WO1998025996A1 - Particules expansees de resine de polyolefine et leur procede de preparation - Google Patents
Particules expansees de resine de polyolefine et leur procede de preparation Download PDFInfo
- Publication number
- WO1998025996A1 WO1998025996A1 PCT/JP1997/002022 JP9702022W WO9825996A1 WO 1998025996 A1 WO1998025996 A1 WO 1998025996A1 JP 9702022 W JP9702022 W JP 9702022W WO 9825996 A1 WO9825996 A1 WO 9825996A1
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- WIPO (PCT)
- Prior art keywords
- resin
- particles
- borate
- resin particles
- expanded
- Prior art date
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Classifications
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- 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
-
- 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
-
- 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
- C08J9/0066—Use of inorganic compounding ingredients
-
- 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
- C08J2201/00—Foams characterised by the foaming process
- C08J2201/02—Foams characterised by the foaming process characterised by mechanical pre- or post-treatments
- C08J2201/03—Extrusion of the foamable blend
-
- 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
Definitions
- the present invention relates to expanded polyolefin-based resin particles used as a raw material for molding and the like and a method for producing the same.
- JP-A-57-195131 and JP-A-58-511123 disclose foaming particles filled in a mold and heated. It discloses a method for producing a molded article having an arbitrary shape by fusing foamed particles together.
- JP-A-61-47338 Japanese Patent Application Laid-Open No. Hei 3-2-23347 discloses that polyolefin resin particles are dispersed in an aqueous medium in a container.
- An object of the present invention is to provide expanded polyolefin resin particles having a high expansion ratio and a uniform cell diameter.
- Another object of the present invention is to provide expanded polyolefin-based resin particles as a raw material for molding capable of producing a molded body having a small shrinkage during molding and excellent dimensional stability.
- the present invention relates to expanded polyolefin resin particles obtained by adding a metal borate (excluding an alkali metal salt) to a base resin.
- a metal borate excluding an alkali metal salt
- Polyolefin as base resin An in-based resin is used, and zinc borate, magnesium borate, or the like is used as the metal borate.
- the alkali metal borate must be excluded. For example, sodium borate and potassium borate cannot be used in the present invention.
- the content of the metal borate in the base resin is preferably from 50 to 500 ppm.
- the resin particles obtained by adding the metal borate to the base resin are dispersed together with a blowing agent in a dispersion medium such as water, and the resin particles are impregnated with the blowing agent. Then, the inside of the container is heated to a predetermined temperature, and the expandable resin particles and the dispersing medium are discharged into an atmosphere at a lower pressure than the inside of the container. As a result, foamed particles foamed at a high magnification can be obtained.
- the expanded particles of the present invention can also be manufactured by another manufacturing method, for example, by an extrusion expansion method.
- This extrusion foaming method is a method in which a base resin containing a metal borate is melt-kneaded in an extruder together with a foaming agent, then extruded and foamed into a strand, and then cut to obtain foamed particles. is there.
- the expanded particles of the present invention are made by using a base resin containing a metal borate (excluding an alkali metal salt), the expanded particles can have a high expansion ratio.
- the expanded particles of the present invention it is possible to obtain expanded particles having a high expansion ratio even when an inorganic gas-based blowing agent is used as a blowing agent.
- the foamed particles of the present invention have a high expansion ratio and a uniform cell diameter.
- a foamed molded article is produced using the foamed particles of the present invention as a raw material for molding, a good molded article can be obtained. it can. That is, the obtained molded article has a small shrinkage ratio and excellent dimensional stability.
- the particle fusion state that appears on the outer surface of the molded article is regular, and a uniform surface state is obtained. can get. Molded products with good appearance increase commercial value I can do it.
- the foamed particles of the present invention have a uniform cell diameter, when the foamed particles of the present invention are colored by adding a carbon black or a pigment, the coloring is performed uniformly. Therefore, when molding is performed using the colored foamed particles of the present invention, a molded article having a uniform appearance without color unevenness and having a uniform colored surface can be obtained.
- an inorganic gas-based foaming agent in order to obtain foamed particles having a high foaming ratio and a uniform cell diameter, an inorganic gas-based foaming agent can be used as a foaming agent, and an inorganic gas-based foaming agent is used.
