JP2000303058A - Gasket - Google Patents
GasketInfo
- Publication number
- JP2000303058A JP2000303058A JP11115559A JP11555999A JP2000303058A JP 2000303058 A JP2000303058 A JP 2000303058A JP 11115559 A JP11115559 A JP 11115559A JP 11555999 A JP11555999 A JP 11555999A JP 2000303058 A JP2000303058 A JP 2000303058A
- Authority
- JP
- Japan
- Prior art keywords
- gasket
- fluororesin
- melt
- resin
- pfa
- 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
- 239000011347 resin Substances 0.000 claims abstract description 29
- 229920005989 resin Polymers 0.000 claims abstract description 29
- 229920000840 ethylene tetrafluoroethylene copolymer Polymers 0.000 claims abstract description 11
- -1 poly(chlorotrifluoroethylene) Polymers 0.000 claims abstract description 9
- 239000000155 melt Substances 0.000 claims abstract description 7
- 229920002493 poly(chlorotrifluoroethylene) Polymers 0.000 claims abstract 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract 2
- 239000005977 Ethylene Substances 0.000 claims abstract 2
- 239000005023 polychlorotrifluoroethylene (PCTFE) polymer Substances 0.000 claims abstract 2
- 239000007788 liquid Substances 0.000 claims description 15
- 238000000465 moulding Methods 0.000 claims description 15
- 230000002093 peripheral effect Effects 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 10
- 230000003746 surface roughness Effects 0.000 claims description 10
- 238000002844 melting Methods 0.000 claims description 2
- 230000008018 melting Effects 0.000 claims description 2
- 239000000126 substance Substances 0.000 abstract description 6
- 238000004925 denaturation Methods 0.000 abstract description 5
- 230000036425 denaturation Effects 0.000 abstract description 5
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000470 constituent Substances 0.000 abstract 1
- 230000002085 persistent effect Effects 0.000 abstract 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 abstract 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 26
- 239000004810 polytetrafluoroethylene Substances 0.000 description 26
- 238000005520 cutting process Methods 0.000 description 11
- 239000004812 Fluorinated ethylene propylene Substances 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 7
- 229920009441 perflouroethylene propylene Polymers 0.000 description 7
- 230000003749 cleanliness Effects 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 238000001746 injection moulding Methods 0.000 description 6
- 238000007789 sealing Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000000635 electron micrograph Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000011084 recovery Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 4
- 239000003513 alkali Substances 0.000 description 3
- 230000006835 compression Effects 0.000 description 3
- 238000007906 compression Methods 0.000 description 3
- 239000003651 drinking water Substances 0.000 description 3
- 235000020188 drinking water Nutrition 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 238000010101 extrusion blow moulding Methods 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 229920001296 polysiloxane Polymers 0.000 description 3
- 229910021642 ultra pure water Inorganic materials 0.000 description 3
- 239000012498 ultrapure water Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 229920002943 EPDM rubber Polymers 0.000 description 2
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical group FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000000748 compression moulding Methods 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000002510 pyrogen Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229920000181 Ethylene propylene rubber Polymers 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
Landscapes
- Gasket Seals (AREA)
- Sealing Material Composition (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、サニタリー配管用
シール部材に関する。さらに詳しくは、特定の性質を有
するフッ素樹脂を溶融成形して得られるサニタリー配管
用シール部材に関する。The present invention relates to a seal member for sanitary piping. More specifically, the present invention relates to a seal member for sanitary piping obtained by melt-molding a fluororesin having specific properties.
【0002】[0002]
【従来の技術】医薬品、食品、飲料水、超純水等の生産
装置に使用されているサニタリー配管用継手部分のガス
ケット、O−リング等のシール部材の材質は、通常の配
管に比べて過酷な条件に曝される。すなわち、医薬品の
生産においては、その製品に不純物が溶出しないこと、
発熱物質のパイロジェンを除去するために、アルカリ洗
浄、飽和水蒸気による洗浄に耐えることが要求される。
また、食品、飲料水、超純水の生産に用いる場合におい
ては、その製品に不純物が溶出しないことはもちろん、
高温高圧の水蒸気滅菌に耐えることが要求される。2. Description of the Related Art The material of seal members such as gaskets and O-rings at joints for sanitary piping used in production equipment for pharmaceuticals, foods, drinking water, ultrapure water, etc. is more severe than ordinary piping. Exposed to various conditions. In other words, in the production of pharmaceuticals, impurities do not elute in the product,
In order to remove pyrogen as a pyrogen, it is required to withstand alkali cleaning and cleaning with saturated steam.
In addition, when used for the production of food, drinking water and ultrapure water, of course, impurities do not elute in the product,
It is required to withstand high temperature and high pressure steam sterilization.
【0003】このような医薬品、食品、飲料水、超純水
等の生産装置において、サニタリー配管用のガスケット
として、エチレンプロピレンゴム(以下、EPDMとい
う)あるいはシリコン系プラスチック製のガスケットが
使用されている。ところが、これらのEPDMやシリコ
ン系プラスチックは、配管内の飽和蒸気、アルカリ液等
を用いて洗浄を繰り返すと経時的に劣化し、劣化部分が
配管中に脱落して液体中に異物として混入したり、長期
の使用によりこれらの材料に含まれる可塑材が溶出する
等の問題がある。さらに、シリコン系プラスチックは、
耐アルカリ性に劣るため、洗浄後にアルカリ成分がわず
かに残存していると、水蒸気滅菌した場合、フランジ金
属表面に固着する等の欠点がある。[0003] In such a production apparatus for pharmaceuticals, foods, drinking water, ultrapure water, etc., a gasket made of ethylene propylene rubber (hereinafter referred to as EPDM) or a silicone plastic is used as a gasket for sanitary piping. . However, these EPDMs and silicone plastics deteriorate over time when washing is repeated using saturated vapor, alkaline solution, etc. in the pipes, and the deteriorated parts fall off in the pipes and mix as foreign substances in the liquid. In addition, there is a problem that the plasticizer contained in these materials elutes due to long-term use. In addition, silicone plastics
Since alkali resistance is inferior, if a small amount of an alkali component remains after washing, there is a defect such as sticking to the flange metal surface when steam sterilized.
