WO2012121075A1 - 射出成形品の製造方法 - Google Patents
射出成形品の製造方法 Download PDFInfo
- Publication number
- WO2012121075A1 WO2012121075A1 PCT/JP2012/055051 JP2012055051W WO2012121075A1 WO 2012121075 A1 WO2012121075 A1 WO 2012121075A1 JP 2012055051 W JP2012055051 W JP 2012055051W WO 2012121075 A1 WO2012121075 A1 WO 2012121075A1
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- WO
- WIPO (PCT)
- Prior art keywords
- injection
- resin
- mold
- molded product
- insulating layer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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Classifications
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- 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
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/72—Heating or cooling
- B29C45/73—Heating or cooling of the mould
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/0025—Preventing defects on the moulded article, e.g. weld lines, shrinkage marks
-
- 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
- B29C33/00—Moulds or cores; Details thereof or accessories therefor
- B29C33/38—Moulds or cores; Details thereof or accessories therefor characterised by the material or the manufacturing process
-
- 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
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/72—Heating or cooling
- B29C45/7207—Heating or cooling of the moulded articles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/76—Measuring, controlling or regulating
- B29C45/78—Measuring, controlling or regulating of temperature
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L81/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen or carbon only; Compositions of polysulfones; Compositions of derivatives of such polymers
- C08L81/02—Polythioethers; Polythioether-ethers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L81/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen or carbon only; Compositions of polysulfones; Compositions of derivatives of such polymers
- C08L81/04—Polysulfides
-
- 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
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/72—Heating or cooling
- B29C45/73—Heating or cooling of the mould
- B29C2045/7356—Heating or cooling of the mould the temperature of the mould being near or higher than the melting temperature or glass transition temperature of the moulding material
-
- 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
- B29C2945/00—Indexing scheme relating to injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould
- B29C2945/76—Measuring, controlling or regulating
- B29C2945/76494—Controlled parameter
- B29C2945/76618—Crystallinity
-
- 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
- B29C33/00—Moulds or cores; Details thereof or accessories therefor
- B29C33/56—Coatings, e.g. enameled or galvanised; Releasing, lubricating or separating agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2081/00—Use of polymers having sulfur, with or without nitrogen, oxygen or carbon only, in the main chain, as moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
- B29K2995/0012—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds having particular thermal properties
- B29K2995/0015—Insulating
Definitions
- the present invention relates to a method for manufacturing an injection molded product.
- Crystalline thermoplastic resins are used in a wide range of industrial fields, mainly in the electric / electronic field and automobile field, due to their excellent chemical resistance, heat resistance, electrical characteristics, mechanical characteristics, and the like.
- the present invention has been made in order to solve the above-described problems, and the object of the present invention is to use a resin molded article composed of a crystalline thermoplastic resin in a use environment without performing heat treatment in advance. It is to provide a technique for sufficiently suppressing the dimensional change.
- the inventors of the present invention have made extensive studies to solve the above problems. As a result, it was found that the above problems can be solved by injection molding a resin composition composed of a crystalline thermoplastic resin using a mold having a heat insulating layer formed on the inner surface of the mold. It came to be completed. More specifically, the present invention provides the following.
- the resin composition is a raw material for an injection-molded product and includes a crystalline thermoplastic resin.
- the crystalline thermoplastic resin include polyethylene resin, polypropylene resin, polyvinyl chloride resin, polyamide resin, polyacetal resin, polyarylene sulfide resin, liquid crystalline polyester resin, polyimide resin, and syndiotactic polystyrene resin.
- the resin composition may contain two or more crystalline thermoplastic resins.
- the polyarylene sulfide resin has a low crystallization rate and is likely to solidify before the resin composition is sufficiently crystallized in the mold. Therefore, in the case of an injection-molded product formed by molding a resin composition composed of these resins, a dimensional change particularly in a use environment tends to be a problem.
- an injection-molded product containing polyarylene sulfide resin can sufficiently reduce the dimensional change of the injection-molded product under the usage environment.
- the polyarylene sulfide resin is mainly composed of — (Ar—S) — (Ar is an arylene group) as a repeating unit.
- a PAS resin having a generally known molecular structure can be used.
- the arylene group is not particularly limited.
