Classifications

• • 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
  • B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
  • B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
  • B29C35/04—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould using liquids, gas or steam
• • 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

Definitions

• the present invention relates to a method for producing foam beads, amorphous resin foam beads, crystalline resin foam beads, and foam molded articles.
• Bead foaming methods and the like are known as techniques for producing resin foams.
• resin particles having foamability are foamed to form foamed beads, and then the foamed beads are foamed and the foamed beads are fused together to obtain a foamed molded article.
• the bead foaming method has the advantages of being able to freely set the product shape and easily obtaining foam molded products with a high expansion ratio, and is widely used in industry in the fields of automobile peripheral parts and electronic device peripheral parts. There is.
• methods for manufacturing expanded beads used in the bead foaming method the methods described in Patent Documents 1 and 2 are known.
• Patent Document 1 describes a method for controlling the crystallinity of a resin contained in a raw material composition for foamed beads as a method for producing foamed beads that have good foamability while having crystallinity.
• Patent Document 2 describes that by heat treating an extruded foam to remove residual stress during extrusion foaming, it is possible to produce a foam that exhibits small dimensional changes even when used at high temperatures.
• Patent Documents 1 and 2, etc. it is not possible to sufficiently remove the residual stress generated in the resin molding, so Dimensional stability after treatment was not sufficient.
• the residual stress generated in the foamed beads cannot be removed by the conventional method, the expansion ability of the foamed beads is poor and the moldability is not sufficient.
• an object of the present invention is to efficiently produce foamed beads that have excellent expansion ability when expanding from foamed beads to foamed molded products, and can produce foamed molded products with small dimensional changes after long-term high-temperature treatment.
• the purpose is to provide a method.
• the present invention is as follows.
• a method for producing foam beads characterized by: [2] a bead foaming step in which a bead raw material containing a resin is foamed, and a bead annealing step in which the bead raw material is heat-treated at a temperature of (softening point temperature -30) °C or higher and (softening point temperature +30) °C or lower after the bead foaming step.
• a method for producing foam beads characterized by: [3] The method for producing expanded beads according to [1] or [2], wherein the resin is an amorphous resin. [4] The method for producing foam beads according to [2], wherein the resin is a crystalline resin. [5] The method for producing expanded beads according to any one of [1] to [4], wherein in the bead annealing step, the heat treatment is performed using steam. [6] The method for producing foamed beads according to any one of [1] to [4], wherein in the bead annealing step, the heat treatment is performed using hot air.
• Amorphous resin foam beads characterized by: [10] Foamed beads made by foaming a bead raw material containing a crystalline resin, the heat shrinkage rate of which is 25% or less when heated for 5 minutes at (softening point temperature -10) °C of the bead raw material, Crystalline resin foam beads characterized by: [11] The amorphous resin foam beads according to [9], which have an expansion capacity of 2.3 or more.
• the method for producing foamed beads of the present invention has excellent expansion ability when expanding from foamed beads to a foamed molded product, and can efficiently produce a foamed molded product with small dimensional change after long-term high temperature treatment. can be manufactured efficiently.
• this embodiment a mode for carrying out the present invention (hereinafter referred to as "this embodiment") will be described in detail.
• the present invention is not limited to the following description, and can be implemented with various modifications within the scope of the gist.
• the method for producing foamed beads of this embodiment includes a bead foaming step in which a bead raw material containing resin is foamed, and a bead annealing step in which the beads are heat-treated at a predetermined temperature after the bead foaming step.
• the method for manufacturing expanded beads of the present embodiment includes a bead foaming step of foaming bead raw material containing resin, and after the bead foaming step, (glass transition temperature -30) °C or higher (glass transition temperature +30) °C of the bead raw material.
• a manufacturing method including a bead annealing step of heat-treating at the following temperature (herein sometimes referred to as “foamed bead manufacturing method A"), or a bead foaming step of foaming a bead raw material containing resin.
• a manufacturing method (herein referred to as “ (sometimes referred to as “Method for producing expanded beads B”) is preferable.
• the method for manufacturing expanded beads of this embodiment may be a method consisting only of the above-mentioned bead foaming step and bead annealing step, or may be a method including further other steps.
• foamed particles obtained after the bead foaming step and before the bead annealing step may be referred to as "pre-foamed beads.” Further, “foamed beads” can be manufactured from pre-foamed beads through a bead annealing process.
• the bead foaming step is a step in which the bead raw material is impregnated with a foaming agent and foamed to obtain pre-foamed beads.
• the bead raw material contains a resin and may further contain other components.
• the resin may be a crystalline resin, an amorphous resin, or a mixture thereof. Moreover, the above-mentioned resin may be used alone or in a mixture of two or more kinds.
• the resin is preferably an amorphous resin
• the resin is preferably an amorphous resin and/or a crystalline resin; It is more preferable that
• the above-mentioned amorphous resin generally has a large dimensional change when subjected to long-term high-temperature treatment, and particularly excellent effects can be obtained by using the foamed beads obtained by the manufacturing method of this embodiment.
• the main component is a resin, and more preferably, the mass ratio of the amorphous resin to 100% of the total mass of the resins contained in the bead raw material is 50% by mass or more, still more preferably 70% by mass or more, and The content is preferably 80% by mass or more, more preferably 90% by mass or more, particularly preferably 95% by mass or more, and it is particularly preferred that the resin consists of only amorphous resin.
• the mass ratio of the crystalline resin to 100% of the total mass of the resins contained in the bead raw material may be 50% by mass or more, 70% by mass or more, or 80% by mass or more.
• the content may be 90% by mass or more, 95% by mass or more, or the resin may be only a crystalline resin.
• the amorphous resin is not particularly limited as long as it is amorphous, and examples include polyphenylene ether (PPE) resin, polyphenylene ether resin/polystyrene resin alloy, polyphenylene ether resin/high impact polystyrene resin alloy, Polyphenylene ether (PPE) resins such as polyphenylene ether resin/polystyrene resin/high-impact polystyrene resin alloy, polyphenylene ether resin/polypropylene resin alloy; polystyrene resin, rubber-reinforced polystyrene resin (high-impact polystyrene resin), acrylonitrile-butadiene - Polystyrene resins such as styrene copolymers (ABS resins); polycarbonate resins such as polycarbonate resins, polycarbonate resin/ABS resin alloys, polycarbonate resins/polybutylene terephthalate resin alloys; polyvin
• polyphenylene ether resins or polystyrene resins are preferable from the viewpoints of further reducing the dimensional change of the foam molded product after long-term high-temperature treatment and further increasing the expansion ability of the foam beads. More preferred are polystyrene resin/high impact polystyrene resin alloy, modified polyphenylene ether resin, and polystyrene resin. By reducing the dimensional changes of these resins after long-term high-temperature treatment, resin foams can be applied to automotive applications and information communication applications.
• polyphenylene ether resin-- examples include, as described above, polyphenylene ether resin, polyphenylene ether resin/polystyrene resin alloy, polyphenylene ether resin/high impact polystyrene resin alloy, or polyphenylene ether resin/polystyrene resin/high impact polystyrene resin. Examples include alloys. These may be used alone or in combination of two or more.
