity of the polypropylene resin foam moldings may be poor.
• the productivity of the polypropylene resin foam moldings may be poor.
• the productivity of the polypropylene resin foam molded product using a mold before taking out the obtained polypropylene resin foam molding from the mold, check the swelling of the polypropylene resin foam molded product after taking it out from the mold. Cooling may be used to reduce this. This cooling time greatly contributes to the productivity of polypropylene resin foam moldings.
• the above-mentioned "case where the productivity of the polypropylene resin foam molded product becomes poor" is intended to mean a case where the cooling time of the polypropylene resin foam molded product becomes long.
• the present inventors developed polypropylene resin foam particles that have excellent productivity in producing polypropylene resin foam molded articles even when a propylene random copolymer and a propylene block copolymer are used in combination. In order to provide this service, we have conducted further studies.
• the present inventors independently discovered the following new findings and completed the present invention:
• a propylene-based random copolymer and a propylene-based block copolymer in a specific ratio By foaming the polypropylene resin particles such that the shrinkage rate of the foamed polypropylene resin particles falls within a specific range, it has surprisingly been possible to produce foamed polypropylene resin particles that have excellent productivity in producing foamed polypropylene resin molded articles. What we can offer.
• the expanded polypropylene resin particles include a base resin containing a propylene random copolymer and a propylene block copolymer, and the content ratio of the block copolymer is set to X (%). ), and the foaming pressure at the time of manufacture is Y (MPa), then X and Y satisfy the following formula (1).
• the expanded polypropylene resin particles according to another embodiment of the present invention include a base resin containing a propylene random copolymer and a propylene block copolymer, and have a peak intensity ratio I 720 /I 810 of 0. 45 to 0.67, and the shrinkage rate is 20% or less.
• the peak intensity ratio I 720 /I 810 is the intensity of the peak at wavelength 720 cm -1 to I 810 which is the intensity of the peak at wavelength 810 cm -1 obtained in the spectrum obtained by infrared spectroscopy.
• the ratio is 720 .
• BD is the bulk density of the expanded polypropylene resin particles obtained by measurement at a temperature of 23° C. and a pressure of 0.1 MPa.
• VBD is the bulk density of the polypropylene resin foam particles obtained by measurement at a temperature of 23° C. and a pressure of ⁇ 0.09 MPa.
• expansion polypropylene resin particles may be referred to as “expanded particles”
• expanded polypropylene resin particles according to an embodiment of the present invention may be referred to as “present expanded particles”
• a "polypropylene resin foam molded product” is sometimes referred to as a “foamed molded product”.
• the present foamed particles have the above-mentioned structure, they have the advantage of being excellent in the productivity of foamed molded products.
• the present foamed particles have the advantage that when the foamed particles are used for in-mold foam molding using a mold, the cooling time of the foamed product in the mold can be shortened. Since the foamed particles have the above-described structure, they also have the advantage of being able to provide a foamed molded product with excellent strength.
• the base resin includes at least a propylene random copolymer and a propylene block copolymer as resin components.
• the base resin may optionally contain additives such as a foaming nucleating agent in addition to the resin component. It can be said that the base resin is a component that substantially constitutes the expanded particles. Therefore, the types and amounts of each component contained in the base resin can also be said to be the types and amounts of each component contained in the expanded particles.
• Both the propylene-based random copolymer and the propylene-based block copolymer are polypropylene-based resins.
• polypropylene resin refers to a resin containing 50 mol% or more of propylene units out of 100 mol% of all structural units constituting the resin.
• the propylene random copolymer contains at least a propylene unit and a constituent unit other than the propylene unit.
• "structural units other than propylene units" contained in the polypropylene resin may be referred to as "comonomer units.”
• the propylene random copolymer contains at least a propylene unit and a comonomer unit.
• Comonomers include ethylene, 1-butene, isobutene, 1-pentene, 3-methyl-1-butene, 1-hexene, 4-methyl-1-pentene, 3,4-dimethyl-1-butene, 1-heptene, Examples include ⁇ -olefins having 2 or 4 to 12 carbon atoms, such as 3-methyl-1-hexene, 1-octene, and 1-decene.
• the comonomer unit contained in the propylene-based random copolymer is preferably an ethylene unit from the viewpoint of lowering the molding temperature when foam-molding the expanded particles in a mold.
• the propylene random copolymer is preferably a propylene/ethylene random copolymer containing propylene units and ethylene units.
• the propylene-based random copolymer is not limited to a propylene/ethylene random copolymer.
• propylene-based random copolymers other than propylene/ethylene random copolymers include propylene/1-butene random copolymers, propylene/ethylene/1-butene random copolymers, and propylene/chlorinated vinyl random copolymers. Copolymer, propylene/maleic anhydride random copolymer, and the like.
• the propylene random copolymer may be a combination of a propylene/ethylene random copolymer and one or more propylene random copolymers other than the propylene/ethylene random copolymer.
• the melting point of the propylene random copolymer is not particularly limited, but is preferably 130°C or higher, more preferably 130°C to 160°C, more preferably 135°C to 155°C, and even more preferably 140°C to 150°C.
• the melting point of the propylene random copolymer is (i) 130°C or higher, the foamed molded product obtained from the foamed particles has excellent heat resistance, and (ii) when it is 160°C or lower, the foamed product has excellent heat resistance. This has the advantage that it becomes easy to increase the expansion ratio of expanded particles in the production of particles.
• the melting points of the propylene-based random copolymer and the propylene-based block copolymer described below are values determined by measurement by differential scanning calorimetry (hereinafter referred to as "DSC method").
• DSC method differential scanning calorimetry
• the specific operating procedure is as described in Examples described later.
