WO1996034902A1 - Elastomere fluore - Google Patents
Elastomere fluore Download PDFInfo
- Publication number
- WO1996034902A1 WO1996034902A1 PCT/JP1995/000870 JP9500870W WO9634902A1 WO 1996034902 A1 WO1996034902 A1 WO 1996034902A1 JP 9500870 W JP9500870 W JP 9500870W WO 9634902 A1 WO9634902 A1 WO 9634902A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- weight
- molecular weight
- parts
- elastomer
- units
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F214/18—Monomers containing fluorine
- C08F214/26—Tetrafluoroethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F214/18—Monomers containing fluorine
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F214/18—Monomers containing fluorine
- C08F214/22—Vinylidene fluoride
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F214/18—Monomers containing fluorine
- C08F214/28—Hexyfluoropropene
Definitions
- the present invention relates to a novel fluorine-containing elastomer, and more particularly, to a fluorine-containing material which is preferably used as a material for fuel hoses, filler hoses, valves, 0-rings, etc., which require chemical resistance and solvent resistance. This is about Elastomer.
- Fluoro-elastomer has excellent heat resistance, solvent resistance, chemical resistance, etc., so it is used under particularly severe conditions.
- 0-Sealing materials such as oil, oil seal, packing, gasket, etc. Widely used as a diaphragm.
- An object of the present invention is to provide a fluoroelastomer which can sufficiently vulcanize both a low molecular weight component and a high molecular weight component and has good moldability, especially extrudability. It is.
- the present invention comprises (a) vinylidenefluoride units, (mouth) hexafluoropropylene units and optionally (c) 35% by weight or less of tetrafluoroethylene units, and (a) units (Mouth) unit weight ratio is 40:60 to 80:20, containing bound iodine,
- (D) A fluorinated elastomer characterized in that the ratio MwZMn between the weight average molecular weight (Mw) and the number average molecular weight (Mn) is 4 or more and less than 8.
- FIG. 1 is a graph showing one example of the molecular weight distribution of the fluorine-containing elastomer of the present invention.
- the fluoroelastomer of the present invention has a vinylidene fluoride unit (hereinafter abbreviated as VdF unit) and a hexafluoropropylene unit (hereinafter abbreviated as HFP) as essential constituent units. Furthermore, tetrafluoroethylene units (hereinafter T (Abbreviated as FE unit), and the ratio of the VdF unit to the HFP unit must be in the range of 0.40: 60 to 80:20 in terms of weight ratio. When the number of VdF units is smaller than this, the polymerization rate is remarkably reduced, and it is difficult to obtain a polymer having a high molecular weight. Force ⁇ becomes resinous and elasticity decreases.
- the fluoroelastomer can further include a TFE unit in addition to the VdF unit and the HFP unit.
- the unit is less than 35% by weight of the total amount, preferably 5 to 2%. It is necessary to be in the range of 5% by weight. If this content exceeds 35% by weight, the elasticity of the obtained fluoroelastomer will decrease.
- the preferred ratio between the VdF unit and the HFP unit in the fluorinated elastomer is in the range of 55:45 to 75:25 by weight in the case of the binary fluorinated elastomer containing no TFE unit. Yes, for ternary fluorine-containing elastomers containing TFE units, the range is 45:55 to 70:30.
- the binary fluorine-containing elastomer is used for applications requiring a low fluorine content, that is, a fluorine content of 65% by weight or less, and the ternary fluorine-containing elastomer has a high fluorine content, that is, a high fluorine content. It is used for applications requiring a fluorine content of 67% by weight Lh, such as automobile parts and chemical equipment parts that require oil resistance and chemical resistance.
- the fluorinated elastomer of the present invention is characterized by specific physical properties based on the molecular weight distribution in addition to the specific composition described above.
- the fluorocarbon elastomer of the present invention needs to be of a multi-peak type in which the molecular weight distribution is formed from two or more peaks.
