JPH061872A - Production of open-cell foam - Google Patents
Production of open-cell foamInfo
- Publication number
- JPH061872A JPH061872A JP4200088A JP20008892A JPH061872A JP H061872 A JPH061872 A JP H061872A JP 4200088 A JP4200088 A JP 4200088A JP 20008892 A JP20008892 A JP 20008892A JP H061872 A JPH061872 A JP H061872A
- Authority
- JP
- Japan
- Prior art keywords
- styrene
- weight
- open
- parts
- thermoplastic elastomer
- 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.)
- Granted
Links
- 239000006260 foam Substances 0.000 title claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims abstract description 49
- 229920002725 thermoplastic elastomer Polymers 0.000 claims abstract description 20
- KAKZBPTYRLMSJV-UHFFFAOYSA-N butadiene group Chemical group C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229920013716 polyethylene resin Polymers 0.000 claims abstract description 9
- 229920001400 block copolymer Polymers 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 27
- 239000000203 mixture Substances 0.000 claims description 24
- 239000004088 foaming agent Substances 0.000 claims description 13
- 239000003431 cross linking reagent Substances 0.000 claims description 10
- 229920006465 Styrenic thermoplastic elastomer Polymers 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 9
- 229910052751 metal Inorganic materials 0.000 abstract description 5
- 239000002184 metal Substances 0.000 abstract description 5
- 229920001971 elastomer Polymers 0.000 abstract description 4
- 239000005060 rubber Substances 0.000 abstract description 4
- 239000004971 Cross linker Substances 0.000 abstract description 3
- 239000004604 Blowing Agent Substances 0.000 abstract 1
- 238000005984 hydrogenation reaction Methods 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 23
- 210000005056 cell body Anatomy 0.000 description 13
- 229920005989 resin Polymers 0.000 description 13
- 239000011347 resin Substances 0.000 description 13
- 238000005187 foaming Methods 0.000 description 12
- 238000010438 heat treatment Methods 0.000 description 11
- -1 polyethylene Polymers 0.000 description 9
- 238000004132 cross linking Methods 0.000 description 8
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 7
- 238000007906 compression Methods 0.000 description 7
- 230000006835 compression Effects 0.000 description 7
- 229920001684 low density polyethylene Polymers 0.000 description 7
- 239000004702 low-density polyethylene Substances 0.000 description 7
- 238000004891 communication Methods 0.000 description 6
- 239000005038 ethylene vinyl acetate Substances 0.000 description 6
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 6
- 239000004793 Polystyrene Substances 0.000 description 4
- 229920002223 polystyrene Polymers 0.000 description 4
- 125000000383 tetramethylene group Chemical group [H]C([H])([*:1])C([H])([H])C([H])([H])C([H])([H])[*:2] 0.000 description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 3
- 239000005977 Ethylene Substances 0.000 description 3
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 238000007493 shaping process Methods 0.000 description 3
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004156 Azodicarbonamide Substances 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000005062 Polybutadiene Substances 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-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
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 150000001451 organic peroxides Chemical class 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 229920002857 polybutadiene Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical class [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- 239000003566 sealing material Substances 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical class [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 229920005992 thermoplastic resin Polymers 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- 235000014692 zinc oxide Nutrition 0.000 description 2
- ASRMWYDEZPXXBA-UHFFFAOYSA-N (sulfonylamino)urea Chemical class NC(=O)NN=S(=O)=O ASRMWYDEZPXXBA-UHFFFAOYSA-N 0.000 description 1
- CHILLBMGESTNSK-UHFFFAOYSA-N 1-butylperoxy-2,3-di(propan-2-yl)benzene Chemical group CCCCOOC1=CC=CC(C(C)C)=C1C(C)C CHILLBMGESTNSK-UHFFFAOYSA-N 0.000 description 1
- YGLLDLZWOUVWCY-UHFFFAOYSA-N 1-butylperoxyhex-1-yne Chemical group C(CCC)OOC#CCCCC YGLLDLZWOUVWCY-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- MWRWFPQBGSZWNV-UHFFFAOYSA-N Dinitrosopentamethylenetetramine Chemical compound C1N2CN(N=O)CN1CN(N=O)C2 MWRWFPQBGSZWNV-UHFFFAOYSA-N 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical group O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- AZFNGPAYDKGCRB-XCPIVNJJSA-M [(1s,2s)-2-amino-1,2-diphenylethyl]-(4-methylphenyl)sulfonylazanide;chlororuthenium(1+);1-methyl-4-propan-2-ylbenzene Chemical class [Ru+]Cl.CC(C)C1=CC=C(C)C=C1.C1=CC(C)=CC=C1S(=O)(=O)[N-][C@@H](C=1C=CC=CC=1)[C@@H](N)C1=CC=CC=C1 AZFNGPAYDKGCRB-XCPIVNJJSA-M 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- UPIWXMRIPODGLE-UHFFFAOYSA-N butyl benzenecarboperoxoate Chemical group CCCCOOC(=O)C1=CC=CC=C1 UPIWXMRIPODGLE-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000002832 nitroso derivatives Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920005678 polyethylene based resin Polymers 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 239000004323 potassium nitrate Chemical class 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000004304 potassium nitrite Chemical class 0.000 description 1
- 235000010289 potassium nitrite Nutrition 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 229910001261 rose's metal Inorganic materials 0.000 description 1
- 238000010058 rubber compounding Methods 0.000 description 1
- DUIOPKIIICUYRZ-UHFFFAOYSA-N semicarbazide Chemical compound NNC(N)=O DUIOPKIIICUYRZ-UHFFFAOYSA-N 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229920006132 styrene block copolymer Polymers 0.000 description 1
- 125000003011 styrenyl group Chemical group [H]\C(*)=C(/[H])C1=C([H])C([H])=C([H])C([H])=C1[H] 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、連続気泡体の製造方法
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an open cell body.