• DSC7020 model manufactured by Seiko Instruments Inc. can be used as the differential scanning calorimeter.
• the melt flow rate (MFR) of the propylene random copolymer is not particularly limited.
• MFR of a propylene-based random copolymer intends the MFR of the propylene-based random copolymer at 230°C.
• the MFR of the propylene random copolymer is preferably from 3 g/10 minutes to 30 g/10 minutes, more preferably from 4 g/10 minutes to 20 g/10 minutes, even more preferably from 5 g/10 minutes to 18 g/10 minutes. If the MFR of the propylene random copolymer at 230° C. is within the above range, it has the advantage that expanded particles having a relatively large expansion ratio can be easily obtained. Furthermore, in this case, there are also advantages in that the surface beauty of the foamed molded product is excellent and the shrinkage rate of the foamed molded product is small.
• MFR melt mass flow rate
• the propylene random copolymer one obtained by a known method may be used, or a recycled resin may be used. It is preferable to use non-recycled resin because the quality of the foamed molded product is stable.
• the propylene block copolymer contains at least a propylene unit and a comonomer unit.
• the comonomer unit contained in the propylene block copolymer is not particularly limited. Specific examples of the comonomer are the same as those explained in the section (propylene random copolymer) above, so the description is incorporated and the explanation is omitted here.
• the comonomer unit contained in the propylene block copolymer is preferably an ethylene unit.
• the propylene block copolymer is preferably a propylene/ethylene block copolymer containing propylene units and ethylene units.
• the propylene block copolymer is preferably a copolymer containing at least an ethylene block (for example, a propylene/ethylene block copolymer).
• the propylene block copolymer includes substances that are considered to be propylene block copolymers in the technical field of polypropylene resins.
• the propylene/ethylene block copolymer includes a polyethylene layer covered with homopolypropylene as a matrix and an ethylene/propylene elastic copolymer as a domain, and is sometimes referred to as an impact copolymer.
• the propylene-based block copolymer is not limited to a propylene/ethylene block copolymer.
• propylene-based block copolymers other than propylene/ethylene block copolymers include propylene/1-butene block copolymers, propylene/ethylene/1-butene block copolymers, and propylene/chlorinated vinyl block copolymers. Copolymer, propylene/maleic anhydride block copolymer, and the like.
• the propylene block copolymer may be a combination of a propylene/ethylene block copolymer and one or more propylene block copolymers other than the propylene/ethylene block copolymer.
• the melting point of the propylene block copolymer is not particularly limited, but is preferably 160°C or higher, more preferably 162°C or higher, and even more preferably 165°C or higher.
• the upper limit of the melting point of the propylene block copolymer is not particularly limited, but is preferably, for example, 180°C or lower, more preferably 175°C or lower, and even more preferably 170°C or lower.
• the difference between the melting point of the propylene-based block copolymer and the melting point of the propylene-based random copolymer i.e., the melting point of the propylene-based block copolymer minus the melting point of the propylene-based random copolymer
• the obtained value (°C) is not particularly limited, but is preferably 30°C or lower, more preferably 21°C or lower. This configuration has the advantage that the minimum molding pressure during in-mold molding can be equivalent to that of expanded particles obtained using only a propylene random copolymer as the base resin.
• the MFR of the propylene block copolymer is not particularly limited.
• MFR of a propylene block copolymer refers to the MFR of a propylene block copolymer at 230°C.
• the MFR of the propylene block copolymer is preferably from 3 g/10 minutes to 30 g/10 minutes, more preferably from 4 g/10 minutes to 20 g/10 minutes, even more preferably from 5 g/10 minutes to 18 g/10 minutes.
• the propylene block copolymer obtained by a known method may be used, it is preferably a recycled resin.
• a recycled polypropylene resin the amount of propylene block copolymer distributed is greater than the amount of propylene random copolymer distributed.
• Recycled propylene block copolymer resins are relatively easily available.
• recycled resin is used as all or part of the propylene-based block copolymer, not only can environmental pollution be reduced, but also the amount of plastic waste generated and the amount of plastic used in production can be significantly reduced. Therefore, embodiments that use recycled resins as all or part of the propylene-based block copolymer have the advantage of contributing to achieving the Sustainable Development Goals (SDGs).
• SDGs Sustainable Development Goals
• recycled resin refers to the form of resin products (e.g., foamed particles, foamed molded bodies, films, packaging containers such as food trays and bags, bottles, miscellaneous goods such as clothing cases and clear files) etc.), it is intended to refer to a resin that has been transformed into a resin (or resin particles) again by means such as melting.
• the propylene-based block copolymer may be a mixture of recycled resin and non-recycled resin (resin that has never been in the form of a resin product).
• the proportion of recycled resin in 100% by weight of the propylene block copolymer is preferably 50% or more, more preferably 70% or more, even more preferably 80% or more, and 100% ( In other words, it is particularly preferable that the resin be composed only of recycled resin.
• the base resin contains (a) 73% to 95% by weight of a propylene-based random copolymer, when the total amount of the propylene-based random copolymer and the propylene-based block copolymer is 100% by weight; (b) It preferably contains 5% to 27% by weight of a propylene-based random copolymer, and (b) contains 74% to 95% by weight of a propylene-based random copolymer, and 5% to 26% by weight of a propylene-based block copolymer.
• the expanded particles have the advantage that the productivity of polypropylene-based resin foam molded products is better.
• the base resin may contain resins other than propylene-based random copolymers and propylene-based block copolymers (sometimes referred to as "other resins, etc.") as resin components to the extent that the effects of one embodiment of the present invention are not impaired. ) may also be included.
