WO1999048952A1 - Powder of ethylene/ tetra fluoro ethylene copolymer and method of depositing the same - Google Patents
Powder of ethylene/ tetra fluoro ethylene copolymer and method of depositing the same Download PDFInfo
- Publication number
- WO1999048952A1 WO1999048952A1 PCT/JP1999/001324 JP9901324W WO9948952A1 WO 1999048952 A1 WO1999048952 A1 WO 1999048952A1 JP 9901324 W JP9901324 W JP 9901324W WO 9948952 A1 WO9948952 A1 WO 9948952A1
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- WIPO (PCT)
- Prior art keywords
- ethylene
- sec
- powder
- tetrafluoroethylene
- etfe
- 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.)
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Classifications
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- 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
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/02—Ethene
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D123/00—Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers
- C09D123/02—Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers not modified by chemical after-treatment
- C09D123/04—Homopolymers or copolymers of ethene
- C09D123/08—Copolymers of ethene
- C09D123/0846—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms
- C09D123/0892—Copolymers of ethene with unsaturated hydrocarbons containing other atoms than carbon or hydrogen atoms containing monomers with other atoms than carbon, hydrogen or oxygen atoms
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D123/00—Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers
- C09D123/26—Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers modified by chemical after-treatment
- C09D123/28—Coating compositions based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Coating compositions based on derivatives of such polymers modified by chemical after-treatment by reaction with halogens or compounds containing halogen
- C09D123/283—Halogenated homo- or copolymers of iso-olefines
Definitions
- the present invention relates to a method for molding an ethylene-tetrafluoroethylene-based copolymer (hereinafter, also referred to as ET FE) powder, and more particularly, to a method for molding an ET FE powder capable of obtaining a coating film having excellent surface smoothness, and a method therefor.
- ET FE ethylene-tetrafluoroethylene-based copolymer
- ETFE is widely used as a material suitable for a corrosion-resistant lining, a corrosion-resistant container, etc. because of its excellent heat resistance and chemical resistance.
- a method of processing the corrosion-resistant lining there is a method of pulverizing ETFE and subjecting it to a known method such as electrostatic powder coating, fluid immersion coating, or rotational molding to coat and mold various substrates.
- a method for processing a corrosion-resistant container there is a method in which ETF E is powdered and supplied to a mold, and a bottle molded article having an arbitrary shape is obtained by a molding method such as rotational molding.
- An object of the present invention is to provide a novel method for molding ETFE powder in which the surface smoothness of the obtained coating film is significantly improved.
- the present invention relates to an ETFE of ethylene, tetrafluoroethylene, and a fluorine-containing monomer copolymerizable therewith, which has a viscoelastic property represented by the formula (1), and a viscosity term in the formula (1).
- an ETFE powder comprising a copolymer, having an average particle size of 5 to 1,000 ⁇ and an apparent specific gravity of 0.5 gZc or more.
- the present invention provides a method for forming an ETFE powder, which comprises forming the coating film by adhering the ETFE powder to the surface of a substrate, heating and melting, and solidifying by cooling.
- the ET FE used in the present invention is obtained by copolymerizing tetrafluoroethylene (hereinafter referred to as TFE) with ethylene and a fluorinated butyl monomer copolymerizable therewith.
- TFE tetrafluoroethylene
- the molar ratio of the polymerized unit based on the unit ethylene is from 90 to 5 to 50.
- Polymerization unit based on TFE If the molar ratio of the polymerization unit based on ethylene is lower than 50/50, the decomposition temperature tends to decrease, and moldability tends to be impaired.
- the content molar ratio is higher than 9010, polytetrafluoroethylene by-produced in the ETFE is present, and the formed coating film easily forms fish eyes, and the present invention intends High surface smoothness is easily lost.
- the fluorinated vinyl monomer used in the present invention is a fluorinated vinyl monomer copolymerizable with PTFE and ethylene, and examples thereof include the following.
- the fluorinated vinyl monomers may be used alone or in combination of two or more.
- CH 2 CH (CF 2 ) 2 F
- CH 2 CH (CF 2 ) F
- CF 2 CF 0 (CF 2 C FX 0) m R f (In the formula, R f is a perfluoroalkyl group having 16 carbon atoms, X is a fluorine atom or a trifluoromethyl group, and m is an integer of 05.) Perfluorovinyl ethers such as
- the content ratio of the polymerized unit based on the fluorine-containing butyl monomer is usually 110 moles, and preferably 27 moles, based on 100 moles of the total amount of the polymerized units based on TFE and the polymerized units based on ethylene.