【0002】[0002]
【従来の技術】従来、架橋ポリオレフィン連続気泡体の
製造方法としては、密閉金型中で発泡性架橋性組成物中
の発泡剤と架橋剤を部分的に分解させ、常圧下で残存す
る発泡剤と架橋剤を分解させて独立気泡体を得、次いで
得られた独立気泡体を圧縮して独立気泡を破壊する方法
が提案されていた(特公昭59−23545号及び特開
昭56−146732号参照)。しかし、このような方
法では、加圧された密閉金型中において加熱により発泡
剤及び架橋剤の分解が行われ、架橋反応は生じているが
気泡の形成は行われておらず、除圧時に初めて発泡する
ことになる。すなわち、まず架橋反応を生ぜしめ、しか
る後に発泡を行わせる方法を採用しており、独立気泡体
の製造段階においていわゆる先架橋が行われているた
め、気泡膜が強靭なものとなる。従って、独立気泡の連
通化が困難であり、連続気泡率100%又は100%に
近い気泡体を得ることができなかった。2. Description of the Related Art Conventionally, as a method for producing a crosslinked polyolefin open-celled body, a foaming agent which partially decomposes a foaming agent and a crosslinking agent in a foamable crosslinkable composition in a closed mold and remains under normal pressure. A method has been proposed in which the cross-linking agent is decomposed to obtain a closed cell body, and then the obtained closed cell body is compressed to break the closed cell body (JP-B-59-23545 and JP-A-56-146732). reference). However, in such a method, the foaming agent and the cross-linking agent are decomposed by heating in a closed mold under pressure, and although the cross-linking reaction occurs, the formation of bubbles is not performed, and at the time of depressurization. It will foam for the first time. That is, a method of first causing a crosslinking reaction and then performing foaming is adopted, and so-called pre-crosslinking is performed in the manufacturing stage of the closed cell body, so that the cell membrane becomes tough. Therefore, it is difficult to connect the closed cells to each other, and it is impossible to obtain a foam body having an open cell ratio of 100% or close to 100%.
【0003】上記問題を解決するため、本出願人は、発
泡性架橋性組成物を所望の形状に加熱整形した後、常圧
下にて加熱して架橋剤及び発泡剤を同時進行的に分解さ
せて気泡体を生成させ、次いで機械的変形を加えて気泡
を連通化させる方法を開発した(特公昭62−1929
4号、特公平1−44499号参照)。In order to solve the above-mentioned problems, the applicant of the present invention heats and shapes the expandable crosslinkable composition into a desired shape and then heats it under normal pressure to decompose the crosslinker and the foaming agent simultaneously in a progressive manner. To generate bubbles, and then mechanically deform the bubbles to make them communicate with each other (Japanese Patent Publication No. Sho 62-1929).
No. 4, Japanese Patent Publication No. 1-44499).
【0004】[0004]
【発明が解決しようとする課題】前記した本出願人の方
法によれば、100%又は100%に近い連続気泡率を
有する連続気泡体を得ることができる。しかしながら、
この方法は、低密度ポリエチレン又はエチレン−酢酸ビ
ニル共重合体を基材とした連続気泡体の製造方法を開示
したものであり、ポリエチレン又はエチレン−酢酸ビニ
ル共重合体を基材とした連続気泡体は、耐熱温度が低い
ため、用途が制限されていた。一方、この方法をポリプ
ロピレンに適用すると、耐熱性は向上するが、ゴム弾性
に劣り、パッキン材、シール材等の用途には使用できな
い。According to the method of the present applicant described above, it is possible to obtain an open cell body having an open cell rate of 100% or close to 100%. However,
This method discloses a method for producing an open cell based on low density polyethylene or an ethylene-vinyl acetate copolymer, and an open cell based on polyethylene or an ethylene-vinyl acetate copolymer. Has a limited heat-resistant temperature, so its use was limited. On the other hand, when this method is applied to polypropylene, the heat resistance is improved, but the rubber elasticity is poor, and it cannot be used for applications such as packing materials and sealing materials.
【0005】従って、本発明の目的は、前記したような
従来の欠点を解消し、エチレン−酢酸ビニル共重合体又
は低密度ポリエチレンを基材とした連続気泡体よりも耐
熱性が高く、且つ、ゴム弾性に優れた連続気泡体の製造
方法を提供することにある。Therefore, an object of the present invention is to solve the above-mentioned conventional drawbacks, have a higher heat resistance than an open cell body based on an ethylene-vinyl acetate copolymer or low density polyethylene, and An object of the present invention is to provide a method for producing an open cell body having excellent rubber elasticity.
