JPH10152575A - Method for foaming thermoplastic resin - Google Patents
Method for foaming thermoplastic resinInfo
- Publication number
- JPH10152575A JPH10152575A JP8327728A JP32772896A JPH10152575A JP H10152575 A JPH10152575 A JP H10152575A JP 8327728 A JP8327728 A JP 8327728A JP 32772896 A JP32772896 A JP 32772896A JP H10152575 A JPH10152575 A JP H10152575A
- Authority
- JP
- Japan
- Prior art keywords
- thermoplastic resin
- heat
- molding
- foaming
- foam
- 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.)
- Pending
Links
- 229920005992 thermoplastic resin Polymers 0.000 title claims abstract description 41
- 238000005187 foaming Methods 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title description 11
- 239000003094 microcapsule Substances 0.000 claims abstract description 46
- 238000001125 extrusion Methods 0.000 claims abstract description 25
- 238000001746 injection moulding Methods 0.000 claims abstract description 14
- 238000010097 foam moulding Methods 0.000 claims abstract description 7
- 238000004898 kneading Methods 0.000 claims abstract description 7
- 239000002994 raw material Substances 0.000 claims description 13
- 238000002844 melting Methods 0.000 claims description 9
- 230000008018 melting Effects 0.000 claims description 9
- 239000006260 foam Substances 0.000 abstract description 10
- 238000000465 moulding Methods 0.000 abstract description 10
- 230000005484 gravity Effects 0.000 abstract description 9
- 238000002347 injection Methods 0.000 abstract description 4
- 239000007924 injection Substances 0.000 abstract description 4
- 230000004927 fusion Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 21
- 238000002156 mixing Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 6
- -1 polypropylene Polymers 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 229920001971 elastomer Polymers 0.000 description 5
- 239000000806 elastomer Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 229920003002 synthetic resin Polymers 0.000 description 5
- 239000000057 synthetic resin Substances 0.000 description 5
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 5
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 4
- 239000004088 foaming agent Substances 0.000 description 4
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 2
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 2
- 239000004156 Azodicarbonamide Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 2
- 235000019399 azodicarbonamide Nutrition 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000004566 building material Substances 0.000 description 2
- 239000002666 chemical blowing agent Substances 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 239000005038 ethylene vinyl acetate Substances 0.000 description 2
- 229920006244 ethylene-ethyl acrylate Polymers 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000001282 iso-butane Substances 0.000 description 2
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- CRSOQBOWXPBRES-UHFFFAOYSA-N neopentane Chemical compound CC(C)(C)C CRSOQBOWXPBRES-UHFFFAOYSA-N 0.000 description 2
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 238000007788 roughening Methods 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 1
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 1
- OZAIFHULBGXAKX-VAWYXSNFSA-N AIBN Substances N#CC(C)(C)\N=N\C(C)(C)C#N OZAIFHULBGXAKX-VAWYXSNFSA-N 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 241000251730 Chondrichthyes Species 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- NEHMKBQYUWJMIP-NJFSPNSNSA-N chloro(114C)methane Chemical compound [14CH3]Cl NEHMKBQYUWJMIP-NJFSPNSNSA-N 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- UQLDLKMNUJERMK-UHFFFAOYSA-L di(octadecanoyloxy)lead Chemical compound [Pb+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O UQLDLKMNUJERMK-UHFFFAOYSA-L 0.000 description 1
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- UKAJDOBPPOAZSS-UHFFFAOYSA-N ethyl(trimethyl)silane Chemical compound CC[Si](C)(C)C UKAJDOBPPOAZSS-UHFFFAOYSA-N 0.000 description 1
- 239000005042 ethylene-ethyl acrylate Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 150000002734 metacrylic acid derivatives Chemical class 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000012994 photoredox catalyst Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N sec-butylidene Natural products CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- CZDYPVPMEAXLPK-UHFFFAOYSA-N tetramethylsilane Chemical compound C[Si](C)(C)C CZDYPVPMEAXLPK-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Molding Of Porous Articles (AREA)
Abstract
(57)【要約】
【課題】 熱可塑性樹脂の押出または射出による発泡成
形において、細かく均一で緻密な発泡状態にでき、表面
がきれいで、しかも目的とする比重に発泡させることが
できる熱可塑性樹脂の発泡成形方法を提供すること。
【解決手段】 熱膨張性のマイクロカプセルを熱可塑性
樹脂に混合するようにし、この熱膨張性マイクロカプセ
ルを混練溶融熱で膨張させて押出成形または射出成形で
発泡成形する。これにより、各気泡をマイクロカプセル
で包んだ状態で安定して発泡させ、細かく均一で緻密な
発泡状態にでき、表面がきれいで、しかも目的とする比
重に発泡させることができるようにしている。PROBLEM TO BE SOLVED: To provide a fine, uniform and dense foamed state in a foaming molding by extrusion or injection of a thermoplastic resin, a clean surface, and a foamable foam having a desired specific gravity. To provide a foam molding method. SOLUTION: A heat-expandable microcapsule is mixed with a thermoplastic resin, and the heat-expandable microcapsule is expanded by kneading heat of fusion and foam-molded by extrusion molding or injection molding. As a result, each bubble can be stably foamed in a state of being wrapped in the microcapsule, and can be made into a fine, uniform and dense foaming state, and the surface can be made clean and foamed to a desired specific gravity.
