SG184158A1 - Fluororesin sheet - Google Patents
Fluororesin sheet Download PDFInfo
- Publication number
- SG184158A1 SG184158A1 SG2012069605A SG2012069605A SG184158A1 SG 184158 A1 SG184158 A1 SG 184158A1 SG 2012069605 A SG2012069605 A SG 2012069605A SG 2012069605 A SG2012069605 A SG 2012069605A SG 184158 A1 SG184158 A1 SG 184158A1
- Authority
- SG
- Singapore
- Prior art keywords
- sheet
- fluororesin
- perlite
- filler
- processing aid
- Prior art date
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- 239000010451 perlite Substances 0.000 claims abstract description 47
- 235000019362 perlite Nutrition 0.000 claims abstract description 47
- 239000000203 mixture Substances 0.000 claims abstract description 32
- 239000000945 filler Substances 0.000 claims abstract description 31
- 239000006057 Non-nutritive feed additive Substances 0.000 claims abstract description 30
- 238000000034 method Methods 0.000 abstract description 16
- 238000005096 rolling process Methods 0.000 description 25
- 239000007789 gas Substances 0.000 description 8
- 229920005989 resin Polymers 0.000 description 8
- 239000011347 resin Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000001035 drying Methods 0.000 description 6
- 238000007789 sealing Methods 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 5
- 241000630665 Hada Species 0.000 description 5
- 238000001354 calcination Methods 0.000 description 5
- 229930195733 hydrocarbon Natural products 0.000 description 5
- 150000002430 hydrocarbons Chemical class 0.000 description 5
- 238000004080 punching Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 239000004927 clay Substances 0.000 description 4
- 229910052570 clay Inorganic materials 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000003960 organic solvent Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 238000004508 fractional distillation Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000011435 rock Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- CNPVJWYWYZMPDS-UHFFFAOYSA-N 2-methyldecane Chemical compound CCCCCCCCC(C)C CNPVJWYWYZMPDS-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229920006026 co-polymeric resin Polymers 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 230000001747 exhibiting effect Effects 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000003566 sealing material Substances 0.000 description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000219357 Cactaceae Species 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 240000004760 Pimpinella anisum Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229920006231 aramid fiber Polymers 0.000 description 1
- 239000003849 aromatic solvent Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004434 industrial solvent Substances 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 229960000869 magnesium oxide Drugs 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- 235000012245 magnesium oxide Nutrition 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 239000011490 mineral wool Substances 0.000 description 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 1
- 239000005332 obsidian Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/18—Manufacture of films or sheets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/32—Component parts, details or accessories; Auxiliary operations
- B29C43/44—Compression means for making articles of indefinite length
- B29C43/46—Rollers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L27/00—Compositions of homopolymers or 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; Compositions of derivatives of such polymers
- C08L27/02—Compositions of homopolymers or 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; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L27/12—Compositions of homopolymers or 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; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or 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; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or 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; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or 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; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Abstract
SF-2226To provide a fluororesin sheet that is inexpensive and has a high compressibility and a process for producing the same.The fluororesin sheet is produced from a sheet-forming composition 5 containing (A) a fluororesin, (B) a filler (except perlite), (C) perlite and (D) a processing aid.
Description
SF-2226 1
FLUORCRESIN SHEET
Technical Field [COOL]
The present invention relates to a fluorcresin sheet.
[0002]
Sheets cbtained by filling a fluorcoresin with a filler and processing the resin into sheets have chemical resistance and heat resistance inherent inthe fluororesin, and in addition, they have been imparted with functicns and properties inherent in the filler or have been improved in creep resistance that is a defect of the fluororesin. Therefore, they have been often used as sealing materials, etc.
[0003]
As such a sealing material, the present inventor has disclosed aprocess for producing a fluorcoresin sheet containing a fluororesin, a filler and a precessing aid in Japanese Patent
Laid-Open Publication No. 2007-253519 (patent literature 1).
As this filler, clay or the like has been mentioned. By this production process, a flucroresin sheet, which has high recovery properties and high gas tight properties compatible with each
SE-2226 2 other and which 1g suited to a gasket material, can be obtained. 10004]
This fluororesin sheet, however, is liable to become a hard sheet having a low compressibility, and therefore, when this sheet isused for a gasket or the like, a high clamp pressure is necessary in order to obtain given sealing properties.
Moreover, when the sheet is hard like this, its processability as in punching the sheet into a gasket with a desired shape is poor. The processability needs to be further improved.