• the polyphenylene ether resin of the polyphenylene ether-based resin refers to a polymer containing a repeating unit (structural unit) represented by the following formula (I).
• a repeating unit structural unit represented by the following formula (I)
• Examples include a polymer, a copolymer containing a repeating unit represented by the following general formula (I), and the like.
• the above copolymer refers to a copolymer whose main repeating unit is a repeating unit represented by the following formula (I) (for example, a repeating unit represented by the following formula (I) based on 100% by mass of the copolymer).
• the above polyphenylene ethers may be used alone or in combination of two or more.
• the number of repeating units represented by the following formula (I) contained in the polyphenylene ether may be one or more.
• R 1 , R 2 , R 3 and R 4 each independently represent a hydrogen atom, a halogen atom, an alkyl group, an alkoxy group, a phenyl group, or a halogen atom in general formula (I).
• n is an integer representing the degree of polymerization.
• the number of carbon atoms in the alkyl group and alkoxy group may be 1 to 7.
• polyphenylene ether resins include poly(2,6-dimethyl-1,4-phenylene) ether, poly(2,6-diethyl-1,4-phenylene) ether, and poly(2-methyl-6-ethyl).
• -1,4-phenylene) ether poly(2-methyl-6-propyl-1,4-phenylene) ether, poly(2,6-dipropyl-1,4-phenylene) ether, poly(2-ethyl-6) -propyl-1,4-phenylene) ether, poly(2,6-dibutyl-1,4-phenylene) ether, poly(2,6-dilauryl-1,4-phenylene) ether, poly(2,6-diphenyl) -1,4-diphenylene) ether, poly(2,6-dimethoxy-1,4-phenylene) ether, poly(2,6-diethoxy-1,4-phenylene) ether, poly(2-methoxy-6-ethoxy
• the above-mentioned polyphenylene ether resin is not particularly limited, and can be produced by a known method, for example, using a complex of a cuprous salt and an amine by Hay described in U.S. Pat. No. 3,306,874 as a catalyst. For example, it can be easily produced by oxidative polymerization of 2,6-xylenol.
• U.S. Patent No. 3,306,875, U.S. Pat. No. 3,257,357, U.S. Pat. Examples include the method described in Japanese Patent No. 152628 and the like.
• polyphenylene ether resin a modified polyphenylene ether resin in which some or all of the constituent units constituting the polyphenylene ether resin are modified with an unsaturated or saturated carboxylic acid or a derivative thereof can be used.
• modified polyphenylene ether resins are disclosed in JP-A-2-276,823 (US Pat. No. 5,159,027, US Reissue Patent No. 35,695) and JP-A-63-108,059 (US Pat. No. 5,214,109). Specifications, No. 5216089), JP-A No. 59-59724, and the like.
• the modified polyphenylene ether resin is produced, for example, by melt-kneading and reacting an unsaturated or saturated carboxylic acid or a derivative thereof with a polyphenylene ether resin in the presence or absence of a radical initiator.
• a radical initiator for example, it is produced by dissolving a polyphenylene ether resin and an unsaturated or saturated carboxylic acid or a derivative thereof in an organic solvent in the presence or absence of a radical initiator and reacting in solution.
• Examples of unsaturated carboxylic acids or derivatives thereof include maleic acid, fumaric acid, itaconic acid, halogenated maleic acid, cis-4-cyclohexene 1,2-dicarboxylic acid, endo-cis-bicyclo(2,2,1)
• Examples include -5-heptene-2,3-dicarboxylic acid, acid anhydrides, esters, amides, imides, etc. of these dicarboxylic acids, as well as acrylic acid, methacrylic acid, etc., and esters, amides, etc. of these monocarboxylic acids. It will be done.
• saturated carboxylic acid or its derivative for example, a compound that can thermally decompose itself at the reaction temperature when producing the modified polyphenylene ether resin and become a derivative of the modified polyphenylene ether resin can be mentioned.
• Specific examples include malic acid and citric acid.
• the content of the polyphenylene ether resin is preferably 40 to 99% by mass, more preferably 50 to 99% by mass based on 100% by mass of the polymer alloy. It is 95% by mass, more preferably 70 to 90% by mass.
• Polystyrene resins that can be used for polyphenylene ether resins include homopolymers of styrene compounds, copolymers of two or more styrene compounds, and rubber-like polymers in a matrix made of polymers of styrene compounds. Examples include rubber-modified styrene resin (high impact polystyrene resin) in which is dispersed in the form of particles.
• styrenic compounds that produce these polymers include styrene, o-methylstyrene, p-methylstyrene, m-methylstyrene, ⁇ -methylstyrene, ethylstyrene, ⁇ -methyl-p-methylstyrene, 2,4- Examples include dimethylstyrene, monochlorostyrene, p-tert-butylstyrene, and the like.
• the polystyrene resin contained in the polyphenylene ether resin may be a copolymer obtained by using two or more styrene compounds together or a high impact polystyrene resin.
• polystyrene resin obtained by polymerizing styrene alone is preferred.
• Polystyrene resins having a stereoregular structure such as atactic polystyrene and syndiotactic polystyrene can be effectively used as the polyphenylene ether resin.
• the weight average molecular weight (Mw) of the polyphenylene ether resin is preferably 20,000 to 60,000.
• the weight average molecular weight (Mw) is determined by measuring the resin by gel permeation chromatography (GPC), and comparing the molecular weight of the peak in the chromatogram with a calibration curve (of standard polystyrene) determined from measurements on commercially available standard polystyrene. (prepared using peak molecular weight).
• the mass ratio of the polyphenylene ether resin to 100 mass% of the bead raw material is preferably 60 to 100 mass%, more preferably 70 to 99 mass%, and even more preferably 80 to 95 mass%.
• the mass proportion of the polyphenylene ether resin is within the above range, it is easy to obtain foamed beads that yield a foamed molded article with small dimensional changes after long-term high temperature treatment.
• the polystyrene resin refers to a homopolymer of styrene and a styrene derivative, or a copolymer containing styrene and a styrene derivative as a main component (a component contained in the polystyrene resin in an amount of 50% by mass or more).
• styrene derivatives include o-methylstyrene, m-methylstyrene, p-methylstyrene, t-butylstyrene, ⁇ -methylstyrene, ⁇ -methylstyrene, diphenylethylene, chlorostyrene, bromostyrene, and the like.
• Examples of the homopolymer polystyrene resin include polystyrene, poly ⁇ -methylstyrene, polychlorostyrene, and the like.
• Examples of the polystyrene resin copolymer include styrene-butadiene copolymer, styrene-acrylonitrile copolymer, styrene-maleic acid copolymer, styrene-maleic anhydride copolymer, styrene-maleimide copolymer, and styrene-maleic anhydride copolymer.
• N-phenylmaleimide copolymer N-phenylmaleimide copolymer, styrene-N-alkylmaleimide copolymer, styrene-N-alkyl substituted phenylmaleimide copolymer, styrene-acrylic acid copolymer, styrene-methacrylic acid copolymer, styrene-methyl acrylate Copolymers, binary copolymers such as styrene-methyl methacrylate copolymers, styrene-n-alkyl acrylate copolymers, styrene-n-alkyl methacrylate copolymers, ethylvinylbenzene-divinylbenzene copolymers; ABS , butadiene-acrylonitrile- ⁇ -methylbenzene copolymer, and other terpolymers; styrene-grafted polyethylene, s
• the polystyrene resin may be manufactured by any conventionally known manufacturing method.
• polycarbonate resin-- examples include polycarbonate resin, polycarbonate resin/ABS resin alloy, polycarbonate resin/polybutylene terephthalate resin alloy, and the like. These may be used alone or in combination of two or more.
• the polycarbonate resin may be a bisphenol A type polycarbonate polymerized using bisphenol A, or various polycarbonates having high heat resistance or low water absorption that are polymerized using other dihydric phenol compounds.
• the other dihydric phenol compounds mentioned above include hydroquinone, 4,4'-dihydroxydiphenyl, bis(4-hydroxyphenyl)methane, 1,1-bis(4-hydroxyphenyl)cyclohexane, 2,2-bis (3,5-dimethyl-4-hydroxyphenyl)propane, bis(4-hydroxyphenyl) sulfide, bis(4-hydroxyphenyl) sulfone, bis(4-hydroxyphenyl) sulfoxide, bis(4-hydroxyphenyl) ketone, Examples include bis(4-hydroxyphenyl) ether and halogenated bisphenols such as 2,2-bis(3,5-dibromo-4-hydroxyphenyl)propane.
• the polycarbonate resin may also be a branched polycarbonate obtained by polymerizing trifunctional phenols, and may further contain aliphatic dicarboxylic acids, aromatic dicarboxylic acids, or divalent aliphatic or fatty acids.
• a copolymerized polycarbonate obtained by copolymerizing a cyclic alcohol may also be used.
• the polycarbonate resin may be manufactured by any conventionally known manufacturing method.
• the bead raw material contains a resin containing a monomer unit having an aromatic group.