- the manufacturing cost can be reduced, there is no problem of environmental pollution, and the handling is safe.
- FIG. 1 is an explanatory diagram for explaining a method of measuring an average cell diameter on a cut surface of a foamed particle.
- BEST MODE FOR CARRYING OUT THE INVENTION the present invention will be described in detail.
- the base resin of the resin particles used in the present invention includes propylene homopolymer, propylene-ethylene random copolymer, propylene-ethylene block copolymer, propylene-butene random copolymer, propylene-ethylene-butene random copolymer.
- Propylene copolymers such as copolymers, or ethylene copolymers such as high-density polyethylene and linear low-density polyethylene-ethylene-vinyl acetate copolymer, which is a copolymer of ethylene and polystyrene Resin such as coalescence. These polymers may be crosslinked or non-crosslinked.
- the metal borate is a compound represented by the following general formula (1) or (2).
- x and y are integers of 1 or more, z is a number of 0 or more, and M represents a monovalent metal element.
- alkali metal salts such as sodium borate, potassium borate, and lithium borate. That is, the alkali metals mentioned here are Li, Na, K, Rb, Cs, and Fr.
- borax as boric acid alkali metal salt (N a 2 B 4 0 7 ⁇ 1 0 H 2 0) in the case of using the high hygroscopicity such as boric acid metal added during the base resin Salt absorbs moisture in the atmosphere, and bubbles are generated during the granulation of resin particles, making granulation unstable. There is a possibility that large bubbles will be generated when the particles are made into foamed particles, and the cell diameter will vary.
- examples of the metal borate include zinc borate and magnesium borate, and zinc borate is particularly preferably used. In the present invention, one or a combination of two or more of these metal borate salts can be used.
- the zinc borate used in the present invention zinc metaborate [Zn (B0 2) 2], basic zinc borate [Zetaitabeta 4 ⁇ 7 ⁇ 2ZnO] and the like, or 2 ⁇ ⁇ 3B 2 ⁇ 3 - 3. 5 H 2 ⁇ and, 3 ZnO ⁇ 2 B 2 ⁇ 3 - include those represented by the chemical formula 5H 2 ⁇ like.
- magnesium orthoboric acid [Mg 3 (B_ ⁇ 3) 2]
- magnesium diboride magnesium pyroborate
- magnesium pyroborate [Mg 2 B 2 0 5 or 2MgO ⁇ B 2 0 3]
- metaborate magnetic Shiumu [MgO ⁇ B 2 ⁇ 3]
- tetraborate tribasic magnesium [Mg 3 B 4 0 9 or 3MgO ⁇ 2 B 2 ⁇ 3]
- 2Mg_ ⁇ -3 beta 2 ⁇ 3 ⁇ nH 2 ⁇ here, n represents a positive integer
- MgO-4 B 2 ⁇ 3 ⁇ 3H 2 ⁇ , Mg_ ⁇ & 6 B 2 ⁇ 3.1 those represented by the chemical formula 8H 2 ⁇ like.
- the particle size of the metal borate is generally 0.1 to 100 m, preferably 0.5 to 50 m. If the particle size of the metal borate is less than 0.1 / m, the foamed particles tend to be fine and the secondary foaming property when producing a molded article using the foamed particles is inferior. If the particle size is larger than 100 / m, it is difficult to obtain a sufficient magnification improving effect, and the bubbles are likely to become coarse.
- the preferred range of the cell diameter of the expanded beads of the present invention is an average cell diameter of 50 to 500 m, more preferably 150 to 300 m.
- the expansion ratio can be improved while maintaining a uniform cell diameter.
- the content of the metal borate in the base resin of the expanded particles is preferably from 50 to 500 ppm by weight, particularly preferably from 100 to 500 ppm by weight. is there. If the content of the metal borate is less than 5 Oppm, it is not possible to prevent variation in the cell diameter of the foamed particles. On the other hand, if the content exceeds 500 ppm, the obtained expanded particles are likely to shrink, and the air bubbles have a strong tendency to become open cells, which may result in poor moldability. .
- the metal borate is usually added to the raw material base resin before granulation when the resin particles are granulated using the base resin.