【0006】[0006]
【課題を解決するための手段】本発明によれば、前記目
的を達成するため、スチレン系熱可塑性エラストマーに
発泡剤及び架橋剤を添加混練し、得られた発泡性架橋性
組成物を気密でない金型中で加熱発泡させて気泡体を生
成させ、次いで機械的変形を加えて気泡を連通化させる
ことを特徴とする連続気泡体の製造方法が提供される。
本発明の方法において、成形性を良くするために、スチ
レン系熱可塑性エラストマー99〜20重量部にポリエ
チレン系樹脂1〜80重量部を添加することが好まし
い。又、スチレン系熱可塑性エラストマー70〜30重
量部にポリエチレン系樹脂30〜70重量部を添加する
と、成形性が更に改善される。According to the present invention, in order to achieve the above object, a foaming agent and a crosslinking agent are added and kneaded to a styrene thermoplastic elastomer, and the resulting foamable crosslinking composition is not airtight. Provided is a method for producing an open-cell body, which comprises foaming by heat-foaming in a mold to form a cell, and then mechanically deforming the cell to make the cells communicate with each other.
In the method of the present invention, in order to improve moldability, it is preferable to add 1 to 80 parts by weight of a polyethylene resin to 99 to 20 parts by weight of the styrene thermoplastic elastomer. Further, by adding 30 to 70 parts by weight of the polyethylene resin to 70 to 30 parts by weight of the styrene thermoplastic elastomer, the moldability is further improved.
【0007】[0007]
【発明の作用及び態様】本発明の方法によれば、上記の
ように、スチレン系熱可塑性エラストマーを基材の樹脂
として使用する。スチレン系熱可塑性エラストマーは、
SBS(スチレン−ブタジエン−スチレンブロックコポ
リマー)系とSEBS(スチレン−エチレン−ブチレン
−スチレンブロックコポリマー)系に大別される。スチ
レン系熱可塑性エラストマーの構造は、ポリスチレン部
分とポリブタジエン(又はエチレン/ブチレン)部分は
互いに非相溶であり、ポリブタジエン(又はエチレン/
ブチレン)の海の中にポリスチレンが島となって分散さ
れている。常温では、このポリスチレン部分がブタジエ
ン(又はエチレン/ブチレン)部分を拘束するが、高温
下(成形加工)において、ポリスチレンが溶融し、熱可
塑性を示すため、熱可塑性樹脂と同様に容易に成形でき
る。又、スチレン系熱可塑性エラストマーはゴムのよう
な弾性と粘性を有しているため、得られた発泡体が特殊
な気泡構造を有し、容易に水を通さず、止水性に優れ
る。According to the method of the present invention, as described above, the styrene-based thermoplastic elastomer is used as the resin for the base material. Styrenic thermoplastic elastomer is
It is roughly classified into SBS (styrene-butadiene-styrene block copolymer) system and SEBS (styrene-ethylene-butylene-styrene block copolymer) system. The structure of the styrene-based thermoplastic elastomer is such that the polystyrene portion and the polybutadiene (or ethylene / butylene) portion are incompatible with each other, and the polybutadiene (or ethylene / butylene)
Butylene) has polystyrene dispersed as islands in the sea. At room temperature, this polystyrene part restrains the butadiene (or ethylene / butylene) part, but at high temperature (molding process), polystyrene melts and exhibits thermoplasticity, so that it can be molded as easily as a thermoplastic resin. Further, since the styrene-based thermoplastic elastomer has elasticity and viscosity similar to rubber, the obtained foam has a special cell structure, does not easily pass water, and is excellent in waterproofness.
【0008】本発明の連続気泡体を得る方法としては、
基材樹脂に発泡剤及び架橋剤を添加混練し、得られた発
泡性架橋性組成物を加熱発泡させて気泡体を形成させ、
次いで機械的変形を加えて気泡を連通化させる方法であ
れば、従来公知の方法が適用でき、特に限定されない。
このような方法のうち、特に特公昭62−19294号
公報及び特公平1−44499号公報に記載されている
ように、発泡性架橋性組成物を所望の形状に加熱整形し
た後、気密でない金型中で常圧下にて加熱して架橋剤及
び発泡剤を同時進行的に分解させて気泡体を形成させ、
次いで機械的変形を加えて気泡を連通化させる方法にお
いて、本発明の効果は特に顕著である。As a method for obtaining the open-cell body of the present invention,
A base material resin is kneaded with a foaming agent and a cross-linking agent, and the foamable cross-linkable composition obtained is heat-foamed to form a foam,
A conventionally known method can be applied as long as it is a method of making mechanical communication to make bubbles communicate with each other and is not particularly limited.
Among such methods, as described in Japanese Patent Publication No. 62-19294 and Japanese Patent Publication No. 1-44499, the foamable crosslinkable composition is heat-molded into a desired shape, and then is not hermetically sealed. By heating in a mold under normal pressure, the crosslinking agent and the foaming agent are simultaneously decomposed to form a foam body,
Then, the effect of the present invention is particularly remarkable in the method in which the bubbles are communicated by applying mechanical deformation.