• a resin containing a monomer unit having an aromatic group When a resin containing a monomer unit having an aromatic group is included, a foamed molded article having good flame retardancy tends to be obtained.
• the resins containing aromatic monomer units include aromatic polyamide resins, polycarbonate resins, polyethylene terephthalate resins, polyimide resins, polyphenylene ether resins, and styrene resins.
• the mass ratio of aromatic monomer units in the resin is determined by the fact that the resin tends to carbonize during combustion, so it is easy to suppress ignition and flame ignition of the resin, and it also suppresses the generation of flammable gas, making it non-flammable.
• the mass proportion of the aromatic monomer unit can be calculated from the molecular structure contained in the constituent units if the molecular structure is known. Even when multiple resins are included, similar calculations are performed for each resin and additive, and the average is calculated according to the mass proportion to be mixed to calculate the aromatic monomer units in the entire resin. It is possible to calculate the mass percentage of Furthermore, if the structure is unknown, it is possible to estimate and calculate the monomer unit having an aromatic group using NMR, IR, etc.
• the foamed molded product obtained from the foamed beads of this embodiment may be used in electronic devices, but for example, when used in a device that transmits and receives radio waves, it is required to reduce the relative dielectric constant and dielectric loss tangent.
• a method to lower the relative permittivity and dielectric loss tangent it is possible to select a resin with low density, low polarity, or a resin with few terminal polar groups in the molecular chain as the resin before foaming in the bead raw material. Can be mentioned.
• resins include polyolefin resins, polystyrene resins, polyphenylene ether resins, polyimide resins, fluorine resins, liquid crystal polymers, polyphenylene sulfide resins, and the like.
• polyolefin resins, polystyrene resins, and polyphenylene ether resins are preferred from the viewpoint of processability, cost, and flame retardancy.
• methods for lowering the water absorption of the bead raw material include lowering the polarity of the constituent units in the resin as a resin in the bead raw material; Examples include reducing chain terminal polar groups.
• suitable resins include polyolefin resins, polystyrene resins, polyphenylene ether resins, polyimide resins, fluorine resins, liquid crystal polymers, polyphenylene sulfide resins, and the like.
• polyolefin resins, polystyrene resins, and polyphenylene ether resins are preferred from the viewpoint of processability, cost, and flame retardancy.
• the crystalline resin is not particularly limited as long as it has crystallinity, such as polyethylene resin, polypropylene resin, polyvinylidene chloride resin, polyamide resin, polyacetal resin, polyethylene terephthalate resin, polybutylene terephthalate resin, polyphenylene sulfide resin, Examples include polyetheretherketone resin, liquid crystal polymer, polytetrafluoroethylene resin, and the like.
• polyamide resins, polyacetal resins, polybutylene terephthalate resins, and polyphenylene sulfide resins are preferred from the viewpoints of heat resistance, flame retardancy, and moldability.
• the polyamide resin is not particularly limited, and any known polyamide resin can be used.
• the polyamide resin include polyamide homopolymers, polyamide copolymers, and the like.
• polyamide homopolymers include nylon 66, nylon 610, nylon 612, nylon 46, and nylon 1212 obtained by polycondensation of diamine and dicarboxylic acid; nylon 6 and nylon 12 obtained by ring-opening polymerization of lactam. etc.
• Examples of the polyamide copolymer include nylon 6/66, nylon 66/6, nylon 66/610, and nylon 66/612.
• As the polyamide resin aliphatic polyamide is preferable, and nylon 6, nylon 66, nylon 6/66, nylon 66/6, etc. are more preferable.
• the glass transition temperature of the resin is preferably 80 to 250°C, more preferably 100 to 230°C, still more preferably 120 to 220°C, from the viewpoint of reducing dimensional changes during long-term high temperature treatment.
• the glass transition temperature of the bead raw material is preferably 80 to 180°C, more preferably 100 to 170°C, still more preferably 120 to 160°C, from the viewpoint of reducing dimensional changes during long-term high temperature treatment.
• the highest glass transition temperature is taken as the glass transition temperature of the bead raw material.
• the glass transition temperature can be measured by the method described in Examples below.
• the softening point temperature of the resin is preferably 80 to 250°C, more preferably 100 to 230°C, and even more preferably 120 to 220°C, from the viewpoint of reducing dimensional changes during long-term high temperature treatment.
• the softening point temperature of the bead raw material is preferably 80 to 180°C, more preferably 100 to 170°C, and even more preferably 120 to 160°C, from the viewpoint of reducing dimensional changes during long-term high temperature treatment.
• the softening point temperature Tm is the melting peak temperature measured by differential scanning calorimetry (DSC) in accordance with JIS K7121. When multiple melting peaks appear, the temperature of the peak appearing on the highest temperature side is defined as Tm.
• Tm be the temperature at which the observed loss tangent tan ⁇ becomes maximum.
• Tm the temperature on the highest temperature side is set as Tm. Specifically, it can be measured by the method described in Examples below.
• the mass ratio of the resin in 100% by mass of the bead raw material is preferably 50 to 100% by mass, more preferably 60 to 95% by mass, even more preferably 70 to 92% by mass, particularly preferably 80 to 90% by mass. Mass%.
• Other components mentioned above include flame retardants, flame retardant aids, heat stabilizers, antioxidants, antistatic agents, inorganic fillers, anti-dripping agents, ultraviolet absorbers, light absorbers, plasticizers, mold release agents, Dyes and pigments, rubber components, resins other than the above-mentioned base resins, and the like can be added within a range that does not impair the effects of the present invention.
• the other components mentioned above may be components other than the resin.
• the mass proportion of the other components in the bead raw material is preferably 0 to 40 parts by mass, more preferably 5 to 30 parts by mass, still more preferably 10 to 20 parts by mass, based on 100 parts by mass of the resin. Department.
• the mass proportion of the other components in 100 mass% of the bead raw material is preferably more than 0 mass% and 50 mass% or less, more preferably 5 to 40 mass%, still more preferably 8 to 30 mass%, especially Preferably it is 10 to 20% by mass.
• Examples of the flame retardant include organic flame retardants and inorganic flame retardants.
• Examples of organic flame retardants include halogen compounds represented by bromine compounds, phosphorus compounds, and non-halogen compounds represented by silicone compounds.
• Examples of inorganic flame retardants include metal hydroxides such as aluminum hydroxide and magnesium hydroxide, and antimony compounds such as antimony trioxide and antimony pentoxide. These may be used alone or in combination of two or more.
• non-halogen flame retardants that are organic flame retardants are preferred, and phosphorus-based or silicone-based flame retardants are more preferred.
• phosphorus-based flame retardant one containing phosphorus or a phosphorus compound can be used.
• phosphorus include red phosphorus.
• the phosphorus compound include phosphoric acid esters, phosphazene compounds having a bond between a phosphorus atom and a nitrogen atom in the main chain, trialkylphosphine oxide, triphenylphosphine oxide, and the like.
• Examples of phosphoric acid esters include trimethyl phosphate, triethyl phosphate, tripropyl phosphate, tributyl phosphate, tripentyl phosphate, trihexyl phosphate, tricyclohexyl phosphate, triphenyl phosphate, tricresyl phosphate, tricylenyl phosphate, cresyl diphenyl.
• phosphoric acid esters modified with various substituents. Also included are compounds, various condensed type phosphoric ester compounds, and phosphoric ester compounds having a cyclic structure.
• phosphazene compounds such as bisphenol A bisphosphate, condensation type phosphoric acid ester compounds, and phosphoric acid ester compounds having a cyclic structure are preferred from the viewpoint of heat resistance, flame retardance, and foamability. These may be used alone or in combination of two or more.
• silicone flame retardants include (mono- or poly)organosiloxanes.
• examples of (mono- or poly)organosiloxanes include monoorganosiloxanes such as dimethylsiloxane and phenylmethylsiloxane; polydimethylsiloxanes and polyphenylmethylsiloxanes obtained by polymerizing these; organopolysiloxanes such as copolymers thereof; etc.