Description
【0001】[0001]
【発明の属する技術分野】この発明は、熱可塑性樹脂を
用いて押出成形または射出成形により発泡成形する方法
に関し、均一かつ緻密に発泡できる成形方法である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for foaming a thermoplastic resin by extrusion molding or injection molding, and more particularly to a molding method capable of foaming uniformly and densely.
【0002】[0002]
【従来の技術】熱可塑性樹脂を用いる発泡成形は種々の
合成樹脂製品に成形に利用されており、発泡させること
により合成樹脂製品の軽量化、断熱性の向上、クッショ
ン性の付与などが図られている。2. Description of the Related Art Foam molding using a thermoplastic resin is used for molding various synthetic resin products. By foaming, it is possible to reduce the weight of the synthetic resin product, improve heat insulation, and impart cushioning properties. ing.
【0003】このような熱可塑性樹脂による発泡成形の
一般的な方法として、例えば熱可塑性樹脂原料に化学発
泡剤を混合しておき、熱可塑性樹脂原料の溶融時の熱に
より化学発泡剤を熱分解させてガスを発生させる方法や
溶融させた熱可塑性樹脂に水蒸気や窒素あるいは炭酸ガ
スなどのガス気体を注入する方法等がある。[0003] As a general method of such foaming molding using a thermoplastic resin, for example, a chemical foaming agent is mixed with a thermoplastic resin raw material, and the chemical foaming agent is thermally decomposed by heat at the time of melting the thermoplastic resin raw material. There are a method of generating a gas by causing the gas to flow, and a method of injecting a gaseous gas such as water vapor, nitrogen or carbon dioxide gas into a molten thermoplastic resin.
【0004】[0004]
【発明が解決しようとする課題】このような熱可塑性樹
脂による発泡成形法では、いずれも熱可塑性樹脂原料を
溶融させて粘度が非常に低下した状態で熱分解ガスや別
に注入するガスによって発泡成形するようにしており、
熱分解ガスや注入するガスのわずかな圧力変動などで気
泡の状態が大きく変化し、均一で緻密な成形品を得るこ
とが難しく、しかもガスが外部に逃げ易く、安定した発
泡状態として目的とする比重の成形品を得ることが難し
いという問題がある。In the foam molding method using such a thermoplastic resin, foam molding is carried out by using a pyrolysis gas or a gas to be injected separately in a state where the thermoplastic resin raw material is melted and the viscosity is extremely reduced. I am trying to
The bubble state changes greatly due to the slight pressure fluctuation of the pyrolysis gas or the injected gas, making it difficult to obtain a uniform and dense molded product. There is a problem that it is difficult to obtain a molded product having a specific gravity.