- the formula (1) and the formula (2) viscosity term is defined in t // is .1 X 1 0 4 P a ' sec or less, the delay elasticity term ⁇ 5 1 0 4 It is important that it is less than Pa.
- the above equation shows the relationship between strain and time when a small stress is applied in a molten state where the polymer is heated to a temperature equal to or higher than the melting point.
- the melt is a Newtonian fluid
- the strain increases linearly with time.
- ETFE is an aggregate of linear molecules, and the melt does not take the ideal Neutral fluid behavior due to the entanglement of the molecules, but has a viscous behavior and elasticity against minute stress. Behavior at the same time, and the strain-time curve becomes nonlinear. In other words, it can be considered as a fluid with ⁇ > 0 in Eq. (2).
- ETF E is melted and left in a static state
- the melt itself becomes smooth due to its own weight and the free movement of the molecules, while linear molecules are entangled. It behaves elastically and prevents the surface from being completely smooth.
- the ET FE in the present invention has a viscosity term of 1 ⁇ 10 4 Pa ⁇ sec or less, preferably 500 7000 Pa ⁇ sec.
- the viscosity term 3 ⁇ 4 1 X 1 0 4 P a .
- ET FE for use in the present invention is delayed elasticity term ⁇ is 5 X 1 0- 4 P a- 1 or less, preferably 1 X 1 0- s ⁇ 1 X 1 0- 4 P a- 1 is there. It can be reduced elastic resistance by the delay elasticity term ⁇ to 5 X 1 0 one 4 P a- 1 below.
- Delay elasticity term & can greatly 5 X 1 0- 4 P a- 1 larger than molecules with each of the entangled effect, show a more elastic behavior dynamic, it is difficult to obtain a smooth surface.
- Viscosity term force S 1 X 1 0 4 P a - sec following ETFE can be obtained by controlling the molecular weight. If the molecular weight is too large, slip between the ETFE molecules is suppressed, so that the viscosity increases and the value of the viscosity term ⁇ is not satisfied.
- the control of the molecular weight of ETFE can be specifically achieved by temperature, pressure, addition of a chain transfer agent and the like in the polymerization.
- the melt index (Ml) is used as an index of the molecular weight of ETFE.
- the delay elasticity term ⁇ is 5 X 1 0- 4 P a following ETFE is, the content of polymerized units based on free off Mmoto Bulle monomer in ETFE is based on polymerized units ⁇ beauty ethylene polymerized units based on TFE Is usually in the range of 1 to 10 moles based on the total amount of 100 moles.
- the delay elasticity term ⁇ is 5 X 1 0- 4 P a- 1 following ETF E is obtained by polymerizing are charged in bulk fluorinated Binirumo Noma foremost initial stage of polymerization.
- the reason for this is not clear, but the more the number of polymerized units based on the fluorinated vinyl monomer having a side chain, and the more uniform its distribution in ETFE, the more the effect of entangling ETFE molecules is increased. It is estimated that the elasticity term ⁇ increases. Therefore, the ratio of the polymerized units based on the fluorine-containing monomer in the ETF produced in the early stage of polymerization is increased by batch-charging and polymerizing the fluorine-containing vinyl monomer in the early stage of the polymerization.
- ETF II with a small proportion of polymerized units based on the bull monomer is formed. in this way By making the distribution of the polymerized units of the fluorinated vinyl monomer non-uniform, an ETF having a suitable elongation modulus ⁇ can be obtained.
- the ETF powder of the present invention has an average particle size of 5 to 1,000 ⁇ , preferably 10 to 700 / im, and an apparent specific gravity of 0.5 g / cc or more, preferably 0.6 to 1.0. g / cc powder.
- the average particle size is smaller than 5 m, the powder particles are liable to form agglomerates containing air due to the action of static electricity. When this is melted and solidified, it becomes a coating film containing air, which impairs the appearance and the surface smoothness which is the object of the present invention. If the average particle size is larger than 10 ⁇ ⁇ , it may cause fouling when melted or solidified, thus impairing the surface smoothness, which is the object of the present invention. If the apparent specific gravity is less than 0.5 g // cc, there is a lot of air inside the powder particles, so if it is melted and solidified, it becomes a coating film containing air, and its appearance and the purpose of the present invention Some surface smoothness is impaired.