• the bonding groups of the main chain and branched side chains are hydrogen, alkyl groups, and phenyl groups, preferably phenyl groups, methyl groups, ethyl groups, and propyl groups, but are not limited thereto.
• the terminal linking group may be a hydroxyl group, an alkoxy group, an alkyl group, or a phenyl group.
• shape of the silicone There is no particular restriction on the shape of the silicone, and any shape such as oil, gum, varnish, powder, pellet, etc. can be used. These may be used alone or in combination of two or more.
• the mass proportion of the flame retardant in 100 mass% of the bead raw material is preferably 1 to 30 mass%, more preferably 5 to 25 mass%, and even more preferably 10 to 20 mass%. Further, the mass ratio of the flame retardant to 100 parts by mass of the resin is preferably 5 to 30 parts by mass, more preferably 10 to 25 parts by mass.
• the rubber component examples include, but are not limited to, butadiene, isoprene, 1,3-pentadiene, and the like. These are preferably dispersed in the form of particles in a continuous phase made of polystyrene resin.
• the rubber component itself may be added, or a resin such as a styrene elastomer or a styrene-butadiene copolymer may be used as a rubber component supply source.
• the content of the rubber component is preferably 0.3 to 15 parts by mass, more preferably 0.5 to 8 parts by mass, and 1 to 5 parts by mass based on 100 parts by mass of the resin. More preferred.
• the amount is 0.3 parts by mass or more, the resin has excellent flexibility and elongation, the foamed cell membrane is difficult to rupture during foaming, and a foamed product with excellent moldability and mechanical strength is easily obtained.
• a rubber component is suitably used to impart foamability to the bead raw material.
• the above-mentioned rubber component is important in bead foaming, in which the temperature is gradually raised from room temperature to foam the resin in an unmolten state.
• inorganic fillers examples include fibrous inorganic fillers such as glass fiber, potassium titanate fiber, gypsum fiber, brass fiber, stainless steel fiber, steel fiber, ceramic fiber, and boron whisker fiber; mica, talc, kaolin, and calcined Examples include plate-like inorganic fillers such as kaolin and glass flakes; granular inorganic fillers such as titanium oxide, apatite, glass beads, silica, calcium carbonate, and carbon black; acicular inorganic fillers such as wollastonite and xonotrite; and the like.
• fibrous inorganic fillers such as glass fiber, potassium titanate fiber, gypsum fiber, brass fiber, stainless steel fiber, steel fiber, ceramic fiber, and boron whisker fiber
• mica, talc, kaolin, and calcined Examples include plate-like inorganic fillers such as kaolin and glass flakes; granular inorganic fillers such as titanium oxide, apatite, glass beads, silic
• fibrous inorganic fillers are preferred, and glass fibers, glass flakes, mica, and talc are more preferred.
• the above inorganic fillers may be used alone or in combination of two or more.
• the mass proportion of the inorganic filler in 100 mass% of the bead raw material is preferably 0.01 to 10 mass%, more preferably 0.1 to 5 mass%, and still more preferably 0.5 to 3 mass%. %.
• blowing agent commonly used gases can be used.
• gases such as air, carbon dioxide gas, nitrogen gas, oxygen gas, ammonia gas, hydrogen gas, argon gas, helium gas, neon gas; trichlorofluoromethane (R11), dichlorodifluoromethane (R12), chlorodifluoromethane Fluorocarbons such as (R22), tetrachlorodifluoroethane (R112), dichlorofluoroethane (R141b), chlorodifluoroethane (R142b), difluoroethane (R152a), HFC-245fa, HFC-236ea, HFC-245ca, HFC-225ca; propane, n- Saturated hydrocarbons such as butane, i-butane, n-pentane, i-pentane, neopentane; dimethyl ether, diethyl
• an inorganic gas is preferable from the viewpoint of maintaining moldability and excellent flame retardancy.
• inorganic gases are less soluble in resin than organic gases such as hydrocarbons, and gas easily escapes from the resin after the bead foaming process or foam molding process, so the dimensional stability of the molded foam over time may be affected. There are even better benefits.
• plasticization of the resin due to residual gas is less likely to occur, and there is also the advantage that excellent heat resistance is easily exhibited from an earlier stage after molding.
• inorganic gases are less soluble in resins than organic gases such as hydrocarbons, and are more likely to dissipate from the pellet surface during foaming, making it easier to form a skin layer and less likely to cause bubbles to break.
• organic gases such as hydrocarbons
• carbon dioxide gas is preferred from the viewpoint of solubility in resin and ease of handling.
• the method of incorporating (impregnating) a foaming agent into the bead raw material and foaming it includes, for example, the method described in Example 1 of JP-A-4-372630.
• bead raw materials pellets, beads, etc.
• a blowing agent gas
• the pressure is released and the bead raw material pellets are transferred from the pressure vessel to the foaming furnace, and the bead raw material pellets are heated and foamed with pressurized steam while rotating the stirring blade in the foaming furnace.
• Examples include methods for producing pre-expanded beads.
• a method for incorporating a foaming agent into the bead raw material commonly used methods can be applied, such as a method using an aqueous medium using a suspension system such as water (suspension impregnation), and a method using a suspension system such as water (suspension impregnation);
• a method using a pyrolytic blowing agent such as sodium hydrogen (foaming agent decomposition method) a method in which the gas is brought into an atmosphere above the critical pressure, brought into a liquid phase, and brought into contact with the bead raw material (liquid phase impregnation), a method in which the gas is brought into contact with the bead material under the critical pressure.
• Examples include a method of contacting the bead raw material in a gaseous state under a high-pressure atmosphere (vapor phase impregnation).
• vapor phase impregnation a method in which gas is impregnated in a gas phase under a high-pressure atmosphere below the critical pressure is particularly preferred.
• the gas phase impregnation method has better solubility of gas in the resin than suspension impregnation performed under high temperature conditions, and it is easier to increase the blowing agent content. Therefore, it is easy to achieve a high expansion ratio, and the bubble size is also easy to become uniform.
• the blowing agent decomposition method is not only carried out under high temperature conditions, but also not all of the added pyrolytic blowing agent turns into gas, so the amount of gas generated tends to be relatively small.
• gas phase impregnation has the advantage of making it easier to increase the blowing agent content.
• equipment such as a pressure-resistant device and a cooling device can be made more compact than in liquid phase impregnation, making it easier to keep equipment costs low.
• the gas phase impregnation conditions are not particularly limited, but the atmospheric pressure is preferably 0.5 to 6.0 MPa, more preferably 1.0 to 5.0 MPa. Further, the ambient temperature is preferably 5 to 30°C, more preferably 7 to 15°C. Further, the impregnation time is preferably 0.5 to 48 hours, more preferably 1 to 24 hours. When the atmospheric pressure, atmospheric temperature, and impregnation time are within the above ranges, gas dissolution into the bead raw material tends to proceed more efficiently. In particular, if the ambient temperature is low, the amount of impregnation increases but the impregnation rate slows down, and if the ambient temperature is high, the amount of impregnation decreases but the impregnation rate increases. It is preferable to set the above ambient temperature for the process to proceed.
• the amount of the blowing agent impregnated is preferably 3 to 13% by mass, more preferably 3.5 to 10% by mass based on the resin contained in the bead raw material.
• the impregnated amount of the blowing agent for example, carbon dioxide gas
• the impregnated amount of the blowing agent is 3% by mass or more, it becomes easier to achieve a higher expansion ratio, and the variation in the bubble size is reduced, making it easier to suppress the variation in the expansion ratio.
• the content is 13% by mass or less, the bubble size becomes appropriate, and it becomes easy to suppress a decrease in the closed cell ratio due to overfoaming.