• the other resins include (a) polypropylene resins other than propylene random copolymers and propylene block copolymers, (b) high density polyethylene, medium density polyethylene, low density polyethylene, linear low density Ethylene resins such as polyethylene, linear ultra-low density polyethylene, ethylene/vinyl acetate copolymer, ethylene/acrylic acid copolymer, and ethylene/methacrylic acid copolymer, (c) polystyrene, styrene/maleic anhydride Acid copolymers and styrenic resins such as styrene/ethylene copolymers, (d) polyolefin waxes such as propylene- ⁇ -olefin waxes, and (e) ethylene/propylene rubber, ethylene/butene rubber, ethylene/hexene rubber , olefin rubbers such as ethylene/octene rubber, and the like.
• the base resin may further optionally contain additives in addition to the propylene random copolymer and propylene block copolymer described above.
• additives include colorants, water-absorbing substances, foaming nucleating agents, antistatic agents, flame retardants, antioxidants, light stabilizers, crystal nucleating agents, conductive agents, lubricants, and the like. Such additives may be added directly to the blend or polypropylene resin composition described below in the production of polypropylene resin particles.
• the expanded particles preferably have a peak intensity ratio I 720 /I 810 of 0.45 to 0.67.
• the peak intensity ratio I 720 /I 810 is calculated by setting the intensity of the peak at a wavelength of 720 cm -1 to "I 720 " and the intensity of the peak at a wavelength of 810 cm -1 to "I 810 " in a spectrum obtained by infrared spectroscopic analysis. , the ratio of I 720 to I 810 .
• Infrared spectroscopy can be measured by the method described in Examples below.
• the peak at a wavelength of 720 cm ⁇ 1 may be a peak primarily derived from ethylene blocks, and the peak at a wavelength of 810 cm ⁇ 1 may be a peak primarily derived from propylene.
• the peak intensity ratio I 720 /I 810 obtained by infrared spectroscopy can relatively accurately reflect the ratio of propylene and ethylene blocks contained in the base resin contained in the expanded particles.
• the propylene-based block copolymer contains an ethylene block
• the larger the value of the peak intensity ratio I 720 /I 810 the greater the total amount of the propylene-based random copolymer and the propylene-based block copolymer. It is intended that the amount of propylene-based block copolymer inside is large.
• the propylene-based propylene-based random copolymer and the propylene-based block contained in the base resin can be measured in advance.
• the ratio with the copolymer can be determined.
• the peak intensity ratio is from 0.45 to 0.67, preferably from 0.45 to 0.65, more preferably from 0.47 to 0.63, even more preferably from 0.49 to 0.61, and even more preferably from 0.49 to 0.61. Even more preferably 50 to 0.60. According to this configuration, the expanded particles have the advantage that the productivity of the polypropylene resin foam molded article is superior.
• the peak intensity ratio can be controlled by the content of each block copolymer contained in the expanded particles.
• BD is the bulk density of the expanded polypropylene resin particles at 23° C. and 0.1 MPa (absolute pressure). In other words, it can be said that BD is the bulk density of polypropylene resin foam particles under standard atmospheric pressure.
• VBD is the bulk density of polypropylene resin foam particles at 23° C. and ⁇ 0.09 MPa (gauge pressure) or less. In other words, it can be said that VBD is the bulk density of expanded polypropylene resin particles under reduced pressure.
• the shrinkage rate is 20% or less, preferably 18% or less, and more preferably 16% or less.
• the lower limit of the shrinkage rate is not particularly limited, but may be, for example, 0% or more.
• the shrinkage rate is within the above-mentioned range, the expanded particles have the advantage that the productivity of the polypropylene resin foam molded article is better.
• the shrinkage rate can be controlled by adjusting the conditions (for example, foaming temperature and foaming pressure) during the production of expanded particles.
• the expanded particles preferably have at least two melting peaks in a DSC curve obtained by differential scanning calorimetry, which will be described later.
• the heat of fusion obtained from the melting peak on the high temperature side is defined as the "heat of fusion on the high temperature side”
• the heat of fusion obtained from the melting peak on the low temperature side is defined as the "heat of fusion on the low temperature side”.
• the heat of fusion determined from the highest temperature melting peak is the "high temperature side heat of fusion”
• the heat of fusion determined from the other melting peaks is the "low temperature side heat of fusion”. shall be.
• the DSC ratio of the expanded particles is not particularly limited, but is preferably 10.0% to 50.0%, more preferably 15.0% to 40.0%, and 18.0% to 30%. More preferably, it is .0%.
• the DSC ratio of the expanded particles is 10.0% or more, the expanded particles have the advantage of being able to provide a foamed molded product with sufficient strength.
• the DSC ratio of the expanded particles is 50.0% or less, there is an advantage that the expanded particles can be molded at a relatively low temperature (molding temperature) to provide a foamed molded article.
• the DSC ratio is intended to be the ratio of the high temperature side heat of fusion to the total heat of fusion, which is calculated from the DSC curve of the expanded particles.
• the DSC curve is obtained using a differential scanning calorimeter (for example, DSC7020 model manufactured by Hitachi High-Tech Science). More specifically, it can be measured by the method described in Examples.
• the DSC ratio of the expanded particles is also a value that serves as a guideline for the amount of crystals with a high melting point contained in the expanded particles. That is, a DSC ratio of 10.0% to 50.0% indicates that the expanded particles contain a relatively large amount of crystals with a high melting point. Further, the DSC ratio of the foamed particles greatly affects the viscoelasticity of the resin particles and the foamed particles when foaming the resin particles and expanding the foamed particles. That is, when the DSC ratio of the expanded particles is 10.0% to 50.0%, the resin particles and expanded particles have excellent foaming properties when foaming the resin particles and molding the expanded particles. and can exhibit expansive properties. As a result, the foamed particles have the advantage that a foamed molded article having excellent internal fusion properties and excellent mechanical strength such as compressive strength can be obtained at a low molding pressure.