- a conventionally known method such as a method in which a resin melt-kneaded by an extruder is extruded into strands, rapidly cooled in water, and then cut.
- a masterbatch is usually prepared by mixing the metal borate with a polyolefin resin so that the concentration is 5 to 200 times the final addition amount.
- a method is used in which this master batch is added to the base resin, but the metal borate may be added directly to the base resin in the form of a powder.
- resin particles obtained by adding a metal borate to a base resin are dispersed in a dispersion medium in a closed container, and then pressurized and heated.
- the resin particles are impregnated with a blowing agent while stirring.
- the foaming resin particles impregnated with the foaming agent and the dispersion medium are discharged into the atmosphere at a lower pressure than the inside of the container to perform foaming.
- a dispersion medium for dispersing the resin particles water, alcohols, Power that does not dissolve resin particles, such as glycerin and glycerin.
- Usable water is usually used.
- an anti-fusing agent is added to the dispersion medium in order to prevent the resin particles from fusing with each other by heating during the dispersion or heating in the subsequent foaming step. be able to.
- the anti-fusing agent any organic or inorganic substance can be used as long as it does not dissolve in the dispersion medium and does not melt by heating.In general, an inorganic anti-fusing agent is used. You.
- the inorganic anti-fusing agent powders such as Myriki, kaolin, aluminum oxide, titanium oxide, and aluminum hydroxide are suitable.
- the anti-fusing agent those having an average particle size of 0.1 to 100 ⁇ m are used, and those having an average particle size of 0.1 to 30 m are particularly preferable.
- an anti-fusion agent it is preferable to use an anionic surfactant such as sodium dodecylbenzenesulfonate, sodium alkylsulfonate or sodium oleate as a dispersing aid.
- the anti-fusing agent is added at about 0.01 to 2 parts by weight per 100 parts by weight of the resin particles, and the dispersing aid is added at about 0.001 to 1 part by weight per 100 parts by weight of the resin particles. Is preferred.
- an inorganic gas or a volatile organic foaming agent can be used as a foaming agent for foaming the resin particles.
- the inorganic gas include carbon dioxide, air, nitrogen, helium, and argon.
- the volatile organic blowing agent include aliphatic hydrocarbons such as propane, butane, and hexane; cycloaliphatic hydrocarbons such as cyclobutane and cyclohexane; chlorofluoromethane; trifluoromethane; —Difluoroethane, 1-chloro-1,1-difluoroethane, 1,2,2,2-tetrahydrofluoroethane, 1-chloro-1,2,2,2,2-tetrafluoroethane, methyl chloride, ethyl chloride, methylene chloride And halogenated hydrocarbons such as
- the above foaming agents may be used alone or as a mixture of two or more. Further, a volatile organic foaming agent and an inorganic gas can be mixed and used. However, many of the compounds used as volatile organic blowing agents have dangers such as toxicity and flammability, and those that cause ozone depletion and environmental pollution, and are less likely to cause these problems. Since these are expensive and impractical, it is preferable to use an inorganic gas in consideration of these.
- the foaming agent When an inorganic gas is used as the foaming agent, it is preferable to add the foaming agent so that the equilibrium vapor pressure in the closed container immediately before the start of foaming is 5 to 60 kgf / cm 2 G. When a volatile foaming agent is used as the agent, it is preferable to add the volatile foaming agent in an amount of 5 to 30 parts by weight based on 100 parts by weight of the resin particles.
- the resin particles are impregnated with the foaming agent in the closed container as described above, one end of the closed container is opened, and the resin particles and the dispersion medium are exposed to a lower pressure atmosphere than the container, usually at atmospheric pressure. By releasing the resin particles, the resin particles can be expanded to obtain expanded particles.
- the pressure in the container is at least 5 atm, and the temperature in the container is preferably in the range of [the melting point of the resin is 110 ° C;] to [the melting point of the resin is 10 ° C].
- the melting point of the resin refers to the melting point of the base resin of the resin particles, and is determined as follows.
