JPH09123211A - Method for producing composite of foamed extrudate of thermoplastic elastomer and rubber molding, and composite produced by the method - Google Patents
Method for producing composite of foamed extrudate of thermoplastic elastomer and rubber molding, and composite produced by the methodInfo
- Publication number
- JPH09123211A JPH09123211A JP7285247A JP28524795A JPH09123211A JP H09123211 A JPH09123211 A JP H09123211A JP 7285247 A JP7285247 A JP 7285247A JP 28524795 A JP28524795 A JP 28524795A JP H09123211 A JPH09123211 A JP H09123211A
- Authority
- JP
- Japan
- Prior art keywords
- rubber
- producing
- thermoplastic elastomer
- foamed
- extrudate
- 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
- 229920002725 thermoplastic elastomer Polymers 0.000 title claims abstract description 31
- 239000002131 composite material Substances 0.000 title claims description 19
- 238000004519 manufacturing process Methods 0.000 title claims description 16
- 238000000034 method Methods 0.000 title claims description 10
- 238000010068 moulding (rubber) Methods 0.000 title claims 2
- 229920001971 elastomer Polymers 0.000 claims abstract description 42
- 239000005060 rubber Substances 0.000 claims abstract description 40
- 229920002397 thermoplastic olefin Polymers 0.000 claims abstract description 32
- 235000012438 extruded product Nutrition 0.000 claims abstract description 22
- 239000006260 foam Substances 0.000 claims abstract description 19
- 150000001875 compounds Chemical class 0.000 claims abstract description 14
- 150000001993 dienes Chemical class 0.000 claims abstract description 9
- 229920001897 terpolymer Polymers 0.000 claims abstract description 8
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 3
- 239000005977 Ethylene Substances 0.000 claims abstract description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims abstract description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 239000002994 raw material Substances 0.000 claims description 12
- 238000004073 vulcanization Methods 0.000 claims description 12
- 239000004088 foaming agent Substances 0.000 claims description 8
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 claims description 5
- 239000004743 Polypropylene Substances 0.000 claims description 4
- 229920000642 polymer Polymers 0.000 claims description 4
- -1 polypropylene Polymers 0.000 claims description 4
- 229920001155 polypropylene Polymers 0.000 claims description 4
- 238000005520 cutting process Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 229920005992 thermoplastic resin Polymers 0.000 claims description 3
- 239000000806 elastomer Substances 0.000 claims 1
- 229920002943 EPDM rubber Polymers 0.000 description 30
- 238000005187 foaming Methods 0.000 description 11
- 239000007787 solid Substances 0.000 description 9
- 239000000203 mixture Substances 0.000 description 7
- OJOWICOBYCXEKR-KRXBUXKQSA-N (5e)-5-ethylidenebicyclo[2.2.1]hept-2-ene Chemical compound C1C2C(=C/C)/CC1C=C2 OJOWICOBYCXEKR-KRXBUXKQSA-N 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 4
- 238000013329 compounding Methods 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 229920001821 foam rubber Polymers 0.000 description 3
- 238000009472 formulation Methods 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 229920003031 santoprene Polymers 0.000 description 3
- 239000003566 sealing material Substances 0.000 description 3
- 238000010059 sulfur vulcanization Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 2
- 239000004902 Softening Agent Substances 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 241000981595 Zoysia japonica Species 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000006261 foam material Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 229910052740 iodine Inorganic materials 0.000 description 2
- 239000011630 iodine Substances 0.000 description 2
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 2
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 2
- 239000010734 process oil Substances 0.000 description 2
- 239000008117 stearic acid Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- HECLRDQVFMWTQS-RGOKHQFPSA-N 1755-01-7 Chemical compound C1[C@H]2[C@@H]3CC=C[C@@H]3[C@@H]1C=C2 HECLRDQVFMWTQS-RGOKHQFPSA-N 0.000 description 1
- 239000004604 Blowing Agent Substances 0.000 description 1
- HECLRDQVFMWTQS-UHFFFAOYSA-N Dicyclopentadiene Chemical compound C1C2C3CC=CC3C1C=C2 HECLRDQVFMWTQS-UHFFFAOYSA-N 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 238000010060 peroxide vulcanization Methods 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000035882 stress Effects 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 description 1
Landscapes
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Building Environments (AREA)
- Seal Device For Vehicle (AREA)
- Laminated Bodies (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Molding Of Porous Articles (AREA)
- Sealing Material Composition (AREA)
- Vehicle Waterproofing, Decoration, And Sanitation Devices (AREA)
- Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Abstract
(57)【要約】
【課題】 熱可塑性エラストマー、とくに完全架橋型の
オレフィン系熱可塑性エラストマーの異形発泡押出物
と、各種形状の役物用ゴム成形物を一体化すること。
【解決手段】 完全架橋型のオレフィン系熱可塑性エラ
ストマーの異形発泡押出物を所定の形状の役物用成形物
を製造する金型に嵌挿し、ついで役物用成形物を製造す
るためのエチレン・プロピレン・ジエン三元共重合体ゴ
ム配合物を前記金型に注入し所定の温度、及び時間で加
硫する。(57) [PROBLEMS] To integrate a deformed foam extruded product of a thermoplastic elastomer, especially a completely cross-linked olefinic thermoplastic elastomer, and a rubber molded product for various forms of accessory. SOLUTION: A completely cross-linked olefinic thermoplastic elastomer profile foamed extrudate is inserted into a mold for producing a shaped article for a shaped article having a predetermined shape, and then ethylene for producing a shaped article for a shaped article. A propylene / diene terpolymer rubber compound is poured into the mold and vulcanized at a predetermined temperature for a predetermined time.