【0009】以下、本発明に係る連続気泡体の製造方法
についてその好適な態様を具体的に説明する。まず、基
材樹脂として、スチレン系熱可塑性エラストマーを使用
する。スチレン系熱可塑性エラストマーは、スチレン系
熱可塑性樹脂としては、一般式、A−(B−A)n、
(ここで、Aはスチレン、Bはブタジエンであり、nは
1〜5の整数。)で表わされるブロック共重合体の水素
添加誘導体を主成分とするものが好ましく、ポリプロピ
レン等のポリオレフィン樹脂、各種軟化剤、充填剤等が
適宜添加される(例えば、三菱油化株式会社製、商品名
「ラバロン」)。該水素添加誘導体は、スチレン−ブタ
ジエン−スチレンブロックコポリマーのブタジエン部分
を高度に水添することにより、主鎖及び側鎖の二重結合
部分を飽和させたものであるため、耐候性、耐熱性に特
に優れている。成形性を改善するために、該組成物99
〜20重量部にポリエチレン系樹脂1〜80重量部を添
加することが好ましい。特に好ましくは、該組成物70
重量部〜30重量部にポリエチレン系樹脂30〜70重
量部を添加する。上記の様な基材樹脂又は基材樹脂とポ
リエチレン系樹脂との混合物に発泡剤、架橋剤、及び必
要に応じて発泡助剤、充填剤、顔料等を添加し、これを
加熱したミキシングロール、加圧形ニーダー、バンバリ
ーミキサー、押出機等によって練和する。上記のように
練和して得られた発泡性架橋性組成物を金型に仕込み、
プレスにて加圧下で樹脂及び架橋剤の種類に応じて11
5℃〜165℃、好ましくは、120℃〜150℃にお
いて加熱整形する。この加熱整形工程において、発泡性
架橋性組成物を、好ましくはゲル分率ゼロの状態に維持
して整形することが、連続気泡率100%又は100%
に近い連続気泡体を得る条件である。ここで、ゲル分率
とは200メッシュの金網の中にサンプルを入れ、ソッ
クスレー抽出器により溶媒トリクロルエチレン還流下で
24時間抽出を行って測定した抽出前サンプルと抽出後
サンプルの重量比である。なお、この加熱整形工程にお
いて、非常に微量の発泡剤が初期分解を生じ、整形した
組成物を金型から取り出した場合に2倍程度まで膨張し
得るが、これは発泡という概念からは程遠く、本発明に
とって何ら差し支えない。A preferred embodiment of the method for producing an open-cell body according to the present invention will be specifically described below. First, a styrene-based thermoplastic elastomer is used as the base resin. The styrene-based thermoplastic elastomer is a styrene-based thermoplastic resin represented by the general formula: A- (BA) n ,
(Wherein A is styrene, B is butadiene, and n is an integer of 1 to 5), and those containing a hydrogenated derivative of a block copolymer as a main component are preferable, and polyolefin resins such as polypropylene and various types. A softener, a filler and the like are appropriately added (for example, trade name "Lavalon" manufactured by Mitsubishi Petrochemical Co., Ltd.). The hydrogenated derivative is obtained by highly hydrogenating the butadiene portion of the styrene-butadiene-styrene block copolymer to saturate the double bond portions of the main chain and side chains, and therefore has high weather resistance and heat resistance. Especially excellent. In order to improve moldability, the composition 99
It is preferable to add 1 to 80 parts by weight of the polyethylene resin to 20 to 20 parts by weight. Particularly preferably, the composition 70
30 to 70 parts by weight of a polyethylene resin is added to 30 to 30 parts by weight. A foaming agent, a cross-linking agent, and a foaming auxiliary agent if necessary, a filler, a pigment, etc., to the mixture of the base material resin or the base material resin and the polyethylene-based resin as described above, and the mixing roll heated to this, Knead with a pressure type kneader, Banbury mixer, extruder or the like. Charge the foamable crosslinkable composition obtained by kneading as described above into a mold,
Depending on the type of resin and crosslinker under pressure in a press, 11
Heat shaping is performed at 5 ° C to 165 ° C, preferably 120 ° C to 150 ° C. In this heat shaping step, it is preferable that the foamable crosslinkable composition is shaped while maintaining the gel fraction at zero, and the open cell ratio is 100% or 100%.
This is a condition for obtaining an open cell body close to. Here, the gel fraction is the weight ratio of the sample before extraction and the sample after extraction measured by putting the sample in a wire mesh of 200 mesh and performing extraction for 24 hours under reflux of the solvent trichlorethylene with a Soxhlet extractor. In this heat shaping step, a very small amount of the foaming agent causes initial decomposition, and when the shaped composition is taken out of the mold, it can expand up to about twice, but this is far from the concept of foaming. There is no problem for the present invention.