【0005】また、熱可塑性樹脂による押出成形の場合
には、発泡状態の樹脂がダイを通過する際、急激な圧力
低下のためガスがさらに膨張し、これによって成形品の
表面に微細な凹凸が生じて鮫肌状に荒れる現象が生じ易
くきれいな表面が得られないという問題がある。[0005] In the case of extrusion molding using a thermoplastic resin, when the foamed resin passes through the die, the gas further expands due to a sudden pressure drop, thereby causing fine irregularities on the surface of the molded product. There is a problem that a phenomenon in which the surface is roughened like a shark skin easily occurs and a clean surface cannot be obtained.
【0006】この発明は、上記従来技術の課題に鑑みて
なされたもので、熱可塑性樹脂の押出または射出による
発泡成形において、細かく均一で緻密な発泡状態にで
き、表面がきれいで、しかも目的とする比重に発泡させ
ることができる熱可塑性樹脂の発泡成形方法を提供しよ
うとするものである。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the prior art. In foam molding by extrusion or injection of a thermoplastic resin, a fine, uniform and dense foam state can be obtained, and the surface is clean. It is an object of the present invention to provide a method for foaming a thermoplastic resin which can be foamed to a specific gravity.
【0007】[0007]
【課題を解決するための手段】上記従来技術の有する課
題を解決するため、この発明では、従来技術のガスを溶
融樹脂中に直接分散させる方法では、その分散をコント
ロールしたり、気泡の径を一定化することが難しいこと
に基づいて成されたもので、その具体的な構成は、熱可
塑性樹脂の押出成形または射出成形による発泡成形方法
において、熱可塑性樹脂原料に熱膨張性マイクロカプセ
ルを混合し、押出成形または射出成形による混練溶融熱
によって当該熱膨張性マイクロカプセルを膨張させて成
形することを特徴とするものである。In order to solve the above-mentioned problems of the prior art, according to the present invention, in the method of directly dispersing a gas in a molten resin according to the prior art, the dispersion is controlled and the diameter of bubbles is reduced. It is based on the difficulty of stabilization, and the specific configuration is to mix the thermoplastic resin raw materials with the heat-expandable microcapsules in the foaming method by extrusion or injection molding of the thermoplastic resin. Then, the heat-expandable microcapsules are expanded and molded by heat of kneading and melting by extrusion molding or injection molding.
【0008】この熱可塑性樹脂の発泡成形方法によれ
ば、熱膨張性のマイクロカプセルを熱可塑性樹脂に混合
するようにし、この熱膨張性マイクロカプセルを混練溶
融熱で膨張させて押出成形または射出成形で発泡成形す
るようにしており、各気泡をマイクロカプセルによって
安定して発泡させ、細かく均一で緻密な発泡状態にで
き、表面がきれいで、しかも目的とする比重に発泡させ
ることができるようにしている。According to the method for foaming and molding a thermoplastic resin, the heat-expandable microcapsules are mixed with the thermoplastic resin, and the heat-expandable microcapsules are expanded by kneading and melting heat to carry out extrusion molding or injection molding. In order to make each bubble stably foamed by microcapsules, it can be made into a fine, uniform and dense foaming state, the surface is clean, and it can be foamed to the desired specific gravity I have.
【0009】ここで、熱可塑性樹脂とは、例えば一般的
な熱可塑性樹脂として知られているPVC(塩化ビニ
ル)、PS(ポリスチレン)、PP(ポリプロピレ
ン)、PPO、PE(ポリエチレン)など、エンジニア
リングプラスチックとしてのPBT(ポリブチレンテレ
フタレート)、ナイロン、PC(ポリカーボネート)、
PET(ポリエチレンテレフタレート)など、エラスト
マーとしてEEA(エチレン−アクリル酸エチル共重合
体)、AAS(アクリルニトリルアクリレートスチレン
コポリマー)、EVA(エチレン酢酸ビニル共重合
体)、TPU(熱可塑性ウレタンエラストマー)、TP
EE(サーモプラスチックエステルエラストマー)など
をあげることができ、これらにその他の助剤として滑
剤、可塑剤、酸化防止剤などを添加して用いる。Here, the thermoplastic resin is, for example, an engineering plastic such as PVC (vinyl chloride), PS (polystyrene), PP (polypropylene), PPO, or PE (polyethylene) which is known as a general thermoplastic resin. (Polybutylene terephthalate), nylon, PC (polycarbonate),
EEA (ethylene-ethyl acrylate copolymer), AAS (acrylonitrile acrylate styrene copolymer), EVA (ethylene vinyl acetate copolymer), TPU (thermoplastic urethane elastomer), TP as elastomers such as PET (polyethylene terephthalate)
EE (thermoplastic ester elastomer) and the like can be used, and a lubricant, a plasticizer, an antioxidant and the like are added to these as an auxiliary agent.