Description
【0001】[0001]
【産業上の利用分野】本発明は、熱可塑性エラストマー
の発泡押出物とゴム成形物との複合体を製造する方法及
びその方法で製造された複合体に関する。本発明は、自
動車用ウエザーストリップ、或いは土木、建築用シーリ
ング材であるガスケットの製造に利用される。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a composite of a foamed extrudate of a thermoplastic elastomer and a rubber molded article, and a composite produced by the method. INDUSTRIAL APPLICABILITY The present invention is used for manufacturing a weather strip for automobiles, or a gasket which is a sealing material for civil engineering and construction.
【0002】[0002]
【従来の技術】本発明者等は、熱可塑性エラストマー
(以下、TPEと略記する)の複合多重異形発泡押出物
を製造する技術を確立すべく研究開発し、すでにそれら
の成果の一つを特許出願した(特願平6−7627
5)。尚、TPEは、それが開発されて久しく、数多く
の文献で公知である。2. Description of the Related Art The present inventors have conducted research and development to establish a technique for producing a composite multiple-profile foamed extrudate of a thermoplastic elastomer (hereinafter abbreviated as TPE), and have already patented one of those results. Filed (Japanese Patent Application No. 6-7627)
5). Incidentally, TPE has been known for a long time since it was developed and has been known in many documents.
【0003】本発明者等が企図するTPEの複合多重異
形発泡押出物の主たる用途は、自動車用ウエザーストリ
ップ、及び土木、建築用シーリング材であるガスケット
である。自動車用ウエザーストリップは、自動車の車体
及びガラスに組み付けられる部品で、シール性を有し、
車体の微振動、ガラスの揺動を防止するとともに、車体
部位の緩衝機能を目的としている。更に自動車の寸法ば
らつきや建て付けのばらつきをも吸収し、組立作業性が
容易であることも要求される。また建築、土木用ガスケ
ットは、構造物や建物に生ずる有害な間隙、目地部分、
ひび割れ箇所、サッシまわり等に使用されて気密性、水
蜜性のシールを与えるものである。The main applications of the composite multi-profile foam extruded product of TPE contemplated by the present inventors are weather strips for automobiles, and gaskets which are civil engineering and construction sealing materials. Weather strips for automobiles are parts that are assembled to the car body and glass of automobiles and have sealing properties.
The purpose is to prevent slight vibration of the vehicle body and rocking of the glass, and also to cushion the vehicle body part. Further, it is required that the dimensional variations of automobiles and the variations in building are absorbed to facilitate the workability of assembling. In addition, gaskets for construction and civil engineering are used for harmful gaps, joints,
It is used for cracked parts, around sashes, etc. to provide an airtight and honey-like seal.
【0004】TPEの複合多重異形発泡押出物を自動車
用ウエザーストリップ、或いは土木、建築用シーリング
材であるガスケットとして実用に供する場合は、板金等
の複雑な形状に適応させなければならない。たとえば、
ウエザーストリップの主要部品であるドアーウエザース
トリップは、ドアーとボディーのクリアランスのばらつ
き、部品寸法のばらつき等を吸収し、ドアー周長約3.
5メートルを一定断面でシールするので、車体パネルに
よっては湾曲面、反転部位に完全に追従させなければな
らない。然しながら、複雑な湾曲面、或いはコーナー、
若しくはT字形等通常の押出物では納まらない箇所に沿
って嵌挿させることは不可能であるので、従来、これら
の部位の部材を金型で別体に製造して押出物と加硫接着
して一体化していた。When the composite multiple-profile foamed extrudate of TPE is put to practical use as a weather strip for automobiles, or a gasket which is a sealing material for civil engineering and construction, it must be adapted to a complicated shape such as sheet metal. For example,
Door weather strips, which are the main components of weather strips, absorb variations in the clearance between the door and body, variations in component dimensions, etc., and the door circumference is approximately 3.
Since 5 meters are sealed with a constant cross section, depending on the body panel, it is necessary to completely follow the curved surface and the inverted portion. However, complicated curved surfaces or corners,
Alternatively, since it is impossible to insert along a portion such as a T-shape that cannot be accommodated by an ordinary extrudate, conventionally, members at these portions are separately manufactured by a mold and vulcanized and bonded to the extrudate. It was integrated.
【0005】尚、本発明では複雑な湾曲面、或いはコー
ナー、若しくはT字形等通常の押出物では納まらない箇
所に適用される部材として押出物とは別体に金型で製造
される成形物を“役物”という。用語“役物”は、建築
業界では慣用されている用語で、たとえば彰国社刊行の
建築大辞典は、概略、平物では納まらない特殊な箇所に
用いる材料、と定義している。In the present invention, a molded product manufactured by a mold separately from the extruded product is used as a member applied to a complicated curved surface, a corner, or a portion such as a T-shape that cannot be accommodated by a normal extruded product. It is called a "feature." The term "goods" is a term that is commonly used in the building industry. For example, the architectural dictionary published by Shokokusha Inc. defines it as an outline, a material used in a special place that cannot be stored in a flat object.