【0010】上記のようにして得られた整形した組成物
は、次いで、常圧下にて加熱することによって、架橋剤
及び発泡剤の分解を同時進行的に行わしめられる。この
発泡・架橋工程は、例えば、整形した組成物を所望の断
面形状、寸法を有する気密でない、すなわち密閉されて
いない金型中に入れ、該金型の金属板を外部から加熱す
ることによって上記組成物を間接的に加熱せしめる。間
接的に加熱せしめる方法としては、例えば金属板外表面
にヒーターを密着させて加熱するか、あるいは金属板に
熱媒の流路を設け、ジャケット方式で蒸気、加熱オイル
等によって加熱する方法がある。あるいは、中間発泡体
を気密でない開閉式の金型に入れ、ローゼ合金、ウッド
合金などを用いるメタルバスやオイルバス中、硝酸ナト
リウム、硝酸カリウム、亜硝酸カリウム等の塩の1種又
は2種以上の溶融塩を用いる塩浴中、もしくは窒素気流
中で、あるいは伸張(ないし拡張)可能な鉄板等により
覆われた状態で直接加熱せしめる。又は、高周波を用い
て加熱しても良い。上記の方法によって、所定時間加熱
した後、冷却して気泡体を得る。加熱温度は、使用する
ポリオレフィンの種類に応じて140℃〜210℃、好
ましくは150℃〜180℃の範囲に設定する。加熱時
間は、好ましくは30〜300分、さらに好ましくは1
00〜200分である。このようにして、機械的変形を
与えることによって容易に破壊しうる気泡膜を有し、か
つ従来の気泡体と同程度の架橋度(ゲル分率90%程度
まで)を有する気泡体が得られる。The shaped composition thus obtained is then heated under normal pressure to simultaneously decompose the crosslinking agent and the foaming agent. This foaming / crosslinking step is carried out, for example, by placing the shaped composition in a mold that is not airtight, that is, has a desired cross-sectional shape and dimensions, that is, is not sealed, and heats the metal plate of the mold from the outside. The composition is allowed to heat indirectly. As a method of indirectly heating, for example, there is a method in which a heater is brought into close contact with the outer surface of a metal plate for heating, or a heat medium flow path is provided in the metal plate and heating is performed with steam, heating oil, etc. in a jacket method. . Alternatively, the intermediate foam is placed in a non-airtight open-close mold, and one or more salts of sodium nitrate, potassium nitrate, potassium nitrite, etc. are melted in a metal bath or oil bath using a rose alloy, wood alloy, or the like. It is heated directly in a salt bath using salt, in a nitrogen stream, or in a state covered with an expandable (or expandable) iron plate or the like. Alternatively, heating may be performed using high frequency. By the above method, after heating for a predetermined time, it is cooled to obtain a foam. The heating temperature is set in the range of 140 ° C to 210 ° C, preferably 150 ° C to 180 ° C, depending on the type of polyolefin used. The heating time is preferably 30 to 300 minutes, more preferably 1
It is from 00 to 200 minutes. In this way, a foam having a foam film that can be easily broken by applying mechanical deformation and having the same degree of crosslinking (up to about 90% gel fraction) as that of the conventional foam is obtained. .
【0011】以上のようにして得られた気泡体(いわゆ
る独立気泡体)は、次いで例えば等速二本ロール等によ
り圧縮変形を加えることによって気泡膜は破壊され、気
泡が連通化されて連続気泡体が得られる。等速二本ロー
ルの表面に無数の小さい針を設けるか、又は等速二本ロ
ールの前及び/又は後に無数の針を設けたロールを配置
して、該気泡体の表面に無数の小孔を開けることによっ
て、気泡の連通化を促進させることができる。この方法
によって、Remington Pariser法に基
づいて測定した連続気泡率で100%又は100%に近
い連続気泡体が得られる。The foamed body (so-called closed-celled body) obtained as described above is then subjected to compressive deformation by, for example, a constant-velocity two-roll roll, whereby the foamed film is destroyed, and the bubbles are made continuous to form continuous cells. The body is obtained. Innumerable small needles are provided on the surface of the constant velocity two rolls, or rolls provided with innumerable needles before and / or after the constant velocity two rolls are arranged, and innumerable small holes are formed on the surface of the foam. By opening the opening, communication of bubbles can be promoted. By this method, an open cell body having an open cell rate measured based on the Remington Pariser method is 100% or close to 100% is obtained.
【0012】本発明で用いられるポリエチレン系樹脂と
しては、例えば通常市販の高、中、低圧法により製造さ
れたポリエチレン、又は酢酸ビニル等との共重合体であ
る。本発明で用いられる発泡剤としては各種の化学発泡
剤、例えばアゾ系化合物のアゾジカルボンアミド、バリ
ウムアゾジカルボキシレート等:ニトロソ系化合物のジ
ニトロソペンタメチレンテトラミン、トリニトロソトリ
メチルトリアミン等;ヒドラジッド系化合物のp,p’
−オキシビスベンゼンスルホニルヒドラジッド等;スル
ホニルセミカルバジッド系化合物のp,p’−オキシビ
スベンゼンスルホニルセミカルジッド、トルエンスルホ
ニルセミカルバジッド等が好適に使用できるが、これら
に限定されるものではない。The polyethylene resin used in the present invention is, for example, a commercially available polyethylene produced by a high, medium or low pressure method, or a copolymer with vinyl acetate or the like. As the foaming agent used in the present invention, various chemical foaming agents, for example, azo compounds such as azodicarbonamide, barium azodicarboxylate, etc .: Nitroso compounds such as dinitrosopentamethylenetetramine, trinitrosotrimethyltriamine, etc .; Hydrazide compounds P, p '
-Oxybisbenzenesulfonyl hydrazide and the like; sulfonyl semicarbazide compounds such as p, p'-oxybisbenzenesulfonyl semicarbazide and toluenesulfonyl semicarbazide can be preferably used, but are not limited thereto. .
【0013】本発明で用いらる架橋剤としては、使用す
る樹脂の流動開始温度以上の分解温度を有するものであ
って、加熱により分解され、遊離ラジカルを発生してそ
の分子間もしくは分子内に架橋結合を生ぜしめるラジカ
ル発生剤であるところの有機過酸化物、例えばジクミル
パーオキサイド、1,1−ジーt−ブチルパーオキシー
3,3,5−トリメチルシクロヘキサン、2,5−ジメ
チルー2,5−ジーt−ブチルパーオキシヘキサン、
2,5−ジメチルー2,5−ジターシャリーブチルパー
オキシヘキシン、α、α−ジターシャリーブチルパーオ
キシジイソプロピルベンゼン、ターシャリーブチルパー
オキシケトン、ターシャリーブチルパーオキシベンゾエ
ート等があるが、その時に使用される樹脂の種類によっ
て最適な有機過酸化物を選ばなければならない。The cross-linking agent used in the present invention has a decomposition temperature higher than the flow initiation temperature of the resin used and is decomposed by heating to generate free radicals to generate intermolecular or intramolecular formation thereof. Organic peroxides that are radical generators that cause cross-linking, such as dicumyl peroxide, 1,1-di-t-butylperoxy-3,3,5-trimethylcyclohexane, 2,5-dimethyl-2,5 -Di-t-butylperoxyhexane,
There are 2,5-dimethyl-2,5-ditertiary butyl peroxyhexyne, α, α-ditertiary butyl peroxydiisopropylbenzene, tertiary butyl peroxyketone, tertiary butyl peroxybenzoate, etc. The optimum organic peroxide must be selected according to the type of resin used.