• the method for foaming the bead raw material in the bead foaming process is not particularly limited, but examples include a method in which the foaming agent (e.g., gas) dissolved in the resin is expanded from a high-pressure condition to a low-pressure atmosphere, and a method in which a foaming agent (e.g., gas) dissolved in the resin is expanded. Examples include a method in which a blowing agent (for example, gas) dissolved in a resin is expanded by heating with hot air or the like. Among these, the method of heating and foaming is particularly preferred. This is because the size of the bubbles inside the resin tends to be more uniform compared to a method in which the resin is exposed to a low-pressure atmosphere all at once from a high-pressure condition.
• the foaming agent e.g., gas
• the heat source for heating and foaming is not particularly limited, such as steam, hot air, or a heater, but heat treatment using steam (preferably pressure steam) is preferred from the viewpoint of shortening the foaming time by taking advantage of its high thermal conductivity. preferable.
• steam preferably pressure steam
• residual stress occurs inside the beads after foaming, so the heat shrinkage rate of foamed beads tends to increase.
• the residual stress small foam beads can be obtained.
• it is preferable to heat and foam using hot air, especially from the viewpoint of obtaining a foamed molded product with excellent heat shrinkage.
• Steam here refers to pressurized steam that is pressurized and heated above atmospheric pressure.
• Hot air refers to dry air heated to 50°C or higher and with a relative humidity of less than 10%.
• the foaming temperature in the bead foaming step is preferably at least the glass transition temperature Tg of the bead raw material - 25°C, more preferably at least the glass transition temperature Tg - 20°C of the bead raw material. Further, the foaming temperature is preferably below the glass transition temperature Tg of the bead raw material + 30°C, more preferably below the glass transition temperature Tg + 20°C of the bead raw material.
• the temperature of the pressure steam is set at (glass transition temperature Tg of bead raw material Tg - 30°C) from the viewpoint of efficiently obtaining pre-foamed beads with a magnification higher than that of foamed beads. It is preferable that the glass transition temperature of the bead raw material Tg + 10°C, more preferably (the glass transition temperature Tg of the bead raw material Tg - 20) °C to (the glass transition temperature Tg + 5 of the bead raw material) °C, and even more preferably (the glass transition temperature Tg of the bead raw material Tg + 5) °C.
• the foaming temperature in the bead foaming step is preferably at least the softening point temperature Tm of the bead raw material - 25°C, more preferably at least the softening point temperature Tm - 20°C of the bead raw material. Further, the foaming temperature is preferably below the softening point temperature Tm+30°C of the bead raw material, and more preferably below the softening point temperature Tm+20°C of the bead raw material.
• the temperature of the pressure steam is (softening point temperature of bead raw material Tm - 30)°C from the viewpoint of efficiently obtaining pre-foamed beads with a magnification higher than that of foamed beads. It is preferably from (softening point temperature of bead raw material Tm + 10) °C, more preferably (softening point temperature of bead raw material Tm - 20) °C to (softening point temperature of bead raw material Tm + 5) °C, even more preferably (bead raw material softening point temperature Tm + 5) °C.
• the softening point temperature Tm of the bead raw material can be determined by the method described in Examples below.
• the foaming temperature may be the maximum temperature in the bead foaming step.
• the foaming time in the bead foaming step is not particularly limited as it depends on the foaming temperature, but generally it is preferably 5 seconds to 120 seconds, more preferably 10 seconds to 60 seconds, even more preferably 15 seconds. It is from seconds to 45 seconds.
• the foaming may be performed in one step to the desired expansion ratio, or it may be foamed to the desired expansion ratio in multiple stages such as secondary foaming and tertiary foaming.
• foaming is performed in multiple stages, it is preferable to provide a bead annealing process described below after each stage.
• the conditions of the bead annealing step after each stage may be the same or different.
• the gas used before each stage may be the same gas or different gases in each stage, but it is preferable that the gas is the same gas.
• the foaming conditions before each stage may be the same or different at each stage.
• the bead foaming process refers to a process in which the bulk density gradually increases after foaming of the bead raw material begins, and includes the period immediately before the bulk density changes or shifts to a state where it gradually decreases.
• the bead foaming step is a step in which the bulk ratio per second increases in the range of 0.1 cm 3 /g to 100 cm 3 /g.
• the pre-foamed beads obtained in the above bead foaming step can be heat-treated in a bead annealing step to produce foamed beads.
• the bead annealing step may be provided consecutively to the bead foaming step, or may be performed after a period of time after the bead foaming step.
• the bead annealing process is a process intended to remove residual stress inside the pre-foamed beads by heat-treating the pre-foamed beads after foaming, and is a process of leaving the beads without foaming or intentional heat treatment. This is a different process.
• the bead annealing process refers to a process that includes the bead foaming process and the bead annealing process, but excludes the part corresponding to the bead foaming process.
• the rate of change in bulk ratio per second of the pre-foamed beads is preferably -0.5 to -0.001 cm 3 /g from the viewpoint of obtaining excellent expansion ability, and - It is more preferably from 0.2 to -0.005 cm 3 /g, and even more preferably from -0.08 to -0.01 cm 3 /g.
• Examples of the above-mentioned heat treatment include heating with steam (preferably pressure steam or water vapor), heating with hot air, heating with a heater, and the like.
• steam preferably pressure steam or water vapor
• heat treatment using hot air is preferred from the viewpoint of good thermal conductivity and ability to anneal in a short time.
• the temperature of the heat treatment is preferably at least ⁇ 30° C. to the glass transition temperature of the bead raw material and at most +30° C., and more preferably from the viewpoint of excellent dimensional change after long-term high-temperature treatment and better expansion ability.
• the temperature may be constant or may be varied. When changing the temperature, it is preferable to change the temperature within the above range.
• the temperature of the heat treatment is preferably -30°C or more, the softening point temperature of the bead raw material, and +30°C or less, and more preferably from the viewpoint of excellent dimensional change after long-term high-temperature treatment and better expansion ability.
• the temperature may be constant or may be varied. When changing the temperature, it is preferable to change the temperature within the above range.
• the temperature of the heat treatment is preferably from -30°C to the glass transition temperature of the bead raw material and +30°C to the glass transition temperature of the bead raw material, and long-term high temperature treatment.
• the glass transition temperature is more preferably -25°C or more and the glass transition temperature +25°C or less, and even more preferably the glass transition temperature is -20°C or more and the glass transition temperature +20°C or less.
• the temperature may be constant or may be varied. When changing the temperature, it is preferable to change the temperature within the above range.
• the time for the above heat treatment is preferably 10 seconds to 600 seconds, more preferably 20 seconds to 300 seconds, still more preferably 30 seconds to It is 120 seconds. If the heat treatment time is less than 10 seconds, the effect of removing residual stress will not be sufficiently obtained, the heat shrinkage rate of the foamed beads will increase, and the dimensional change rate of the resulting foamed molded product will increase, which is preferable. do not have. If the heat treatment time exceeds 600 seconds, the foamed beads will shrink significantly, leading to an extreme decrease in expansion ratio, which is not preferable.
• the temperature of the steam used in the heat treatment is preferably -30°C or higher, the glass transition temperature of the bead raw material and 30°C or lower, and more preferably -25°C or higher, and 10°C or lower than the glass transition temperature of the bead raw material. More preferably, the glass transition temperature is -20°C or higher and the glass transition temperature is +5°C or lower. Further, the softening point temperature of the bead raw material is preferably -30°C or more and softening point temperature +30°C or less, more preferably softening point temperature -25°C or more and softening point temperature +10°C or less, and even more preferably softening point temperature -20°C.