【0004】この欠点を解消するために、フッ素樹脂で
あるポリテトラフルオロエチレン(以下、PTFEとい
う)樹脂製のシール部材が用いられている。PTFE樹
脂は、耐熱性、耐薬品性に優れているが、経時的な応力
変性が大きく、弾性回復力に劣るという欠点がある。こ
のため、ガスケットが配管内径側にはみ出し、液溜りの
原因になり、雑菌の繁殖の機会が生じ、清浄さが保てな
い。また、PTFE樹脂は硬度が高いため、フランジ部
分の締め付け圧を高くしなければ蒸気などのガス洩れが
防止できず、かついったん締め直すと弾性回復が困難で
あり、二度目以降はガス洩れが防止できないという欠点
がある。さらに、PTFE樹脂のシール部材は圧縮成形
で製造され、表面処理も切削加工に頼らざるを得ず、生
産性、材料の歩留まりの面で効率的といえない上、表面
を滑らかにすることが困難であるため、表面の凹凸に起
因して、配管内の清潔さ維持の能力に欠け、液体の付着
残留や着香が生じるという欠点もある。In order to solve this drawback, a seal member made of polytetrafluoroethylene (hereinafter referred to as PTFE) resin which is a fluororesin is used. Although PTFE resin is excellent in heat resistance and chemical resistance, it has a drawback in that it undergoes large stress denaturation with time and is inferior in elastic recovery power. For this reason, the gasket protrudes to the inner diameter side of the pipe, causing a pool of liquid, causing an opportunity for propagation of various germs, and the cleanliness cannot be maintained. In addition, since the hardness of PTFE resin is high, gas leakage such as steam cannot be prevented unless the tightening pressure of the flange portion is increased, and it is difficult to recover elasticity once retightened, and gas leakage is prevented after the second time. There is a drawback that you can not. Furthermore, the sealing member made of PTFE resin is manufactured by compression molding, and the surface treatment must rely on cutting, which is not efficient in terms of productivity and material yield, and it is difficult to smooth the surface. Therefore, there is also a disadvantage that due to the unevenness of the surface, the ability to maintain the cleanliness in the pipe is lacking, and the adhesion of the liquid and the aroma occur.
【0005】このPTFE樹脂製ガスケットの欠点を解
消すべく、多孔質PTFE樹脂を用い、形状に特徴を持
たせたサニタリー配管用ガスケットが提案されている
(特開平5−99343号公報)。このガスケットは、
多孔質で構成されているため、被密封流体がガスケット
の内周と接触し、この内周部分から被密封流体が浸透す
る、いわゆる浸透洩れを起こす可能性がある。特に、ガ
スシールとして使用する場合には、浸透洩れは大きな問
題となる可能性があるため、多孔質PTFE樹脂ガスケ
ットの内周部分の表面を無孔質の溶融固化層とする試み
がなされ(特開平8−121599号公報)、使用レベ
ルに到達しつつある。In order to eliminate the disadvantages of the gasket made of PTFE resin, a gasket for sanitary piping using porous PTFE resin and having a characteristic shape has been proposed (JP-A-5-99343). This gasket is
Because of the porous structure, the sealed fluid comes into contact with the inner periphery of the gasket, and the sealed fluid may penetrate from the inner periphery, so-called permeation leakage may occur. In particular, when used as a gas seal, permeation leakage may be a serious problem, and an attempt has been made to use a non-porous, melt-solidified layer on the inner peripheral surface of a porous PTFE resin gasket. Japanese Unexamined Patent Publication No. Hei 8-121599), which is reaching a use level.
【0006】しかしながら、内周表面に無孔質を溶融固
化したPTFE樹脂製ガスケットは、作製にさらにコス
トがかかるという問題点もある。このように、PTFE
樹脂を用いるシール部材は、硬度が高く、経時的な応力
変性が大きいという欠点とそれをカバーするには、製造
コストがかかるという問題点がある。However, a gasket made of PTFE resin in which non-porous material is melted and solidified on the inner peripheral surface has a problem that the production cost is further increased. Thus, PTFE
A sealing member using a resin has a drawback that hardness is high and stress change with time is large, and there is a problem that manufacturing cost is required to cover it.
【0007】そこで、耐薬品性に優れ、長時間の使用に
よっても応力変性を生じることなく気密性と清潔さを維
持でき、製品に部材材料の溶出がなく安全で、生産性に
も優れたサニタリー配管用部材が望まれている。Therefore, sanitary products which are excellent in chemical resistance, can maintain airtightness and cleanliness without causing stress denaturation even when used for a long time, are safe without elution of component materials in products, and have excellent productivity. A piping member is desired.