【0014】本発明に於ては、使用する組成物の物性の
改良或は価格の低下を目的として、架橋結合に著しい悪
影響を与えない配合剤(充填剤)、例えば酸化亜鉛、酸
化チタン、酸化カルシウム、酸化マグネシウム、酸化ケ
イ素等の金属酸化物、炭酸マグネシウム、炭酸カルシウ
ム等の炭酸塩、或はパルプ等の繊維物質、又は各種染
料、顔料並びに蛍光物質、その他の常用のゴム配合剤等
を必要に応じて添加することができる。In the present invention, for the purpose of improving the physical properties of the composition to be used or lowering the price, a compounding agent (filler) which does not exert a significant adverse effect on cross-linking, such as zinc oxide, titanium oxide, or oxidation. Metal oxides such as calcium, magnesium oxide and silicon oxide, carbonates such as magnesium carbonate and calcium carbonate, fiber materials such as pulp, various dyes, pigments and fluorescent materials, and other commonly used rubber compounding agents are required. Can be added according to
【0015】[0015]
【実施例】以下に実施例を挙げて本発明についてさらに
具体的に説明するが、本発明は下記実施例により何ら限
定されるものではない。 実施例1 スチレン系熱可塑性エラストマー(商品名:ラバロンS
J4400N、三菱油化(株)製)100重量部、アゾ
ジカルボンアミド17重量部、亜鉛華0.03重量部、
ステアリン酸亜鉛0.01重量部、尿素0.01重量
部、ジクミルパーオキサイド0.8重量部からなる組成
物を110℃のミキシングロールにて練和し、135℃
に加熱されたプレス内の金型(160x160x37m
m)に上記練和物を充填し、上記温度で50分間加圧下
で加熱し、前記組成物を整形した。次いで、該組成物
を、既に170℃に加熱されている気密でない開閉式の
金型(500x500x100mm)に入れ、ジャケッ
ト式により170℃の蒸気で140分間加熱し、冷却後
取り出し、発泡体を得た。得られた発泡体をロール間隔
20mmに設定した等速二本ロールの間を4回通過させ
て気泡を破壊させ、気泡の連通化を行った。得られた連
通後の表皮付発泡体のサイズは500x500x100
mmであり、みかけ密度0.027g/cm3、連続気
泡率100%であり、内部の気泡が均一であった。JI
S K 6767に準拠して、得られた連続気泡体の圧
縮永久歪を測定(50%、70℃で22時間圧縮し、2
0℃で(a)1時間放置、(b)24時間放置)した結
果、(a)34%、(b)35%であり、耐熱性の高い
ことがわかった。The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to the following examples. Example 1 Styrenic thermoplastic elastomer (trade name: Lavalon S
J4400N, manufactured by Mitsubishi Petrochemical Co., Ltd.) 100 parts by weight, azodicarbonamide 17 parts by weight, zinc white 0.03 parts by weight,
A composition comprising 0.01 parts by weight of zinc stearate, 0.01 parts by weight of urea, and 0.8 parts by weight of dicumyl peroxide was kneaded with a mixing roll at 110 ° C., and 135 ° C.
The mold in the press (160x160x37m)
m) was filled with the above kneaded product and heated at the above temperature for 50 minutes under pressure to shape the composition. Next, the composition was placed in a non-airtight open-close mold (500 x 500 x 100 mm) that had already been heated to 170 ° C, heated by steam at 170 ° C for 140 minutes by a jacket type, taken out after cooling, and a foam was obtained. . The obtained foam was passed between two constant-velocity two-rolls set at a roll interval of 20 mm four times to break the bubbles, thereby making the bubbles continuous. The size of the obtained foam with skin after communication is 500x500x100.
mm, the apparent density was 0.027 g / cm 3 , the open cell ratio was 100%, and the cells inside were uniform. JI
In accordance with SK 6767, the compression set of the obtained open-cell body was measured (50%, compressed at 70 ° C. for 22 hours, and
As a result of (a) left for 1 hour and (b) left for 24 hours at 0 ° C., the results were (a) 34% and (b) 35%, showing high heat resistance.
【0016】実施例2 スチレン系熱可塑性エラストマー(前出)70重量部と
低密度ポリエチレン(商品名:ユカロンYF−30、M
FR1.0、密度0.920g/cm3三菱油化株式会
社製)30重量部を混合し、混合した樹脂100重量部
にジクミルパーオキサイドを0.7重量部添加した以外
は、実施例1と同じ配合及び同じ発泡条件、連通化条件
で、連続気泡体を得た。得られた連続気泡体のサイズ、
見掛け密度及び連続気泡率は、実施例1と同じであり、
実施例1と同じ方法で圧縮永久歪を測定した結果、
(a)35%、(b)36%であり、耐熱性の高いこと
がわかった。Example 2 70 parts by weight of styrene thermoplastic elastomer (described above) and low density polyethylene (trade name: Yucaron YF-30, M
Example 1 except that 30 parts by weight of FR 1.0, density 0.920 g / cm 3 manufactured by Mitsubishi Petrochemical Co., Ltd.) were mixed, and 0.7 parts by weight of dicumyl peroxide was added to 100 parts by weight of the mixed resin. An open-cell body was obtained under the same composition, the same foaming conditions and the same communication conditions. The size of the obtained open cells,
The apparent density and the open cell ratio are the same as in Example 1,
As a result of measuring the compression set by the same method as in Example 1,
(A) was 35% and (b) was 36%, showing that the heat resistance was high.