Patent Literature [GOC5]
Patent literature 1: Japanese Patent Laid-Open
Publication No. 2Z007-253518
Technical Problem [cooe]
The present invention has been made in the light of such problems as above, and 1t is an object of the present invention to provide a flucroresin sheet which has a high compressibility at a low clamp pressure, 1s inexpensive and has good processability.
SF-2226 3
Solution to Problem [C007]
Incrder to solve the above problems, the present inventors have earnestly studied, and as a result, they have found that a sheet produced from a composition containing a flucroresin, a filler (except perlite), perlite and a processing ald is inexpensive, has a high compressibility, acguires sealing properties equal to or higher than those of conventional products at a low clamp pressure and has good punching processability in punching the sheet into a gasket with a desired shape or the like, and they have accomplished the present invention.
Specific constitution of the present invention is described below.
The fluororesin sheet of the present invention is characterizedbybeingproduced froma sheet-forming composition containing (A} a flucroresin, (B) a filler {except perlite), {C) perlite and (D} a processing aid.
[0008]
The amount of the perlite (CC) in the composition is preferably 4 to 20 parts by weight based on 100 parts by weight of the total amount of the fluororesin (A), the filler (B) {except perlite) and the perlite (C}).
The “filler” referred to in the present application means
SF-2226 4 a filler other than perlite.
The amount of the processing aid (D) in the composition ig 5 to 50 parts by weight based on 100 parts by welght of the total amount of the fluororesin (A), the filler (B) (except perlite) and the perlite (C).
[0009]
In the fluororesin sheet of the present invention, porous perlite (C) and a filler (B) other than the perlite, such as clay, are used in combination, and the fluororesin sheet can be produced inexpensively.
By the present invention, a fluorocresin sheet which is excellent in secondary processing such as punchability into a shape of a gasket or the like, has a high compressibility at a low clamp pressure and exhibits good sealing properties even when it is used at a low clamp pressure can be obtained.
[0010]
The present invention is described in more detail hereinafter. <Fiuororesin sheet>
The fluororesin sheet of the present invention is
SE-22256 5 characterizedbybeingproduced froma sheet-forming composition containing (A) a flucroresin, (BY a filier (except perlite), (C) perlite and (DP) a processing aid. [C011] <{A) Fluorcresin>
Rs the fluororesin (A), anyof hitherto known fluororesins, such as polytetraflucroethylene resin (PTFE}, modified PTFE, polyvinylidene fluoride resin (PVDE), ethylene/tetraflucroethylene copolymer resin (ETFE), polychlorotrifluorcethylene resin (PCTIFE}, tetrafluorcethylene/hexafliuoropropylene ethylene copolymer resin (FEP) and tetrafluorocethylene/perflucroalkyl copolymer resin (PFA), can be preferably used. From the viewpoint of processability in extrusion molding, relling, etc., polytetrafluorcethylene resin (PTFE) is preferable among them, and PTFE fine powder obtained by emulsicn polymerization is particularly preferable. Since the PTFE fine powder has properties that it becomes fibrous when a shear force is applied, a composition and/or a sheet wherein the resin has been intertwined with the filler (B) and the perlite (CC) in the later-described process of stirring and mixing the components of the composition or forming of a sheet can be obtained, and therefore, a fluorcresin sheet having more excellent sealing properties and mechanical strength can be obtained.
SE-2226 6 0012]
When PYFE is used as the fluororesin (A), the aforesaid fluororesins other than the PTFE may be contained insmall amounts, for example, not more than 10% by weight (total amount of fluorocresins: 100% by weight).
As the fluororesin (A), a fluororesin in the form of a powder may be used as it is, or a dispersion in which fluororesin fine particles are dispersed in water may be used.
[0013] <{B} fillexr>
As the filler (BR), a filler other than the below—described perlite, for example, a carbon-based filler, such as graphite, carbon black, expanded graphite, activated carbon or carbon nanotube, an inorganic filler, suchas talc, mica, clay, calcium carbonate, magnesiumoxide, silicon carbide, alumina or silica, a powder of a resin, such as PPS, or the like is used according to the use purpose. A fiber material having a fiber length of not more than 10 mm, which is composed of carbon fiber, aramid fiber, rock wool or the like, may be used as the filler (B).
[0014]
According to the present invention, a fiuororesin sheet which has a low filling ratio of the flucroresin (A) andexhibits a high compressibility even if it has a high filling ratio of the filler (BR) can be obtained. The weight ratio between the
SF-2226 7 fluorcresin {A) andthe filler (B) (except perlite) ispreferably 1:0.1 to 3, more preferably 1:0.1 to 2.