【0010】熱膨張性のマイクロカプセルとは、合成樹
脂カプセルの中に、加熱することにより膨張する液体や
気体を内包させたものであり、押出成形や射出成形の際
のスクリュなどによる混練溶融熱で内包された液体や気
体が膨張することにより外殻となるマイクロカプセルを
膨張させるが、成形時の温度条件によっては溶融した
り、破裂することなく成形が完了するものを用いる。A heat-expandable microcapsule is a synthetic resin capsule in which a liquid or a gas that expands when heated is included, and the heat of kneading and melting by a screw or the like during extrusion molding or injection molding. The liquid or gas contained therein expands to expand the microcapsules that become the outer shell by expansion, but depending on the temperature conditions at the time of molding, a material that completes molding without melting or bursting is used.
【0011】マイクロカプセルの素材としては、アクリ
ルニトリルをモノマー成分の一つとした共重合体が用い
られ、アクリルニトリルと共重合しても良い他のモノマ
ー成分として、例えばアクリル酸、メタクリル酸、アク
リル酸エステル、メタクリル酸エステル、スチレン、酢
酸ビニル、塩化ビニリデンなどを上げることができる
が、これらに限定するものでない。As a material for the microcapsules, a copolymer containing acrylonitrile as one of the monomer components is used. As other monomer components which may be copolymerized with acrylonitrile, for example, acrylic acid, methacrylic acid, acrylic acid Examples include, but are not limited to, esters, methacrylates, styrene, vinyl acetate, vinylidene chloride, and the like.
【0012】マイクロカプセルに内包する液体または気
体としては、マイクロカプセルの軟化点以下の温度でガ
スになって膨張するもので、例えばプロパン、プロピレ
ン、ブテン、ノルマルブタン、イソブタン、イソペンタ
ン、ネオペンタン、ノルマルペンタン、ヘキサン、ペプ
タン、石油エーテル、メタンのハロゲン化物、例えば塩
化メチル、メチレンクロリド、CCl3 F、CCl2 F
2 などのクロロフルオロカーボン、テトラメチルシラ
ン、トリメチルエチルシランなどのテトラアルキルシラ
ンなどの低沸点液体のほか、加熱により熱分解してガス
状になるAIBNなどの化合物を用いる。The liquid or gas contained in the microcapsules is a gas or a gas that expands at a temperature lower than the softening point of the microcapsules. For example, propane, propylene, butene, normal butane, isobutane, isopentane, neopentane, normal pentane , Hexane, peptane, petroleum ether, halides of methane such as methyl chloride, methylene chloride, CCl 3 F, CCl 2 F
In addition to low-boiling liquids such as chlorofluorocarbons such as 2 and tetraalkylsilanes such as tetramethylsilane and trimethylethylsilane, compounds such as AIBN that is thermally decomposed by heating and becomes gaseous are used.
【0013】[0013]
【発明の実施の形態】以下、この発明の一実施の形態を
具体的に説明する。この発明の熱可塑性樹脂の発泡成形
方法では、熱可塑性樹脂を用いて押出成形、あるいは射
出成形する場合に、原料である熱可塑性樹脂と熱膨張性
マイクロカプセルとをホッパーに同時に投入して混合さ
せ、熱可塑性樹脂と熱膨張性マミクロカプセルを混合状
態のまま押出機や射出機でダイや金型に圧入して発泡成
形するものである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be specifically described below. In the thermoplastic resin foam molding method of the present invention, when extrusion molding or injection molding is performed using a thermoplastic resin, the thermoplastic resin as a raw material and the thermally expandable microcapsules are simultaneously charged into a hopper and mixed. In this method, the thermoplastic resin and the heat-expandable mamicrocapsules are pressed into a die or a mold by an extruder or an injection machine in a mixed state and foamed.