【0017】実施例3 スチレン系熱可塑性エラストマー(前出)50重量部と
低密度ポリエチレン(前出)50重量部を混合し、混合
した樹脂100重量部にジクミルパーオキサイドを0.
6重量部添加した以外は、実施例1と同じ配合及び同じ
発泡条件、連通化条件で、連続気泡体を得た。得られた
連続気泡体のサイズ、見掛け密度及び連続気泡率は、実
施例1と同じであり、実施例1と同じ方法で圧縮永久歪
を測定した結果、(a)36%、(b)37%であり、
耐熱性の高いことがわかった。 実施例4 スチレン系熱可塑性エラストマー(前出)30重量部と
低密度ポリエチレン(前出)70重量部を混合し、混合
した樹脂100重量部にジクミルパーオキサイドを0.
5重量部添加した以外は、実施例1と同じ配合及び同じ
発泡条件、連通化条件で、連続気泡体を得た。得られた
連続気泡体のサイズ、見掛け密度及び連続気泡率は、実
施例1と同じであり、実施例1と同じ方法で圧縮永久歪
を測定した結果、(a)37%、(b)38%であり、
耐熱性の高いことがわかった。Example 3 50 parts by weight of a styrene-based thermoplastic elastomer (described above) and 50 parts by weight of low-density polyethylene (described above) were mixed, and 100 parts by weight of the mixed resin was mixed with dicumyl peroxide of 0.
An open-cell body was obtained under the same composition, the same foaming conditions, and the same communication conditions as in Example 1 except that 6 parts by weight was added. The size, apparent density, and open cell ratio of the obtained open-cell body were the same as in Example 1, and the compression set was measured by the same method as in Example 1, resulting in (a) 36% and (b) 37. %,
It turned out that it has high heat resistance. Example 4 30 parts by weight of a styrene-based thermoplastic elastomer (described above) and 70 parts by weight of low density polyethylene (described above) were mixed, and 100 parts by weight of the mixed resin was mixed with dicumyl peroxide in an amount of 0.
An open-cell body was obtained under the same composition, the same foaming conditions, and the same communication conditions as in Example 1 except that 5 parts by weight was added. The size, apparent density and open cell ratio of the obtained open-cell body were the same as in Example 1, and the compression set was measured by the same method as in Example 1, and as a result, (a) 37%, (b) 38 %,
It turned out that it has high heat resistance.
【0018】比較例1 スチレン系熱可塑性エラストマー(前出)10重量部と
低密度ポリエチレン(前出)90重量部を混合し、混合
した樹脂100重量部にジクミルパーオキサイドを0.
45重量部添加した以外は、実施例1と同じ配合及び同
じ発泡条件、連通化条件で、連続気泡体を得た。得られ
た連続気泡体のサイズ、見掛け密度及び連続気泡率は、
実施例1と同じであり、実施例1と同じ方法で圧縮永久
歪を測定した結果、(a)43%、(b)43%であ
り、耐熱性が低く、熱圧成形されて厚みが回復しなかっ
た。 比較例2 エチレン−酢酸ビニル共重合体(商品名エバフレックス
P1403、酢酸ビニル含有率14重量%、デュポン−
三井ポリケミカル株式会社製)100重量部にジクミル
パーオキサイド0.6重量部を添加した以外は、実施例
1と同じ配合を用意し、ミキシングロールの温度を90
℃にした以外は、実施例1と同じ発泡及び連通化条件で
連続気泡体を得た。得られた連続気泡体のサイズ、見掛
け密度及び連続気泡率は、実施例1と同じであり、実施
例1と同じ方法で圧縮永久歪を測定した結果、(a)4
3%、(b)43%であり、耐熱性が低く、熱圧成形さ
れて厚みが回復しなかった。Comparative Example 1 10 parts by weight of a styrene-based thermoplastic elastomer (previously described) and 90 parts by weight of low density polyethylene (previously described) were mixed, and 100 parts by weight of the mixed resin was mixed with dicumyl peroxide in an amount of 0.
An open-cell body was obtained under the same composition, the same foaming conditions and communicating conditions as in Example 1 except that 45 parts by weight was added. The size, apparent density and open cell ratio of the obtained open cell body are
The compression set was the same as in Example 1, and the compression set was measured by the same method as in Example 1. As a result, (a) 43%, (b) 43%, the heat resistance was low, and the thickness was restored by thermocompression molding. I didn't. Comparative Example 2 Ethylene-vinyl acetate copolymer (trade name: Evaflex P1403, vinyl acetate content 14% by weight, DuPont-
(Mitsui Polychemical Co., Ltd.) except that 0.6 part by weight of dicumyl peroxide was added to 100 parts by weight, the same formulation as in Example 1 was prepared, and the temperature of the mixing roll was 90.