- Another method for obtaining the polyolefin-based resin foamed particles of the present invention is to melt-knead a base resin containing a metal borate together with a foaming agent in an extruder, and then extrude and foam into strands. And then cutting it into foamed particles Alternatively, a foaming agent is impregnated in a closed container with a base resin containing a metal borate to form foamable resin particles, and the foamable resin particles are heated by spraying high-temperature steam or hot air. And a known method such as a method of foaming. According to the present invention, expanded particles having a high expansion ratio can be obtained. For example, particles having an expansion ratio of 5 to 50 times can be easily obtained.
- the polyolefin resin foam particles obtained by the method of the present invention as described above are aged at atmospheric pressure, and then subjected to a pressure treatment under pressurized air to apply an internal pressure.
- this step is referred to as two-stage foaming), it is possible to obtain foamed particles having a higher magnification.
- the foamed particles obtained by the method of the present invention By filling the foamed particles obtained by the method of the present invention in a mold and heating with steam or the like, the foamed particles are fused to each other to obtain a molded article formed into a desired shape according to the mold. be able to.
- the following ethylene-propylene random copolymer was used as the base resin.
- the above-mentioned ethylene-propylene random copolymer of the base resin and the additives shown in Table 1 were melt-kneaded by a pressure kneader to prepare one master batch.
- As zinc borate zinc borate from Tomita Pharmaceutical Co., Ltd. was used.
- the master batch and the base resin are mixed in the extruder so that the content of the additives in the base resin is as shown in Table 1.
- the mixture was melt-kneaded, extruded into strands, quenched in water, and then cut with a pelletizer to obtain pellets (resin particles) having an average weight per pellet of 2 mg.
- the above-mentioned predetermined aging step is as follows.
- Example 2 the obtained foamed particles were allowed to stand at room temperature and atmospheric pressure for 24 hours, and then at room temperature under 2 kg iZcm 2 G compressed air. For 24 hours, and then left at room temperature and atmospheric pressure for 24 hours to adjust the internal pressure of the foamed particles to the atmospheric pressure, thereby completing the aging step.
- the foamed particles after the completion of the aging step are filled in a mold having an inner dimension of 30 Ommx30 Ommx60 mm using a known filling apparatus, and after preheating with steam, A foam was formed by heating with steam having a steam pressure shown in 1 (in Table 1, indicated as “formed steam pressure”).
- steam in the range of [forming steam pressure—0.8 kgf / cm 2 G]-[forming steam pressure—0.4 kgf / cm 2 G] was used.
- the obtained molded body is heated at 60 ° C under atmospheric pressure. Cured for 4 hours.
- the obtained secondary expanded particles are allowed to stand at room temperature and atmospheric pressure for 24 hours, and then the expansion ratio and average cell diameter of the secondary expanded particles are measured, and the uniformity of the cells is further observed. did. Table 3 shows the results.
- the secondary foamed particles after standing for 24 hours at normal temperature and atmospheric pressure are applied to the secondary foamed particles using pressurized air at room temperature to generate an internal pressure of 1.4 kgf / cm 2 G.
- the same mold as in the above Examples and Comparative Examples was filled, and preheated in the same manner, and then steam having a molding steam pressure shown in Table 3 To form a molded article.
- the expansion ratio was calculated by the following equation.
- Expansion ratio true density of base resin (gZcm 3 ) Bulk density of Z expanded particles (g / cm 3 )
- the bulk density of the expanded particles was determined by preparing a container having a volume of 1 000 cm 3 and having an opening at the top, filling the container with the expanded particles at normal temperature and pressure, and passing through the opening of the container. The foamed particles are removed, the height of the foamed particles is made substantially coincident with the opening of the container, and the weight (g) of the foamed particles in the container at that time is divided by 1,000 cm 3 .
- the uniformity of cells of the expanded particles was evaluated according to the following criteria. ⁇ ⁇ ⁇ , For each of the expanded particles, almost no variation in the size of the bubbles observed on the cut surface was observed, and among these expanded particles, the value of the average cell diameter was observed. The number of foamed particles less than 3 is smaller than the average value of 2Z3 of the average cell diameter.
- each of the expanded particles there is a variation in the size of the bubbles observed on the cut surface, or the average value of the bubble diameter among these expanded particles is 20. There are three or more particles having a value smaller than 2/3 of the average value of the average cell diameter of the expanded particles.
- Shrinkage (%) ((300-A) / 300) X100 (4)
- the dimensional stability of the molded article was evaluated based on the following criteria.