- arylene sulfide groups composed of the above arylene groups in addition to a homopolymer using the same repeating unit, a polymer containing a repetition of different arylene sulfide groups is preferable depending on the application.
- the homopolymer preferably has a p-phenylene sulfide group as a repeating unit as an arylene group. This is because a homopolymer having a p-phenylene sulfide group as a repeating unit has extremely high heat resistance and exhibits high strength, high rigidity and high dimensional stability in a wide temperature range. By using such a homopolymer, a molded product having very excellent physical properties can be obtained.
- a combination of two or more types of arylene sulfide groups which are different from the arylene sulfide groups containing the above-mentioned arylene groups can be used.
- a combination containing a p-phenylene sulfide group and an m-phenylene sulfide group is preferable from the viewpoint of obtaining a molded product having high physical properties such as heat resistance, moldability, and mechanical properties.
- a polymer containing 70 mol% or more of p-phenylene sulfide groups is more preferred, and a polymer containing 80 mol% or more is more preferred.
- the PAS resin having the p-phenylene sulfide group and m-phenylene sulfide group as a repeating unit as described above is a material that is particularly required to improve the crystallinity of a molded product.
- a high crystallinity of the molded product can be realized.
- the manufacturing method of the injection molded product of the present invention has no problem of workability and productivity.
- the PAS resin having a phenylene sulfide group is a PPS (polyphenylene sulfide) resin.
- the resin composition used in the present invention may contain other resins as long as the effects of the present invention are not impaired.
- inorganic fillers such as nucleating agents, carbon black and glass fibers, pigments such as inorganic calcined pigments, antioxidants, stabilizers, plasticizers, lubricants, mold release agents
- a resin composition added with desired characteristics by adding an additive such as a flame retardant is also included in the resin composition used in the present invention.
- die used for the manufacturing method of this invention has the heat insulation layer formed in the metal mold
- any material may be used as long as it has low heat conductivity and has heat resistance to such an extent that it does not cause a problem even when in contact with a high-temperature resin composition, and the material constituting the heat insulating layer is not particularly limited.
- a heat insulating layer is formed on the entire inner surface of the mold.
- the heat insulation layer is not formed.
- Examples of the material that satisfies the heat resistance and thermal conductivity required for the heat insulating layer include resins having high heat resistance such as polyimide resin and low thermal conductivity, and porous ceramics such as porous zirconia. Hereinafter, these materials will be described.
- polyimide resin examples include pyromellitic acid (PMDA) -based polyimide, biphenyltetracarboxylic acid-based polyimide, polyamideimide using trimellitic acid, bismaleimide-based resin (bismaleimide / triazine-based, etc.), benzophenone tetracarboxylic acid Based polyimide, acetylene-terminated polyimide, thermoplastic polyimide, and the like.
- Preferable materials other than polyimide resin include, for example, tetrafluoroethylene resin.
- the heat insulating layer may contain a resin other than polyimide resin and tetrafluoroethylene resin, additives, and the like as long as the effects of the present invention are not impaired.
- the method for forming the heat insulating layer on the inner surface of the mold is not particularly limited.
- a solution of a polymer precursor such as a polyimide precursor capable of forming a polymer heat insulating layer is applied to the mold surface, heated to evaporate the solvent, and further heated to polymerize to form a heat insulating layer such as a polyimide film.
- a polymer precursor such as a polyimide precursor capable of forming a polymer heat insulating layer
- die using an adhesive tape-shaped polymer heat insulation film, and forming a heat insulation layer is mentioned. It is also possible to form a polyimide film and further form a chromium (Cr) film or a titanium nitride (TiN) film as a metal-based hard film
- the thermal conductivity required for the heat insulating layer composed of the resin as described above varies depending on the use and the like, but is particularly preferably 2 W / m ⁇ K or less.
- the thermal conductivity of the heat insulating layer within the above range, an injection molded product with a very high degree of crystallinity can be obtained more easily.
- the said heat conductivity points out the heat conductivity measured by the method as described in an Example.
- the thickness of the heat insulating layer is not particularly limited, and can be appropriately set to a preferable thickness depending on the material used, the shape of the molded product, and the like.