【0006】本発明者等は、環境問題、及びスクラップ
の回収、リサイクルを念願において、TPEを主原料と
し、発泡剤として水を使用して多重異形発泡押出物を製
造する方法を開発し、それを前記特許出願した。The present inventors have developed a method for producing a multi-profile foam extrudate by using TPE as a main raw material and water as a foaming agent in view of environmental problems and recovery and recycling of scraps. Applied for the above patent.
【0007】ところで、TPEを主原料とし水を発泡剤
として使用して製造した異形発泡押出物とゴムを加硫接
着させて一体化させることは従来不可能であったため、
水発泡によるTPEの発泡押出物(通常形が単純ではな
い異形発泡押出物)を、役物を使用する箇所が多い自動
車用ウエザーストリップ、或いは各種ガスケットとして
広く実用化する技術がなかなか進展しなかった。[0007] By the way, it has been impossible to vulcanize and bond a profiled foamed extrudate produced by using TPE as a main raw material and water as a foaming agent so that the rubber is integrated.
The technology to widely put TPE foam extruded by water foaming (atypical foamed extruded product, which is not a simple shape in general) into weather strips for automobiles, where many parts are used, or various gaskets, has not progressed easily. .
【0008】因みに、本発明と関連のある従来技術とし
て、たとえば豊田合成株式会社の出願になる特願昭59
−272622号(特開昭61−148012号)明細
書、或いは横浜ゴム株式会社の出願になる特願平3−3
41284号(特開平5−170934号)明細書に記
載された発明があるが、これらの従来技術はいずれもT
PEのソリッド成形物とゴムを加硫接着させる方法であ
って、TPEの異形発泡押出物とゴムとの加硫接着を、
いわんやTPEの水発泡による異形発泡押出物とゴムと
の加硫接着を開示していない。Incidentally, as a conventional technique related to the present invention, for example, Japanese Patent Application No. 59-59, filed by Toyoda Gosei Co., Ltd.
-272622 (JP-A-61-148012) or Japanese Patent Application No. 3-3 filed by Yokohama Rubber Co., Ltd.
There is an invention described in the specification of Japanese Patent No. 41284 (Japanese Patent Laid-Open No. 5-170934).
A method for vulcanizing and adhering a PE solid molded article and rubber, which comprises vulcanizing and adhering a TPE profiled foam extrudate and rubber.
It does not disclose vulcanization adhesion between a rubber foam and a shaped foam extrudate of TPE.
【0009】[0009]
【発明が解決しようとする課題】発明が解決しようとす
る課題は、熱可塑性エラストマーの異形発泡押出物とゴ
ム成形物を加硫接着することが出来なかったことであ
る。The problem to be solved by the present invention is that it was not possible to vulcanize and bond the deformed foam extruded product of the thermoplastic elastomer and the rubber molded product.
【0010】発明が解決しようとする別の課題は、オレ
フィン系熱可塑性エラストマーを主原料とし、水を発泡
剤として製造される異形発泡押出物と、役物用ゴム成形
物とを加硫接着し一体化することが出来なかったことで
ある。Another problem to be solved by the invention is to vulcanize and bond a profiled extruded product produced by using an olefinic thermoplastic elastomer as a main raw material and water as a foaming agent, and a rubber molded product for an accessory. It was not possible to be united.
【0011】発明が解決しようとするさらなる課題及び
利点は以下逐次明らかにされる。Further problems and advantages to be solved by the invention will be made clear successively below.
【0012】[0012]
【課題を解決するための手段】本発明者等は、各種の熱
可塑性エラストマーの適応性を検討した。その結果、本
発明における発泡押出物の原料である熱可塑性エラスト
マーとしては、熱可塑性樹脂ポリプロピレンをマトリッ
クス成分とし、エチレン・プロピレン・ジエン三元共重
合体ゴム(以下、EPDMと略記する)がポリマーブレ
ンドされた、いわゆるオレフィン系熱可塑性エラストマ
ー(以下、TPOという)、特に完全架橋型のオレフィ
ン系熱可塑性エラストマーが好ましいことが解った。The present inventors have examined the adaptability of various thermoplastic elastomers. As a result, as a thermoplastic elastomer which is a raw material of the foamed extrudate in the present invention, a thermoplastic resin polypropylene is used as a matrix component, and an ethylene / propylene / diene terpolymer rubber (hereinafter abbreviated as EPDM) is a polymer blend. It was found that the above-mentioned so-called olefinic thermoplastic elastomer (hereinafter referred to as TPO), particularly the completely crosslinked olefinic thermoplastic elastomer is preferable.