- a multi-peak type not only provides excellent mechanical properties based on a high molecular weight component, but also provides good workability based on a low molecular weight component.
- an elastomer having a monopeak type that is, an elastomer having a single molecular weight distribution, it is not possible to simultaneously satisfy mechanical properties and processability.
- the fluorinated elastomer of the present invention has an intrinsic viscosity of 60 to 30 m 1 /, preferably 70 to 120 m 1, and a low molecular weight of 50,000 or less.
- the intrinsic viscosity number [77] is an index indicating the molecular weight. If the intrinsic viscosity is less than 60 m 1 / g, the tackiness at the time of roll kneading becomes large, making it difficult to handle, and if it exceeds 130 m 1 Z g, The molecular weight is too high, the flowability is reduced and extrusion is not possible.
- the vulcanization time is shorter and the degree of vulcanization is higher than that of a polymer to which bromine is bonded, and vulcanization having excellent physical properties is achieved.
- sulphate As described above, since iodine is easily desorbed as compared with other halogens such as bromine, the vulcanization time is shorter and the degree of vulcanization is higher than that of a polymer to which bromine is bonded, and vulcanization having excellent physical properties is achieved. Give sulphate.
- a method for introducing iodine into a polymer chain a method of co-polymerizing an iodine-containing vinyl compound and a method of polymerizing using an iodine compound as a chain transfer agent are known, but in the case of the present invention, The latter is advantageous, for example, by the methods described in JP-A-53-12591 and JP-A-60-221409, the molecular chain ends can be easily prepared. Iodine can be introduced.
- the chain transfer agent used in this case is, for example, monoiod methane, 1-iod methane, 1-o-d-11-propane , I-isopropyl, iodomethane, 1,2-jodoethane, 1,3-jodo-n-propane, and perfluoroiodide in which all hydrogen atoms of these compounds are replaced by fluorine atoms are preferred. It is.
- the iodine content in the polymer is usually in the range of 0.01 to 5% by weight, preferably 0.1 to 2.5% by weight, based on the total amount of Vd'F units, HFP units, TFE units and iodine. Is chosen.
- the multi-peak type fluorine-containing elastomer in the present invention can also be produced, for example, by blending a high molecular weight polymer and a low molecular weight polymer, each of which is produced separately.
- a chain transfer agent is added during the polymerization by the suspension polymerization method to carry out the polymerization, a multi-peak type polymer having a relatively sharp peak and a molecular weight distribution is advantageously obtained.
- a high molecular weight polymer having a peak on the high molecular weight side is first generated, and then a low molecular weight polymer having a peak on the low molecular weight side is generated by adding a chain transfer catalyst and, if necessary, a polymerization catalyst.
- a chain transfer agent the above-mentioned iodine compound is preferably used.
- an inert organic solvent in which a predetermined mixed monomer (prepared monomer) is dissolved is dispersed in an aqueous medium, and a suspension stabilizer and an oil-soluble catalyst are further added.
- the above-mentioned mixed monomer (additional monomer) is newly added to advance the polymerization.
- the composition of the monomer units in the resulting fluorinated elastomer is determined by the relationship between the charged monomer composition and the additional monomer composition.
- the composition of the charged monomer and the composition of the additional monomer are measured by gas chromatography, and the composition of the monomer unit in the fluorine-containing elastomer is measured by 1 SF-NMR after dissolving the elastomer in acetone.
- the molecular weight distribution is adjusted and iodine is introduced by adding the chain transfer agent.
- the inert organic solvent used in this suspension polymerization method an organic solvent which does not have a carbon-ice bond which easily causes radical chain transfer is used. -Trifluoretane is preferred both in terms of performance and economy. Methyl cellulose is preferred as the suspension stabilizer.
- a dialkyl peroxydicarbonate such as diisopropyl peroxydicarbonate is preferable because it has a high decomposition temperature.