【0008】[0008]
【発明が解決しようとする課題】本発明者らは、上記の
問題点を解決すべく、鋭意シール部材、特にサニタリー
配管用部材について検討を重ねた結果、耐薬品性に優
れ、長時間の使用によっても応力変性が小さく、気密性
と清潔さを維持でき、製品に部材材料の溶出がなく安全
で、生産性にも優れたシール部材を見出し、本発明を完
成させたものである。本発明により、上記の課題が解決
される。SUMMARY OF THE INVENTION The present inventors have conducted intensive studies on sealing members, particularly sanitary piping members, in order to solve the above-mentioned problems. As a result, they have excellent chemical resistance and can be used for a long time. The present invention has also found a seal member which is small in stress denaturation, can maintain airtightness and cleanliness, does not elute component materials in a product, is safe, and has excellent productivity, and has completed the present invention. According to the present invention, the above problems are solved.
【0009】[0009]
【課題を解決するための手段】本発明は、230℃〜3
80℃における溶融粘度が108ポアズ以下であるフッ
素樹脂を溶融成形してなるガスケットに関する。SUMMARY OF THE INVENTION The present invention relates to a method for producing an object at 230.degree.
The fluororesin melt viscosity of 10 8 poises at 80 ° C. relates gasket formed by melting.
【0010】好ましい実施態様においては、前記ガスケ
ットがフッ化アルコキシエチレン樹脂(PFA)、フッ
化エチレンプロピレン(FEP)、三フッ化塩化エチレ
ン樹脂(PCTFE)およびエチレン−四フッ化エチレ
ン樹脂(ETFE)からなる群から選択されるフッ素樹
脂から溶融成形される。In a preferred embodiment, the gasket is made of fluorinated alkoxyethylene resin (PFA), fluorinated ethylene propylene (FEP), chlorotrifluoroethylene resin (PCTFE) and ethylene-tetrafluoroethylene resin (ETFE). It is melt molded from a fluororesin selected from the group consisting of:
【0011】また、好ましい実施態様においては、前記
フッ素樹脂が、230℃〜380℃における溶融粘度が
106ポアズ以下のフッ素樹脂である。[0011] In a preferred embodiment, the fluorine resin is 230 ° C. to 380 melt viscosity at ° C. is 10 6 poises fluororesin.
【0012】また、好ましい実施態様では、接液面とな
るガスケット内周面の表面粗さがRz0.4μm以下で
ある。In a preferred embodiment, the inner peripheral surface of the gasket which is a liquid contact surface has a surface roughness of Rz 0.4 μm or less.
【0013】さらに好ましい実施態様では、本発明のガ
スケットは、フッ化アルコキシエチレン樹脂(PFA)
を溶融成形して得られる。In a further preferred embodiment, the gasket of the present invention comprises a fluorinated alkoxyethylene resin (PFA)
Is obtained by melt molding.
【0014】[0014]
【発明の実施の形態】本発明においては、特定の溶融粘
度を有するフッ素樹脂を溶融成形する点に特徴がある。
このような構成を採用することにより、応力緩和率およ
び内径寸法変化率が小さい(すなわち、長時間に渡り、
応力に対して変化が小さく、応力安定性がある)という
特性が生じ、フランジの締め付け圧が高くなってもガス
洩れ等を起こすことなく、かつ、再使用も可能となる
上、ガスケットの接液面の粗さを極力小さくすることが
できるため、上記応力安定性とあいまって、清潔さが維
持されるという効果を生じる。具体的な効果としては、
特にサニタリー配管において顕著に表れる。すなわち、
配管内へのガスケットのはみ出しがないかあっても最小
限に抑制されるため、配管中の液流を妨げることもな
く、かつ、接液部分の粗さが極めて小さいことから、液
の滞留が防止され、配管中の雑菌の繁殖が抑制される。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention is characterized in that a fluororesin having a specific melt viscosity is melt-molded.
By adopting such a configuration, the stress relaxation rate and the inner diameter dimensional change rate are small (that is, over a long time,
(Small change with respect to stress and stable in stress) occurs, and even if the tightening pressure of the flange increases, gas leakage does not occur and reuse is possible. Since the surface roughness can be made as small as possible, an effect of maintaining cleanliness in combination with the stress stability is produced. Specific effects include:
In particular, it appears remarkably in sanitary piping. That is,
Even if the gasket does not protrude into the pipe, it is minimized, so it does not hinder the flow of liquid in the pipe, and the roughness of the liquid contact part is extremely small, so that the liquid stays This prevents the growth of various bacteria in the piping.
【0015】溶融成形可能なフッ素樹脂をガスケット形
状に溶融成形したときに、ガスケットの応力安定性、良
好な弾性回復性という特性が発揮され、フランジの締め
付け圧が高くなってもガス洩れ等を起こすことがないこ
と及び接液面の粗さが小さくなるという効果が生じるこ
とは知られていない。特に、フッ素樹脂は全般に硬度が
高く、溶融成形可能なフッ素樹脂であってもPTFE樹
脂と同程度かそれより高い硬度を有するフッ素樹脂も多
い。そのようなフッ素樹脂を溶融成形することにより、
PTFE樹脂が有する応力不安定性(弾性回復の困難
性)等を改善できたことは、本発明者等が初めて発見し
た知見である。When a melt-moldable fluororesin is melt-molded into a gasket shape, the gasket exhibits the characteristics of stress stability and good elastic recovery, and even if the tightening pressure of the flange is increased, gas leakage occurs. It is not known that there is no such effect and that the effect of reducing the roughness of the liquid contact surface occurs. In particular, the fluororesin generally has a high hardness, and many fluororesins that can be melt-molded have the same or higher hardness as the PTFE resin. By melt molding such a fluororesin,
The fact that the PTFE resin was able to improve stress instability (difficulty of elastic recovery) and the like was a finding discovered by the present inventors for the first time.