【0014】この押出成形や射出成形では、熱可塑性の
原料樹脂の加熱溶融時に熱膨張性マイクロカプセルの合
成樹脂製の外殻が軟化するとともに、内部に入れた液体
や気体が加熱されてガスとなって膨張し、合成樹脂製の
外殻を押し拡げて膨張させ、発泡状態を得るようにして
いる。In this extrusion molding or injection molding, the outer shell made of synthetic resin of the heat-expandable microcapsules is softened when the thermoplastic raw resin is heated and melted, and the liquid or gas contained therein is heated to form a gas. Then, the outer shell made of synthetic resin is expanded by pushing and expanding to obtain a foamed state.
【0015】したがって、熱膨張性マイクロカプセルの
外殻は熱可塑性樹脂原料の成形温度条件では軟化するが
溶融はしない温度特性を有する必要があり、既にあげた
熱可塑性樹脂の種類に応じて既にあげた熱膨張性マイク
ロカプセルの中から素材や温度特性が適宜選定され、内
部に入れられる低沸点液体等も熱可塑性樹脂原料の溶融
温度でガス状になって膨張するものを既に上げたものの
中から選んで用いられる。Therefore, the outer shell of the heat-expandable microcapsule must have a temperature characteristic of softening but not melting under the molding temperature conditions of the thermoplastic resin raw material. The material and temperature characteristics are appropriately selected from among the heat-expandable microcapsules, and the low-boiling liquid, etc., which is contained inside is also selected from those that have become gaseous and expand at the melting temperature of the thermoplastic resin raw material. Used to choose.
【0016】また、押出成形や射出成形では、押出機や
射出機によってホッパーから投入された原料がスクリュ
ーなどで混練されることから、熱膨張性マイクロカプセ
ルにも混練による剪断力などが加わるとともに、ダイや
金型に押出されるときに押出力や射出力が加わることか
ら、これらの力が加わってもマイクロカプセルが壊れな
いものである必要があり、大きさなどが選定される。In extrusion molding and injection molding, the raw material supplied from the hopper is kneaded by an extruder or an injection machine by a screw or the like, so that shearing force due to kneading is applied to the heat-expandable microcapsules. Since a pushing force and a radiating force are applied when the microcapsule is extruded into a die or a mold, the microcapsule must be one that does not break even when these forces are applied, and the size is selected.
【0017】このように押出成形または射出成形によっ
て、熱可塑性樹脂中に熱膨張性マイクロカプセルが膨張
されて包含された状態で発泡体を成形することができ、
各気泡はマイクロカプセルで包まれた状態で安定してお
り、押出成形の場合で、ダイから押出されて圧力が開放
された状態でもガスが直接成形品の外部に抜けることも
なく、表面外観の良好な発泡体を得ることができる。As described above, by the extrusion molding or the injection molding, a foam can be molded in a state where the thermally expandable microcapsules are expanded and contained in the thermoplastic resin.
Each bubble is stable in a state of being wrapped in microcapsules, and in the case of extrusion molding, even when the pressure is released by extruding from the die, gas does not escape directly to the outside of the molded product, and the surface appearance A good foam can be obtained.
【0018】したがって、このような押出成形または射
出成形によって成形される発泡成形体では、膨張した後
の熱膨張性マイクロカプセルの数(混合量)と粒径によ
って気泡の量と大きさが定まり、これらから成形体の比
重が定まることから、熱可塑性樹脂原料に混合する未膨
張の熱膨張性マイクロカプセルの数(混合量)と成形途
中の加熱量による膨張後の熱膨張性マイクロカプセルの
粒径の予測によって発泡状態のコントロールが可能とな
り、従来のガスを直接膨張させる場合に比べてガスだけ
が外部に逃げることもなく、簡単に目的の比重にするこ
とができる。Therefore, in the foam molded article formed by such extrusion molding or injection molding, the amount and size of the bubbles are determined by the number (mixing amount) and the particle size of the thermally expandable microcapsules after expansion. From these, the specific gravity of the molded body is determined, so that the number (mixing amount) of the unexpanded thermally expandable microcapsules to be mixed with the thermoplastic resin raw material and the particle size of the thermally expandable microcapsules after expansion due to the heating amount during molding According to the prediction, it is possible to control the foaming state, and it is possible to easily obtain the target specific gravity without escaping only the gas to the outside as compared with the conventional case where the gas is directly expanded.