- polyol vulcanization, polyamine calosulfurization, and baroxide vulcanization are used for vulcanizing the elastomer of the present invention.
- Examples of the compounding agent for vulcanizing a polyol include, for example, a polyhydroxy aromatic compound as a cross-linking agent, and at least one selected from an ammonium salt, a phosphonium salt, and an iminium salt as a vulcanization accelerator, and a biacid as an acid acceptor. And at least one selected from a valence metal oxide and a divalent metal hydroxide.
- Examples of the polyhydroxy aromatic compound include, for example, hydroquinone, 22-bis-hydroxyphenyl) propane (bisphenol A) .2,2-bis (4-hydroxyphenyl) fluorene (bisphenol AF) 4, 4′-dihydroxydiphenylmethane, 2,2-bis (4-hydroxyphenyl) butane, etc.
- ammonium salts, phosphonium salts, and immine salts include tetramethylammonium chloride, tetraethylammonium chloride, tetrabutylammonium chloride, tetrabutylammonium chloride, and tetrabutylammonium chloride.
- Muchloride tetrabutylammonium bromide, bis (benzyldiphenylphosphine) imidimchloride, tetrabutylphosphonium chloride, benzyltriphenylphosphonyl chloride, benzyltrioctylphosphonide Is suitable. It is used in an amount of usually 0.5 to 2 parts by weight, preferably 0.1 to 1 part by weight, per 100 parts by weight of the fluoroelastomer. Each of these may be used alone or in combination of two or more. Further, as the divalent metal oxide or metal ice oxide, for example, oxides or hydroxides such as magnesium, potassium, zinc, and lead are used.
- vulcanization accelerating activators can be added in order to enhance the effect of the vulcanization accelerating agent.
- Representative examples of the vulcanization accelerating activator include sulfone compounds such as dimethyl sulfone / dichloro mouth diphenyl sulfone.
- the compounding agent for polyamine vulcanization for example, a combination of a polyamine compound as a crosslinking agent and a divalent metal oxide as an acid acceptor is used.
- this polyamide compound examples include hexamethylene diamine dilutamate, ⁇ , ⁇ ′ -dicinamilidene-6-hexamethylene diamine, and 4, 4′-bis (amino amino acid).
- Hexyl The methane carbamate or the like is used in an amount of usually 1 to 10 parts by weight, preferably 0.5 to 5 parts by weight, per 100 parts by weight of the fluorine-containing elastomer.
- These polyamine compounds may be used alone or in combination of two or more.
- the divalent metal oxide for example, oxides such as magnesium, calcium, zinc, and lead are used. The amount of the divalent metal oxide is usually from 30 to 30 weight parts per 100 weight parts of the fluorine-containing elastomer.
- Parts preferably in the range of 5 to 20 parts by weight. These may be used alone or in combination of two or more. Furthermore, when both the polyol vulcanizing compound and the polyamine vulcanizing compound are used in combination, the amount of the polyhydroxy aromatic compound per 100 parts by weight of the fluorinated elastomer is used. 0.1 to 5 parts by weight, a salt selected from among ammonium salt, phosphonium salt and iminium salt 0.05 to 2 parts by weight, polyamine compound 0.1 to 5 parts by weight, divalent metal oxide and divalent metal oxide It is preferable to mix 1 to 40 parts by weight of a compound selected from among the monovalent metal hydroxides.
- Organic peroxides used as baroxide vulcanizing compounds include those that easily generate peroxy radicals when heated, for example, 2,5-dimethyl-2,5-di (t-butylvinyloxy) hexine. Dialkyl peroxides such as -3,2,5-dimethyl-2,5-di (t-butylpyroxy) hexane are preferred. These organic peroxides generate radicals by heat during vulcanization, and these radicals act on iodine in the polymer to generate radicals in the polymer, and two radicals in the polymer follow each other. It is presumed that crosslinks are formed by bonding.
- the organic peroxide may be used singly or in combination of two or more.