【0013】本発明は、熱可塑性エラストマーの発泡押
出物とゴム成形物との複合体を製造する方法であって; 断面の大きさが同じ1種の又は断面の大きさが異な
る2種以上の熱可塑性エラストマーの発泡押出物を製造
すること; 所定の形状の役物用ゴム成形物を製造するための金
型を準備すること; 前記役物用ゴム成形物を製造するためのエチレン・
プロピレン・ジエン三元共重合体ゴムを主原料とするゴ
ム配合物を準備すること; 前記熱可塑性エラストマーの発泡押出物を所定の長
さに切断し、2個の同じ種類又は異なる種類の発泡押出
物のそれぞれの1端部を前記金型内に嵌挿し、ついで前
記役物用ゴム成形物を製造するためのエチレン・プロピ
レン・ジエン三元共重合体ゴムを主原料とするゴム配合
物を注入すること;ついで 所定の温度、及び時間で加硫して、前記2個の熱可
塑性エラストマーの発泡押出物と前記役物用ゴム成形物
を加硫接着させ一体化させることを含む熱可塑性エラス
トマーの発泡押出物とゴム成形物との複合体を製造する
方法に関する。The present invention is a method for producing a composite of a foamed extrudate of a thermoplastic elastomer and a rubber molded article; one kind having the same cross section size or two or more kinds having different cross section sizes Producing a foamed extrudate of a thermoplastic elastomer; Preparing a mold for producing a rubber molded product for a accessory having a predetermined shape; Ethylene for producing a rubber molded product for an accessory;
Providing a rubber compound containing propylene / diene terpolymer rubber as a main raw material; cutting the foamed extrudate of the thermoplastic elastomer into a predetermined length to obtain two foamed extrudates of the same type or different types. One end of each of the products is inserted into the mold, and then a rubber compound containing ethylene / propylene / diene terpolymer rubber as a main raw material for producing the rubber molded product for the accessory is injected. Then, vulcanization is performed at a predetermined temperature for a predetermined time to vulcanize and bond the foamed extruded products of the two thermoplastic elastomers and the rubber molded product for the accessory to be integrated with each other. The present invention relates to a method for producing a composite of a foam extrudate and a rubber molded product.
【0014】TPEとして、たとえば、エーイーエス・
ジャパン株式会社から商品名“サントプレン101−6
8W228”として入手できる。サントプレンのような
完全架橋型のオレィン系熱可塑性エラストマーを使用し
ないと、金型から脱型するときに変形したり、加硫後に
型崩れするというおそれがある。As the TPE, for example, AES
Product name "Santoprene 101-6" from Japan Co., Ltd.
8W228 ″. If a completely crosslinked olein-based thermoplastic elastomer such as Santoprene is not used, there is a risk that it may be deformed when it is released from the mold, or may lose its shape after vulcanization.
【0015】本発明者等は、TPOの異形発泡押出物と
加硫接着させる役物を製造するためのゴムを、耐候
性、耐オゾン性、耐老化性に優れていること、車体等
への汚染性がないこと、温度による引張応力の変化が
小さいこと、低コストであること等を要件として選択
した。その結果、EPDMを選択した。The present inventors have made a rubber for producing a material for vulcanizing and adhering a TPO profiled foam extrudate excellent in weather resistance, ozone resistance and aging resistance, and to a vehicle body and the like. It was selected as a requirement that it is not contaminated, that the change in tensile stress with temperature is small, and that it is low cost. As a result, EPDM was selected.
【0016】従って、課題を解決するための手段は、T
POの異形発泡押出物と加硫接着させる役物用成形物の
原料ゴムとしてEPDMを使用することである。Therefore, the means for solving the problem is T
That is, EPDM is used as a raw material rubber of a molded article for accessory that is vulcanized and adhered to the odd-shaped foam extrudate of PO.
【0017】本発明でTPOの異形発泡押出物と加硫接
着させる役物用成形物の原料ゴムとして使用されるEP
DMは、主としてジエン成分(第3成分)の種類、量、
分布、重合体の分子量、分子量分布等により各種特徴の
あるものが市販されており、希望の要件に応じて選択す
ればよく、特段に限定されない。たとえば、硫黄加硫系
で速い加硫速度を希望するならば、第3成分としてエチ
リデンノルボーネン(ENB)を用いたEPDMが分子
量、よう素価を考慮しても最も速く、逆にジシクロペン
タジエン(DCPD)は遅い、一方過酸化物加硫系では
第3成分の差はほとんど見られない。従って、第3成分
の種類だけでEPDMを選択することはそれほど技術的
意味はない。硫黄加硫系での加硫速度、ムーニー粘度、
よう素価、加工性、用途等を総合的に勘案した本発明で
最も好ましいEPDMは第3成分がENBのものである
と云える。これらは、たとえば住友化学工業株式会社、
日本合成ゴム株式会社から入手できる。EP used in the present invention as a raw material rubber for a molded article for accessory that is vulcanized and adhered to a profiled extruded product of TPO
DM is mainly the type and amount of the diene component (third component),
Those having various characteristics depending on the distribution, the molecular weight of the polymer, the molecular weight distribution, etc. are commercially available, and the selection may be made according to the desired requirements, and there is no particular limitation. For example, if a high vulcanization rate is desired in a sulfur vulcanization system, EPDM using ethylidene norbornene (ENB) as the third component is the fastest even considering the molecular weight and iodine value, and conversely dicyclopentadiene. (DCPD) is slow, while in the peroxide vulcanization system there is almost no difference in the third component. Therefore, it is not technically significant to select EPDM only by the type of the third component. Vulcanization speed in sulfur vulcanization system, Mooney viscosity,
It can be said that the most preferable EPDM of the present invention in which the iodine value, processability, application and the like are taken into consideration is that the third component is ENB. These are, for example, Sumitomo Chemical Co., Ltd.
Available from Japan Synthetic Rubber Co., Ltd.