- the heat insulating layer is composed of a polyimide resin, it is preferable that the heat insulating layer has a thickness of 20 ⁇ m or more because a sufficiently high heat insulating effect can be obtained.
- the thickness of the heat insulating layer formed on the inner surface of the mold may be uniform or may include portions having different thicknesses.
- the zirconia contained in the porous zirconia is not particularly limited, and may be any of stabilized zirconia, partially stabilized zirconia, and unstabilized zirconia.
- Stabilized zirconia is one in which cubic zirconia is stabilized even at room temperature, and is excellent in mechanical properties such as strength and toughness and wear resistance.
- Partially stabilized zirconia refers to a state in which tetragonal zirconia partially remains even at room temperature, and when subjected to external stress, a martensitic transformation from tetragonal to monoclinic crystal occurs, and is particularly advanced by the action of tensile stress. Suppresses crack growth and has high fracture toughness.
- Unstabilized zirconia refers to zirconia that is not stabilized by a stabilizer. In addition, you may use combining at least 2 or more types selected from stabilized zirconia, partially stabilized zirconia, and unstabilized zirconia.
- the stabilizer contained in the stabilized zirconia and the partially stabilized zirconia conventionally known general ones can be employed.
- yttria, ceria, magnesia and the like can be mentioned.
- the amount of the stabilizer used is not particularly limited, and the amount used can be appropriately set according to the application, the material used, and the like.
- porous ceramics other than porous zirconia can be used, but porous zirconia has higher durability than other porous ceramics. For this reason, if a mold having a heat insulating layer composed of porous zirconia is used, defects such as deformation of the heat insulating layer are unlikely to occur. Is greatly increased.
- the raw material for forming the heat insulating layer may further contain conventionally known additives in addition to the above-mentioned zirconia and stabilizer as long as the effects of the present invention are not impaired.
- the method for forming the heat insulating layer using the above raw materials is not particularly limited, but it is preferable to employ a thermal spraying method.
- the thermal spraying method By adopting the thermal spraying method, the thermal conductivity of porous zirconia is easily adjusted to a desired range. Moreover, problems such as a significant decrease in the mechanical strength of the heat insulating layer due to excessive formation of bubbles inside the porous zirconia do not occur.
- the structure of a heat insulation layer becomes a thing suitable for the use of this invention.
- Formation of the heat insulation layer by thermal spraying can be performed as follows, for example. First, the raw material is melted to form a liquid. This liquid is accelerated and collides with the inner surface of the cavity. Finally, the material that collides with and adheres to the inner surface of the cavity is solidified. By doing so, a very thin heat insulating layer is formed on the inner surface of the mold. The thickness of the heat insulating layer can be adjusted by causing the melted raw material to collide with the very thin heat insulating layer and solidify it. As a method for solidifying the raw material, a conventionally known cooling means may be used, or the raw material may be solidified simply by leaving it to stand.
- the thermal spraying method is not particularly limited, and a preferable method can be appropriately selected from conventionally known methods such as arc spraying, plasma spraying, and flame spraying.
- the thermal conductivity of the heat insulating layer made of porous ceramic can be adjusted as appropriate according to the use of the molded product, the type of PAS resin, and the like. In the present invention, it is preferably 2 W / m ⁇ K or less, more preferably 0.3 W / m ⁇ K or more and 2 W / m ⁇ K or less. A thermal conductivity of 2 W / m ⁇ K or less is preferable because an injection-molded product having a high degree of crystallinity tends to be obtained even when an injection-molded product is molded at a mold temperature of 100 ° C. or less.
- the thermal conductivity is 0.3 W / m ⁇ K or more, the productivity of the injection-molded product is hardly lowered due to the decrease in the strength of the heat insulating layer due to the excessive number of bubbles in the heat insulating layer.
- the thermal conductivity of the heat insulation layer is 0.7 W / m ⁇ K or more, the decrease in strength of the heat insulation layer due to excessive bubbles in the heat insulation layer tends to be suppressed to a very small range. preferable.
- the value obtained with the measuring method as described in an Example is employ
- the thickness of the heat insulating layer is not particularly limited but is preferably 200 ⁇ m or more, more preferably 500 ⁇ m or more and 1000 ⁇ m or less. If it is 500 micrometers or more, it is preferable because the intensity
- the injection-molded article obtained by the production method of the present invention has a mold temperature at the time of injection molding of Tg + 30 ° C. or more and Tg + 80 ° C. or less, and molding when left for 2 hours in an environment of mold temperature at injection molding + 20 ° C.