An open-cell body was obtained under the same foaming and communicating conditions as in Example 1 except that the temperature was changed to ° C. The size, apparent density, and open cell ratio of the obtained open-cell body were the same as in Example 1, and the compression set was measured by the same method as in Example 1, and as a result, (a) 4
3% and (b) 43%, the heat resistance was low, and the thickness was not recovered by thermocompression molding.
【0019】[0019]
【発明の効果】以上のように、本発明の方法によれば、
スチレン系熱可塑性エラストマーを基材樹脂として使用
するため、得られる連続気泡体は、エチレン−酢酸ビニ
ル共重合体又は低密度ポリエチレンを基材とする連続気
泡体よりも、耐熱性に優れ、且つ、エチレン−酢酸ビニ
ル共重合体の連続気泡体と同等の弾性を有し、エアコ
ン、自動車等のパッキン材、シール材、断熱材として好
適である。又、スチレン系熱可塑性エラストマーにポリ
エチレン系樹脂を添加することにより、発泡工程におけ
る成形性及び加工性が良くなり、簡単な作業で物性が均
一で優れた連続気泡体を得ることができる。更に、スチ
レン系熱可塑性エラストマーとして、一般式、A−(B
−A)n、(ここで、Aはスチレン、Bはブタジエンで
あり、nは1〜5の整数。)で表わされるブロック共重
合体の水素添加誘導体を使用することによって、二重結
合がないため、耐熱性、耐候性に特に優れた連続気泡体
を得ることができる。As described above, according to the method of the present invention,
Since the styrene-based thermoplastic elastomer is used as the base resin, the obtained open cells have excellent heat resistance than the open cells having an ethylene-vinyl acetate copolymer or low density polyethylene as a base material, and It has elasticity equivalent to that of an open cell of ethylene-vinyl acetate copolymer, and is suitable as a packing material for air conditioners, automobiles, sealing materials, and heat insulating materials. Further, by adding a polyethylene resin to the styrene thermoplastic elastomer, the moldability and processability in the foaming step are improved, and it is possible to obtain an open cell body having uniform physical properties and excellent by simple work. Further, as the styrene-based thermoplastic elastomer, the general formula, A- (B
-A) n , (wherein A is styrene, B is butadiene, and n is an integer of 1 to 5), by using the hydrogenated derivative of the block copolymer, there is no double bond. Therefore, it is possible to obtain an open cell body having particularly excellent heat resistance and weather resistance.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B29K 105:04 C08L 25:00 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Office reference number FI technical display location B29K 105: 04 C08L 25:00
Claims (4)
剤及び架橋剤を添加混練し、得られた発泡性架橋性組成
物を気密でない金型中で加熱発泡させて気泡体を生成さ
せ、次いで機械的変形を加えて気泡を連通化させること
を特徴とする連続気泡体の製造方法1. A foaming agent and a cross-linking agent are added to and kneaded with a styrene-based thermoplastic elastomer, and the foamable cross-linkable composition obtained is heat-foamed in a mold that is not airtight to form a foam, and then mechanically. A method for producing an open-cell body, characterized in that deformation is applied to make the cells communicate with each other.
20重量部にポリエチレン系樹脂1〜80重量部を添加
したことを特徴とする請求項1記載の製造方法。2. A styrene-based thermoplastic elastomer 99 to
The production method according to claim 1, wherein 1 to 80 parts by weight of a polyethylene resin is added to 20 parts by weight.
30重量部とポリエチレン系樹脂30〜70重量部を添
加したことを特徴とする請求項1記載の製造方法。3. A styrene-based thermoplastic elastomer 70 to
The manufacturing method according to claim 1, wherein 30 parts by weight and 30 to 70 parts by weight of a polyethylene resin are added.
般式、A−(B−A)n、(ここで、Aはスチレン、B
はブタジエンであり、nは1〜5の整数。)で表わされ
るブロック共重合体の水素添加誘導体から成る請求項
1,2又は3記載の製造方法。4. The styrenic thermoplastic elastomer has the general formula A- (BA) n , where A is styrene and B.
Is butadiene, and n is an integer of 1 to 5. 4. The method according to claim 1, 2 or 3, which comprises a hydrogenated derivative of a block copolymer represented by
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20008892A JP3163588B2 (en) | 1992-06-16 | 1992-06-16 | Method for producing open-cell foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20008892A JP3163588B2 (en) | 1992-06-16 | 1992-06-16 | Method for producing open-cell foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH061872A true JPH061872A (en) | 1994-01-11 |
| JP3163588B2 JP3163588B2 (en) | 2001-05-08 |
Family
ID=16418659
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20008892A Expired - Fee Related JP3163588B2 (en) | 1992-06-16 | 1992-06-16 | Method for producing open-cell foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3163588B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005535476A (en) * | 2002-08-15 | 2005-11-24 | アドバンスド エラストマー システムズ,エル.ピー. | Thermoplastic elastomer with enhanced foaming and physical properties |
| US10702069B2 (en) | 2017-11-10 | 2020-07-07 | Grammer Ag | Vehicle seat comprising an adjustment device |
-
1992
- 1992-06-16 JP JP20008892A patent/JP3163588B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005535476A (en) * | 2002-08-15 | 2005-11-24 | アドバンスド エラストマー システムズ,エル.ピー. | Thermoplastic elastomer with enhanced foaming and physical properties |
| US10702069B2 (en) | 2017-11-10 | 2020-07-07 | Grammer Ag | Vehicle seat comprising an adjustment device |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3163588B2 (en) | 2001-05-08 |
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