• the method of controlling the DSC ratio within a predetermined range for the foamed beads includes the conditions during production of the foamed beads (in particular, the foaming temperature, foaming pressure, holding time, and temperature of the area (space) from which the dispersion is released). etc.). From the viewpoint of easy adjustment, a method of adjusting the foaming temperature, foaming pressure, and/or holding time is preferred as a method for controlling the DSC ratio within a predetermined range.
• the DSC ratio tends to decrease, and conversely, when the foaming temperature is decreased, the DSC ratio tends to increase. This is because the amount of unmelted crystals changes depending on the foaming temperature. Further, when the foaming pressure is increased, the DSC ratio tends to decrease, and conversely, when the foaming pressure is decreased, the DSC ratio tends to increase. This is because the degree of plasticization changes depending on the foaming pressure, which changes the amount of unmelted crystals. Furthermore, the longer the holding time is, the higher the DSC ratio tends to be. This is because the amount of unmelted crystal growth changes depending on the holding time.
• the foamed particles preferably have an expansion ratio of 15 times to 50 times, more preferably 18 times to 40 times, and even more preferably 20 times to 25 times. If the expansion ratio of the foamed particles is (i) 15 times or more, a lightweight foam molded product can be obtained with good production efficiency, and (ii) if it is 50 times or less, the strength of the obtained foam molded product is insufficient. There is no risk of it happening.
• the expansion ratio can be measured by the method described in Examples below.
• the present expanded particles have the advantage that a foamed molded article having an excellent fusion rate (for example, a fusion rate of 80% or more) can be obtained using the expanded particles at a low molding pressure.
• the present expanded particles have the advantage of being able to provide a foamed molded product with excellent fusion rate at the same molding pressure as expanded particles obtained using only a propylene random copolymer as the base resin. .
• the lowest value of the molding pressure that can provide a foamed molded product having an excellent fusion rate is also called the "minimum molding pressure".
• the minimum molding pressure can be measured by the method described in Examples below.
• the expanded particles also have the advantage of low minimum molding pressure. In other words, the minimum molding pressure of the expanded particles may be equivalent to that of expanded particles obtained using only a propylene random copolymer as the base resin.
• the minimum molding pressure for the expanded particles is not particularly limited, but is preferably, for example, 0.30 MPa or less, more preferably 0.28 MPa or less, and even more preferably 0.26 MPa or less.
• the lower limit of the minimum molding pressure is not particularly limited, but may be, for example, 0.15 MPa or more.
• a method for producing expanded polypropylene resin particles according to an embodiment of the present invention includes polypropylene resin particles containing a base resin containing a propylene random copolymer and a propylene block copolymer at a foaming temperature of 163° C. It has a foaming step of performing depressurized foaming at a temperature of .5° C. or lower and a foaming pressure of 2.80 MPa or lower.
• a method for producing expanded polypropylene resin particles according to another embodiment of the present invention includes polypropylene resin particles containing a base resin containing a propylene random copolymer and a propylene block copolymer at a foaming temperature.
• the base resin has a foaming process in which the total amount of the propylene-based random copolymer and the propylene-based block copolymer is When 100% by weight, it contains 73% to 95% by weight of the propylene random copolymer and 5% to 27% by weight of the propylene block copolymer (granulation step)
• This manufacturing method may further include a step (granulation step) of manufacturing polypropylene resin particles containing a base resin containing a propylene random copolymer and a propylene block copolymer.
• polypropylene resin particles may be referred to as "resin particles.”
• resin particles examples include a method using an extruder.
• resin particles can be produced, for example, by the following methods (1) to (5): (1) Block copolymers, random copolymers, and other materials as necessary.
• a blend is produced by blending one or more selected from the group consisting of a resin and an additive; (2) The blend is put into an extruder, and the blend is melt-kneaded to produce a polypropylene resin composition.
• step (3) Extrude the polypropylene resin composition from a die included in an extruder; (4) Solidify the extruded polypropylene resin composition by cooling it by passing it through water, etc.; (5) ) Thereafter, the solidified polypropylene resin composition is cut into desired shapes such as cylinders, ellipses, spheres, cubes, rectangular parallelepipeds, hollow cylinders, polygonal columns, etc. using a cutter.
• step (3) the melt-kneaded polypropylene resin composition is directly extruded into water from a die included in an extruder, and immediately after extrusion, the polypropylene resin composition is cut into particle shapes, cooled, and solidified. Also good. By melt-kneading the blend in this manner, more uniform resin particles can be obtained.
• the weight per particle of the resin particles obtained as described above is preferably from 0.2 mg/grain to 10.0 mg/grain, more preferably from 0.5 mg/grain to 6.0 mg/grain.
• the weight of each resin particle is (A) 0.2 mg/grain or more, the handling properties of the resin particles tend to improve, and the shrinkage of the foam molded product obtained by molding the obtained foam particles tends to be reduced. The rate tends to be smaller.
• the method may further include a dispersion step of dispersing a dispersion aid into the container.
• the dispersion step can also be said to be a step of preparing a dispersion liquid in which a base resin, a blowing agent, and, if necessary, a dispersant and/or a dispersion aid are dispersed in an aqueous dispersion medium.
• the base resin in the dispersion step may be resin particles obtained in the above-mentioned granulation step.
• the container is not particularly limited, it is preferably a container that can withstand the foaming temperature and foaming pressure described below.
• a pressure-resistant container is preferable, and an autoclave-type pressure-resistant container is more preferable.
• the container may include a stirrer within the container.
• the aqueous dispersion medium is not particularly limited as long as it can uniformly disperse resin particles, blowing agents, etc.