【0018】本発明で使用されるEPDM配合物のゴム
含有量は10〜70%、EPDM配合物の最低ムーニー
粘度は、Lローター121℃で20〜30、スコーチ時
間は20〜30分の範囲が好ましい。The rubber content of the EPDM compound used in the present invention is 10 to 70%, the minimum Mooney viscosity of the EPDM compound is 20 to 30 at 121 ° C. L rotor, and the scorch time is 20 to 30 minutes. preferable.
【0019】本発明で使用される役物用ゴム成形物を製
造するためのEPDM配合物の配合例を下記に例示す
る;配合成分 配合比率(重量部) EPDM(ENB系) 100 カーボンブラック 0〜100 ステアリン酸 1〜3 酸化亜鉛 4〜10 硫黄 1〜3 加硫促進剤 2〜5 発泡剤 0〜7 プロセスオイル 0〜50 軟化剤 0〜20 炭酸カルシュウム 0〜100 上記配合範囲内において、各種希望条件、例えば最低ム
ーニー粘度、スコーチ時間等を勘案して適宜設定され
る。A compounding example of an EPDM compound for producing a rubber molded product for an accessory used in the present invention is exemplified below: compounding component compounding ratio (parts by weight) EPDM (ENB type) 100 carbon black 0 100 Stearic acid 1 to 3 Zinc oxide 4 to 10 Sulfur 1 to 3 Vulcanization accelerator 2 to 5 Foaming agent 0 to 7 Process oil 0 to 50 Softening agent 0 to 20 Calcium carbonate 0 to 100 Various desired values within the above range. It is appropriately set in consideration of the conditions such as the minimum Mooney viscosity and the scorch time.
【0020】本発明によって、予め製造したTPOの発
泡押出物を用途に応じて所定の長さに切断し、役物の形
状に成形してある金型内に前記切断した端部を嵌挿し、
前記EPDM配合物を金型に注入し、所定の金型温度で
所定の時間加硫させることによって発泡押出物と役物用
EPDM成形物が加硫接着され一体化される。According to the present invention, a foamed extruded product of TPO produced in advance is cut into a predetermined length according to the use, and the cut end is fitted into a mold formed into a shape of an accessory,
The EPDM compound is injected into a mold and vulcanized at a predetermined mold temperature for a predetermined time to vulcanize and bond the foamed extrudate and the accessory EPDM molded product.
【0021】本発明を実施する場合、TPOの発泡押出
物の製造において、TPOの発泡に使用される発泡剤は
特段に限定されないが、前述した本発明者等の開発理念
を勘案すれば水による発泡が最も理想的である。In carrying out the present invention, the foaming agent used for foaming TPO in the production of the foamed extrudate of TPO is not particularly limited, but in consideration of the above-mentioned development idea of the inventors, water is used. Foaming is the most ideal.
【0022】本発明を実施する場合の加硫温度、及び加
硫時間は、使用したEPDMの種類と量、加硫方法等諸
条件に依存して決定されるが、硫黄加硫の場合は、金型
温度140〜200℃、加硫時間が2〜10分間の範囲
で選択される。The vulcanization temperature and vulcanization time for carrying out the present invention are determined depending on various conditions such as the type and amount of EPDM used and the vulcanization method. In the case of sulfur vulcanization, The mold temperature is selected in the range of 140 to 200 ° C. and the vulcanization time is in the range of 2 to 10 minutes.
【0023】本発明は、高伸長度、及び低硬度のEPD
M配合物を使用するので、中子を使用した中空部を有す
るTPOの発泡押出物と、コーナー部等の役物用ゴム配
合物と容易に加硫接着させて一体化することができ、中
子を外すときに破損等不都合は発生しない。The present invention has a high elongation and a low hardness EPD.
Since the M compound is used, it is possible to easily vulcanize and integrate the foamed extruded product of TPO having a hollow portion using a core and the rubber compound for accessory materials such as the corners. No problems such as breakage occur when removing the child.
【0024】以下、実施例により本発明を具体的に説明
する。Hereinafter, the present invention will be described specifically with reference to examples.
【0025】[0025]
【実施例1】TPOを原料とする水発泡押出物の製造 (1) 使用したTPO エーイーエス・ジャパン株式会社“サントプレン101
−68W228” (2) 使用した押出装置 下記の諸元のTPO水発泡用押出機、冷却水槽、引取機
から主として構成される押出装置を使用した;TPO水発泡用押出機諸元 押出機のスクリュー直径:90mm 押出機のL/D :30 スクリュー回転数 :30rpm TPO水発泡用押出機のシリンダー部を4つのゾーンに
区分し、各々を170℃乃至175℃に温度設定し、ヘ
ッド部とダイズ部のそれを185℃と183℃に設定し
た。TPO水発泡用に配合した配合物をTPO水発泡用
押出機に投入し、シリンダー後部、即ちホッパー側か
ら、約12Dの位置で、TPO配合物に対して約0.4
%の比率で水を注入しながら約51kg/Hr の比率でT
PO配合物を押出してU字形断面を有する比重0.45
の発泡押出物を製造した。[Example 1] Production of water-foamed extrudate using TPO as a raw material (1) TPO used AES Japan Co., Ltd. "Santoprene 101"
-68W228 "(2) Extruder used Extruder mainly composed of TPO water foaming extruder, cooling water tank, and take-off machine having the following specifications was used; TPO water foaming extruder specifications Extruder screw Diameter: 90 mm Extruder L / D: 30 Screw rotation speed: 30 rpm The cylinder part of the extruder for TPO water foaming is divided into four zones, each of which is set to a temperature of 170 ° C to 175 ° C, and the head part and the soybean part are set. It was set to 185 ° C. and 183 ° C. The compounded mixture for TPO water foaming was put into an extruder for TPO water foaming, and the TPO compounding was carried out at a position of about 12D from the cylinder rear part, that is, from the hopper side. About 0.4
While injecting water at a rate of T, T at a rate of about 51 kg / Hr
Extruded PO formulation with specific gravity 0.45 with U-shaped cross section
Foamed extrudates were produced.