- the dimensional change rate of the product is 0.2% or less.
- the mold temperature + 20 ° C. at the time of injection molding is approximately 160 ° C. Therefore, when a polyarylene sulfide-based resin is used, the dimensional change rate of an injection molded product exposed to 160 ° C. for 2 hours may be used as a reference.
- An injection molded product having a small dimensional change rate as described above can be easily obtained by using a mold having a heat insulating layer formed on the inner surface. The reason is as follows.
- the heat of the resin composition that has flowed into the mold is difficult to be released into the mold due to the presence of the heat insulating layer. For this reason, it takes a long time until the resin composition is cooled in the mold, and the resin composition contains a crystalline thermoplastic resin that is difficult to crystallize, and the resin composition contains a crystalline thermoplastic resin that has a slow crystallization rate. Even in the case of using as a raw material, the crystallinity of the crystalline thermoplastic resin contained in the injection-molded product can be sufficiently increased.
- the crystallinity contained in the injection molded product It is considered that the crystallinity of the thermoplastic resin can be sufficiently increased.
- “above the temperature necessary for crystallization of the crystalline thermoplastic resin” varies depending on the type of resin and the like, but is approximately the glass transition temperature (Tg) of the crystalline thermoplastic resin contained in the resin composition + 30 ° C. That's it.
- Tg glass transition temperature
- the thermal conductivity of the heat insulating layer is not 0, the heat of the resin composition that has flowed into the mold is gradually released out of the mold. At this time, if the mold temperature is high, the heat of the resin composition is not easily released outside the mold. Therefore, the conditions of the mold temperature also affect that the resin composition in the mold maintains a certain temperature or higher.
- the mold temperature condition greatly affects increasing the crystallinity of the thermoplastic resin contained in the injection molded product.
- the mold temperature condition necessary for increasing the crystallinity of the injection-molded product and reducing the dimensional change rate varies depending on the type of resin, but is, for example, Tg + 30 ° C. or higher and Tg + 80 ° C. or lower. Tg + 30 ° C.
- Tg + 80 ° C. or lower is preferable because the molding cycle does not become long. More preferably, it is Tg + 50 degreeC or more and Tg + 70 degreeC or less.
- the crystalline thermoplastic resin used is a polyarylene sulfide resin
- the injection-molded product obtained by the production method of the present invention has a mold temperature at the time of injection molding of Tg + 30 ° C. or more and Tg + 80 ° C. or less, and left for 2 hours in an environment of the mold temperature at injection molding + 20 ° C.
- the dimensional change rate of the molded product at the time of molding is 0.2% or less.
- the injection molding product obtained by the production method of the present invention has a high temperature environment because the dimensional change rate of the injection molding product in the above severe environment is 0.2% or less. It can be preferably used as a component used below.
- the high temperature environment is an environment having a temperature of 80 ° C. or higher and 140 ° C. or lower.
- the injection molded product obtained by the production method of the present invention has a high degree of crystallinity.
- “high degree of crystallinity” means the degree of crystallinity of a molded product obtained by molding a crystalline thermoplastic resin using a mold in which a heat insulating layer is not formed and the mold temperature is Tg + 55 ° C.
- the crystallinity is 101 or more.
- PAS resin composition Polyphenylene sulfide resin composition (“Fortron 1140A64”, manufactured by Polyplastics Co., Ltd.), melt viscosity 230 Pa ⁇ S measured according to ISO 11443, glass transition temperature measured at 10 ° C./min with DSC 85 ° C
- Raw material for heat insulation layer porous zirconia, polyimide Mold: Mold for flat plate molding 40mm wide x 40mm long x 2mm thick
- a raw material mainly composed of zirconia was sprayed on the inner surface of the mold by a thermal spraying method.
- the surface of the heat insulating layer was adjusted so as to increase the density, and a heat insulating layer having a multilayer structure was formed on the inner surface of the mold.
- Thermal spraying was continued until the thickness of the heat insulation layer reached 500 ⁇ m, and a mold 1 was produced.