- ETF E As a method of pulverizing ETF E, various known pulverization methods can be employed. For example, a method in which ET FE is supplied to a mechanical pulverizer such as a pin mill or impeller mill to powder it by the action of impact, shearing force, etc., and a liquid in which ETF E is dispersed in a solvent is sprayed into an atmosphere having a melting point or higher. And pulverizing the ETFE by subjecting the ETFE to a granulator such as a helical mixer, a high-speed mixer, and a mechanofusion.
- a mechanical pulverizer such as a pin mill or impeller mill to powder it by the action of impact, shearing force, etc.
- a liquid in which ETF E is dispersed in a solvent is sprayed into an atmosphere having a melting point or higher.
- pulverizing the ETFE by subjecting the ETFE to a granulator such as a helical mixer, a high
- the ETFE powder of the present invention is characterized by high melt flowability under low shear stress, and achieves extremely high surface smoothness even when melted and solidified under static conditions such as powder molding.
- the PTFE powder is adhered to the substrate surface, melted by heating, and solidified by cooling to form a coating film.
- Specific methods for adhering the ETFE powder to the substrate surface include a method in which the powder is adhered to the substrate surface by an electrostatic action using an electrostatic powder coating machine, and a method in which the powder is supplied to a fluidized immersion tank and the heated substrate is heated. Examples include a method of melting and adhering the powder to the surface, a method of putting the powder into a hollow substrate, supplying the powder to a rotary molding machine, and rotating the substrate to adhere the powder to the surface of the substrate.
- the heating and melting of the ETFE powder attached to the substrate surface can be performed by various known heating means. For example, heating in an electric furnace, heating in a gas burner furnace, heating with an open flame, a continuous electric furnace, and the like can be mentioned.
- the heating and melting temperature may be any temperature at which the ETFE powder melts, and is usually at 250 to 350 ° C.
- the heated and melted ETF E powder is cooled and solidified, and the cooling and solidification may be performed at a temperature at which the heated and melted ET FE powder is solidified, and is usually equal to or lower than the melting point, specifically, from room temperature to 20 ( It is performed at about TC.
- the film thickness of the coating film formed by the ETFE powder may be usually 30 ⁇ or more, and preferably 50 to 5000 izm.
- the coating film formed according to the present invention may be a single layer or a multilayer.
- a method of forming a coating film into multiple layers includes, for example, one or more of a coating layer formed by the ETFE powder used in the present invention and a layer formed by another ETFE, or both.
- One or more composite layers are coated on each of the layers, and the ETFE powder of the present invention is deposited thereon, melted by heating, and solidified by cooling to form a coating film.
- the ETFE powder of the present invention has good compatibility with other ETFE in a molten state, and can form a multilayer coating film that is difficult to peel off.
- the other ETFE layer may be a coating film formed by adhering another ETFE powder to the surface of the substrate, heating and melting, and then solidifying by cooling.
- the other ETFE layer may be coated on the surface of the substrate with another ETFE-containing paint. It may be a coating film formed, or may be a product obtained by laminating a molded product such as another ETFE sheet / film on the substrate surface.
- ETFEs are ETFEs other than the ETFE used in the present invention, and specifically include copolymers of ethylene and TFE, ethylene and TFE, and copolymers of fluorinated butyl monomers copolymerizable therewith.
- a polymer which viscosity term I / in equation (1) exceeds 1 X 1 0 4 P a * sec
- delay elastic term in equation (2) epsilon exceeds 5 x 10 "4 P a one 1
- the coating film formed according to the present invention has a surface smoothness measured at a surface roughness Ra of 0. It can be less than 1 ⁇ .
- the substrate that can be used in the present invention is not particularly limited, and examples thereof include various materials such as inorganic materials such as metals, concrete and ceramics, and organic materials such as heat-resistant plastics.
- Melt index (Ml) Measured at 297 ° C and 5 kg load using a melt indexer (manufactured by Takara Kogyo Co., Ltd.) according to ASTM D3159.
- Average particle size Measured by a dry method using a laser diffraction single-diffraction particle size distribution analyzer (manufactured by Synpatec, HE L0S & R0D0S).
- the magnetic substrate was measured using an electromagnetic film thickness meter, and the non-magnetic substrate was measured using an eddy current film thickness meter.
- a 10 liter stainless steel autoclave was evacuated, 3360 g of water, 5056 g of C 6 F 13 H, and a chain transfer agent CC 1 F 2 CF 2 CHC 1 F (hereinafter referred to as HCFC 225 cb) 543 g, (perfluorobutyl) ethylene (hereinafter, referred to as PFBE) 80 g, TFE 743 g, and ethylene 26 g, and the mixture was stirred at 400 rpm and heated to 65 ° C.