When the filler (B) 1s contained in such an amount, 2 fluororesin sheet exhibiting properties of the filler ’ sufficiently can be obtained.
[0015] <{C) Perlite>
The perlite (C) is a foam of a volcanic-based rock having a high silica content {SiC;), and it is composed of silica {S10y, 70 to 80%), alumina (Al-Cs, 10 to 20%), and Na;0 and K:0 (total: 0 to 10%). Examples of the volcanic-based rocks include pearlstone, obsidian andpitchstone. Inthe present invention, any of foam of these rocks can be used, but pearlstone that is porous and has an excellent ¢il absorption ratio is particularly is preferable.
[0016]
Such perlite (C) is extremely lightweight, has excellent heat insulationproperties, is inexpensive andis incombustible.
On that account, a fulororesin sheet that is suitable for uses at high temperatures and is inexpensive can be obtained.
Moreover, the perlite {(C} is excellent also in liguid absorption properties, and therefore, it is considered that the perlite can absorb a processing aid (D) in the sheet-forming composition in the present invention. It is considered that
SF-2226 8 when the following process (I) is used for forming a sheet from the sheet-forming composition, a large number of pores in the perlite are impregnated with the processing aid (D} and keep it therein in the rolling step. It is also considered that by virtueof this, theporestructureocftheperliteisrarelycrushed in the rolling step, and when the processing aid (D} is vaporized in the subsequent drying step, voids (pores) are held in the perlite in the resulting sheet. Accordingly, it is considered that a fluororesin sheet having a particularly high compressibility and exhibiting proper sealing properties at a low clamp pressure can be cbtained.
[0017]
The amount of the perlite (C) in the sheet-forming compositionispreferably4to20partsbyweight, morepreferably 5 to 8 parts by weight, based on 100 parts by weight of the total amount [((AY+{B)+(C)) of the fluororesin {A), the filler (B) {except perlite} and the perlite (C).
Also in the resulting fluororesin sheet of the present : invention, the amount of the perlite {C) based on 100 parts by weight of (R)+{B}+{(C) is the same as above.
The mean particle diameter of the perlite (C} (measured by laser particle size distribution analyzer) is preferably not more than 150 pm, more preferably about 75 to 125 pm.
When the perlite (C) is contained in such an amount and
SF-2226 5 the mean particle diameter of the perlite (C) is in the above range, a fluororesin sheet having a high compressibility while maintaining high gas tight properties can be obtained.
When the amount of the perlite (C} in the sheet-forming composition is 5 to 8 parts by weight based on 100 parts by weight of the total amount of the fluororesin (A), the filler (B) (except perlite) and the perlite (C), a fluororesin sheet having a particularly goed balance of properties, such as low compressibility, highsealingproperties, hightensile strength and low stress relaxation properties, can be cbtained, so that such an amount is preferable. [00181 <{D} Processing aid>
As the processing aids (D), hithertc publicly known processing aids, such as petroleum-based hydrocarbon solvents, alcohols and water, can be used without any restriction.
[0019]
Examples of commercial products of the petroleum-based hydrocarbon solvents include Isopar C (hydreoccarbon-based organic solvent, fractional distillation temperature: 87 to 104°C), Isopar G (hydrocarbon-based organic solvent, fractional distillation temperature: 158 to 175°C) and Isopar M (hydrocarbon-based organic solvent, fractional distillation temperature: 218 to 253°C) (all manufactured by Exxon Mobil
SF-22246 106
Corporation), and Cactus Solvent REN (manufactured by Japan
Energy Corporation) as an industrial solvent having advantages, such as non normal hexane, low benzene and low aromatic solvent.
[06020]
When the following process (I) is used for preparing a fluororesin sheet, the amount of the processing aid (D) has only to be such an amount that an appropriate amount of the processing ald is present after the rolling step, and specifically, the amount of the processing aid (D) in the sheet~forming composition is preferably 5 to 50 parts by weight, more preferably 10 to 40 parts by weight, based on 100 parts by weight of the total amount of the fluororesin (A), the filler (B} (except perlite) and the perlite (C). When the processing aid (D) is used in such an amount, the raw materials can be easily homogeneously mixed and dispersed after blending, and besides, the resulting composition is excellent in processability into a sheet. When the following process {I} 1s used for preparing a fluororesin sheet, the fluororesincanbesufficientlyswollenintheinitial stage of the later-described rolling step. Moreover, all the processing aid does not vaporize before the later-described calcining step, and a sheet containing an appropriate amount of the processing aid after rolling can be obtained. : [00213
The sheet~forming composition consists essentially of the
SF-2226 11 fluororesin (A), the filler (B), the perlite (C) and the processing aid (D).