• aqueous dispersion medium examples include (a) a dispersion medium obtained by adding methanol, ethanol, ethylene glycol, glycerin, etc. to water, and (b) water such as ultrapure water, pure water, tap water, and industrial water. , and (c) a solution (aqueous solution) containing a salt such as sodium chloride or sodium sulfate.
• aqueous dispersion media such as RO water (water purified by reverse osmosis membrane method), distilled water, deionized water (water purified by ion exchange resin), etc. It is preferable to use pure water, ultrapure water, or the like.
• blowing agent As a blowing agent, (a) (a-1) an inorganic gas such as nitrogen, carbon dioxide, or air (a mixture of oxygen, nitrogen, and carbon dioxide); and (a-2) an inorganic blowing agent such as water; (b) (b-1) Saturated hydrocarbons having 3 to 5 carbon atoms such as propane, normal butane, isobutane, normal pentane, isopentane, neopentane, etc. (b-2) Ethers such as dimethyl ether, diethyl ether, and methyl ethyl ether (b-3) Organic blowing agents such as halogenated hydrocarbons such as monochloromethane, chloroethane, and hydrofluoroolefins; and the like.
• the blowing agent at least one type selected from the group consisting of the above-mentioned inorganic blowing agents and organic blowing agents can be used.
• the mixing ratio may be adjusted as appropriate depending on the purpose.
• inorganic foaming agents are preferred.
• carbon dioxide is preferable because it has a suitably high plasticizing effect and can easily improve the foamability of the expanded particles in the production of the expanded particles.
• one type of each may be used alone, or two or more types may be used in combination.
• the present method for producing expanded particles uses dispersants (e.g., inorganic substances such as tricalcium phosphate, kaolin, and talc) and dispersion aids (e.g., anionic surfactants such as sodium alkanesulfonate and sodium dodecylbenzenesulfonate). It is preferable to do so. According to this configuration, coalescence (sometimes referred to as blocking) between resin particles can be reduced, and the stability of the dispersion in the container can be improved. As a result, there is an advantage that expanded particles can be stably produced.
• dispersants e.g., inorganic substances such as tricalcium phosphate, kaolin, and talc
• dispersion aids e.g., anionic surfactants such as sodium alkanesulfonate and sodium dodecylbenzenesulfonate. It is preferable to do so. According to this configuration, coalescence (sometimes referred to as blocking) between resin particles can be reduced,
• the specific mode of the foaming process is not particularly limited.
• the foaming step includes, for example, (a) a heating-pressure raising step in which the temperature inside the container is raised to a constant temperature and the pressure inside the container is raised to a constant pressure to foam the resin particles under reduced pressure; (b) a holding step of maintaining the temperature and pressure inside the container at a constant temperature and constant pressure; (c) A discharge step of opening one end of the container and releasing the dispersion liquid in the container to a region (space) having a pressure lower than the foaming pressure (namely, the pressure inside the container) may be included.
• the temperature and pressure raising step is preferably carried out after the dispersion step, and the holding step is preferably carried out after the temperature and pressure raising step.
• the foaming temperature is 163.5°C or lower, preferably 163.3°C or lower, and more preferably 163.2°C or lower.
• the lower limit of the foaming temperature is not particularly limited as long as the resin particles can be foamed under reduced pressure, and may be, for example, 150° C. or higher.
• the foaming pressure is 2.80 MPa or less, preferably 2.75 MPa or less, more preferably 2.70 MPa or less, and even more preferably 2.60 MPa or less.
• the lower limit of the foaming pressure is not particularly limited as long as the resin particles can be foamed under reduced pressure, but may be, for example, 1.5 MPa or more.
• the present inventor discovered the new finding that in order to obtain foamed particles with a low shrinkage rate, it is preferable to appropriately set the foaming pressure depending on the amount of the propylene block copolymer. Obtained independently. Specifically, the present inventor independently obtained the new finding that in order to obtain expanded particles with a low shrinkage rate, the larger the amount of the propylene-based block copolymer, the lower the foaming pressure is preferably set. .
• the X and Y more preferably satisfy the following formula (3), further preferably satisfy the following formula (4), and particularly preferably satisfy the following formula (5): Y ⁇ -0.07X+3.55...(3) Y ⁇ -0.07X+3.5...(4) Y ⁇ -0.07X+3.45...(5).
• the time (holding time) for holding the dispersion in the container near the foaming temperature and foaming pressure is not particularly limited.
• the holding time is preferably 10 minutes to 60 minutes, more preferably 12 minutes to 55 minutes, even more preferably 15 minutes to 50 minutes.
• the amount of unmelted crystals (crystals of polypropylene resin) in the resin particles can be set to a sufficient amount during the foaming process from resin particles to foamed particles. As a result, foamed particles with a low open cell ratio can be obtained, and shrinkage of the obtained foamed particles can be reduced.
• the holding time is 60 minutes or less, the amount of unmelted crystals in the resin particles does not become excessive during the foaming process from resin particles to expanded particles. Therefore, the obtained expanded particles can be molded at a relatively low temperature (molding temperature) to provide a foamed molded product.
• the release step is preferably carried out after (a) the temperature raising and pressure raising step if the holding step is not carried out, and after the holding step if (b) the holding step is carried out.
• the ejection step allows the resin particles to be foamed, resulting in expanded particles.
• area with a pressure lower than the foaming pressure is intended to mean “an area under a pressure lower than the foaming pressure” or “a space under a pressure lower than the foaming pressure”, and "an atmosphere with a pressure lower than the foaming pressure”. It can also be said to be “lower”.
• the region of pressure lower than the foaming pressure is not particularly limited as long as it is lower than the foaming pressure, and may be, for example, a region under atmospheric pressure.