【0016】本発明に用いられるフッ素樹脂の溶融粘度
は230℃〜380℃において、約108ポアズ以下で
ある。108ポアズを超えると、溶融成形がしにくくな
る傾向にある。The melt viscosity of the fluororesin used in the present invention is at 230 ° C. to 380 ° C., is less than or equal to about 10 8 poises. More than 10 8 poises, tends to be difficult to melt molding.
【0017】本発明に用いられるフッ素樹脂としては、
例えば、フッ化アルコキシエチレン樹脂(PFA)、フ
ッ化エチレンプロピレン(FEP)、三フッ化塩化エチ
レン樹脂(PCTFE)、エチレン−四フッ化エチレン
樹脂(ETFE)等が用いられる。取り扱い、応力緩和
性、表面粗さを小さくする観点からは、PFA、FE
P、ETFEが好ましい。The fluororesin used in the present invention includes:
For example, fluorinated alkoxyethylene resin (PFA), fluorinated ethylene propylene (FEP), chlorotrifluoroethylene resin (PCTFE), ethylene-tetrafluoroethylene resin (ETFE) and the like are used. From the viewpoint of handling, stress relaxation, and reducing surface roughness, PFA, FE
P and ETFE are preferred.
【0018】上記のフッ素樹脂の中でも、230℃〜3
80℃における溶融粘度が106ポアズ以下のフッ素樹
脂がより好ましい。溶融粘度が106ポアズを超える
と、高温の溶融状態を維持しつつ金型の隅々まで樹脂を
注入するためには、若干流動性が低下するため、長時間
にわたり溶融状態を維持しなければならなくなり、結果
として、熱エネルギーによる樹脂の分子鎖の切断が進
み、固化させた後の成形物の機械的強度が低下しやすく
なるからである。このような条件を満たす樹脂として
は、フッ化アルコキシエチレン樹脂(PFA)、フッ化
エチレンプロピレン(FEP)、またはエチレン−四フ
ッ化エチレン樹脂(ETFE)が挙げられる。Among the above fluororesins, 230 ° C to 3 ° C
Melt viscosity at 80 ° C. and more preferably 10 6 poises fluororesin. If the melt viscosity exceeds 10 6 poise, the fluidity is slightly reduced in order to inject the resin into every corner of the mold while maintaining the molten state at a high temperature, so the molten state must be maintained for a long time. This is because, as a result, the cutting of the molecular chains of the resin by thermal energy proceeds, and the mechanical strength of the solidified product tends to decrease. Examples of the resin satisfying such conditions include fluorinated alkoxyethylene resin (PFA), fluorinated ethylene propylene (FEP), and ethylene-tetrafluoroethylene resin (ETFE).
【0019】溶融成形とは、フッ素樹脂を加熱して流動
状態にして、金型に注入、固化させて成形する方法の総
称であり、射出成形、押出成形、ブロー成形等が挙げら
れる。これらの方法は、用いるフッ素樹脂により適宜選
択すれば良い。例えば、PFAあるいはPCTFEを用
いる場合は、押出成形、射出成形が好ましく、FEPあ
るいはETFEを用いる場合は、押出成形、ブロー成
形、射出成形が用いられる。The term "melt molding" is a general term for a method of heating a fluororesin into a fluidized state, injecting it into a mold, and solidifying the same, and includes injection molding, extrusion molding, blow molding and the like. These methods may be appropriately selected depending on the fluororesin used. For example, when PFA or PCTFE is used, extrusion molding and injection molding are preferable, and when FEP or ETFE is used, extrusion molding, blow molding and injection molding are used.
【0020】射出成形、押出成形、ブロー成形等の溶融
成形は、それぞれの形態に応じた適切な装置を当業者が
選択し、適切な条件を設定して行えばよい。The melt molding such as injection molding, extrusion molding, blow molding and the like may be performed by a person skilled in the art selecting an appropriate apparatus according to each form and setting appropriate conditions.
【0021】本発明の溶融可能なフッ素樹脂を溶融成形
して得られるガスケット(以下、本発明のガスケットと
いう)の接液面となる内周面の表面粗さは、Rz約0.
4μm以下が好ましい。Rz約0.2μm以下がより好
ましく、Rz約0.15μm以下がさらに好ましい。本
発明のガスケットの表面粗さは、溶融成形することによ
り所望の値(Rz約0.15μm〜約0.2μm)が得
られ、微小な調整を要する場合を除き、切削加工する必
要がほとんどない。従来から用いられているPTFEを
圧縮成形した後、切削して得られるガスケットの表面粗
さが、ほぼ、Rz5μm前後、よく切れるバイトを用い
てもRz約0.6μmである点を考慮すると、本発明
は、切削加工が不要であって、かつ、表面が滑らかな接
液面を有するガスケットが得られるという、さらに優れ
た効果を生じる。すなわち、従来のガスケットと比較し
て、効率よく、かつ性能の優れたガスケットを安価に提
供できる。The gasket obtained by melt-molding the fusible fluororesin of the present invention (hereinafter referred to as the gasket of the present invention) has a surface roughness Rz of about 0.
It is preferably 4 μm or less. Rz is preferably about 0.2 μm or less, and more preferably about 0.15 μm or less. A desired value (Rz of about 0.15 μm to about 0.2 μm) can be obtained by melt-molding the surface roughness of the gasket of the present invention, and there is almost no need to perform a cutting process unless a minute adjustment is required. . Considering that the surface roughness of the gasket obtained by compression molding of the conventionally used PTFE and then cutting is approximately Rz 5 μm, and Rz about 0.6 μm even when using a cutting tool that cuts well, The present invention has an even more excellent effect that a gasket that does not require cutting and has a smooth liquid contact surface can be obtained. That is, a gasket that is more efficient and has higher performance than the conventional gasket can be provided at low cost.
