WO2011116498A1 - 氟树脂片材 - Google Patents

氟树脂片材 Download PDF

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Publication number
WO2011116498A1
WO2011116498A1 PCT/CN2010/000368 CN2010000368W WO2011116498A1 WO 2011116498 A1 WO2011116498 A1 WO 2011116498A1 CN 2010000368 W CN2010000368 W CN 2010000368W WO 2011116498 A1 WO2011116498 A1 WO 2011116498A1
Authority
WO
WIPO (PCT)
Prior art keywords
sheet
fluororesin
perlite
processing aid
composition
Prior art date
Application number
PCT/CN2010/000368
Other languages
English (en)
French (fr)
Chinese (zh)
Inventor
黄振
丁宏贵
Original Assignee
华尔卡密封件制品(上海)有限公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 华尔卡密封件制品(上海)有限公司 filed Critical 华尔卡密封件制品(上海)有限公司
Priority to SG2012069605A priority Critical patent/SG184158A1/en
Priority to CN201080065721.0A priority patent/CN102985472B/zh
Priority to KR1020127024432A priority patent/KR20120126107A/ko
Priority to PCT/CN2010/000368 priority patent/WO2011116498A1/zh
Publication of WO2011116498A1 publication Critical patent/WO2011116498A1/zh

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C43/00Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
    • B29C43/32Component parts, details or accessories; Auxiliary operations
    • B29C43/44Compression means for making articles of indefinite length
    • B29C43/46Rollers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00Compositions 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
    • C08L27/02Compositions 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
    • C08L27/12Compositions 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
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2327/00Characterised 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
    • C08J2327/02Characterised 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
    • C08J2327/12Characterised 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