- the amount of the organic peroxide is appropriately selected depending on the amount of active oxygen and the decomposition temperature.
- the amount is selected in the range of 0.05 to 10 parts by weight, preferably 0.05 to 5 parts by weight, per 0.05 part by weight. If the amount is less than 0.05 part by weight, the amount of generated radicals is so small that crosslinking does not proceed sufficiently.If the amount exceeds 10 parts by weight, the effect of the amount is not improved, and the economy is rather reduced.
- foaming due to peroxide decomposition gas occurs, and the mechanical properties tend to decrease. Also, in order to make the crosslinking reaction proceed more effectively, it is advantageous to use a polyfunctional unsaturated compound.
- the polyfunctional ⁇ ⁇ As an unsaturated compound, for example, Triaryl isocyanurate, tris (diarylamine) -S-triazine and the like are useful, and particularly preferred is triallyl isocyanurate. These polyfunctional unsaturated compounds may be used alone or in combination of one or more. The compounding amount thereof is usually 0.0 per 100 parts by weight of the elastomer. It is selected in the range of 1 to 0 parts by weight, preferably 0.1 to 5 parts by weight.
- the organic peroxide is added in an amount of 0.05 to 0.6 parts by weight based on 100 parts by weight of the fluorinated elastomer. Parts, preferably 0.05 to 0.4 parts by weight, and the amount of the polyfunctional unsaturated compound is 0.0! ⁇ 1.5 parts by weight, preferably 0.0! It is desirable to mix it with up to 1.0 part by weight.
- the compounding amount of the polyhydroxyaromatic compound is 0.5 to 3 parts by weight, preferably 1.0 to 2.5 parts by weight
- the compounding amount of the salt selected from the group consisting of ammonium salt, phosphonium salt and iminium salt is as follows. 0.1 to 0 parts by weight, preferably 0.2 to 0.75 parts by weight.
- various additives for example, reinforcing agents such as Ribonbon black, silica, clay, and talc, and processing aids such as resins can be added.
- the composition containing the fluorinated elastomer of the present invention is prepared by mixing and kneading the elastomer, the vulcanizing compounding agent and optional components used as necessary with a roll or Banbury mixer. be able to. After sufficiently kneading the composition thus obtained, it can be cut into long strips and extruded into an extruder to obtain a tube-shaped rod-shaped material.o Injection molding, press molding It is also possible to carry out molding by calendar molding or the like. Next, by performing secondary vulcanization as necessary, a desired vulcanized product can be obtained.
- a fluorinated elastomer having a limited molecular weight distribution processability, particularly extrusion processability, vulcanization properties are excellent, and there is no roll sticking, and the work efficiency is very good.
- An elastomer compound having excellent performance in productivity can be obtained. That is, an elastomer composed of two or more peaks of a low molecular weight component and a high molecular weight component and further containing iodine in at least the low molecular weight component is used. As a result, it is possible to obtain a compound having excellent processing properties with a low molecular weight component while maintaining excellent vulcanization properties with a high molecular weight component.
- the low molecular weight component is bound by the iodine in the molecule at the time of vulcanization, so that the properties of the vulcanized material are not reduced.
- the vulcanizates have low molecular weight components that are difficult to extract when immersed in a solvent or fuel oil, and have excellent solvent resistance. Therefore, the fluoroelastomer of the present invention requires heat resistance, solvent resistance, and fuel oil resistance of fuel hoses and parts around automobile engines, and is continuously processed by extrusion molding or the like, or is complicated. It is suitable for use as a material for parts and members that are difficult to process due to its complex shape. Further, it is suitably used as a molding material for injection molding, calender molding, compression molding and the like.
- the physical properties of the fluorinated elastomer, the physical properties of the vulcanized product, and the workability in each example were determined by the following methods.
- Intrinsic viscosity Dissolve the sample in methylethyl ketone to prepare a solution with a concentration of 0.1100 ml, and measure it at 35 ° C using a capillary viscometer.