【0022】なお、溶融成形条件等によってはガスケッ
トの内周面(すなわち接液面)の表面粗さがRz約0.
4μmを超える場合があるが、この場合、内周面側を熱
処理することにより、Rzを約0.4μm以下とするこ
とができる。熱処理の方法としては、300℃〜500
℃により所定時間発熱体表面に接触させる方法が挙げら
れる。The surface roughness of the inner peripheral surface (that is, the liquid contact surface) of the gasket may be about Rz of about 0,0 depending on the melt molding conditions and the like.
Although it may exceed 4 μm, in this case, Rz can be reduced to about 0.4 μm or less by heat-treating the inner peripheral surface side. As a method of heat treatment, 300 ° C to 500 ° C
A method of contacting the surface of the heating element with the temperature for a predetermined time.
【0023】なお、表面粗さRzは、十点平均粗さを意
味し、粗さ曲線からその平均線の方向に0.8mm抜き
取り、この抜き取り部分の平均線から縦倍率の方向に測
定した、最も高い山頂から5番目までの山頂の標高の絶
対値の平均値と、最も低い谷底から5番目までの谷底の
標高の絶対値の平均値との和を求め、この値をμmで表
したものをいう。The surface roughness Rz means a ten-point average roughness, and 0.8 mm was extracted from the roughness curve in the direction of the average line, and was measured in the direction of the longitudinal magnification from the average line of the extracted portion. The sum of the average of the absolute values of the altitudes of the valley bottoms from the highest to the fifth and the average of the absolute values of the valleys of the lowest valley from the fifth to the fifth is expressed in μm. Say.
【0024】また、ガスケットの形状は特定されない。
図1は本発明のガスケットの形状を示す断面模式図であ
る。図1の(1)はシール面平滑形状であり、図1の
(2)および(3)は、シール面テーパ形状であり、図
1の(4)は、(1)と(2)との組み合わせであり、
図1の(5)及び(6)は、シール面凸型形状であるガ
スケットである。Further, the shape of the gasket is not specified.
FIG. 1 is a schematic sectional view showing the shape of the gasket of the present invention. FIG. 1 (1) shows a smooth sealing surface, FIGS. 1 (2) and (3) show a sealing surface taper shape, and FIG. 1 (4) shows a relationship between (1) and (2). Combination
(5) and (6) of FIG. 1 are gaskets having a convex shape on the sealing surface.
【0025】以下、本発明のガスケットの特性について
記載する。本発明のガスケットを、60Kgf/cm2
の締め付け面圧で、130℃で24時間処理した場合、
その応力緩和率は、好ましくは約15%以下、より好ま
しくは約10%以下、さらに好ましくは約5%以下であ
る。応力緩和率が約15%を超えると、弾性回復ができ
にくくなりガス洩れが生じる虞がある。特に、PFA
は、上記範囲であることが好ましい。Hereinafter, characteristics of the gasket of the present invention will be described. The gasket of the present invention was used for 60 kgf / cm 2
When treated at 130 ° C for 24 hours with the tightening surface pressure of
The stress relaxation rate is preferably about 15% or less, more preferably about 10% or less, and even more preferably about 5% or less. If the stress relaxation rate exceeds about 15%, it is difficult to recover elasticity, and gas leakage may occur. In particular, PFA
Is preferably in the above range.
【0026】また、60Kgf/cm2の締め付け面圧
で、130℃で48時間処理した場合、本発明のガスケ
ット、例えば、PFA製ガスケットの応力緩和率は約5
%以下、好ましくは約2%以下となるのに対し、従来の
PTFEは20%を超え、PFA製のガスケットは応力
耐性に優れており、変形が少なく、弾性回復性にも優れ
ていることがわかる。 なお、応力緩和率は以下の式で
求められる。Further, when the gasket of the present invention, for example, a gasket made of PFA, is treated at 130 ° C. for 48 hours with a tightening surface pressure of 60 kgf / cm 2 , the stress relaxation rate is about 5%.
% Or less, preferably about 2% or less, whereas the conventional PTFE exceeds 20%, and the gasket made of PFA has excellent stress resistance, low deformation and excellent elastic recovery. Understand. The stress relaxation rate is obtained by the following equation.
【0027】[0027]
【数1】 (Equation 1)
【0028】また、本発明のガスケットの内径寸法変化
率は、極めて小さい。室温で30〜90Kgf/cm2
の締め付け面圧で、24時間〜48時間荷重をかけた場
合でも、好ましくは約−0.2%〜約0.5%程度、好
ましくは約−0.1%〜約0.2%程度である。130
℃で、24〜48時間荷重をかけた場合でも、好ましく
は約−0.1%〜約0.5%程度であり、好ましくは0
%〜約0.3%程度である。なお、内径寸法変化率は以
下の式で求められる。The rate of change in the inner diameter of the gasket of the present invention is extremely small. 30 to 90 kgf / cm 2 at room temperature
Even if a load is applied for 24 hours to 48 hours at a tightening surface pressure of about, preferably about -0.2% to about 0.5%, preferably about -0.1% to about 0.2%. is there. 130
Even when a load is applied at 24 ° C. for 24 to 48 hours, it is preferably about −0.1% to about 0.5%, and preferably about 0% to about 0.5%.
% To about 0.3%. The inner diameter dimensional change rate is obtained by the following equation.