[0022]
For preparing the sheet-forming composition containing these components, these components have only to be added to the container at once or plural times by portions in an arbitrary order, then stirred and mized.
[0023]
Although the method to stir and mix the components is not specifically restricted, the fluororesin (A), the filler (B}, the perlite (C) and the processing aid (D) are blended in such
Amounts as correspond to the composition of the fluororesin sheet to be produced, and they are stirred and mixed in an arbitrary order. When the stirring efficiency is poor, it is possible that the processing aid is added in a large amount and after completion of stirring an excess processing aid is removed by filtration.
[0024]
As the temperature in the stirring and mixing of the components, a temperature that is lower than the roll temperature in the rolling step is preferable in order that the processing aid will not vaporize.
[0025] : [Process for producing fluororesin sheet]
SF-2226 12
The process for producing a flucororesin sheet of the praesent invention is not specifically restricted as long as a fluororesin sheet can be formed from the above-mentioned sheet-forming composition, and hitherto known processes are employable. Aprocess comprising subjecting the sheet-forming composition to preforming, rolling the resulting preform at a roll temperature of 40 to 80°C, then drying the preform and calcining it (also referred to as a “process (I}” hereinafter) is preferable. 16 This process (I) 1s described below in detail.
[0026] <Process (I>
The process (I) includes a preforming step, arolling step, a drying step and a calcining step in this order.
[6027] <Preforming step>
In the preforming step, the sheet-forming composition is extruded to produce a preform (extrudate).
The shape of the preform is not specifically restricted, but when efficiency of the subsequent sheet formation, homogeneity of sheet properties, etc. are taken into consideration, the preform preferably has a shape of a rod or a ribbon.
SF-2226 13
In the producticn process of the present invention, the preforming step is preferably carried out at a temperature lower than the roll temperature in the rolling step so that the processing aid will not vaporize.
[0028] <Rolling step>
In the rolling step subsequent to the preforming step, the preform is allowed to pass between rolling mill rolls such as twin rells te roll and form it into a sheet. i0 In the production process of the present invention, the rolling step is carried out at a roll temperature of 40 to 80°C.
When the roll temperature is in the above range, the hardness ¢f the fluororesin (A) is lowered a little, and the fluororesin sheet is apt to be densified. Moreover, all the processing aid (BD) does not completely vaporize. 10030]
If the rolling step is carried out at a temperature lower than 40°C, the processing aid tends to rarely vaporize. On the other hand, if the rolling is carried out at a temperature higher than 80°C, the processing aid (D) excessively vaporizes, and a filler-containing fluororesin sheet having a high compressibility tends to be unable tobe formed. Further, since the processing aid (D) excessively vaporizes, the amount of the processing aid remaining at the beginning of the rolling step
SF-2226 14 is small. Therefore, it tends to become impossible to sufficiently swell the fluorcresin (A) and make it fibrous, and the resulting fluororesin sheet tends to have poor strength.
Furthermore, because of abrupt vaporization of the processing h aid (D) in the composition, a bulge phenomenon occurs, and the gas tight properties of the fluororesin sheet tend tobe lowered. [00317
In the production process of the present invention, a step of further rolling the rolled sheet prepared by the above rolling stepmaybe included, that is, it is possible torepeat therolling step plural times {e.g., 3 to 50 times). In order that an appropriate amount cf the processing aldmay be left in the sheet after the rolling step, it is preferable to properly control the number of rolling times. When the rolling step is repeated, the distance between rolls is narrowed every time the rolling is repeated.
[0032]
In the sheet formation by rolling the preform using twin rolls, for example, the distance between rells is set to 0.5 to 20 mm, and the preform is rolled at a roll surface moving rate {sheet extrusicn rate) of 5 to 50 mm/sec. [C033] <Drying step>
In the drying step, the rolled sheet is allowed to stand
SF-2226 15 at ordinary temperature or heated at a temperature lower than the melting point of the fluororesin to remove the processing aid. [C034] <Calcining step> :
In the calcining step, the sheet given after the drying step is heated at a temperature not lower than the melting point . of the fluorcresin to sinter the sheet. When it is taken into consideration that thewhole sheet needs tobeuniformly calcined and in the cass of an excessively high temperature a fluorine-based harmful gas 1s generated, a suitable heating temperature is, for example, 340 to 370°C though it varies a little depending upon the type of the fluorcresin.