- the polyimide precursor was apply
- die used with the manufacturing method of an Example was obtained.
- the thermal conductivity of the heat insulating layer is measured by the laser flash method, the thermal diffusivity by DSC, the specific heat by DSC, and the specific gravity by water displacement method (based on the JIS Z8807 solid specific gravity measurement method). Rate ⁇ specific heat ⁇ specific gravity].
- the values of thermal conductivity are shown in Table 1.
- the thermal conductivity ( ⁇ ) of the heat insulating layer having a multilayer structure is obtained by calculating the thermal conductivity of each of the low density layer and the high density layer, and the thermal conductivity ( ⁇ l) of the low density layer and the thermal conductivity of the high density layer.
- Example 1 The PAS resin composition was used as a molding material, and an injection molded product was produced using the mold 1 under the following molding conditions.
- Example 2 An injection molded product was produced under the same molding conditions as in Example 1 except that the mold 2 was used.
- the measurement of crystallinity by the X-ray diffraction method was performed using wide-angle X-ray diffraction (reflection method). Specifically, the degree of crystallinity was determined by the Ruland method.
- Example 2 Comparative Example 1, even when a mold having a heat insulating layer is used, the crystallinity is not improved under conditions where the mold temperature is low, and the dimensions under a high temperature environment are not obtained. It was confirmed that the change was also large.
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- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
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- Injection Moulding Of Plastics Or The Like (AREA)
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- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
樹脂組成物は、射出成形品の原料であり、結晶性熱可塑性樹脂を含む。結晶性熱可塑性樹脂とは、ポリエチレン樹脂、ポリプロピレン樹脂、ポリ塩化ビニル樹脂、ポリアミド樹脂、ポリアセタール樹脂、ポリアリーレンサルファイド樹脂、液晶性ポリエステル樹脂、ポリイミド樹脂、シンジオタクチックポリスチレン樹脂等をあげることができる。なお、樹脂組成物は2種以上の結晶性熱可塑性樹脂を含んでもよい。
本発明の製造方法に用いる金型は、金型内表面に断熱層が形成されている。断熱層が形成されているため、金型内に流れ込んだ樹脂組成物の持つ熱が金型外に放出されにくくなる。その結果、金型の内表面に接する樹脂組成物が急冷されにくくなり、成形品表面の結晶化度も充分に高めることができる。
本発明の製造方法で得られる射出成形品は、射出成形時の金型温度がTg+30℃以上、Tg+80℃以下であり、射出成形時の金型温度+20℃の環境で2時間放置した際の成形品の寸法変化率が0.2%以下である。結晶性熱可塑性樹脂がポリアリーレンサルファイド系樹脂の場合には、射出成形時の金型温度+20℃は、およそ160℃である。したがって、ポリアリーレンサルファイド系樹脂を用いる場合には、160℃の環境下に2時間曝した射出成形品の寸法変化率を基準とすればよい。
上述の通り、本発明の製造方法で得られる射出成形品は、射出成形時の金型温度がTg+30℃以上、Tg+80℃以下であり、射出成形時の金型温度+20℃の環境で2時間放置した際の成形品の寸法変化率が0.2%以下である。用途に応じて使用環境が異なるものの、上記の過酷な環境での射出成形品の寸法変化率が0.2%以下であることから、本発明の製造方法で得られる射出成形品は、高温環境下で使用される部品として好ましく使用できる。高温環境下とは、例えば、ポリアリーレンサルファイド樹脂の場合は温度80℃以上140℃以下の環境である。