【0026】EPDM配合物の製造 下記の配合比率で役物用EPDM配合物を製造した;配合成分 配合比率(重量部) EPDM(ENB系) 100 カーボンブラック 60 ステアリン酸 1.5 酸化亜鉛 5 硫黄 1.5 加硫促進剤 2 発泡剤 5 プロセスオイル 45 軟化剤 5 炭酸カルシュウム 50 上記配合物を50℃度で5分間ニーダー混練りして、1
21℃におけるムーニー粘度が25の混練り物を製造し
た。[0026] were prepared EPDM blends character object for EPDM formulation in blend ratio of production following; Ingredients Ratio (parts by weight) EPDM (ENB system) 100 Carbon black 60 Stearic acid 1.5 Zinc oxide 5 Sulfur 1 .5 Vulcanization accelerator 2 Foaming agent 5 Process oil 45 Softening agent 5 Calcium carbonate 50 Kneader kneading the above composition for 5 minutes at 50 ° C to give 1
A kneaded product having a Mooney viscosity of 25 at 21 ° C. was produced.
【0027】前記TPOの発泡押出物を所定の長さに切
断し、その両端部を、予め製造しておいたL字型役物用
金型に込め、前記EPDM配合物の混練り物を金型に注
入し、金型温度を190℃に設定し、5分間加硫して、
TPOの発泡押出物をL字型のゴム発泡物と加硫接着さ
せて一体化させた。The foamed extruded product of TPO is cut into a predetermined length, and both ends thereof are put into a preformed L-shaped accessory mold, and the kneaded product of the EPDM compound is molded into a mold. , Set the mold temperature to 190 ° C, vulcanize for 5 minutes,
The foamed extrudate of TPO was vulcanized and bonded to the L-shaped rubber foam to be integrated.
【0028】製造されたTPOの発泡押出物とL字型の
ゴム発泡物が加硫接着され一体化された複合体の接着力
を剥離テストによって測定したところ、20.5kgf/c
m2で発泡物の材料が破壊された。The adhesive strength of the composite body obtained by vulcanizing and adhering the foamed extruded product of TPO and the L-shaped rubber foam was measured by a peeling test to find that it was 20.5 kgf / c.
The foam material broke at m 2 .
【0029】[0029]
【実施例2】実施例1で使用したEPDM配合物から発
泡剤を除去したことを除いて実施例1と同じ手順を繰返
してTPO発泡押出物とL字型のEPDMのソリッド成
形物を加硫接着させ一体化させた複合体を製造した。Example 2 The same procedure as in Example 1 was repeated, except that the blowing agent was removed from the EPDM formulation used in Example 1, to vulcanize the TPO foam extrudate and the L-shaped EPDM solid molding. A bonded and integrated composite was produced.
【0030】製造されたTPOの発泡押出物とL字型の
EPDMのソリッド成形物とが接着一体化された複合体
の接着力を剥離テストによって測定したところ20.0
kg/cm2で剥離によって発泡物の材料は破壊された。The adhesive strength of the composite body in which the foamed extruded product of TPO and the solid molded product of L-shaped EPDM adhered and integrated was measured by a peeling test to be 20.0.
The foam material was destroyed by peeling at kg / cm 2 .
【0031】[0031]
【比較例】実施例1で使用されたTPOを原料とするソ
リッド押出物を製造した。このTPOのソリッド押出物
を使用した以外には実施例1と同じ手順を繰り返してT
POのソリッド押出物とL字型のEPDMの発泡成形物
とが加硫接着され一体化された複合体を製造した。Comparative Example A solid extrudate made from the TPO used in Example 1 was prepared. The same procedure as in Example 1 was repeated except that the solid extrudate of TPO was used.
A solid extruded product of PO and a foamed product of L-shaped EPDM were vulcanized and bonded to each other to produce a composite.
【0032】製造されたTPOのソリッド押出物とL字
型のEPDMの発泡成形物とが加硫接着され一体化され
た複合体の接着力を剥離テストによって測定したところ
10.0kg/cm2で剥離によって両者の界面が剥離され
た。The adhesive strength of the composite obtained by vulcanizing and adhering the solid extruded product of TPO and the foamed molded product of L-shaped EPDM measured by a peel test was 10.0 kg / cm 2 . The interface between the two was peeled by peeling.
【0033】上述した実施例、及び比較例の結果から、
TPOの押出物がソリッドの場合は本発明の効果が奏効
されないこと、また役物としてのEPDM成形物は発泡
体でもソリッドでも本発明の効果が奏効されることが理
解される。From the results of the above Examples and Comparative Examples,
It is understood that when the extruded product of TPO is solid, the effect of the present invention is not effective, and when the EPDM molded product as a role is a foam or a solid, the effect of the present invention is effective.