- Roll adhesiveness Using a 6-inch kneading roll, a raw rubber or a vulcanizing agent-incorporated rubber was wound around the roll, and evaluated for the ease of peeling.
- a nitrogen autoclave equipped with an electromagnetic induction stirrer and having a volume of about 501 was thoroughly scavenged with nitrogen gas, and depressurization-nitrogen filling was repeated three times to replace with nitrogen and then deoxygenated under reduced pressure.
- CFC 1 2-Trichloro mouth-1, 2, 2-Trifluoroethane
- CFC 1 2-Trichloro mouth-1, 2, 2-Trifluoroethane
- a mixed monomer consisting of 16% by weight of vinylidenefluoride, 79.1% by weight of hexafluoropropylene and 6.3% by weight of tetrafluoroethylene was used as a charged gas to obtain 15 kgcm 2 It was charged until it became G.
- 0.2 g of iodomethane was charged, and further, as a catalyst, 15.6 g of a freon 1 13 solution containing 20.1% by weight of diisopropyl peroxydicarbonate was charged to initiate polymerization. As the polymerization reaction progresses, the pressure starts to drop.
- polymerization was carried out in the same manner as in Example 1 to produce a fluorine-containing elastomer.
- the polymerization initiator was diluted with Freon R113 to a concentration of 20% by weight and added.
- Table 2 shows the physical properties of the fluorinated elastomer thus obtained.
- Table 2 also shows the physical properties of a commercially available Florel FT-2320 [Sumitomo 3M Co., Ltd.] as Comparative Example 2.
- Reference Examples 1 and 2 With respect to 100 parts by weight of the elastomer obtained in Examples 1 to 5 and Comparative Example 1, 12 parts by weight of SRF force [Asahi Carbon Co., Ltd., “Shisto S”], C a (OH) 2 [Kyodai Chemical Industry Co., Ltd., “Calbit”] 6 parts by weight, MgO (I) [Kyowa Chemical Industry Co., Ltd., “Kyo-Mag 150”] 3 parts by weight, bisphenol AF 2 parts by weight Parts, bis (benzyldiphenylphosphine) iminium chloride 0.5 parts by weight, 2,5-dimethyl-2,5-di (t-butylvinyloxy) hexane [Nippon Oils & Fats Co., Ltd.
- the fluorine-containing elastomer obtained in the present example of the present invention does not stick to rolls and is easier to knead than the one of the comparative example.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP95917508A EP0824121A4 (en) | 1995-05-02 | 1995-05-02 | FLUORINATED ELASTOMER |
PCT/JP1995/000870 WO1996034902A1 (fr) | 1995-05-02 | 1995-05-02 | Elastomere fluore |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/JP1995/000870 WO1996034902A1 (fr) | 1995-05-02 | 1995-05-02 | Elastomere fluore |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1996034902A1 true WO1996034902A1 (fr) | 1996-11-07 |
Family
ID=14125896
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP1995/000870 WO1996034902A1 (fr) | 1995-05-02 | 1995-05-02 | Elastomere fluore |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0824121A4 (ja) |
WO (1) | WO1996034902A1 (ja) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1379563A2 (fr) * | 2001-01-10 | 2004-01-14 | Solvay (Societe Anonyme) | Procede de preparation de polymeres halogenes en deux etapes et polymeres halogenes plurimodales |