【0029】[0029]
【数2】 (Equation 2)
【0030】特に、PFA製のガスケットの内径寸法変
化率は、室温で、30〜90Kgf/cm2の締め付け
面圧で、24時間〜48時間荷重をかけた場合、約−
0.1%〜約0.2%程度であるのに対し、従来のPT
FE製ガスケットの内径寸法変化率は、約−0.3%〜
約−0.9%である。このことは、PTFE製のガスケ
ットが内径の約0.3%〜0.9%の分だけ、配管内に
はみ出していることを示しているが、本発明のガスケッ
トは、ほとんど、はみ出していないことを示している。In particular, the rate of change in the inner diameter of the gasket made of PFA is about-when the load is applied for 24 to 48 hours at room temperature with a tightening surface pressure of 30 to 90 kgf / cm 2.
While it is about 0.1% to about 0.2%, the conventional PT
The inner diameter dimensional change rate of the FE gasket is about -0.3% ~
About -0.9%. This indicates that the PTFE gasket protrudes into the pipe by about 0.3% to 0.9% of the inner diameter, but the gasket of the present invention hardly protrudes. Is shown.
【0031】また、本発明のガスケットを、60Kgf
/cm2の締め付け面圧で、130℃で48時間処理し
た場合、内径寸法変化率は、好ましくは約0.5%〜約
−0.5%、より好ましくは約0.4%〜約0%、さら
に好ましくは約0.3%〜約0%である。約0.5%を
超えるとガスケットの内径が拡大し、パイプとガスケッ
トの接液面との間に滞留部分が生じて好ましくなく、約
−0.5%より小さくなるとガスケットの内径が縮小し
て、ガスケットが管内にはみ出し、滞留やガスケットの
汚れを生じて、反応の遅延、副反応の原因、汚染の原因
となるので好ましくない。Also, the gasket of the present invention is
When treated at 130 ° C. for 48 hours at a clamping surface pressure of / cm 2, the rate of change in inner diameter is preferably about 0.5% to about −0.5%, more preferably about 0.4% to about 0%. %, More preferably from about 0.3% to about 0%. If it exceeds about 0.5%, the inner diameter of the gasket increases, and a stagnant portion is formed between the pipe and the liquid contact surface of the gasket, which is not preferable. If it is less than about -0.5%, the inner diameter of the gasket decreases. In addition, the gasket protrudes into the pipe, causing stagnation and contamination of the gasket, which is undesirable because it causes a reaction delay, a side reaction, and a contamination.
【0032】本発明のPFA製のガスケットを60Kg
f/cm2の締め付け面圧で、130℃で48時間処理
した場合、内径寸法変化率は約0.33%であるのに対
して、同一条件でPTFE製のガスケットの内径寸法変
化率は約−5%であるので、一層本発明の優位性が明ら
かとなる。The gasket made of PFA of the present invention is 60 kg.
When treated at 130 ° C. for 48 hours with a tightening surface pressure of f / cm 2, the rate of change in inner diameter is about 0.33%, while the rate of change in inner diameter of a PTFE gasket is about the same under the same conditions. Since it is -5%, the superiority of the present invention becomes clearer.
【0033】[0033]
【実施例】以下、本発明を実施例に基づいて説明する
が、本発明がこの実施例に限られないことはいうまでも
ない。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on embodiments, but it goes without saying that the present invention is not limited to these embodiments.
【0034】(実施例1)PFA(ダイキン工業株式会
社製)を射出成形機(名機製作所製)を用いて370℃
で射出成形し、図1の(6)の形状を有する厚さ3m
m、外径65mm、内径35mm、面積23.56cm2の
ガスケットを作成した。Example 1 PFA (manufactured by Daikin Industries, Ltd.) was heated at 370 ° C. using an injection molding machine (manufactured by Meiki Seisakusho).
Injection molding with a thickness of 3 m having the shape of (6) in FIG.
m, an outer diameter of 65 mm, an inner diameter of 35 mm, and an area of 23.56 cm 2 were prepared.
【0035】同様に、比較例として、PTFE(デュポ
ン社製)を切削加工機を用いて、厚さ3mm、外径65
mm、内径35mm、面積23.56cm2のガスケットを
作成した。Similarly, as a comparative example, PTFE (manufactured by DuPont) was cut using a cutting machine to a thickness of 3 mm and an outer diameter of 65 mm.
A gasket having a diameter of 35 mm, an inner diameter of 35 mm and an area of 23.56 cm 2 was prepared.
【0036】得られたガスケットを用いて、その性能を
調べた。結果を表1に示す。The performance of the obtained gasket was examined. Table 1 shows the results.
【0037】[0037]
【表1】 [Table 1]
【0038】表1の結果を、図2および図3で示す。図
2は、締付面圧と応力緩和率との関係を示した図であ
り、図3は締付面圧とガスケットの内径寸法変化率の関
係を示す図である。図2から室温及び130℃での応力
緩和率は、本発明のPFA製のガスケットの方が比較例
のPTFE製ガスケットより小さく、弾力性に富んでい
ることが示された。また、図3からPFAは内径寸法変
化率がほとんど0に近いのに対して、比較例のPTFE
は−1%〜−4%であり、大きく配管内にはみ出すこと
が明らかである。The results in Table 1 are shown in FIG. 2 and FIG. FIG. 2 is a diagram showing the relationship between the tightening surface pressure and the stress relaxation rate, and FIG. 3 is a diagram showing the relationship between the tightening surface pressure and the rate of change in the inner diameter of the gasket. FIG. 2 shows that the gasket made of PFA of the present invention has a smaller stress relaxation rate at room temperature and 130 ° C. than the gasket made of PTFE of the comparative example, and has a higher elasticity. In addition, from FIG. 3, the PFA has an inner diameter dimensional change rate of almost zero, whereas the PTFE of the comparative example
Is from -1% to -4%, and it is apparent that it largely protrudes into the piping.