PAS樹脂組成物:ポリフェニレンサルファイド樹脂組成物(「フォートロン1140A64」、ポリプラスチックス社製)、ISO11443に準拠して測定した溶融粘度230Pa・S、DSCにて10℃/minで測定したガラス転移温度85℃
断熱層の原料:多孔質ジルコニア、ポリイミド
金型:幅40mm×長さ40mm×厚さ2mmの平板成形用金型
主としてジルコニアから構成される原料を、溶射法にて上記金型の内表面に溶射した。断熱層の表面は密度が高くなるように調整し、多層構造の断熱層を金型内表面に形成した。断熱層の厚みが500μmになるまで溶射を続け金型1を作製した。また、上記金型の内表面にポリイミド前駆体を塗布し加熱固化させ断熱層の厚みを150μmとし金型2を作製した。このようにして、実施例の製造方法で用いる金型が得られた。
断熱層の熱伝導率はレーザーフラッシュ法にて熱拡散率、DSCにて比熱、水中置換法(JIS Z8807固体比重測定方法に準拠)にて比重を測定し、[熱伝導率]=[熱拡散率×比熱×比重]により算出した。熱伝導率の値は表1に示した。なお、多層構造の断熱層の熱伝導率(λ)は密度の低い層と高い層のそれぞれの熱伝導率を求め、密度の低い層の熱伝導率(λl)、密度の高い層の熱伝導率(λh)、断熱層全体の厚さに対する密度の低い層の厚さ割合(t)とした場合、[1/λ]=[t/λl]+[(1-t)/λh]の式を用い計算により求めた。
成形用材料としてPAS樹脂組成物を用い、金型1を用い下記の成形条件で射出成形品を製造した。
[成形条件]
スクリュー回転数:100rpm
射出速度:100mm/sec
金型温度:140℃
樹脂温度:320℃
金型2を用いた以外は実施例1と同様の成形条件で射出成形品を作製した。
金型温度を80℃に変更した以外は実施例2と同様の条件で射出成形品を作製した。
断熱層を有する金型を、断熱層を有さない金型に変更した以外は、実施例1と同様の条件で射出成形品を作製した。
射出成形品に対して、160℃、2時間の条件で熱処理を施した以外は比較例2と同様の方法で射出成形品を製造した。
実施例、比較例、参考例の射出成形品を160℃、2時間の条件で加熱し、加熱後の射出成形品の流動直角方向、流動方向を測定し、流動直角方向、流動方向のそれぞれについて寸法変化率を測定した。寸法変化率の結果を表1に示した。
実施例、比較例、参考例に含まれるPPS樹脂の結晶化度を、X線回折法を用いて測定した。また、比較例2の結晶化度を100として、実施例1及び2、比較例1、参考例1の結晶化度を算出した。算出結果は表1に示した。
Claims (6)
- 結晶性熱可塑性樹脂から構成される樹脂組成物を射出成形した際の金型温度+20℃の環境で2時間放置したときの射出成形品の寸法変化率が0.2%以下の射出成形品を製造する方法であって、
金型内表面に断熱層が形成された金型を用い、
前記金型温度を、前記結晶性熱可塑性樹脂のガラス転移温度(Tg)+30℃以上Tg+80℃以下とし、前記樹脂組成物を射出成形する射出成形品の製造方法。 - 前記金型温度+20℃が、160℃であり、
前記結晶性熱可塑性樹脂が、ポリアリーレンサルファイド樹脂である請求項1に記載の射出成形品の製造方法。 - 前記断熱層は、多孔質ジルコニアから構成される請求項1又は2に記載の射出成形品の製造方法。
- 前記断熱層は、熱伝導率が2W/m・K以下である請求項1から3のいずれかに記載の射出成形品の製造方法。
- 前記断熱層は、溶射法で形成された請求項1から4のいずれかに記載の射出成形品の製造方法。
- 前記断熱層は、厚みが200μm以上である請求項1から5のいずれかに記載の射出成形品の製造方法。
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020137024059A KR20140006028A (ko) | 2011-03-08 | 2012-02-29 | 사출 성형품의 제조방법 |
| CN2012800119217A CN103402731A (zh) | 2011-03-08 | 2012-02-29 | 注塑成型品的制造方法 |
| US14/003,401 US20140035200A1 (en) | 2011-03-08 | 2012-02-29 | Method for manufacturing an injection-molded article |
| EP12755571.2A EP2684670A4 (en) | 2011-03-08 | 2012-02-29 | METHOD FOR PRODUCING AN INJECTION MOLDED OBJECT |
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| Application Number | Priority Date | Filing Date | Title |
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| JP2011-050886 | 2011-03-08 | ||
| JP2011050886A JP2012187729A (ja) | 2011-03-08 | 2011-03-08 | 射出成形品の製造方法 |
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| Country | Link |
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| US (1) | US20140035200A1 (ja) |
| EP (1) | EP2684670A4 (ja) |
| JP (1) | JP2012187729A (ja) |
| KR (1) | KR20140006028A (ja) |
| CN (1) | CN103402731A (ja) |
| TW (1) | TW201247391A (ja) |
| WO (1) | WO2012121075A1 (ja) |