- the polymerization was started by adding 50 cc of a polymerization initiator (50% by weight of a solution of tert-butylvinylisobutyrate in HCFC 225 cb).
- the ET FE is, M l 2 1.9, viscosity term is 4285 P a - sec, delayed elasticity term ⁇ was 8. 38 X 1 0- S P a- 1. Further, as a result of analysis by NMR, the polymerization unit based on TFE of the ETFE, the polymerization unit based on ethylene, and the polymerization unit based on ZPFFE were 68Z32Z3.3 (molar ratio).
- the ETFE was pulverized with an impact mill LS-1 (manufactured by Dalton) to obtain a powder having an average particle size of 35 ⁇ and an apparent specific gravity of 0.61 g cc.
- This ETFE powder was applied to an electrostatic coating machine (GX 3300S manufactured by Onoda), coated on a 150 ⁇ 150 ⁇ 2 mmt aluminum plate, and heated and melted at 280 ° C. for 20 minutes in an electric furnace. Then, it was cooled to room temperature and solidified. The thickness of the obtained coating film was about 63 ⁇ . The surface roughness R a of the coating film was 0. 054 m.
- Example 1 the same operation was repeated except that the initially charged HC FC 225 c b was changed to 435 g, to obtain 920 g of white ETF E.
- the ETFE is the MI force s1 3.
- the polymerization unit based on TFE of the ETFE / polymerization unit based on ethylene ZP FBE has a polymerization unit of 71 / 29.2.
- the ET FE was pulverized with an impact mill LS-1 (manufactured by Dalton) to obtain a powder having an average particle size of 168 ⁇ and an apparent specific gravity of 0.73 g / cc.
- a flat plate of 50 ⁇ 100 ⁇ 3 mmt steel SS400 preheated to 350 ° C was immersed in a fluidized immersion tank (manufactured by Sammes) provided with this powder, and the flat plate was further subjected to electric power. Heated in a furnace at 30 CTC for 20 minutes.
- the thickness of the coating film was about 513 ⁇ .
- Surface roughness R a of the coating film was 0. 084 ⁇ .
- Example 2 The same procedure as in Example 1 was repeated except that the initial charge of HCFC 225 cb was changed to 71 g, to obtain 820 g of white ETF E in 7 hours.
- the ET FE has an M l of 34.5, a viscous term t / of 2797 Pa ⁇ sec, a Feng rolling elasticity ⁇ force s 5.35 x 10 One was 5 Pa- 1 .
- the polymerization unit based on TFE of the ETFE was found to be 64/36 / 3.8 (molar ratio) of polymerization units based on T ethylene / polymerization units based on PFB E. .
- the ETFE was pulverized with a power mill P-3 type (manufactured by Dalton) to obtain a powder having an average particle size of 543 ⁇ 0 and an apparent specific gravity of 0.81 g / cc.
- This powder was injected into SGP piping of 50 A, 100 mm long carbon steel pipe with flange, and both flanges were sealed with special covers. This was set on a rotary molding machine, heated at 300 ° C for 1.5 hours while rotating on two axes, and melted. Then, after cooling to room temperature and solidifying, the piping was removed from the molding machine.
- the ETF E was lined on the inner surface of the pipe, and the thickness of the coating film was about 2.1 mm. Surface roughness R a of the coating film was 0. 0 67 ⁇ m.
- the ETFE powder obtained in Example 3 was previously lined with ETF E (Aflon COP • ZL522, manufactured by Asahi Glass), the thickness of the coating film was about 2.1 mm, and the surface roughness of the coating Ra was injected into SGP pipe of 50A, 100mm long flanged carbon steel pipe with 0.764 ⁇ , and both flanges were sealed with special covers. This was set in a rotary molding machine, heated at 300 ° C for 1.5 hours while rotating on two axes, and melted. Next, after cooling to room temperature and solidifying, the piping was removed from the molding machine. The ETFE was lined on the inner surface of the pipe, and the thickness of the coating film was about 3.8 mm. Surface roughness R a of the coating film was 0. 035 / xm.
- Example 1 is the same as in Example 1, except that the initial charge of PFBE was 53 g, and the mixed gas of TFE ethylene ZP FBE (60/40/3 (molar ratio)) was added. Repeat the operation, white £ cho? You got 5796 ⁇ .
- the ETFE may, MI 1 9.8, viscosity term is 6851 P a 'sec, delay bullet resistant term ⁇ is 6.