- ⁇ ⁇ 'Shrinkage rate is less than 2.7%
- the surface of the molded product was visually observed and evaluated according to the following criteria.
- the expanded polyolefin-based resin particles of the present invention have the characteristics of high expansion ratio and uniform cell diameter, and are excellent in dimensional stability and excellent in appearance. It is useful.
- polyolefin resin expanded particles having a high expansion ratio can be easily produced using existing production equipment such as a photoclave or an extruder.
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- Chemical Kinetics & Catalysis (AREA)
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- Inorganic Chemistry (AREA)
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Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/125,272 US6133331A (en) | 1996-12-13 | 1997-06-11 | Expanded particles of polyolefin resin and process for preparing the same |
JP52646498A JP3638960B2 (ja) | 1996-12-13 | 1997-06-11 | ポリオレフィン系樹脂発泡粒子及びその製造方法 |
KR1019980706267A KR100341651B1 (ko) | 1996-12-13 | 1997-06-11 | 폴리올레핀계수지발포입자및그제조방법 |
DE69727377T DE69727377T2 (de) | 1996-12-13 | 1997-06-11 | Expandierte polyolefinpartikel und verfahren zu ihrer herstellung |
BR9706836-5A BR9706836A (pt) | 1996-12-13 | 1997-06-11 | Partìculas espumadas de resina de poliolefina e processo de produção das mesmas |
EP97926228A EP0905176B1 (en) | 1996-12-13 | 1997-06-11 | Expanded particles of polyolefin resin and process for preparing the same |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8/352771 | 1996-12-13 | ||
JP35277196 | 1996-12-13 |
Publications (1)
Publication Number | Publication Date |
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WO1998025996A1 true WO1998025996A1 (fr) | 1998-06-18 |
Family
ID=18426333
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP1997/002022 WO1998025996A1 (fr) | 1996-12-13 | 1997-06-11 | Particules expansees de resine de polyolefine et leur procede de preparation |
Country Status (7)
Country | Link |
---|---|
US (1) | US6133331A (ja) |
EP (1) | EP0905176B1 (ja) |
JP (1) | JP3638960B2 (ja) |
KR (1) | KR100341651B1 (ja) |
BR (1) | BR9706836A (ja) |
DE (1) | DE69727377T2 (ja) |
WO (1) | WO1998025996A1 (ja) |
Cited By (4)
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WO2009075208A1 (ja) | 2007-12-11 | 2009-06-18 | Kaneka Corporation | ポリオレフィン系樹脂発泡粒子の製造方法およびポリオレフィン系樹脂発泡粒子 |
JP2012224786A (ja) * | 2011-04-21 | 2012-11-15 | Jsp Corp | ポリオレフィン系樹脂発泡粒子の製造方法 |
JP6757871B1 (ja) * | 2019-03-19 | 2020-09-23 | 株式会社ジェイエスピー | ポリオレフィン系樹脂発泡粒子、ポリオレフィン系樹脂発泡粒子成形体、及び、ポリオレフィン系樹脂発泡粒子の製造方法 |
WO2020189389A1 (ja) * | 2019-03-19 | 2020-09-24 | 株式会社ジェイエスピー | ポリオレフィン系樹脂発泡粒子、ポリオレフィン系樹脂発泡粒子成形体、及び、ポリオレフィン系樹脂発泡粒子の製造方法 |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW200530297A (en) * | 2004-01-13 | 2005-09-16 | Jsp Corp | Thermoplastic resin pellet, process for preparing thermoplastic resin pellets and expanded thermoplastic resin bead |