US20100068436A1 (en) * | 2006-10-25 | 2010-03-18 | Unimatec CO. Ltd | Fluorine-containing elastomer for molding fuel system parts and composition thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6440509A (en) * | 1987-08-07 | 1989-02-10 | Asahi Chemical Ind | Fluorine-containing elastomer for extrusion molding |
JPH02124910A (ja) * | 1988-07-29 | 1990-05-14 | Asahi Chem Ind Co Ltd | 易加工性フルオロエラストマー |
JPH04258614A (ja) * | 1991-02-14 | 1992-09-14 | Asahi Chem Ind Co Ltd | 含フッ素エラストマー |
JPH06279548A (ja) * | 1989-12-20 | 1994-10-04 | Asahi Chem Ind Co Ltd | 含フッ素エラストマー |
-
1995
- 1995-05-02 WO PCT/JP1995/000870 patent/WO1996034902A1/ja not_active Application Discontinuation
- 1995-05-02 EP EP95917508A patent/EP0824121A4/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6440509A (en) * | 1987-08-07 | 1989-02-10 | Asahi Chemical Ind | Fluorine-containing elastomer for extrusion molding |
JPH02124910A (ja) * | 1988-07-29 | 1990-05-14 | Asahi Chem Ind Co Ltd | 易加工性フルオロエラストマー |
JPH06279548A (ja) * | 1989-12-20 | 1994-10-04 | Asahi Chem Ind Co Ltd | 含フッ素エラストマー |
JPH04258614A (ja) * | 1991-02-14 | 1992-09-14 | Asahi Chem Ind Co Ltd | 含フッ素エラストマー |
Non-Patent Citations (1)
Title |
---|
See also references of EP0824121A4 * |
Also Published As
Publication number | Publication date |
---|---|
EP0824121A4 (en) | 1998-12-02 |
EP0824121A1 (en) | 1998-02-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2509388B2 (ja) | 含フッ素エラストマ―組成物 | |
RU2342403C2 (ru) | Полимеризация в водной эмульсии без эмульгатора для получения сополимеров фторированного олефина и углеводородного олефина | |
EP0127407B1 (en) | Core/shell fluoropolymer compositions | |
JP5465175B2 (ja) | (パー)フルオロエラストマー組成物 | |
CN102365326B (zh) | 含氟弹性体混合物、其制造方法、过氧化物硫化用组合物和成型品 | |
EP2373734B1 (en) | (per)fluoroelastomer composition | |
EP0543342A1 (en) | Fluorine-containing thermoplastic elastomer composition and process for its production | |
JPWO2008050588A1 (ja) | 燃料系部品成形用含フッ素エラストマーおよびその組成物 | |
KR101643423B1 (ko) | 가황성 플루오로엘라스토머 조성물 | |
JPH07196881A (ja) | 含フッ素系エラストマー加硫組成物 | |
JP2549255B2 (ja) | 含フッ素エラストマー | |
JP5051517B2 (ja) | エチレン/テトラフルオロエチレン共重合体組成物 | |
JP2013234215A (ja) | 含フッ素エラストマーの製造法 | |
JP2007056215A (ja) | パーオキサイド架橋可能なフッ素ゴム | |
JP4168189B2 (ja) | アクリルゴムとフッ素ゴムとの複合体、その製造方法および加硫性ゴム組成物 | |
JPH0711087A (ja) | フッ素系エラストマー組成物 | |
EP0824120A1 (en) | Fluoroelastomer | |
JP5998588B2 (ja) | 含フッ素エラストマーブレンド物およびその組成物 | |
JPH04258614A (ja) | 含フッ素エラストマー | |
WO1996034902A1 (fr) | Elastomere fluore | |
JP3001755B2 (ja) | 含フッ素エラストマー | |
JP2005140196A (ja) | 燃料電池用ガスケット | |
WO2000059999A1 (en) | Hydrogenated nitrile butadiene rubber thermoplastic fluoropolymer blend | |
JPS63277217A (ja) | 含フッ素エラストマ−及びその成形体 | |
JPH02160810A (ja) | 含フッ素エラストマー |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): US |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 1995917508 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref country code: US Ref document number: 1998 930119 Date of ref document: 19980211 Kind code of ref document: A Format of ref document f/p: F |
|
WWP | Wipo information: published in national office |
Ref document number: 1995917508 Country of ref document: EP |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 1995917508 Country of ref document: EP |