Definitions

  • the present invention relates to a fluororesin sheet. Background technique
  • the fluororesin is filled with a filler to form a sheet-like sheet, and not only the chemical resistance and heat resistance of the fluororesin but also the properties* inherent to the filler or the resistance of the fluororesin are improved.
  • a method for producing a fluororesin sheet comprising a fluororesin, a filler, and a processing aid has been disclosed in Japanese Laid-Open Patent Publication No. 2007-253519 (Patent Document 1).
  • the filler clay or the like can be mentioned. According to this production method, it is possible to obtain a fluororesin sheet which is compatible with high resilience and high sealing property and which is suitable for a gasket material.
  • Patent Document 1 Japanese Laid-Open Patent Publication No. 2007-253519 SUMMARY OF INVENTION
  • the present invention has been made in view of the above problems, and an object thereof is to provide a fluororesin sheet which has a large compression ratio under low pressure and is excellent in workability and low in cost.
  • the present inventors conducted intensive studies to solve the above problems, and as a result, found that a sheet made of a composition containing a fluororesin, a filler (excluding perlite), perlite, and a processing aid is inexpensive.
  • the compression ratio is large, and the sealing property equivalent to or better than that of the conventional product can be obtained under a low pressure, and the workability in which the sheet is punched into a desired shape or the like is also good, and the present invention has been completed.
  • the specific structure of the present invention is as follows.
  • the fluororesin sheet of the present invention is characterized by comprising: (A) a fluororesin, (B) a filler (excluding perlite), (C) perlite, and (D) a processing aid for sheet formation.
  • the composition is manufactured.
  • the content of the (C) perlite in the above composition is preferably 4 to 20 parts by weight relative to 100 parts by weight of the total of (A) fluororesin, (B) filler (excluding perlite), and (C) perlite. .
  • the "filling material” referred to means a filling material excluding perlite.
  • the content of the (D) processing aid in the above composition is preferably 5 to 50 by weight with respect to 100 parts by weight of the total of (A) fluororesin, (B) filler (excluding perlite), and (C) perlite. Share. Effect of the invention
  • the fluororesin sheet of the present invention can be produced at low cost by using (C) porous structure perlite and (B) other fillers, for example, in combination with clay.
  • the fluororesin sheet of the present invention is characterized by: a sheet for forming a sheet containing (A) fluororesin, (B) filler (excluding perlite), (C) perlite, and (D) processing aid.
  • the composition is manufactured.
  • polytetrafluoroethylene resin PTFE
  • modified PTFE polyvinylidene fluoride resin
  • PVDF polyvinylidene fluoride resin
  • ETFE tetrafluoroethylene-ethylene copolymer resin
  • chlorotrifluoroethylene resin preferably used.
  • a PTFE ultrafine powder obtained by emulsion polymerization is particularly preferable. Since the PTFE ultrafine powder has a property of fibrillation under the action of shearing force, the (B) filler material can be obtained in the process of each component in the stirring and mixing composition described later, and in the process of forming the sheet. Further, (C) a composition and/or a sheet composed of perlite or the like, whereby a fluororesin sheet excellent in sealing property and mechanical strength can be obtained.
  • the fluororesin may contain a small amount of a fluororesin other than the above PTFE, for example, 10% by weight or less (the total weight of the fluororesin is 100% by weight) or less.
  • a powdery fluororesin may be used as it is, or a dispersion obtained by dispersing fluororesin fine particles in water may be used.
  • the following (C) perlite is not included, and carbon-based fillers such as graphite, carbon black, expanded graphite, activated carbon, and carbon nanotubes may be used depending on the purpose; talc, mica, clay, An inorganic filler such as calcium carbonate, magnesium oxide, silicon carbide, aluminum oxide or silica; or a powder of a resin such as PPS. Further, as the (B) filler, a fiber material having a fiber length of 10 mm or less composed of carbon fiber, aramid fiber, or asbestos may be used.
  • the filling rate of the fluororesin is low and (B) the filling ratio of the filler is high, a fluororesin sheet having a large compression ratio can be obtained.
  • the weight ratio of the above (A) fluororesin and the above (B) filler (excluding perlite) is preferably 1: 0.1 to 3, more preferably 1: 0.1 to 2.
  • perlite is silica (Si0 2) high content of foam volcanic rock system, consisting of silicon dioxide (SiO 2 70 ⁇ 80%), alumina (A1 2 0 3 10 ⁇ 20 %) and Na 2 0, K 2 0 (total 0 to 10%).
  • Examples of the volcanic rock are perlite, obsidian, and rosin.
  • a foam of any of the above rocks may be used, and perlite having a porous structure and excellent oil absorption rate is particularly preferable.
  • Such (C) perlite is extremely light in weight, excellent in heat insulation, and inexpensive and non-flammable. Thus, an inexpensive fluororesin sheet suitable for use at high temperatures can be obtained. Further, since (C) perlite is excellent in liquid absorbing property, it is considered in the present invention that it can absorb the (D) processing aid in the composition for sheet formation. Therefore, when a sheet is formed from a composition for sheet formation, in the case of the following method (I), the (D) processing aid is impregnated and held in the perlite in the rolling step. Most of the holes.
  • the pore structure of the perlite is not easily collapsed, and in the subsequent drying step, the (D) processing aid is volatilized, and the obtained sheet retains voids (pores) in the perlite. Therefore, in particular, a fluororesin sheet having a large compression ratio and an appropriate sealing property under a low pressure tightness can be obtained.
  • composition for sheet formation relative to (A) fluororesin, (B) filler (excluding perlite), and (C) perlite ((A) + (B) + (C)
  • the amount of the above (C) perlite is preferably 4 to 20 parts by weight, more preferably 5 to 8 parts by weight, per 100 parts by weight.
  • the average particle diameter of (C) perlite is preferably 150 ⁇ m or less, more preferably 75 to 125 ⁇ m.
  • composition for sheet formation a total of 100 parts by weight relative to ( ⁇ ) fluororesin, ( ⁇ ) filler (excluding perlite), and (C) perlite, the above (C) perlite
  • amount is 5 to 8 parts by weight
  • a fluororesin sheet having properties such as low compression ratio, high sealing property, high tensile strength, and low stress relaxation property can be obtained, which is preferable.
  • the (D) processing aid is not particularly limited, and a known processing aid such as a petroleum hydrocarbon solvent, ethanol, water or the like can be used.
  • Isopar C manufactured by ExxonMobil (internal organic solvent, fractionation temperature: 97 to 104 ° C), Isopar G (hydrocarbon organic solvent, fractionation temperature: 158) can be cited. ⁇ 175 ° C ) and Isopar M (hydrocarbon organic solvent, fractionation temperature: 218 to 253 ° C).
  • an industrial solvent having characteristics such as n-hexanide, low benzene ring number, and low aromatic solvent, Japan Energy CACTUS SOLVENT R5N manufactured by Corp.
  • the (D) processing aid may be used in the production of a fluororesin sheet in the case of the following method (I), as long as it may contain an appropriate amount of processing aid after the rolling step;
  • the amount of the processing aid (D) is preferably 5 with respect to 100 parts by weight of the total of (A) fluororesin, (B) filler (excluding perlite), and (C) perlite. It is -50 parts by weight, more preferably 10 to 40 parts by weight.
  • the fluororesin sheet when the following method (I) is employed, the fluororesin can be sufficiently swollen in the initial stage of the rolling step to be described later, and before the firing step described later, The processing aid is not completely volatilized, so that the rolled sheet containing an appropriate amount of processing aid is obtained.