TWI400286B (zh) | 2005-03-29 | 2013-07-01 | Jsp Corp | 聚丙烯系樹脂發泡粒子、聚丙烯系樹脂發泡粒子成形體的製造方法及聚丙烯系樹脂發泡粒子成形體 |
US7957947B2 (en) * | 2006-08-25 | 2011-06-07 | Chevron Phillips Chemical Company Lp | Method and apparatus for managing volatile organic content in polyolefin |
WO2008069865A1 (en) * | 2006-12-06 | 2008-06-12 | Dow Global Technologies Inc. | Styrene acrylonitrile copolymer foam with infrared attenuating agents |
CN102471516B (zh) * | 2009-06-26 | 2014-03-05 | 株式会社Jsp | 聚丙烯系树脂发泡颗粒和发泡颗粒成型体 |
WO2011086938A1 (ja) | 2010-01-15 | 2011-07-21 | 株式会社カネカ | 無架橋ポリエチレン系樹脂発泡粒子及び無架橋ポリエチレン系樹脂発泡成形体 |
JP5727210B2 (ja) * | 2010-12-15 | 2015-06-03 | 株式会社ジェイエスピー | ポリオレフィン系樹脂発泡粒子成形体の製造方法、及びポリオレフィン系樹脂発泡粒子成形体 |
KR101674610B1 (ko) * | 2015-06-15 | 2016-11-09 | 롯데케미칼 주식회사 | 고분자 발포 입자 및 이의 제조 방법 |
WO2018088551A1 (ja) * | 2016-11-14 | 2018-05-17 | 株式会社ジェイエスピー | 発泡粒子成形体、靴底用クッション、及び発泡粒子の製造方法 |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03166238A (ja) * | 1989-11-24 | 1991-07-18 | Jsp Corp | 重合体発泡粒子の製造法 |
JPH03244643A (ja) * | 1990-02-23 | 1991-10-31 | Furukawa Electric Co Ltd:The | 発泡体用難燃性樹脂組成物 |
Family Cites Families (48)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US32780A (en) * | 1861-07-09 | Steering- apparatus | ||
US4021380A (en) * | 1976-02-27 | 1977-05-03 | Mattel, Inc. | Expandable resin composition |
JPS5923731B2 (ja) * | 1980-11-22 | 1984-06-04 | 日本スチレンペ−パ−株式会社 | ポリプロピレン系樹脂予備発泡粒子 |
JPS5851019B2 (ja) * | 1981-05-25 | 1983-11-14 | 日本スチレンペ−パ−株式会社 | ポリオレフィン系樹脂発泡成型体の製造方法 |
JPS5943490B2 (ja) * | 1981-06-27 | 1984-10-22 | 日本スチレンペ−パ−株式会社 | ポリプロピレン系合成樹脂発泡成型体 |
JPS5943492B2 (ja) * | 1981-08-05 | 1984-10-22 | 日本スチレンペ−パ−株式会社 | ポリプロピレン系樹脂発泡成型体の製造方法 |
JPS5943491B2 (ja) * | 1981-08-05 | 1984-10-22 | 日本スチレンペ−パ−株式会社 | ポリプロピレン系樹脂発泡成型体 |
JPS5851123A (ja) * | 1981-09-22 | 1983-03-25 | Japan Styrene Paper Co Ltd | ポリプロピレン系樹脂予備発泡粒子の型内成形法 |
JPS5855231A (ja) * | 1981-09-28 | 1983-04-01 | Japan Styrene Paper Co Ltd | ポリオレフイン系樹脂予備発泡粒子の製造方法 |
JPS58101025A (ja) * | 1981-12-09 | 1983-06-16 | Japan Styrene Paper Co Ltd | ポリオレフイン系樹脂予備発泡粒子の加圧処理方法 |
JPS58221745A (ja) * | 1982-06-19 | 1983-12-23 | Japan Styrene Paper Co Ltd | 自動車のバンパ−用芯材 |
US4504601A (en) * | 1982-10-01 | 1985-03-12 | Japan Styrene Paper Corporation | Process for producing pre-foamed particles of polypropylene resin |
US4464484A (en) * | 1982-12-20 | 1984-08-07 | Japan Styrene Paper Corporation | Process for producing prefoamed polymer particles |
JPS59176147A (ja) * | 1983-03-24 | 1984-10-05 | Japan Styrene Paper Co Ltd | バンパ−用芯材およびその製造方法 |
EP0123144B1 (en) * | 1983-03-25 | 1987-10-07 | Japan Styrene Paper Corporation | Polypropylene resin prefoamed particles |