【0019】これにより、建材のように軽量でかつ断熱
性が要求される場合には、熱膨張性マイクロカプセルの
粒径を比較的大きいものとし、しかも混合量を多くする
ようにするなどで対応することができる。Accordingly, when lightweight and heat insulating properties are required as in building materials, the size of the thermally expandable microcapsules is made relatively large, and the mixing amount is increased. can do.
【0020】また、事務機器用発泡ローラのように均一
かつ緻密な発泡状態にする必要がある場合には、熱可塑
性樹脂中に混合する熱膨張性マイクロカプセルを非常に
小さい球状のものとし、例えば粒径が5〜30μmのも
のを用い、膨張後の粒径を10〜100μmとして均一
かつ緻密な発泡成形体を得ることができる。When a uniform and dense foaming state is required as in the case of a foaming roller for office equipment, the heat-expandable microcapsules to be mixed with the thermoplastic resin are made to be very small and spherical. By using one having a particle size of 5 to 30 μm and a particle size after expansion of 10 to 100 μm, a uniform and dense foamed product can be obtained.
【0021】さらに、靴底用スポンジ等のようにクショ
ン性を持ち、しかも水が浸透しないように発泡する必要
がある場合にも、熱膨張性マイクロカプセルにより気泡
が形成されることから、独立気泡となって水の浸透はな
く、必要なクッション性に応じて気泡の大きさと量をコ
ントロールすることで対応することができる。Further, even in the case where foam such as a sponge for a shoe sole or the like needs to be formed so as to prevent water from penetrating, the closed cells are formed by the heat-expandable microcapsules. Thus, there is no water permeation, and it can be dealt with by controlling the size and amount of bubbles according to the required cushioning property.
【0022】[0022]
【実施例】以下、本発明の実施例、比較例を述べる。EXAMPLES Examples of the present invention and comparative examples will be described below.
【0023】(実施例1)熱可塑性樹脂として熱可塑性
ウレタンエラストマーを用い、熱膨張性マイクロカプセ
ルの配合量を変えた4種類の押出成形を行った(実施例
A〜D)。(Example 1) Four types of extrusion molding were performed using a thermoplastic urethane elastomer as a thermoplastic resin and changing the blending amount of the heat-expandable microcapsules (Examples A to D).
【0024】また、比較例として同一の熱可塑性樹脂原
料に化学発泡剤を添加した発泡押出成形を行った。As a comparative example, foam extrusion extrusion was carried out by adding a chemical foaming agent to the same thermoplastic resin raw material.
【0025】使用樹脂は熱可塑性ウレタンエラストマー
(TPU)(日本ミラクトラン製)。The resin used is a thermoplastic urethane elastomer (TPU) (manufactured by Nippon Milactran).
【0026】熱膨張性マイクロカプセルとして商品名:
エクスパンセル(日本フィライト製)を用いた。この熱
膨張性マイクロカプセルの殻は塩化ビニリデン/アクリ
ルニトリル・コポリマーで内包ガスはイソブタンであ
り、この熱膨張性マイクロカプセルの膨張前後の性質は
表1に示す通りである。Trade name as heat-expandable microcapsule:
Expancel (manufactured by Nippon Philite) was used. The shell of this heat-expandable microcapsule is a vinylidene chloride / acrylonitrile copolymer and the contained gas is isobutane. The properties of the heat-expandable microcapsule before and after expansion are as shown in Table 1.
【0027】熱膨張性マイクロカプセルの配合量は熱可
塑性樹脂100部(重量、以下同じ)に対して1.5 、
3、5、10部の4種類とした。The amount of the heat-expandable microcapsules is 1.5 parts per 100 parts (weight, the same applies hereinafter) of the thermoplastic resin.
Three, five, and ten parts were provided.
【0028】比較例の化学発泡剤はアゾジカーボンアミ
ドを用いた。その他種々の助剤を添加した。Azodicarbonamide was used as the chemical blowing agent of the comparative example. Various other auxiliaries were added.