【0034】従って、本発明の最も好ましい態様は;ポ
リプロピレンと、エチレン・プロピレン・ジエン三元共
重合体ゴム(EPDM)をポリマーブレンドした完全架
線型のオレフィン系熱可塑性エラストマーの水発泡によ
る異形発泡押出物とEPDMの成形物との複合体を製造
する方法であって; 水を発泡剤として使用して前記熱可塑性エラストマ
ーの異形発泡押出物を製造すること; 所定の形状の役物用成形物を製造するための金型を
準備すること; 前記役物用成形物を製造するための材料として、E
PDMを主原料とし、ゴム含量が10〜70%、最低ム
ーニー粘度がLローター121℃で20〜30、スコー
ム時間が20〜20分のEPDM配合物を準備するこ
と; 前記熱可塑性エラストマーの異形発泡押出物を所定
の長さに切断し、その両端部を前記金型内に嵌挿し、つ
いで前記役物用成形物を製造するためのEPDM配合物
を注入すること;ついで 金型温度140〜200℃、加硫時間2〜10分間
の条件で加硫して、前記熱可塑性エラストマーの水発泡
による異形発泡押出物と前記役物用EPDM成形物を加
硫接着させ一体化させることから成るポリプロピレンと
エチレン・プロピレン・ジエン三元共重合体ゴムをポリ
マーブレンドした完全架線型のオレフィン系熱可塑性エ
ラストマーの水発泡による異形発泡押出物とEPDMの
成形物との複合体を製造する方法である。Therefore, the most preferred embodiment of the present invention is: Shaped foam extrusion by completely foaming a completely catenary type olefinic thermoplastic elastomer obtained by polymer blending polypropylene and ethylene propylene diene terpolymer rubber (EPDM). A method for producing a composite of a molded article and a molded article of EPDM; using water as a foaming agent to produce a modified foam extrudate of the thermoplastic elastomer; Preparing a mold for manufacturing; E as a material for manufacturing the accessory molding
Preparing an EPDM compound containing PDM as a main raw material, a rubber content of 10 to 70%, a minimum Mooney viscosity of 20 to 30 at L rotor 121 ° C., and a scour time of 20 to 20 minutes; Cutting the extrudate into a predetermined length, inserting both ends of the extrudate into the mold, and then injecting the EPDM compound for producing the shaped product for the accessory; and then a mold temperature of 140 to 200. A polypropylene obtained by vulcanizing at a temperature of 2 ° C. for 2 to 10 minutes and vulcanizing and adhering the shaped foam extruded product of the thermoplastic elastomer by water foaming and the EPDM molded product for accessory. EPDM and odd-shaped foam extruded product by water-expanding of completely overhead line type olefin-based thermoplastic elastomer obtained by polymer blending ethylene / propylene / diene terpolymer rubber A method for producing a complex of moldings.
【0035】[0035]
【発明の効果】以上説明したように、本発明によって、
TPOの水発泡による異形発泡押出物と、役物用ゴム成
形物を容易に加硫接着して一体化された複合体に成形す
ることができるので、たとえば車体パネルの複雑な湾曲
面、コーナー部等にも完全に追従させることができ、T
POの水発泡による異形発泡押出物の用途が著しく拡大
される。As described above, according to the present invention,
Since it is possible to easily vulcanize and bond a deformed foam extruded product of TPO with water and a rubber molded product for an accessory to form an integrated composite, for example, a complicated curved surface or a corner portion of a vehicle body panel. Etc. can be made to completely follow, and T
The application of the shaped foam extrudate by the water foaming of PO is significantly expanded.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B60J 5/00 501 B60J 5/00 501G B60R 13/06 B60R 13/06 C09K 3/10 C09K 3/10 C E04B 1/66 E04B 1/66 // B29K 23:00 105:04 B29L 9:00 31:10 31:30 (72)発明者 黒田 健司 広島県福山市松浜町2丁目2番11号 広島 化成株式会社内 (72)発明者 佐藤 文彦 広島県福山市松浜町2丁目2番11号 広島 化成株式会社内 (72)発明者 佐々木 剛 広島県福山市松浜町2丁目2番11号 広島 化成株式会社内 (72)発明者 寺澤 勇 東京都港区芝5丁目33番8号 三菱自動車 工業株式会社内 (72)発明者 濱田 知則 東京都港区芝5丁目33番8号 三菱自動車 工業株式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location B60J 5/00 501 B60J 5/00 501G B60R 13/06 B60R 13/06 C09K 3/10 C09K 3 / 10 C E04B 1/66 E04B 1/66 // B29K 23:00 105: 04 B29L 9:00 31:10 31:30 (72) Inventor Kenji Kuroda 2-2-11 Matsuhama-cho, Fukuyama City, Hiroshima Prefecture Hiroshima Chemical Co., Ltd. Inside the company (72) Fumihiko Sato 2-21-11 Matsuhama-cho, Fukuyama City, Hiroshima Prefecture Hiroshima Kasei Co., Ltd. ) Inventor Isamu Terasawa 5-3-8-3 Shiba, Minato-ku, Tokyo Within Mitsubishi Motors Corporation (72) Inventor Tomonori Hamada 5-33-8 Shiba, Minato-ku, Tokyo Mitsubishi Motors Corporation Within the corporation
Claims (4)
ム成形物との複合体を製造する方法であって; 断面の大きさが同じ1種の又は断面の大きさが異な
る2種以上の熱可塑性エラストマーの発泡押出物を製造
すること; 所定の形状の役物用ゴム成形物を製造するための金
型を準備すること; 前記役物用ゴム成形物を製造するためのエチレン・
プロピレン・ジエン三元共重合体ゴムを主原料とするゴ
ム配合物を準備すること; 前記熱可塑性エラストマーの発泡押出物を所定の長
さに切断し、 2個の同じ種類又は異なる種類の発泡押出物のそれぞれ
の1端部を前記金型内に嵌挿し、ついで前記役物用ゴム
成形物を製造するためのエチレン・プロピレン・ジエン
三元共重合体ゴムを主原料とするゴム配合物を注入する
こと;ついで 所定の温度、及び時間で加硫して、前記2個の熱可
塑性エラストマーの発泡押出物と前記役物用ゴム成形物
を加硫接着させ一体化させることを含む熱可塑性エラス
トマーの発泡押出物とゴム成形物との複合体を製造する