• the temperature of the hot air used in the heat treatment is preferably from -30°C to glass transition temperature +30°C, more preferably from -20°C to glass transition temperature +20°C, more preferably from glass transition temperature -20°C to glass transition temperature +20°C. More preferably, the glass transition temperature is ⁇ 10° C. or higher and the glass transition temperature is +10° C. or lower.
• the softening point temperature of the bead raw material is preferably -30°C or more and softening point temperature +30°C or less, more preferably softening point temperature -20°C or more and softening point temperature +20°C or less, and even more preferably softening point temperature -10°C. °C or higher and softening point temperature +10°C or lower.
• the temperature of the steam and the temperature of the hot air may be constant or may be changed. When changing the temperature, it is preferable to change the temperature within the above range.
• the heat treatment temperature is determined from the viewpoint of excellent dimensional change after long-term high-temperature treatment and even better expansion ability. Temperature) is preferably lower, more preferably 2°C or more, and even more preferably 4°C or more.
• the heat treatment temperature is preferably kept at a constant temperature, gradually raised from a low temperature to a high temperature, or a combination thereof. In particular, a temperature program in which the temperature is gradually raised during the bead annealing process is preferable because it can be expected to shorten the process time.
• the temperature of the heat treatment is preferably below the foaming temperature in the bead foaming step, from the viewpoint of excellent dimensional change after long-term high temperature treatment and better expansion ability. It is more preferable to lower the temperature by 2°C or more, and even more preferably by 4°C or more. If the temperature of the heat treatment in the bead annealing step is 20° C. or more lower than the foaming temperature in the bead foaming step, it is not preferable because an extremely long time is required for the annealing.
• the temperature of the heat treatment in the bead annealing step may be lower than the foaming temperature at the end of the bead foaming step. Further, the heat treatment temperature in the bead annealing step may be lower than the maximum foaming temperature in the bead foaming step.
• the bulk factor of the pre-foamed beads obtained in the bead foaming step may be reduced after the bead annealing step.
• the ratio of the bulk magnification of the foamed beads after the bead annealing step to 100% of the bulk magnification of the pre-foamed beads before the bead annealing step is preferably 30 to 99%, more preferably 40 to 95%.
• the lower limit of the final bulk ratio after the bead foaming step is preferably 2 cc/g or more from the viewpoint of weight reduction, more preferably 3 cc/g or more, and even more preferably 5 cc/g or more. preferable.
• the upper limit of the final bulk ratio after the bead foaming step is preferably 30 cc/g or less, more preferably 20 cc/g or less, and 15 cc/g or less. It is more preferable that During the bead annealing step, the bulk factor of the expanded beads may be gradually decreased.
• the bead annealing step may be a step in which the bulk factor of the beads remains the same or decreases (preferably decreases) during the process.
• the bulk density of the pre-foamed beads and foamed beads can be measured by the method described in Examples below.
• the bulk ratio of the pre-foamed beads is reduced through the bead annealing step. Therefore, in consideration of the decrease in bulk ratio in the bead annealing process, it is preferable to foam the beads in the bead foaming process until the volume ratio becomes higher than the intended volume ratio of the foamed beads.
• a step may be provided in which the proportion of the bulk factor reduced in the beer annealing step is measured in advance and the planned bulk factor after the bead foaming step is determined.
• the bead foaming step and the bead annealing step may be performed in different devices or in the same device.
• continuous bead annealing without taking the pre-foamed beads out of the equipment simplifies the process and makes it easier to control the bulk ratio of the foamed beads obtained, so it is preferable to perform the process in the same equipment. preferable.
• the foam molding step is a step of manufacturing a foam molded product from the foam beads obtained in the bead annealing step.
• a foamed molded product can be obtained by filling a mold with foamed beads obtained in a bead annealing process, expanding the foamed beads by heating with water vapor, etc., and simultaneously thermally fusing the foamed beads together.
• a mold having a desired shape is prepared and foamed beads are filled into the mold and molded, so that the foamed molded product can be easily molded into finer or more complex shapes.
• the bead foaming method easily increases the expansion ratio of the foamed molded product, and the obtained foamed molded product easily exhibits flexibility in addition to heat insulation properties.
• the foamed beads obtained in the bead annealing step may be used continuously in the foam molding step, or may be used in the foam molding step at intervals.
• Filling methods for foamed beads include, for example, the cracking method, in which the mold is left slightly open during filling, the compression method, in which the mold is kept closed and pressurized and filled with compressed beads, and the compressed bead filling method. Examples include compression cracking methods in which cracking is performed afterwards.
• a pressurization process in which a pressure treatment is performed under an inorganic gas atmosphere before filling the foamed beads. This is because by applying the pressure treatment, a constant gas pressure can be applied to the bubbles within the foam beads, making it easier to foam and mold them more uniformly.
• the pressure source for performing the pressure treatment is not particularly limited, it is preferable to use the above-mentioned inorganic gas.
• inorganic gases include air, carbon dioxide gas, nitrogen gas, oxygen gas, ammonia gas, hydrogen gas, argon gas, helium gas, neon gas, etc. From the viewpoint of ease of handling and economic efficiency, carbon dioxide gas and air are preferable.
• the method of pressure treatment is also not particularly limited, but foamed beads are filled in a pressurized tank, inorganic gas is supplied into the tank, and the pressure is increased to a maximum pressure of 0.1 to 20 MPa over 10 minutes to 96 hours. Examples include a method of pressurizing by doing so.
• the foamed beads obtained by the manufacturing method of this embodiment are used, it is possible to manufacture foamed molded articles with fine shapes or complicated shapes by a known in-mold molding method, and the range of possible uses is expanded. is also a feature.
• the foam beads do not expand sufficiently in the corners of the mold or in the thin cavity space (thin molded product space), so the mold is opened slightly and filled with more foam beads to perform foam molding. Many cracking methods have been used.
• the foamed beads obtained by the production method of the present invention have high expansion ability, so even if the amount of foamed beads filled is small, it can fill the gaps between beads and the corners in the mold, and the mold can be closed to form the foam. It can be performed.
• the foamed beads obtained by the manufacturing method of this embodiment have excellent expansion ability, so the number of foamed beads filled in the mold can be reduced, allowing molding to be performed with the mold completely closed, and the thickness accuracy is also excellent.
• a foam molded article can be obtained. Furthermore, even in a foam molded product having portions with different thicknesses, there is an advantage that a foam molded product with small variations in expansion ratio can be obtained. In addition, it is possible to achieve both weight reduction and freedom in shape design, which are the advantages of foam.
• the foamed beads obtained by the manufacturing method of this embodiment for example, a pair of molds for molding conventional foamed beads in the mold is used, and the foamed beads are placed in the mold cavity under pressurized atmospheric pressure or reduced pressure. Fill the tee and close the mold to compress the mold cavity volume by 0 to 70%, then supply a heat medium such as steam into the mold to heat it and heat-fuse the foamed beads.
• the vacuum molding method for example, Japanese Patent Publication No. 46-38359
• the secondary foamability of the foamed beads is increased by pre-pressurizing the foamed beads with pressurized gas to increase the pressure inside the foamed beads.