【0029】こうして得られた発泡成形体の密度を測定
するとともに、表面外観および断面のセル構造を観察
し、その結果を表2に示した。The density of the foam molded article thus obtained was measured, and the surface appearance and the cell structure of the cross section were observed. The results are shown in Table 2.
【0030】[0030]
【表1】 [Table 1]
【0031】[0031]
【表2】 [Table 2]
【0032】同表からも明らかなように、この発明の熱
膨張性マイクロカプセルを用いた押出成形による発泡成
形体では、表面外観に肌荒れはなくいずれも良好であ
り、断面のセル構造も均一であった。As is clear from the table, the foamed molded product obtained by extrusion molding using the heat-expandable microcapsules of the present invention has good surface appearance without any roughening, and has a uniform cell structure in cross section. there were.
【0033】また、発泡成形体の密度は熱膨張性マイク
ロカプセルの配合量に応じて変化することを確認した。Further, it has been confirmed that the density of the foamed molded article changes according to the blending amount of the heat-expandable microcapsules.
【0034】(実施例2)熱可塑性樹脂として塩化ビニ
ルを用い、熱膨張性マイクロカプセルの配合量を変えた
3種類の押出成形を行った(実施例A〜C)。Example 2 Three types of extrusion molding were performed using vinyl chloride as the thermoplastic resin and changing the blending amount of the heat-expandable microcapsules (Examples A to C).
【0035】また、比較例として同一の熱可塑性樹脂原
料に化学発泡剤を添加した発泡押出成形を行った。As a comparative example, foam extrusion extrusion was performed by adding a chemical foaming agent to the same thermoplastic resin raw material.
【0036】使用樹脂は重合度800の塩化ビニルを用
い、安定剤として鉛系の鉛ステアレートを0.5部、添
加した。The resin used was vinyl chloride having a degree of polymerization of 800, and 0.5 part of lead-based lead stearate was added as a stabilizer.
【0037】熱膨張性マイクロカプセルとして実施例1
と同一の商品名:エクスパンセル(日本フィライト製)
を用いた。Example 1 as a heat-expandable microcapsule
Same product name as: Expancel (Nippon Philite)
Was used.
【0038】熱膨張性マイクロカプセルの配合量は熱可
塑性樹脂100部に対して1.5 、3、10部の3種類と
した。The amounts of the heat-expandable microcapsules were 1.5, 3, and 10 parts per 100 parts of the thermoplastic resin.
【0039】比較例の化学発泡剤はアゾジカーボンアミ
ドを用いた。Azodicarbonamide was used as the chemical blowing agent of the comparative example.
【0040】その他滑剤としてカルシウムステアレート
を0.5部添加するとともに、種々の助剤として充填
剤、顔料などを添加した。In addition, 0.5 part of calcium stearate was added as a lubricant, and fillers, pigments and the like were added as various auxiliaries.
【0041】こうして得られた発泡成形体の密度を測定
するとともに、表面外観および断面のセル構造を観察
し、その結果を表3に示した。The density of the foam molded article thus obtained was measured, and the surface appearance and the cell structure of the cross section were observed. The results are shown in Table 3.
【0042】[0042]
【表3】 [Table 3]
【0043】同表からも明らかなように、この発明の熱
膨張性マイクロカプセルを用いた押出成形による発泡成
形体では、表面外観に肌荒れはなくいずれも良好であ
り、断面のセル構造も均一であった。As is clear from the table, the foamed molded article obtained by extrusion molding using the heat-expandable microcapsules of the present invention has good surface appearance without any roughening, and has a uniform cell structure in cross section. there were.
【0044】また、発泡成形体の密度は熱膨張性マイク
ロカプセルの配合量に応じて変化することを確認した。Further, it was confirmed that the density of the foamed molded article changed according to the blending amount of the heat-expandable microcapsules.
【0045】なお、上記実施例1,2では、熱膨張性マ
イクロカプセルの配合量を熱可塑性樹脂原料100部に
対して1.5部から10分までの場合で説明したが、発
泡成形体として必要な比重などに応じて適宜変更可能で
あり、これら実施例1,2に限定するものでない。In Examples 1 and 2, the amount of the heat-expandable microcapsules was from 1.5 parts to 10 minutes based on 100 parts of the thermoplastic resin raw material. It can be appropriately changed according to the required specific gravity and the like, and is not limited to Examples 1 and 2.