JPS60110734A (ja) * | 1983-11-21 | 1985-06-17 | Japan Styrene Paper Co Ltd | 無架橋ポリプロピレン系樹脂予備発泡粒子 |
JPS60123540A (ja) * | 1983-12-07 | 1985-07-02 | Japan Styrene Paper Co Ltd | 無架橋ポリプロピレン系樹脂予備発泡粒子 |
JPS60189660A (ja) | 1984-03-08 | 1985-09-27 | Japan Styrene Paper Co Ltd | 自動車バンパ−用芯材 |
US4704239A (en) * | 1984-04-28 | 1987-11-03 | Japan Styrene Paper Corp. | Process for the production of expanded particles of a polymeric material |
JPS60235849A (ja) * | 1984-05-08 | 1985-11-22 | Japan Styrene Paper Co Ltd | ポリプロピレン系樹脂予備発泡粒子 |
JPS60252636A (ja) * | 1984-05-30 | 1985-12-13 | Japan Styrene Paper Co Ltd | 予備発泡粒子の製造法 |
EP0337584B1 (en) * | 1984-06-14 | 1994-08-17 | Japan Styrene Paper Corporation | Process for the production of expanded particles of a polypropylene resin |
US4676939A (en) * | 1984-06-14 | 1987-06-30 | Japan Styrene Paper Corporation | Process for the production of expanded particles of a polypropylene resin |
US4867923A (en) * | 1984-12-21 | 1989-09-19 | Union Carbide Corporation | Process of producing foamed products |
US4822542A (en) * | 1985-02-21 | 1989-04-18 | Japan Styrene Paper Corporation | Method of production of expansion-molded article, from foamable thermoplastic resin particles and apparatus therefor |
EP0195512B1 (en) * | 1985-02-27 | 1990-10-24 | Japan Styrene Paper Corporation | Casting method |
JPS61215631A (ja) * | 1985-03-20 | 1986-09-25 | Japan Styrene Paper Co Ltd | 型内成型に使用する無架橋予備発泡粒子製造用プロピレン系ランダム共重合体樹脂粒子の製造方法 |
JPS6218214A (ja) * | 1985-07-17 | 1987-01-27 | Japan Styrene Paper Co Ltd | ポリオレフイン系樹脂粒子の加熱処理装置 |
JPH0649795B2 (ja) * | 1985-11-29 | 1994-06-29 | 日本スチレンペ−パ−株式会社 | ポリプロピレン系樹脂予備発泡粒子成型体の製造方法 |
US4695593A (en) * | 1986-02-21 | 1987-09-22 | Japane Styrene Paper Corporation | Prefoamed propylene polymer-base particles, expansion-molded article produced from said particles and production process of said article |
EP0254530B1 (en) * | 1986-07-22 | 1990-10-10 | Japan Styrene Paper Corporation | Core material for automobile bumpers |
JPH082989B2 (ja) * | 1987-05-11 | 1996-01-17 | 日本スチレンペ−パ−株式会社 | ポリオレフィン系樹脂粒子の予備発泡方法 |
JPH0739501B2 (ja) * | 1987-06-23 | 1995-05-01 | 日本スチレンペ−パ−株式会社 | 無架橋直鎖状低密度ポリエチレン予備発泡粒子 |
US5084814A (en) * | 1987-10-30 | 1992-01-28 | Motorola, Inc. | Data processor with development support features |
JPH02187434A (ja) * | 1989-01-17 | 1990-07-23 | Hitachi Cable Ltd | 難燃性発泡シート |
JP2887291B2 (ja) * | 1989-08-30 | 1999-04-26 | 株式会社ジェイエスピー | ポリオレフィン系樹脂発泡粒子の製造方法 |
CA2030754C (en) * | 1989-11-24 | 1997-06-03 | Kazuo Turugai | Production method of prefoamed synthetic resin particles |
CA2032719C (en) * | 1989-12-21 | 1994-11-08 | Makoto Kamiyama | Production process of expansion-molded article |
US5284431A (en) * | 1990-08-28 | 1994-02-08 | Jsp Corporation | Filling apparatus for filling foamed particles of a thermoplastic resin into a mold |