• a heating medium such as steam into the mold.
• Examples include a pressure molding method (for example, Japanese Patent Publication No. 51-22951) that involves fusing.
• a heating medium such as steam is supplied into the cavity to heat the foamed beads. It can also be molded by a compression filling molding method (Japanese Patent Publication No. 4-46217) in which the materials are heated and fused.
• the secondary foaming power of foamed beads is increased under special conditions, and after the foamed beads are filled into the cavities of a pair of molds under atmospheric pressure or reduced pressure, a heating medium such as steam is supplied. Molding can also be performed by a normal pressure filling molding method (Japanese Patent Publication No. 6-49795) in which foamed beads are heated and fused by heating, or a method combining the above methods (Japanese Patent Publication No. 6-22919). can.
• the maximum vapor pressure of the pressurized steam in the mold is preferably 30 to 700 kPa from the viewpoint of easily obtaining the desired magnification and improving the appearance.
• the foamed beads of this embodiment can be manufactured by the manufacturing method of this embodiment described above.
• Examples of the foamed beads include amorphous resin foamed beads and crystalline resin foamed beads, which will be described later.
• the foamed beads mentioned above are preferably foamed beads made by foaming a bead raw material containing an amorphous resin. It is preferable to use amorphous resin foam beads that have a heat shrinkage rate of 25% or less when heated for 5 minutes at the glass transition temperature of the bead raw material containing an amorphous resin plus 10° C. Examples of the amorphous resin include those mentioned above, and the same amorphous resins as mentioned above are preferred.
• the bead raw materials include those mentioned above, and those similar to those mentioned above are preferred.
• the foamed beads described above are preferably foamed beads made by foaming a bead raw material containing a crystalline resin.
• the foamed beads are preferably crystalline resin foamed beads having a heat shrinkage rate of 25% or less when heated for 5 minutes at a softening point temperature of -10° C. of the bead raw material containing a crystalline resin.
• Examples of the amorphous resin include those mentioned above, and the same amorphous resins as mentioned above are preferred.
• the bead raw materials include those mentioned above, and those similar to those mentioned above are preferred.
• the heat shrinkage rate of the foamed beads is preferably 25% or less, more preferably 20% or less, still more preferably 18% or less, from the viewpoint of excellent dimensional stability after long-term high temperature treatment.
• the heating shrinkage rate can be adjusted by adjusting the conditions of the bead annealing process (for example, the type of medium used for heating, heating temperature, heating time, pressure, etc.).
• the heat shrinkage rate can be measured by the method described in Examples below.
• the expansion ability of the foamed beads is preferably 2.3 or more, more preferably 2.5 to 10, from the viewpoint of excellent moldability. .0, more preferably 3.0 to 5.0.
• the expansion ability can be adjusted by adjusting the conditions of the bead annealing process (for example, the type of medium used for heating, heating temperature, heating time, pressure, etc.). The expansion ability can be measured by the method described in Examples below.
• the foamed molded article of this embodiment can be obtained by foam-molding the foamed beads of this embodiment described above.
• the above-mentioned foamed molded product is a foamed product made by molding amorphous resin foam beads that have a heat shrinkage rate of 25% or less when heated for 5 minutes at "glass transition temperature of bead raw material containing amorphous resin + 10" °C.
• the above-mentioned foamed molded product can be suitably used for, for example, peripheral parts of automobiles, peripheral parts of electronic devices, and the like.
• the melting peak temperature (° C.) of the bead raw material was measured using a differential scanning calorimeter (“DSC8500” manufactured by PerkinElmer) under the following conditions, and was defined as the softening point temperature.
• Sample amount 10mg
• Pan Aluminum crimp pan
• Atmosphere Nitrogen Measurement temperature: 50°C to 220°C
• Temperature increase/decrease rate 10° C./min Measurement cycle: 2 cycles
• a change in melting enthalpy of 1 J/g or more during the temperature increase process in the 2nd run was defined as the softening point temperature.
• the glass transition temperature measured by the following evaluation method was taken as the softening point temperature (Tm).
• the dynamic viscoelasticity of the bead raw material was measured using a rheometer (Physica MCR301 manufactured by Anton Paar) under the following conditions, and the peak temperature (°C) of the loss tangent (tan ⁇ ) was determined by the glass transition temperature (°C) of the bead raw material. Tg) and softening point temperature (Tm).
• Heating shrinkage rate of amorphous resin foam beads 20 cm 3 of foamed beads were placed on a metal tray so as not to overlap, placed in an oven set to the glass transition temperature Tg of the bead raw material + 10°C, and taken out after 5 minutes. After cooling to room temperature, the bulk ratio after heating was determined, and the heating shrinkage rate (%) was calculated using the following formula. (1-Xb/Xa) ⁇ 100(%) Xa: Bulk magnification before heating (cm 3 /g) Xb: Bulk magnification after heating (cm 3 /g)
• the above-mentioned predetermined pressure was determined according to the following formula, taking into account the glass transition temperature when the resin contained in the bead raw material is an amorphous resin, and the softening point temperature when it is a crystalline resin.
• Pressure 8 x (glass transition temperature Tg or softening point temperature Tm of the bead raw material) - 756 (kPa) (wherein, Tg if the resin contained in the bead raw material is an amorphous resin, and Tg if the resin contained in the bead raw material is a crystalline resin) Tm)
• Expansion ability Xc/Xa Xa: bulk ratio of foamed beads before heating (before expansion) (cm 3 /g)
• Xc Bulk ratio of expanded foam beads (cm 3 /g)
• a test piece of a foamed molded product measuring 150 mm x 150 mm x 3 mm in thickness was prepared by the method described in Examples and Comparative Examples described below. This test piece was dried for 24 hours using a 60°C drying oven (Satake Safe Bend Dryer N50-S5) to remove moisture contained in the test piece. Regarding this test piece, referring to the dimensional stability test at high temperature (Method B) described in JIS K6767, three pieces of length 100 mm were placed in the center of the test piece parallel to each other in the vertical and horizontal directions in a grid pattern.
• the foam was tested for flame retardancy in accordance with the UL-94 vertical method (10 mm vertical combustion test) of the U.S. UL standard. Details of the measurement method are shown below. With reference to the methods of Examples and Comparative Examples described below, five test pieces each having a length of 125 mm, a width of 13 mm, and a thickness of 10 mm were prepared and used. The test piece was attached vertically to a clamp, and indirect flame was applied twice for 10 seconds using a 10 mm flame, and V-0, V-1, and V-2 were determined based on the combustion behavior.
• V-0 Both the first and second flaming combustion durations are within 10 seconds, the total of the second flaming combustion duration and non-flame combustion time is within 30 seconds, and 5 test pieces are flammable. Total combustion time is less than 50 seconds, no sample burns to the position of the fixing clamp, and no cotton ignites due to falling objects.
• V-1 Both the first and second flaming combustion durations are within 30 seconds, and the total of the second flaming combustion duration and non-flame combustion time is within 60 seconds, and 5 test pieces are flammable. Total combustion time is within 250 seconds, no sample burns to the position of the fixing clamp, and no cotton ignites due to falling objects.
• V-2 Both the first and second flaming combustion durations are within 30 seconds, and the total of the second flaming combustion duration and non-flame combustion time is within 60 seconds, and five test pieces are flammable. The total combustion time was less than 250 seconds, there was no sample that burned to the position of the fixing clamp, and the cotton was ignited by falling objects. Cases that corresponded to any of the above V-0, V-1, and V-2 were judged as good (A), and cases that did not fall under any of them were judged as bad (B).