• the dispersion liquid In the discharge process, when the dispersion liquid is discharged into a region with a pressure lower than the foaming pressure, the dispersion liquid is passed through an opening orifice with a diameter of 1 mm to 5 mm for the purpose of adjusting the flow rate of the dispersion liquid and reducing the variation in the expansion ratio of the resulting expanded particles. can also be released. Further, for the purpose of improving foamability, the low pressure region (space) may be filled with saturated steam.
• the first-stage expanded beads obtained in the first-stage foaming step may be expanded again.
• the process of increasing the expansion ratio of the first-stage foamed particles is called a "two-stage foaming process," and the polyolefin resin foam particles obtained by the two-stage foaming process are called “two-stage foamed particles.”
• the specific method of the two-stage foaming step is not particularly limited, and any known method can be employed.
• the polypropylene resin foam molded article according to one embodiment of the present invention includes [1. This is a foam molded article obtained by foam-molding the polypropylene resin foam particles described in the section [Expanded Polypropylene Resin Particles].
• the polypropylene resin foam molded article according to one embodiment of the present invention includes [2. It may also be a foam molded article obtained by foam-molding polypropylene resin foam particles obtained by the manufacturing method described in the section "Production Method of Expanded Polypropylene Resin Particles".
• the polypropylene resin foam molded article according to one embodiment of the present invention includes [1. Expanded polypropylene resin particles], or the expanded polypropylene resin particles described in [2. It can also be said to include foamed polypropylene resin particles obtained by the manufacturing method described in the section "Production Method of Expanded Polypropylene Resin Particles".
• the "polypropylene resin foam molded product according to an embodiment of the present invention” may be referred to as "the present foam molded product”.
• the present foamed molded article has the above-mentioned structure, it has the advantage of being excellent in productivity and strength.
• the productivity of the foamed molded article is evaluated by the time (seconds) from the start of molding of the foamed particles to the completion of molding (molding cycle).
• the molding start point was the time when the expanded particles were filled into the mold.
• the molding completion point was defined as the time when the molded body was cooled (water-cooled), and the mold was opened when the surface pressure decreased to 0.01 MPa using a surface pressure gauge attached to the surface of the Planck mold, and mold release was completed. It is intended that the shorter the molding cycle, the better the productivity of the foamed molded article.
• the surface beauty of the foamed molded product is evaluated by the degree of gaps between foam particles (hereinafter sometimes referred to as "intergranular") on the surface of the foamed molded product, and wrinkles on the surface of the foamed molded product. do. It is intended that the smaller the size of the intergranules present on the surface of the foamed molded product and the smaller the number of grains, the more excellent the surface beauty of the foamed molded product will be. Furthermore, it is intended that the fewer wrinkles present on the surface of the foamed molded product, the better the surface beauty of the foamed molded product will be.
• This foamed molded article also has the advantage of being excellent in strength.
• the strength of a foamed molded article is evaluated by static compressive strength. The method for measuring the static compressive strength of a foamed molded product will be explained in detail in Examples below.
• the static compressive strength of the present foamed molded product is preferably 0.212 MPa or more, more preferably 0.217 MPa or more, and even more preferably 0.229 MPa or more.
• the upper limit of the static compressive strength is not particularly limited, but may be, for example, 0.300 MPa or less. This structure has the advantage that it can withstand use in applications such as automobile interior parts, core materials for automobile bumpers, heat insulating materials, cushioning packaging materials, returnable boxes, and the like.
• An embodiment of the present invention may include the following configuration.
• Polypropylene resin particles containing a base resin containing a propylene random copolymer and a propylene block copolymer are subjected to conditions such as a foaming temperature of 163.5°C or lower and a foaming pressure of 2.80 MPa or lower.
• the base resin contains 73% by weight of the propylene-based random copolymer. % to 95% by weight, and 5% to 27% by weight of the propylene block copolymer.
• the propylene-based random copolymer contains 50 mol% or more of propylene units in 100 mol% of the total structural units, and the propylene-based block copolymer contains propylene units in 100 mol% of the total structural units.
• the peak intensity ratio I 720 /I 810 is 0.45 to 0.67, and the shrinkage rate is 20%
• the peak intensity ratio I 720 /I 810 is the intensity of the peak at wavelength 720 cm -1 to I 810 which is the intensity of the peak at wavelength 810 cm -1 obtained in the spectrum obtained by infrared spectroscopy.
• the ratio is 720
• the shrinkage rate (%) is a value determined by the following formula (2);
• the shrinkage rate (%) (BD-VBD) ⁇ 100/VBD...(2)
• the BD is the bulk density of polypropylene resin foam particles obtained by measurement at a temperature of 23° C. and a pressure of 0.1 MPa
• the VBD is the bulk density of the expanded polypropylene resin particles obtained when the temperature is 23° C. This is the bulk density of polypropylene resin foam particles obtained by measuring at 23° C. and under a pressure of ⁇ 0.09 MPa.
• the base resin contains 73% to 95% by weight of the propylene random copolymer when the total amount of the propylene random copolymer and the propylene block copolymer is 100% by weight,
• the expanded polypropylene resin particles according to [16] which contain 5% to 27% by weight of the propylene block copolymer.
• the propylene-based random copolymer contains 50 mol% or more of propylene units in 100 mol% of the total structural units, and the propylene-based block copolymer contains propylene units in 100 mol% of the total structural units.
• the expanded polypropylene resin particles according to any one of [16] to [19], containing 50 mol% or more of.
• polypropylene resin foam particles according to any one of [16] to [20], wherein the propylene random copolymer includes a propylene/ethylene random copolymer containing a propylene unit and an ethylene unit. .