【0046】[0046]
【発明の効果】以上、一実施の形態とともに具体的に説
明したようにこの発明の熱可塑性樹脂の発泡成形方法に
よれば、熱膨張性のマイクロカプセルを熱可塑性樹脂に
混合するようにし、この熱膨張性マイクロカプセルを混
練溶融熱で膨張させて押出成形または射出成形で発泡成
形するようにしたので、各気泡をマイクロカプセルによ
って安定して発泡させ、細かく均一で緻密な発泡状態に
でき、表面がきれいで、しかも目的とする比重に発泡さ
せることができる。According to the method for foaming and molding a thermoplastic resin of the present invention, as described above in detail together with one embodiment, the thermally expandable microcapsules are mixed with the thermoplastic resin. Since the heat-expandable microcapsules are expanded by extruding or injection molding by expanding by kneading and melting heat, each bubble can be stably foamed by the microcapsules, and a fine, uniform and dense foaming state can be obtained. But it can be foamed to the desired specific gravity.
【0047】これにより、事務機器用発泡ローラの紙送
りに必要な均一で緻密な気泡の表面特性としたり、建材
の軽量で断熱性に優れた特性にしたり、靴底用スポンジ
などのクッション性を持ち、水を浸透させない特性にす
ることが簡単にできる。Thus, the uniform and dense air bubbles required for paper feeding of the foaming roller for office equipment can be provided, the lightweight and heat insulating properties of building materials can be improved, and the cushioning properties of sponges for shoe soles can be improved. It can easily be made to have characteristics that make it impermeable to water.
Claims (1)
による発泡成形方法において、熱可塑性樹脂原料に熱膨
張性マイクロカプセルを混合し、押出成形または射出成
形による混練溶融熱によって当該熱膨張性マイクロカプ
セルを膨張させて成形することを特徴とする熱可塑性樹
脂の発泡成形方法。In a foam molding method by extrusion molding or injection molding of a thermoplastic resin, a heat-expandable microcapsule is mixed with a thermoplastic resin raw material, and the heat-expandable microcapsule is heated by kneading and melting heat by extrusion molding or injection molding. And foaming the thermoplastic resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8327728A JPH10152575A (en) | 1996-11-22 | 1996-11-22 | Method for foaming thermoplastic resin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8327728A JPH10152575A (en) | 1996-11-22 | 1996-11-22 | Method for foaming thermoplastic resin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10152575A true JPH10152575A (en) | 1998-06-09 |
Family
ID=18202330
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8327728A Pending JPH10152575A (en) | 1996-11-22 | 1996-11-22 | Method for foaming thermoplastic resin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10152575A (en) |
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| JP2006517859A (en) * | 2003-02-18 | 2006-08-03 | インクロ リミテッド | Dispensing nozzle |
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| WO2007074773A1 (en) * | 2005-12-27 | 2007-07-05 | Sekisui Chemical Co., Ltd. | Molded foam article and method of producing molded foam article |
| JP2008037524A (en) * | 2006-08-02 | 2008-02-21 | Sumitomo Rubber Ind Ltd | Manufacturing method for paper feeding roller and paper feeding roller |
| KR101433382B1 (en) * | 2007-03-31 | 2014-08-26 | 브루그 로드 아게, 홀딩 | Flexible heat-insulated pipes |
| JP2008256209A (en) * | 2007-03-31 | 2008-10-23 | Brugg Rohr Ag Holding | Flexible heat insulating conduit |
| JP2009286969A (en) * | 2008-05-30 | 2009-12-10 | Ix Co Ltd | Resin foamed sheet, laminated resin sheet having the same and method of manufacturing the same |
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| US11213093B2 (en) | 2013-02-13 | 2022-01-04 | Adidas Ag | Cushioning element for sports apparel |
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| CN106457627A (en) * | 2014-05-06 | 2017-02-22 | 泰科电子公司 | Substrate with a low dielectric constant material and method of molding |
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