• Bead raw material pellet E PA 100 parts by mass of a copolymer of nylon 6 and nylon 66 (trade name: Novamid 2430A, manufactured by DSM) as a polyamide resin and 0.8 parts by mass of talc as a nucleating agent were heated, melted and kneaded in an extruder, and then extruded. Bead raw material pellets E were produced.
• Bead raw material pellet F PLA To 100 parts by weight of polylactic acid (manufactured by Cargill Japan) with an L-form/D-form ratio of 88.5/11.5, 2.0 parts by weight of an isocyanate compound (Millionate MR-200, manufactured by Nippon Polyurethane Industries), and talc (LMP- 100 (manufactured by Fuji Talc Industries) was heated, melted, kneaded, and extruded using an extruder to produce bead raw material pellets F.
• polylactic acid manufactured by Cargill Japan
• an isocyanate compound manufactured by Nippon Polyurethane Industries
• talc LMP- 100 (manufactured by Fuji Talc Industries) was heated, melted, kneaded, and extruded using an extruder to produce bead raw material pellets F.
• Example 1 According to the method described in Example 1 of JP-A-4-372630, the bead raw material pellets shown in Table 1 were placed in a pressure-resistant container, and after replacing the gas in the pressure-resistant container with dry air, carbon dioxide was added as a blowing agent. After injecting carbon (gas) and impregnating the bead raw material pellet with carbon dioxide for 3 hours under the conditions of a pressure of 3.0 MPa and a temperature of 10°C, the bead raw material pellet was taken out from the pressure vessel and immediately transferred.
• carbon dioxide carbon dioxide
• the bead raw material pellets were foamed with pressurized steam using the pressure program shown in Table 2 while rotating a stirring blade at 77 rpm in a foaming furnace to perform a bead foaming process and an annealing bead process to obtain foamed beads.
• the hydrocarbon gas content of the foamed beads was measured by gas chromatography immediately after foaming, and was found to be below the detection limit (0.01% by mass).
• the increase in bulk ratio per second was 0.1 cm 3 /g or more and 100 cm 3 /g or less, but the bulk ratio decreased in the bead annealing process.
• the expanded beads were placed in a container, and pressurized air was introduced (the pressure was increased to 0.4 MPa over 4 hours, and then maintained at 0.4 MPa for 16 hours) to perform a pressure treatment.
• This is filled into an in-mold mold with steam holes (cracking rate 0%), heated with steam to expand and fuse the foamed beads to each other, cooled, and taken out from the mold.
• a foamed molded article made of foamed beads was obtained. Table 1 shows the measurement and evaluation results of each physical property.
• Example 2-5, 16-17, Comparative Example 2 A foamed molded body was obtained in the same manner as in Example 1, except that the pressure program of pressurized steam for producing foamed beads from bead raw materials was set as shown in Table 2. Table 1 shows the measurement and evaluation results of each physical property. In addition, in Examples 2 to 5, 16 to 17 and Comparative Example 2, in the bead foaming process shown in Table 2, the increase in bulk ratio per second was 0.1 cm 3 /g or more and 100 cm 3 /g or less. , the bulk factor decreased in the bead annealing process.
• Examples 6 to 10 According to the method described in Example 1 of JP-A-4-372630, the bead raw material pellets shown in Table 1 were placed in a pressure-resistant container, and after replacing the gas in the container with dry air, carbon dioxide ( After injecting carbon dioxide into the bead raw material pellets for 3 hours under the conditions of a pressure of 3.0 MPa and a temperature of 10 ° C., the bead raw material pellets were taken out from the pressure vessel and immediately transferred. The bead raw material pellets were foamed with pressurized steam using the pressure program shown in Table 2 while rotating the stirring blade at 77 rpm in a foaming furnace to perform a foaming process to obtain pre-foamed beads.
• the hydrocarbon gas content of the foamed beads was measured by gas chromatography immediately after foaming, and was found to be below the detection limit (0.01% by mass).
• the obtained pre-foamed beads were put into a hot air dryer and heated at the temperature and time shown in Table 3 to obtain foamed beads.
• the increase in bulk ratio per second was 0.1 cm 3 /g or more and 100 cm 3 /g or less, but in the bead annealing process, the bulk ratio increased decreased.
• the expanded beads were placed in a container, and pressurized air was introduced (the pressure was increased to 0.4 MPa over 4 hours, and then maintained at 0.4 MPa for 16 hours) to perform a pressure treatment.
• Examples 11-12, 14 According to the method described in Example 1 of JP-A-4-372630, the bead material resin pellets shown in Table 1 were placed in a pressure-resistant container, and after replacing the gas in the container with dry air, carbon dioxide was added as a blowing agent. (gas) was injected, and the bead material resin pellets were impregnated with carbon dioxide over a period of 3 hours under conditions of a pressure of 3.0 MPa and a temperature of 10°C. Subsequently, the bead raw material resin pellets were put into a mesh basket, heated with hot air under the conditions shown in Table 4 while stirring, and foamed and annealed to obtain foamed beads.
• gas gas
• the expanded beads were placed in a container, and pressurized air was introduced (the pressure was increased to 0.4 MPa over 4 hours, and then maintained at 0.4 MPa for 16 hours) to perform a pressure treatment.
• This is filled into an in-mold mold with steam holes (cracking rate 0%), heated with steam to expand and fuse the foamed beads to each other, cooled, and taken out from the mold.
• a foamed molded article made of foamed beads was obtained. Table 1 shows the measurement and evaluation results of each physical property.
• Example 13 A foamed molded body was obtained in the same manner as in Example 1, except that the bead raw material was changed as shown in Table 1, and the pressure program of pressurized steam for producing foamed beads from the bead raw material was set as shown in Table 2.
• Table 1 shows the measurement and evaluation results of each physical property.
• the increase in bulk ratio per second was 0.1 cm 3 /g or more and 100 cm 3 /g or less, but the bulk ratio decreased in the bead annealing process.
• Resin pellet E was made to contain carbon dioxide gas as a blowing agent in the bead raw material resin pellet according to the method described in Examples of JP-A-2011-105879. Then, foamed beads were obtained by heating and foaming the bead raw material resin pellets containing carbon dioxide gas. This is filled into an in-mold mold with steam holes (cracking rate 0%), heated with steam to expand and fuse the foamed beads to each other, cooled, and taken out from the mold. A foamed molded article made of foamed beads was obtained. Table 1 shows the measurement and evaluation results of each physical property. In addition, in the bead foaming process shown in Table 4, the increase in bulk ratio per second was 0.1 cm 3 /g or more and 100 cm 3 /g or less, but the bulk ratio decreased in the bead annealing process.
• Example 4 To 100 parts by weight of the same bead material resin pellets as in Example 1, 10 parts by weight of n-pentane (boiling point 36.1°C) was added as a blowing agent, and the mixture was heated and kneaded in an extruder to obtain unfoamed particles. The resin particles were heated with pressurized steam in a foaming furnace while rotating a stirring blade at 77 rpm, and foamed to obtain foamed beads. The foaming temperature at this time was 155°C. Thereafter, pressure treatment and molding were attempted in the same manner as in Example 1 without bead annealing, but a foamed molded product could not be obtained due to insufficient fusion of the beads. Table 1 shows the measurement and evaluation results of each physical property.
• the foamed molded article obtained from the foamed beads produced by the production method of the present embodiment can be suitably used for automobile peripheral parts, electronic device peripheral parts, etc.

Landscapes

• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Materials Engineering (AREA)
• Thermal Sciences (AREA)
• Oral & Maxillofacial Surgery (AREA)
• Engineering & Computer Science (AREA)
• Physics & Mathematics (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
• Compositions Of Macromolecular Compounds (AREA)

Priority Applications (1)

Applications Claiming Priority (2)

Publications (1)

Family

ID=90013171

Family Applications (1)

Country Status (3)

Citations (7)

Family Cites Families (2)

• 2023
  • 2023-02-17 CN CN202380019705.5A patent/CN118647657A/zh active Pending
  • 2023-08-09 JP JP2024542745A patent/JPWO2024043103A1/ja active Pending
  • 2023-08-09 WO PCT/JP2023/029135 patent/WO2024043103A1/ja not_active Ceased

Patent Citations (7)

Also Published As

Similar Documents

Legal Events