• the minimum molding pressure required to provide a polypropylene resin foam molded product with a fusion rate of 80% or more is 0.30 MPa or less, [16] - The expanded polypropylene resin particles according to any one of [26].
• Another embodiment of the present invention includes the following configuration.
• [1] Contains a base resin containing a propylene-based random copolymer and a propylene-based block copolymer, has a peak intensity ratio I 720 /I 810 of 0.45 to 0.65, and has a shrinkage rate of 20%
• the following polypropylene resin foam particles is the intensity of the peak at wavelength 720 cm -1 to I 810 which is the intensity of the peak at wavelength 810 cm -1 obtained in the spectrum obtained by infrared spectroscopy.
• the ratio is 720
• the shrinkage rate (%) is a value determined by the following formula (1);
• the shrinkage rate (%) (BD-VBD) ⁇ 100/VBD...(1)
• the BD is the bulk density of polypropylene resin foam particles obtained by measuring at a temperature of 23° C. and a pressure of 0.1 MPa
• the VBD is the bulk density of the expanded polypropylene resin particles obtained when the temperature is 23° C. This is the bulk density of polypropylene resin foam particles obtained by measuring at 23° C. and under a pressure of ⁇ 0.09 MPa.
• the base resin contains 75% to 95% by weight of the propylene random copolymer when the total amount of the propylene random copolymer and the propylene block copolymer is 100% by weight,
• the expanded polypropylene resin particles according to [1] which contain 5% to 25% by weight of the propylene block copolymer.
• Polypropylene resin particles containing a base resin containing a propylene random copolymer and a propylene block copolymer are subjected to conditions such as a foaming temperature of 163.5° C. or lower and a foaming pressure of 2.80 MPa or lower.
• the melting point of the polypropylene resin particles was measured using a differential scanning calorimeter (DSC7020, manufactured by Hitachi High-Tech Science Co., Ltd.).
• the specific measurement method is as follows: (1) 5 to 6 mg of the sample to be measured was melted by heating it from 40°C to 220°C at a heating rate of 10°C/min; (2) Thereafter, the temperature was lowered from 220°C to 40°C at a rate of 10°C/min for crystallization; (3) The temperature was further raised from 40°C to 220°C at a rate of 10°C/min.
• the temperature at the peak (melting peak) of the DSC curve obtained during the second heating was defined as the melting point of the polypropylene resin particles.
• MFR melt mass flow rate measuring device described in JIS K7210 under the following conditions: orifice 2.0959 ⁇ 0.005 mm ⁇ , orifice length 8.000. ⁇ 0.025mm, load 2160g, and temperature 230 ⁇ 0.2°C.
• the DSC ratio was measured using a differential scanning calorimeter (DSC7020, manufactured by Hitachi High-Tech Science Co., Ltd.). Specifically, the melting on the low-temperature side of the DSC curve at the first temperature increase obtained when 5 to 6 mg of expanded polypropylene resin particles is heated from 40 °C to 220 °C at a temperature increase rate of 10 °C/min.
• the peak area was defined as Ql
• the melting peak area on the high temperature side was defined as Qh , and it was calculated from the following formula.
• DSC ratio (%) Q h / (Q l + Q h ) ⁇ 100 Strictly speaking, the area surrounded by the melting peak on the low-temperature side and the tangent to the melting start baseline from the maximum point between the melting peak on the low-temperature side and the melting peak on the high-temperature side is defined as Ql ;
• the melting peak heat amount on the high temperature side which is the heat amount surrounded by the melting peak on the side and the tangent to the melting end baseline from the maximum point between the melting peak on the low temperature side and the melting peak on the high temperature side, was defined as Q h . .
• ⁇ Infrared spectroscopic analysis of expanded polypropylene resin particles The ratio of peak intensities derived from propylene and block ethylene was determined by infrared spectroscopic analysis of expanded polypropylene resin particles. The measurement was performed by an Attenuated Total Reflection method (hereinafter referred to as ATR method). After crushing polypropylene resin foam particles between metal plates, the particles were pressed against the crystal of an ATR measuring device (Spectrum Two, manufactured by PerkinElmer Japan Co., Ltd.), and the resolution was 4 cm -1 and the number of integrations was 16 times. The spectrum was obtained. At this time, the pressure at the time of crimping was adjusted so that the peak intensity at 1376 cm -1 was 0.15 A.
• ATR method Attenuated Total Reflection method
• the peak intensity (I 810 ) at a wavelength of 810 cm ⁇ 1 and the peak intensity (I 720 ) at a wavelength of 720 cm ⁇ 1 were a peak intensity derived from CH 3 of propylene
• the peak intensity at a wavelength of 720 cm -1 was a peak intensity derived from an ethylene chain.
• the measurement was performed using five arbitrary expanded polypropylene resin particles, and the arithmetic average value was used.
• Comparative Example 3 since expanded particles were not obtained, measurements were conducted in the same manner using resin particles. If the measurement conditions are the same, it is expected that there will be almost no difference in the measurement results of the ratio of peak intensities between when expanded particles are used as the sample and when resin particles are used as the sample.
• ⁇ Measurement of expansion ratio of polypropylene resin foam particles Take about 3g or more and 10g or less of polypropylene resin foam particles, dry them at 60°C for 6 hours, condition them indoors at 23°C and 50% humidity, measure the weight w 1 (g), and then dry them at 60°C for 6 hours.
• the shrinkage rate of the expanded polypropylene resin particles was calculated from the bulk density (hereinafter referred to as BD) and the bulk density of the expanded polypropylene resin particles under reduced pressure (hereinafter referred to as VBD) by the following method.