  • composition for sheet formation consists only of the above (A) fluororesin, (B) filler, (C) perlite, and (D) processing aid.
  • the above components may be added to the container in a single order or in small portions at a time, stirred, mixed, or the like.
  • the stirring and mixing method is not particularly limited as long as it corresponds to the composition of the fluororesin sheet to be produced, and is blended with (A) a fluororesin, (B) a filler, (C) perlite, and (D) a processing aid. Stir and mix in any order. When the stirring efficiency is not good, a processing aid can be added, and after the stirring is completed, excess processing aid is removed by filtration.
  • the temperature at the time of mixing and mixing is preferably a temperature which is lower than the temperature of the roll in the rolling process without volatilizing the processing aid.
  • the method for producing a fluororesin sheet of the present invention is not particularly limited as long as it can form a fluororesin sheet from the composition for forming a sheet, and a conventionally known method can be employed. Preferably, the above method is employed.
  • the composition for sheet formation is preformed, and the obtained preform is rolled at a roll temperature of 40 to 80 ° C, and then dried and fired (hereinafter also referred to as method (I)).
  • the method (I) includes a pre-forming step, a rolling step, a drying step, and a baking step in this order. ⁇ Preforming process>
  • the above composition for forming a sheet is extrusion molded to obtain a preform (extruded product).
  • the shape of the preform is not particularly limited, but a rod shape or a belt shape is preferable in consideration of the subsequent sheet formation efficiency, the uniformity of the sheet shape, and the like.
  • the preforming step is preferably carried out at a temperature at which the processing aid is not volatilized and is lower than the roll temperature in the rolling step.
  • the preform is rolled into a sheet shape by rolling between rolling rolls represented by a biaxial roll.
  • the rolling step is carried out at a roll temperature of 40 to 80 °C. If the roll temperature is within the above range, the hardness of the (A) fluororesin is slightly lowered, and the fluororesin sheet is more easily densified. Moreover, (D) the processing aid is not completely volatilized.
  • the processing aid tends to be difficult to volatilize.
  • the above-mentioned (D) processing aid is excessively volatilized, and there is a tendency that a fluororesin sheet containing a filler having a large compression ratio cannot be formed.
  • the processing aid (D) is excessively volatilized, the processing aid remaining in the initial stage of the rolling process is reduced. Therefore, the fluororesin which is not sufficiently swollen (A) fluororesin and which is not fibrillated can be obtained. The tendency to be inferior. Further, since the (D) processing aid in the composition is rapidly vaporized to cause swelling, the sealing property of the fluororesin sheet tends to be lowered.
  • the step of further rolling the rolled sheet produced by the rolling step described above is repeated, that is, the rolling step is repeated a plurality of times (for example, 3 to 50 times). Since an appropriate amount of processing aid remains in the sheet after the rolling step, it is preferred to appropriately adjust the number of rolling. Further, when the rolling process is repeated, the roll pitch is made narrower every time the rolling is repeated.
  • the roll pitch is set to 0.5 to 20 mm
  • the roll surface moving speed is 5 to 50 mm/sec. body.
  • the sheet after the rolling is placed at a normal temperature or at a small temperature.
  • the processing aid is removed by heating at the temperature of the melting point of the fluororesin.
  • the dried sheet is heated at a temperature equal to or higher than the melting point of the fluororesin to be sintered.
  • the heating temperature it is considered that it is necessary to uniformly burn all the sheets, and a fluorine-based harmful gas is generated at an excessively high temperature, and although there are some differences depending on the type of the fluororesin, for example, 340 is appropriate. ⁇ 370 ° C.
  • the fluororesin sheet is not particularly limited as long as it is produced from the above composition for forming a sheet, and it is preferred to produce the sheet by the above method (I).
  • the fluororesin sheet is inexpensive and has a large compression ratio. Specifically, the compression ratio is preferably 7% or more, more preferably 8% or more, and the upper limit thereof may be 15%; leakage amount (sealing test, for The test piece having a thickness of 1.5 mm and a thickness of 1.5 mm is preferably 7.0 x 10' 3 Pa «m 3 /s or less, and further preferably 2.0 x 10 ⁇ 3 - m 3 under conditions of a surface pressure of 19.6 MPa and a nitrogen internal pressure of 0.98 MPa. Below /s, the lower limit value may also be 1.0x10 - 5 Pa ⁇ m 3 /s.
  • the fluororesin sheet of the present invention as described above can be used in a gasket, and the gasket made of the fluororesin sheet of the present invention can be used at a high temperature (for example, at 200 ° C or higher) for a long period of time, even at a low pressure.
  • a gasket with high sealing properties can also be obtained.
  • the above gasket can be easily produced by punching the fluororesin sheet of the present invention into a desired shape.
  • the fluororesin sheet of the present invention is easy to punch and has high processability.
  • a test piece was prepared from a sheet having a thickness of 1.5 mm, and the sealing property was measured as described below. Leakage (sealing)
  • the stress relaxation rate at 100 °C and 200 °C was measured based on the ASTM F38 B method.
  • the compression ratio was measured based on ASTM F36.
  • Micro-powder clay (XN-D325, manufactured by Anhui Xuena Non-Metal Materials Co., Ltd.): 9.6kg,
  • composition was extruded at room temperature (25 ° C) using an extruder having a metal port of 300 mm x 20 mm to prepare a preform.
  • the preform was rolled by a twin-axis roll under the conditions of a roll diameter of 700 mm, a roll pitch of 20 mm, a roll speed of 6 m/min, and a roll temperature of 70 °C. Immediately after the rolling, the obtained sheet was again rolled at a roll pitch of 10 mm. Subsequently, the obtained sheet was rolled five times with a gradually narrower roll pitch of 8 mm, 6 mm, 4 mm, 2 mm, and 1.5 mm to obtain a sheet having a thickness of 1.5 mm.
  • the sheet was allowed to stand at room temperature (25 ° C) for 24 hours to remove the processing aid, and then fired in an electric furnace at 350 ° C for 3 hours to obtain a fluororesin sheet.
  • a fluororesin sheet was produced in the same manner as in Example 1 except that the composition of the composition for sheet formation used in Example 1 was changed as shown in Table 1 below, and the roll temperature was changed to 80 °C.
  • the leakage (sealing property) of the fluororesin sheet is UxlO ⁇ -4
  • Example 1 The composition for sheet formation used in Example 1 was changed as shown in Table 1 below, and extruded at room temperature (25 ° C) with an annular die extruder having an outer diameter of 300 mm and an inner diameter of 260 mm.
  • a fluororesin sheet was produced in the same manner as in Example 1 except that a preform was formed.
  • the leakage amount (sealing property) of the fluororesin sheet is The compression ratio is 9%.
  • a fluororesin sheet was produced in the same manner as in Example 3 except that the composition for sheet formation used in Example 3 was changed as shown in Table 1 below.
  • the leakage amount (sealing property) of the fluororesin sheet is SJxlO ⁇ Pa ⁇ m 3 /s, and the compression ratio is
  • a fluororesin sheet was produced in the same manner as in Example 1 except that the composition for sheet formation used in Example 1 was changed as shown in Table 1 below.
  • the leakage amount (sealing property) of the fluororesin sheet was 1.1 lx (T 4 Pa * m 3 / S , and the compression ratio was
  • a fluororesin sheet was produced in the same manner as in Example 1 except that the composition for sheet formation used in Example 1 was changed as shown in Table 1 below.
  • the leakage amount (sealing property) of the fluororesin sheet is Compression ratio