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| JP6085450B2 (ja) * | 2012-10-31 | 2017-02-22 | ポリプラスチックス株式会社 | 入れ子の製造方法 |
| JP7182161B2 (ja) * | 2018-12-25 | 2022-12-02 | パナソニックIpマネジメント株式会社 | 樹脂成形品の製造方法 |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001191378A (ja) * | 2000-01-06 | 2001-07-17 | Ono Sangyo Kk | 合成樹脂成形方法 |
| JP2001348478A (ja) * | 2000-06-08 | 2001-12-18 | Toray Ind Inc | ポリフェニレンスルフィド樹脂組成物 |
| JP2006062369A (ja) * | 1997-05-28 | 2006-03-09 | Mitsubishi Engineering Plastics Corp | 熱可塑性樹脂成形用の金型組立体及び成形品の製造方法 |
| JP2008266600A (ja) * | 2007-03-23 | 2008-11-06 | Toray Ind Inc | 二軸配向フィルム |
| JP2009274352A (ja) * | 2008-05-15 | 2009-11-26 | Mitsubishi Engineering Plastics Corp | 金型組立体、射出成形方法、及び、成形品 |
| JP2010110892A (ja) | 2010-01-21 | 2010-05-20 | Kureha Corp | 研磨装置用ワークピース保持リング |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01225660A (ja) * | 1988-03-04 | 1989-09-08 | Polyplastics Co | ポリアリーレンサルファイド樹脂組成物 |
| JPH06246797A (ja) * | 1992-12-28 | 1994-09-06 | Nippon Steel Chem Co Ltd | 成形品外観へのヒケ防止方法および射出成形用金型 |
| JP2005271429A (ja) * | 2004-03-25 | 2005-10-06 | Mitsubishi Electric Corp | 成形金型装置および成形方法 |
-
2011
- 2011-03-08 JP JP2011050886A patent/JP2012187729A/ja active Pending
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2012
- 2012-02-29 KR KR1020137024059A patent/KR20140006028A/ko not_active Withdrawn
- 2012-02-29 WO PCT/JP2012/055051 patent/WO2012121075A1/ja not_active Ceased
- 2012-02-29 US US14/003,401 patent/US20140035200A1/en not_active Abandoned
- 2012-02-29 EP EP12755571.2A patent/EP2684670A4/en not_active Withdrawn
- 2012-02-29 CN CN2012800119217A patent/CN103402731A/zh active Pending
- 2012-03-02 TW TW101106893A patent/TW201247391A/zh unknown
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006062369A (ja) * | 1997-05-28 | 2006-03-09 | Mitsubishi Engineering Plastics Corp | 熱可塑性樹脂成形用の金型組立体及び成形品の製造方法 |
| JP2001191378A (ja) * | 2000-01-06 | 2001-07-17 | Ono Sangyo Kk | 合成樹脂成形方法 |
| JP2001348478A (ja) * | 2000-06-08 | 2001-12-18 | Toray Ind Inc | ポリフェニレンスルフィド樹脂組成物 |
| JP2008266600A (ja) * | 2007-03-23 | 2008-11-06 | Toray Ind Inc | 二軸配向フィルム |
| JP2009274352A (ja) * | 2008-05-15 | 2009-11-26 | Mitsubishi Engineering Plastics Corp | 金型組立体、射出成形方法、及び、成形品 |
| JP2010110892A (ja) | 2010-01-21 | 2010-05-20 | Kureha Corp | 研磨装置用ワークピース保持リング |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP2684670A4 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103402731A (zh) | 2013-11-20 |
| TW201247391A (en) | 2012-12-01 |
| JP2012187729A (ja) | 2012-10-04 |
| EP2684670A1 (en) | 2014-01-15 |
| US20140035200A1 (en) | 2014-02-06 |
| EP2684670A4 (en) | 2015-02-11 |
| KR20140006028A (ko) | 2014-01-15 |
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