【0039】また、得られたPFA及びPTFE製ガス
ケットの内周面(接液面)の表面粗さRzは、それぞ
れ、0.2μmおよび0.6μmであり、本発明のPF
A製ガスケットの方が滑らかであった。その電子顕微鏡
写真を図4〜図7に示す。図4及び図5は、それぞれ、
PFAを溶融成形して得られたガスケットの内周面の倍
率100倍、及び10,000倍の写真であり、図6お
よび図7は、それぞれ、PTFEを切削加工して得られ
たガスケットの内周面の倍率100倍、及び10,00
0倍の写真である。同倍率の図4と図6、および図5と
図7とを比較すると表面の滑らかさの相違は歴然として
いる。このように、PFAの溶融成形で得られたガスケ
ットの内周面は、明らかに切削加工して得られたPTF
Eの内周面よりも滑らかであることがわかる。The surface roughness Rz of the inner peripheral surface (liquid contact surface) of the obtained gasket made of PFA and PTFE is 0.2 μm and 0.6 μm, respectively.
The gasket made from A was smoother. The electron micrographs are shown in FIGS. FIG. 4 and FIG.
FIGS. 6 and 7 are photographs at magnifications of 100 times and 10,000 times of the inner peripheral surface of the gasket obtained by melt-molding PFA. FIGS. 6 and 7 show the gasket obtained by cutting PTFE, respectively. Peripheral magnification of 100x and 10,000
It is a photograph of 0 times. 4 and 6 and FIGS. 5 and 7 at the same magnification, the difference in surface smoothness is obvious. As described above, the inner peripheral surface of the gasket obtained by the melt molding of PFA is clearly formed of the PTF obtained by cutting.
It turns out that it is smoother than the inner peripheral surface of E.
【0040】以上の結果から、本発明のガスケットは従
来のPTFE製のガスケットに比べて、応力耐性に優れ
ており、変形が少なく、弾性回復性にも優れていること
がわかる。また、本発明のガスケットは容易に製造でき
る上に、表面が極めて平滑である。From the above results, it can be seen that the gasket of the present invention has better stress resistance, less deformation, and better elastic recovery than the conventional PTFE gasket. In addition, the gasket of the present invention can be easily manufactured and has a very smooth surface.
【0041】(実施例2)実施例1で作成したガスケッ
トを用いて、熱サイクル試験によるガスケット圧縮量と
ガス漏洩量とを測定した。試験フランジに本発明のPF
A製ガスケット又は比較例のPTFEガスケットを装着
してN2ガス(0.392Mpa(4.0kgf/cm2))が密閉でき
るまで締込みナットを締め、130℃の熱風炉中に放置
し、所定の加熱時間経過後取り出した。加熱した圧力容
器を室温まで冷却されるのを待って、密閉した圧力容器
中にN2ガスを充填し、水中置換法によりガスケット部
分から漏洩するガスを所定時間回収して、洩れとした。
ガス漏洩の測定後、再びテストガスを密閉できる状態ま
でナットに増締めを行い、所望の累計加熱時間まで、加
熱と測定を繰り返した。結果を表2に示す。(Example 2) The gasket prepared in Example 1 was used to measure the amount of gasket compression and the amount of gas leakage in a heat cycle test. Test flange of the present invention
Wearing the PTFE gasket A gasket or Comparative Example N 2 gas (0.392Mpa (4.0kgf / cm 2) ) to tighten the tightening nut until it sealed and left in a hot air oven at 130 ° C., predetermined heating Removed after a lapse of time. After the heated pressure vessel was cooled to room temperature, the sealed pressure vessel was filled with N 2 gas, and the gas leaking from the gasket portion by the underwater replacement method was collected for a predetermined time to be leaked.
After the measurement of gas leakage, the nut was retightened until the test gas could be sealed again, and heating and measurement were repeated until the desired cumulative heating time. Table 2 shows the results.
【0042】[0042]
【表2】 [Table 2]
【0043】表2の結果は、比較例のPTFE製ガスケ
ットは、圧縮率を高めても漏洩量が多いのに対して本発
明のPFA製ガスケットは圧縮率が小さいにも係わら
ず、漏洩量も少なかった。このことは、本発明のガスケ
ットが耐熱性、応力耐性に優れていることを示してい
る。The results in Table 2 show that the PTFE gasket of the comparative example has a large amount of leakage even when the compression ratio is increased, whereas the PFA gasket of the present invention has a small amount of leakage despite the small compression ratio. There were few. This indicates that the gasket of the present invention is excellent in heat resistance and stress resistance.
【0044】[0044]
【発明の効果】特定の溶融粘度を有するフッ素樹脂を溶
融成形して得られるガスケットは、耐薬品性に優れ、長
時間の使用によっても応力変性が小さく、気密性に優れ
ているうえ、生産性にも優れている。また、ガスケット
の接液面の粗さを極力小さくすることができるため、上
記応力安定性とあいまって、液の滞留が防止され、配管
中の雑菌の繁殖が抑制されるので、清潔さが維持され
る。The gasket obtained by melt-molding a fluororesin having a specific melt viscosity is excellent in chemical resistance, has small stress denaturation even after long-term use, has excellent airtightness, and has high productivity. Is also excellent. In addition, since the roughness of the liquid contact surface of the gasket can be minimized, in combination with the above-mentioned stress stability, the accumulation of liquid is prevented, and the propagation of various bacteria in the piping is suppressed, so that the cleanliness is maintained. Is done.