方法。1. A method for producing a composite of a foamed extruded product of a thermoplastic elastomer and a rubber molded product; one kind of thermoplastic resin having the same sectional size or two or more thermoplastic resins having different sectional sizes. Producing a foamed extrudate of an elastomer; Preparing a mold for producing a rubber molded product for a accessory having a predetermined shape; Ethylene for producing the rubber molded product for an accessory;
Providing a rubber compound containing propylene / diene terpolymer rubber as a main raw material; cutting the foamed extrudate of the thermoplastic elastomer into a predetermined length, and extruding two foamed extrudates of the same type or different types. One end of each of the products is inserted into the mold, and then a rubber compound containing ethylene / propylene / diene terpolymer rubber as a main raw material for producing the rubber molded product for the accessory is injected. Then, vulcanization is performed at a predetermined temperature for a predetermined time to vulcanize and bond the foamed extruded products of the two thermoplastic elastomers and the rubber molded product for the accessory to be integrated with each other. A method for producing a composite of a foamed extrudate and a rubber molding.
造を水を発泡剤として行なうことを特徴とする請求項1
に記載の方法。2. The method for producing a foamed extrudate of a thermoplastic elastomer, wherein water is used as a foaming agent.
The method described in.
ンとエチレン・プロピレン・ジエン三元共重合体ゴムを
ポリマーブレンドした完全架橋型オレフィン系熱可塑性
エラストマーであることを特徴とする請求項1、或いは
請求項2に記載の方法。3. The thermoplastic elastomer is a completely crosslinked olefinic thermoplastic elastomer obtained by polymer blending polypropylene and an ethylene / propylene / diene terpolymer rubber. The method described in.
ラストマーの発泡押出物とゴム生成物との複合体。4. A composite of a foam extrudate of a thermoplastic elastomer produced by the method of claim 1 and a rubber product.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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JP07285247A JP3090600B2 (en) | 1995-11-01 | 1995-11-01 | Method for producing composite of foamed extrudate of thermoplastic elastomer and rubber molding and composite produced by the method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP07285247A JP3090600B2 (en) | 1995-11-01 | 1995-11-01 | Method for producing composite of foamed extrudate of thermoplastic elastomer and rubber molding and composite produced by the method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09123211A true JPH09123211A (en) | 1997-05-13 |
JP3090600B2 JP3090600B2 (en) | 2000-09-25 |
Family
ID=17689027
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Application Number | Title | Priority Date | Filing Date |
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JP07285247A Expired - Lifetime JP3090600B2 (en) | 1995-11-01 | 1995-11-01 | Method for producing composite of foamed extrudate of thermoplastic elastomer and rubber molding and composite produced by the method |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999030885A3 (en) * | 1997-12-16 | 1999-08-19 | Armstrong Insulation Products | Method for continuous production of a plastic plate-shaped article |
JP2020172101A (en) * | 2019-04-05 | 2020-10-22 | ビウイ ソシエテ アノニム | Manufacture of elastomeric parts made by replication based on the reference standard model |
CN112277349A (en) * | 2020-10-28 | 2021-01-29 | 马鞍山联洪合成材料有限公司 | Processing technology of foaming type reinforcing rubber sheet for automobile |
-
1995
- 1995-11-01 JP JP07285247A patent/JP3090600B2/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999030885A3 (en) * | 1997-12-16 | 1999-08-19 | Armstrong Insulation Products | Method for continuous production of a plastic plate-shaped article |
JP2020172101A (en) * | 2019-04-05 | 2020-10-22 | ビウイ ソシエテ アノニム | Manufacture of elastomeric parts made by replication based on the reference standard model |
CN112277349A (en) * | 2020-10-28 | 2021-01-29 | 马鞍山联洪合成材料有限公司 | Processing technology of foaming type reinforcing rubber sheet for automobile |
CN112277349B (en) * | 2020-10-28 | 2022-09-20 | 马鞍山联洪合成材料有限公司 | Processing technology of foaming type reinforcing rubber sheet for automobile |
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Publication number | Publication date |
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JP3090600B2 (en) | 2000-09-25 |
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