[0035] [Fluororesin sheet]
The fluororesin sheet 1s not specifically restricted provided that the sheet is produced from the sheet-forming composition. The fluororesin sheet is preferably a sheet produced by the above process (I). This flucroresin sheet is inexpensive and has a high compressibility. Specifically, the compressibility is preferably net less than 7%, more preferably not less than 8%, and its upper limit may be 15%. The leakage (gas tight properties, contactpressure against specimen of @48mm x 67mm x 1.5mm (thickness): 19.6 MPa, nitrogen gas internal
SE-2226 16 pressure: 0.98 MPa) is preferably not more than 7.0x107° Pa -m’/s, more preferably not more than 2.0x107? Pa-m’/s, and its lower limit may be 1.0x107° Pa-m’/s.
[0036]
Such a fluororesin sheet of the present invention can be used for a gasket, and a gasket made of the fluororesin sheet of the present invention can be used at high temperatures (e.qg., above 200°C) over a long period of time. From the fluororesin sheet, a gasket having high sealing properties can be obtained 16 even at a low clamp pressure.
The gasket canbe easily producedby cutting out (punching; an article of a desired shape from the fluororesin sheet of the present invention. The filler-containing fluororesin sheet of the present invention has ease of cutting (punching) and high handling properties.
[0037]
The production process of the present invention is further describedwithreference tothe followingexamples, but it should be construed that the present invention is in no way limited to those examples. 10038] <Test method>
SF-2226 17
From a sheet having a thickness of 1.5 mm, a specimen was prepared, andgas tight properties weremeasured inthe following manner.
[0038]
Leakage (gas tight properties)
A punched gasket specimen having a size of z48mm x 67mm was set between steel flanges (each flange: 100mm x 50mm (height), surface roughness Rmax = 12 um}, and a load was applied fo the specimen by a compression tester so that the contact pressure might become 19.6 MPa (Z0C kgf /cm*G) . Through a through-~hole for pressure injection provided at the flange, a nitrogen gas internal pressure of 0.98 MPa (1.0 kgf/cm?G) was applied to the gasket inner diameter side, thereafter the pressure injection pipe was sealed, and the specimen was kept for 1 hour. A change in pressure before and afier keeping of the specimen was read out by a pressure sensor, and from the pressure drop, a leakage was determined. [C040]
Stress relaxation
Stress relaxation ratios at 100°C and 200°C were measured on the basis of ASTM F38 B method.
[0041]
Compressibility
Compressibility was measured on the basis of ASTM F36.
SF-2226 18
Tensile strength
Tensile strength was measured on the basis of JIS R3453. [C042] [Example 1] :
In a kneader, 17.1 kg of PTFE (CD-1, manufactured by Asahi
Glass Co., Ltd.), 9.6 kg of finely powdered clay {(XN-D325, manufacturedby Anhui Snow SatisfiedNon~MetallicMaterialsCo.,
Ltd.), 1.7 kg of perlite (mean particle diameter: 100 um, manufactured by Qingdao Yuzhou Chemical Co., Ltd.) and 7.5 kg of a hydrocarbon-based organic solvent (Isopar G, Exxon Mobil
Corporation) were mixed at room temperature for 15 minutes.
Thereafter, themixture was allowed to stand at room temperature (25°C) for 16 hours to age the mixture, whereby a sheet-forming composition was prepared.
This composition was extruded by an extruder with a die of 200 mm x 20 ram at room temperature (25°C) to prepare a preform.
[0043]
This preformwas rolled by twin rolls under the conditions of a roll diameter of 700 mm, a roll distance of 20mm, a rolling rate of 6 m/min and a roll temperature of 70°C. Immediately after the rolling, the resulting sheet was rolled again under the conditions of a roll distance of 10 mm, and further, while the roll distance was narrowed gradually to 8 mm, © mm, 4 mm, 2 mm and 1.5 mm, rolling was carried out 5 times in the same
SEm2226 18 manner as above to obtain a sheet having a thickness of 1.5 mm.
[0044]
This sheet was allowed to stand at rcom temperature (25°C) for 24 hours to remove the processing aid, and thereafter, the sheet was calcined in an electric furnace at 350°C for 3 hours to obtain a fluorcresin sheet.