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
PCT/CN2010/000368 2010-03-25 2010-03-25 氟树脂片材 WO2011116498A1 (zh)

Priority Applications (4)

Application Number Priority Date Filing Date Title
SG2012069605A SG184158A1 (en) 2010-03-25 2010-03-25 Fluororesin sheet
CN201080065721.0A CN102985472B (zh) 2010-03-25 2010-03-25 氟树脂片材
KR1020127024432A KR20120126107A (ko) 2010-03-25 2010-03-25 불소 수지 시트
PCT/CN2010/000368 WO2011116498A1 (zh) 2010-03-25 2010-03-25 氟树脂片材

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2010/000368 WO2011116498A1 (zh) 2010-03-25 2010-03-25 氟树脂片材

Publications (1)

Publication Number Publication Date
WO2011116498A1 true WO2011116498A1 (zh) 2011-09-29

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Application Number Title Priority Date Filing Date
PCT/CN2010/000368 WO2011116498A1 (zh) 2010-03-25 2010-03-25 氟树脂片材

Country Status (4)

Country Link
KR (1) KR20120126107A (ko)
CN (1) CN102985472B (ko)
SG (1) SG184158A1 (ko)
WO (1) WO2011116498A1 (ko)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3196354B1 (en) 2014-07-28 2019-06-12 Bridgestone Corporation Steel cord for reinforcing rubber article

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008081173A1 (en) * 2006-12-29 2008-07-10 World Minerals, Inc. Polymer compositions comprising fluoro elastomers and expanded perlite
CN101405121A (zh) * 2006-03-24 2009-04-08 日本华尔卡工业株式会社 含填充材料的氟树脂片材的制造方法及含填充材料的氟树脂片材

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101405121A (zh) * 2006-03-24 2009-04-08 日本华尔卡工业株式会社 含填充材料的氟树脂片材的制造方法及含填充材料的氟树脂片材
WO2008081173A1 (en) * 2006-12-29 2008-07-10 World Minerals, Inc. Polymer compositions comprising fluoro elastomers and expanded perlite

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3196354B1 (en) 2014-07-28 2019-06-12 Bridgestone Corporation Steel cord for reinforcing rubber article

Also Published As

Publication number Publication date
CN102985472B (zh) 2014-08-20
SG184158A1 (en) 2012-10-30
CN102985472A (zh) 2013-03-20
KR20120126107A (ko) 2012-11-20

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