【図1】 本発明のガスケットの形状を示す模式図であ
る。FIG. 1 is a schematic view showing a shape of a gasket of the present invention.
【図2】 締付面圧と応力緩和率との関係を示す図であ
る。FIG. 2 is a diagram showing a relationship between a tightening surface pressure and a stress relaxation rate.
【図3】 締付面圧とガスケットの内径寸法変化率の関
係を示す図である。FIG. 3 is a diagram illustrating a relationship between a tightening surface pressure and a rate of change in an inner diameter dimension of a gasket.
【図4】 PFAを溶融成形して得られたガスケットの
内周面を100倍に拡大した電子顕微鏡写真である。FIG. 4 is an electron micrograph of the inner peripheral surface of a gasket obtained by melt-molding PFA at a magnification of 100 times.
【図5】 PFAを溶融成形して得られたガスケットの
内周面を10,000倍に拡大した電子顕微鏡写真であ
る。FIG. 5 is an electron micrograph of the inner peripheral surface of a gasket obtained by melt-molding PFA at a magnification of 10,000 times.
【図6】 PTFEを切削加工して得られたガスケット
の内周面を100倍に拡大した電子顕微鏡写真である。FIG. 6 is an electron micrograph of the inner peripheral surface of a gasket obtained by cutting PTFE, which is magnified 100 times.
【図7】 PTFEを切削加工して得られたガスケット
の内周面を10,000倍に拡大した電子顕微鏡写真で
ある。FIG. 7 is an electron micrograph of the inner peripheral surface of a gasket obtained by cutting PTFE, which is magnified 10,000 times.
1 シール面テーパ形状 2 シール面凸型形状 1 Sealed surface tapered shape 2 Sealed surface convex shape
─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成12年1月31日(2000.1.3
1)[Submission date] January 31, 2000 (200.1.3
1)
【手続補正1】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】特許請求の範囲[Correction target item name] Claims
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【特許請求の範囲】[Claims]
Claims (5)
108ポアズ以下であるフッ素樹脂を溶融成形してな
る、ガスケット。1. A melt viscosity at 230 ° C. to 380 ° C. is formed by melting the fluororesin is 10 8 poises, gaskets.
チレン樹脂(PFA)、フッ化エチレンプロピレン(F
EP)、三フッ化塩化エチレン樹脂(PCTFE)およ
びエチレン−四フッ化エチレン樹脂(ETFE)からな
る群から選択されるフッ素樹脂である請求項1に記載の
ガスケット。2. The method according to claim 2, wherein the fluororesin is a fluoroalkoxyethylene resin (PFA), a fluoroethylenepropylene (F)
The gasket according to claim 1, wherein the gasket is a fluororesin selected from the group consisting of EP), ethylene trifluorochloride resin (PCTFE), and ethylene-tetrafluoroethylene resin (ETFE).
における溶融粘度が106ポアズ以下のフッ素樹脂であ
る請求項1または2に記載のガスケット。3. The method according to claim 1, wherein the fluororesin is 230 to 380 ° C.
The gasket of claim 1 or 2 melt viscosity of less fluororesin 10 6 poise at.
さがRz0.4μm以下である、請求項1ないし3いず
れかの項に記載のガスケット。4. The gasket according to claim 1, wherein a surface roughness of an inner peripheral surface of the gasket serving as a liquid contact surface is Rz 0.4 μm or less.
レン樹脂(PFA)を溶融成形して得られたガスケット
である、請求項1ないし4いずれかの項に記載のガスケ
ット。5. The gasket according to claim 1, wherein the gasket is a gasket obtained by melt-molding a fluorinated alkoxyethylene resin (PFA).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11115559A JP3056482B1 (en) | 1999-04-22 | 1999-04-22 | gasket |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11115559A JP3056482B1 (en) | 1999-04-22 | 1999-04-22 | gasket |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP3056482B1 JP3056482B1 (en) | 2000-06-26 |
| JP2000303058A true JP2000303058A (en) | 2000-10-31 |
Family
ID=14665547
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11115559A Expired - Fee Related JP3056482B1 (en) | 1999-04-22 | 1999-04-22 | gasket |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3056482B1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023157914A1 (en) * | 2022-02-17 | 2023-08-24 | Ntn株式会社 | Sealing resin composition and seal |
| JP2023120166A (en) * | 2022-02-17 | 2023-08-29 | Ntn株式会社 | Resin composition for seal, and seal |
| JP7364811B1 (en) | 2022-06-03 | 2023-10-18 | Ntn株式会社 | Seal resin composition and seal |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6416840B1 (en) | 1994-11-04 | 2002-07-09 | Daikin Industries, Ltd. | Fluorine-containing meltable resin composition |
-
1999
- 1999-04-22 JP JP11115559A patent/JP3056482B1/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023157914A1 (en) * | 2022-02-17 | 2023-08-24 | Ntn株式会社 | Sealing resin composition and seal |
| JP2023120166A (en) * | 2022-02-17 | 2023-08-29 | Ntn株式会社 | Resin composition for seal, and seal |
| JP7364812B2 (en) | 2022-02-17 | 2023-10-18 | Ntn株式会社 | Seal resin composition and seal |
| JP7364811B1 (en) | 2022-06-03 | 2023-10-18 | Ntn株式会社 | Seal resin composition and seal |
| JP2023178194A (en) * | 2022-06-03 | 2023-12-14 | Ntn株式会社 | Sealing resin composition and seal |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3056482B1 (en) | 2000-06-26 |
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