• the weight of the expanded polypropylene resin particles to be measured is defined as W 1 , and the volume V 1 was determined using a measuring cylinder at 23° C. and under atmospheric pressure (standard atmospheric pressure 0.1 MPa).
• W 1 bulk density BD of the polypropylene resin foam particles at 23° C. and 0.1 MPa (under standard atmospheric pressure) was determined.
• BD (g/L) W 1 ⁇ V 1
• the foamed polypropylene resin particles were weighed again, the weight was set as W 2 , and the weight was placed in a graduated pressure container, and the pressure inside the pressure container was reduced using a vacuum pump or the like. After confirming with a pressure gauge that the pressure is reduced to -0.09 MPa (gauge pressure) or less, use a vibrator to vibrate the pressure container until there is no change in the scale on the top of the foam particles, and then remove the pressure container. The scale on the top of the foamed polypropylene resin particles inside was read, and this was taken as the volume V2 .
• the foamed particles may press against each other and change in volume may be inhibited, so the pressure container was placed on its side so that the volumetric change would not be inhibited by the foamed particles, and the pressure was gradually reduced.
• VBD bulk density of the polypropylene resin foam particles at 23° C. and under reduced pressure of -0.09 MPa (gauge pressure) or less was determined.
• VBD (g/L) W 2 ⁇ V 2
• the shrinkage rate of the expanded polypropylene resin particles was determined from the following formula.
• Molding was carried out by changing the steam pressure set in the main heating step in [Production of polypropylene resin in-mold foam molded product] described later in increments of 0.01 MPa within the range of 0.20 to 0.32 MPa (gauge pressure).
• foamed molded articles to be evaluated were obtained.
• For the obtained foamed molded product make a crack with a depth of approximately 5 mm on the surface with a knife, split the foamed molded product in the mold along the crack, observe the fractured surface, and calculate the number of broken particles relative to the total number of particles on the fractured surface.
• the percentage of the molded body was determined and the molded body fusion rate was evaluated. The lowest steam pressure at which the fusion rate reached 80% or more was defined as the lowest molding pressure.
• the molding cycle in the method for producing an in-mold polypropylene resin foam molded article was from the start of molding to the end of molding when the molded article was released. Molding starts when the foamed polypropylene resin particles begin to be filled into the mold, and the mold is heated by sending steam into the mold. The molded product is then cooled with water, and the surface attached to the surface of the Planck mold is heated. The mold was opened at the timing when the surface pressure decreased to 0.01 MPa using a pressure gauge, and the molding was completed when the mold release was completed. The evaluation was made as the lowest molding pressure determined. The evaluation criteria for productivity are as follows. ⁇ (Excellent): Molding cycle is within 180 seconds. ⁇ (Excellent): Molding cycle is longer than 180 seconds and within 210 seconds. ⁇ (poor): Molding cycle is 210 seconds or more.
• Example 1 [Method for producing polypropylene resin particles] Weigh out 89.75 parts by weight of ethylene/propylene random copolymer, 10 parts by weight of ethylene/propylene block copolymer, 0.2 parts by weight of glycerin, and 0.05 parts by weight of talc, and use a blender. Dry blended using The dry blended mixture was melt-kneaded using a twin-screw extruder (manufactured by Toshiba Machine Co., Ltd., TEM26-SX) at a resin temperature of 220°C, and the extruded strand was cooled with water in a 2 m long water tank. It was cut to produce polypropylene resin particles (1.2 mg/particle).
• a twin-screw extruder manufactured by Toshiba Machine Co., Ltd., TEM26-SX
• This operation is performed by changing the pressure of steam from 0.20 MPa (gauge pressure) to 0.32 MPa in 0.01 MPa increments, and the minimum pressure required for the polypropylene resin foam particles to sufficiently fuse together is determined, which is the lower limit for molding. It was considered as pressure.
• the obtained in-mold foam molded product was allowed to stand at 23°C for 2 hours, and then cured at 75°C for 13 hours.
• Example 1 except that in [Preparation of polypropylene resin particles], the resin formulation was changed as shown in Table 1, and in [Preparation of expanded polypropylene resin particles], the foaming conditions were changed as shown in Table 1.
• Polypropylene resin particles, foamed polypropylene resin particles, and in-mold polypropylene resin foam molded articles were produced by the same operations as described above. Note that in Comparative Example 3, the foaming step was not performed.
• 158°C was selected as the foaming temperature to obtain expanded particles of suitable quality.
• the peak intensity ratio determined by infrared spectroscopy is 0.45 or more, it means that it contains enough propylene block copolymer, so if recycled polypropylene resin is used as the propylene block copolymer, it will not be recycled. Improves sex.
• Table 1 it can be seen that when the peak intensity ratio is 0.7, the molding temperature becomes high and expanded particles cannot be obtained, or productivity becomes poor.
• Comparative Example 1 which was foamed at a foaming pressure of 2.90 MPa, which is almost the same as Reference Example 1, the molding cycle became longer and productivity deteriorated, and the static compressive strength of the foam molded product decreased significantly. I understand that. Furthermore, in Comparative Example 2 in which the foaming temperature was 163.7° C., the molding cycle was similarly prolonged, and the static compressive strength of the foam molded product was significantly reduced.
• polypropylene resin foam particles containing an ethylene/propylene block copolymer can be molded in a mold at the same molding pressure as polypropylene resin foam particles consisting only of an ethylene/propylene random copolymer, and the resulting foam molding The body has excellent surface beauty.
• one embodiment of the present invention since the molding time during in-mold molding is short, it is possible to provide expanded polypropylene resin particles with improved productivity. Therefore, one embodiment of the present invention can be used in various applications such as automobile interior parts, core materials for automobile bumpers, heat insulating materials, cushioning packaging materials, and returnable boxes.

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