JPH04189840A (ja) * | 1990-11-22 | 1992-07-08 | Jsp Corp | 重合体発泡粒子の製造方法 |
JP3195674B2 (ja) * | 1992-12-24 | 2001-08-06 | 株式会社ジエイエスピー | 無架橋エチレン系重合体発泡粒子の製造方法 |
JP3195676B2 (ja) * | 1992-12-28 | 2001-08-06 | 株式会社ジエイエスピー | ポリオレフィン系樹脂発泡粒子の製造方法 |
JP3279382B2 (ja) * | 1993-03-17 | 2002-04-30 | 株式会社ジエイエスピー | 無架橋ポリエチレン系樹脂発泡粒子及びその製造方法 |
JP3441165B2 (ja) * | 1994-05-19 | 2003-08-25 | 株式会社ジェイエスピー | 難燃性ポリオレフィン系樹脂発泡粒子 |
US5679450A (en) * | 1994-07-15 | 1997-10-21 | Jsp Corporation | Expanded polyolefin body having thermosetting resin layer directly bonded thereto |
TW294691B (en) * | 1994-08-16 | 1997-01-01 | Jsp Corp | Expansion-molded article of polyolefin resin having open voids and production thereof |
JP2787281B2 (ja) * | 1994-09-20 | 1998-08-13 | 株式会社ジェイエスピー | 凹凸模様を有するコンクリート面形成用化粧型及び凹凸模様を有するコンクリート面の形成方法 |
JPH08277340A (ja) * | 1995-04-05 | 1996-10-22 | Jsp Corp | ポリプロピレン単独重合体発泡粒子、及び発泡粒子成型体 |
-
1997
- 1997-06-11 EP EP97926228A patent/EP0905176B1/en not_active Expired - Lifetime
- 1997-06-11 KR KR1019980706267A patent/KR100341651B1/ko not_active IP Right Cessation
- 1997-06-11 WO PCT/JP1997/002022 patent/WO1998025996A1/ja active IP Right Grant
- 1997-06-11 BR BR9706836-5A patent/BR9706836A/pt not_active IP Right Cessation
- 1997-06-11 DE DE69727377T patent/DE69727377T2/de not_active Expired - Lifetime
- 1997-06-11 US US09/125,272 patent/US6133331A/en not_active Expired - Lifetime
- 1997-06-11 JP JP52646498A patent/JP3638960B2/ja not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03166238A (ja) * | 1989-11-24 | 1991-07-18 | Jsp Corp | 重合体発泡粒子の製造法 |
JPH03244643A (ja) * | 1990-02-23 | 1991-10-31 | Furukawa Electric Co Ltd:The | 発泡体用難燃性樹脂組成物 |
Non-Patent Citations (1)
Title |
---|
See also references of EP0905176A4 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009075208A1 (ja) | 2007-12-11 | 2009-06-18 | Kaneka Corporation | ポリオレフィン系樹脂発泡粒子の製造方法およびポリオレフィン系樹脂発泡粒子 |
EP2754687A1 (en) | 2007-12-11 | 2014-07-16 | Kaneka Corporation | Process for producing expanded polyolefin resin particles and expanded polyolefin resin particles |
JP2012224786A (ja) * | 2011-04-21 | 2012-11-15 | Jsp Corp | ポリオレフィン系樹脂発泡粒子の製造方法 |
JP6757871B1 (ja) * | 2019-03-19 | 2020-09-23 | 株式会社ジェイエスピー | ポリオレフィン系樹脂発泡粒子、ポリオレフィン系樹脂発泡粒子成形体、及び、ポリオレフィン系樹脂発泡粒子の製造方法 |
WO2020189389A1 (ja) * | 2019-03-19 | 2020-09-24 | 株式会社ジェイエスピー | ポリオレフィン系樹脂発泡粒子、ポリオレフィン系樹脂発泡粒子成形体、及び、ポリオレフィン系樹脂発泡粒子の製造方法 |
Also Published As
Publication number | Publication date |
---|---|
US6133331A (en) | 2000-10-17 |
DE69727377T2 (de) | 2004-09-16 |
EP0905176B1 (en) | 2004-01-28 |
DE69727377D1 (de) | 2004-03-04 |
EP0905176A1 (en) | 1999-03-31 |
KR19990082531A (ko) | 1999-11-25 |
KR100341651B1 (ko) | 2002-11-23 |
EP0905176A4 (en) | 2000-11-22 |
JP3638960B2 (ja) | 2005-04-13 |
BR9706836A (pt) | 1999-12-28 |
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