This fluororesin sheet hada leakage (gastightproperties) of 2.1x107° (also described as 2.1E-05) Pa'm’/s and a compressibility of 9%.
[0045] [Example 2]
A fluocroresin sheet was produced in the same manner as in Example 1, except that the formulaticn of the sheet-forming compositiconusedinExample lwaschangedas showninthe following
Table 1 and the roll temperature was changed te 80 °C.
[0048]
This flucroresinsheet hada leakage (gastight properties) of 1.1x107* Pa-m’/s and a compressibility of 10%. [0G47] [Example 3]
A fluororesin sheet was produced in the same manner as in Example 1, except that the sheet-forming composition used in Example 1 was changed as shown in Table 1 and the composition was extrudedbyanextruderwitharingdiehavinganouterdiameter
SF-2226 20 of 300 mm and an inner diameter of 260 mm at room temperature (25°C) to prepare a preform. [00481
This fluorcresinsheethada leakage (gastightproperties) of 6.2x107% Pa.m’/s and a compressibility of 9%.
[0049] [Example 4]
A fluororesin sheet was produced in the same manner as in Example 3, except that the sheet-forming composition used in Example 3 was changed as shown in Table 1.
[0050]
This flucroresinsheet hada leakage {(gastight properties) of 5.3x107" Pa-m®/s and a compressibility of 10%.
[0051] [Comparative Example 1]
A fluorcresin sheet was produced in the same manner as in Example 1, except that the sheet-forming composition used in Example 1 was changed as shown in Table 1.
[0052]
This fluororesinsheet hada leakage {gas tightproperties) of 1.1x10™% Pa-m’/s and a compressibility of 6%.
[0053] [Comparative Example 2]
A fluororesin sheet was produced in the same manner as
SE~-2226 21 in Example 1, except that the sheet-forming composition used in Example 1 was changed as shown in Table 1.
[0054]
This flucroresinsheet hada leakage (gas tight properties) of 1.1x107% Parm’/s and a compressibility of 4%.
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Claims (3)
1. A fluororesin sheet produced from a sheet-forming compositioncontaining (A) a flucororesin, (B) a filler {exceptperlite), (CY perlite and (ID) a processing aid.
2. The fluororesin sheet as claimed in ¢laim 1, wherein the amount of the perlite (C) in the composition is 4 to 20 parts by weight based on 100 parts by weight of the tctal amount of the fluororesin (A), the filler (B) (except perlite} and the perlite (C).
3. The fluororesin sheet as claimed in claim 1, wherein the amount of the processing aid (D) in the composition is 5 to 50 parts by weight based on 100 parts by weight of the total amount of the fluororesin (A), the filler (B) (except perlite) and the perlite (C).
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/CN2010/000368 WO2011116498A1 (en) | 2010-03-25 | 2010-03-25 | Fluororesin sheet |
Publications (1)
Publication Number | Publication Date |
---|---|
SG184158A1 true SG184158A1 (en) | 2012-10-30 |
Family
ID=44672427
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SG2012069605A SG184158A1 (en) | 2010-03-25 | 2010-03-25 | Fluororesin sheet |
Country Status (4)
Country | Link |
---|---|
KR (1) | KR20120126107A (en) |
CN (1) | CN102985472B (en) |
SG (1) | SG184158A1 (en) |
WO (1) | WO2011116498A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6560677B2 (en) | 2014-07-28 | 2019-08-14 | 株式会社ブリヂストン | Steel cord for rubber article reinforcement |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4213167B2 (en) * | 2006-03-24 | 2009-01-21 | 日本バルカー工業株式会社 | Method for producing filled fluororesin sheet |
US8357747B2 (en) * | 2006-12-29 | 2013-01-22 | Imerys Filtration Minerals, Inc. | Polymer compositions comprising fluoro elastomers and expanded perlite |
-
2010
- 2010-03-25 SG SG2012069605A patent/SG184158A1/en unknown
- 2010-03-25 KR KR1020127024432A patent/KR20120126107A/en not_active Application Discontinuation
- 2010-03-25 WO PCT/CN2010/000368 patent/WO2011116498A1/en active Application Filing
- 2010-03-25 CN CN201080065721.0A patent/CN102985472B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN102985472A (en) | 2013-03-20 |
KR20120126107A (en) | 2012-11-20 |
WO2011116498A1 (en) | 2011-09-29 |
CN102985472B (en) | 2014-08-20 |
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