- the polymerized unit based on the polymerized unit PFBE based on the polymerized unit based on TFE of the ETF E was 64Z36 / 3.9 (molar ratio). Further, the ETFE was pulverized with an Impact Mill LS-1 (manufactured by Dalton) to obtain a powder having an average particle size of 28 / xm and an apparent specific gravity of 0.57 gZc c.
- This powder was applied to an electrostatic coating machine (GX 3300S manufactured by Onoda), coated on a 150 ⁇ 150 ⁇ 2 mmt aluminum plate, and heated and melted at 280 ° C. for 20 minutes in an electric furnace. Then, it was cooled to room temperature and solidified. The thickness of the coating film was about 51 / xm. The surface roughness Ra was 0.194 jm.
- Example 1 the same operation was repeated except that the initially charged HCFC 225 cb was changed to 0 g of 2 O, and 820 g of white ETFE was obtained in 8 hours.
- the ETFE had an M l of 6.74, a viscosity term of 11096 Pa.sec, and a delayed elasticity term ⁇ of 1.41 x 1 O-sp a 1 .
- the polymerization unit based on TFE of the ETFE was 67/33 / 2.5 (molar ratio) in the polymerization unit based on ethylene and the polymerization unit based on ZP FBE.
- the ETFE was pulverized with a power mill P-3 type (manufactured by Dalton) to obtain a powder having an average particle size of 643 m and an apparent specific gravity of 0.82 c.
- This powder was charged into a flanged SGP pipe of 50 A and length of 100 mm, and both flanges were sealed with a special cover. This was set on a rotary molding machine and heated and melted for 30 hours (TC for 1.5 hours) while rotating about two axes. After cooling to room temperature and solidifying, the piping was removed from the molding machine. The inner surface of the pipe was lined with the ETFE, the thickness of the coating film was about 2.6 mm, and the surface roughness Ra was 0.678 ⁇ According to the method for molding ETF powder of the present invention, The surface smoothness of the obtained coating film can be greatly improved.
- the ETFE powder of the present invention has high melt flowability under low shear stress, and a coating film having a smooth surface can be obtained by powder molding.
- Corrosion-resistant lining material of inorganic materials such as metal and concrete, and organic materials such as heat-resistant resin. Can be widely used as corrosion-resistant container material
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- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Wood Science & Technology (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Paints Or Removers (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
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Description
Claims
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP99909204A EP1069152B1 (en) | 1998-03-20 | 1999-03-17 | Powder of ethylene/ tetra fluoro ethylene copolymer and method of depositing the same |
| DE69929514T DE69929514T2 (de) | 1998-03-20 | 1999-03-17 | Pulver aus ethylen/tetrafluorethylencopolymer und verfahren zum abscheiden desselben |
| US09/646,100 US6589597B1 (en) | 1998-03-20 | 1999-03-17 | Ethylene/Tetrafluoroethylene/fluorinated vinyl monomer copolymer powder and molding method therefor |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP07267098A JP3951277B2 (ja) | 1998-03-20 | 1998-03-20 | エチレン/テトラフルオロエチレン系共重合体粉末及びその成形方法 |
| JP10/72670 | 1998-03-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1999048952A1 true WO1999048952A1 (en) | 1999-09-30 |
Family
ID=13496038
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP1999/001324 Ceased WO1999048952A1 (en) | 1998-03-20 | 1999-03-17 | Powder of ethylene/ tetra fluoro ethylene copolymer and method of depositing the same |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US6589597B1 (ja) |
| EP (1) | EP1069152B1 (ja) |
| JP (1) | JP3951277B2 (ja) |
| DE (1) | DE69929514T2 (ja) |
| ES (1) | ES2257036T3 (ja) |
| WO (1) | WO1999048952A1 (ja) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000229388A (ja) * | 1999-02-09 | 2000-08-22 | Du Pont Mitsui Fluorochem Co Ltd | 熱溶融性フッ素樹脂被覆ポリテトラフルオロエチレン成形体 |
| IT1318595B1 (it) | 2000-06-23 | 2003-08-27 | Ausimont Spa | Microsfere di copolimeri termoprocessabili del tetrafluoroetilene. |
| US6541589B1 (en) * | 2001-10-15 | 2003-04-01 | Gore Enterprise Holdings, Inc. | Tetrafluoroethylene copolymer |
| US7604818B2 (en) * | 2004-12-22 | 2009-10-20 | Advanced Cardiovascular Systems, Inc. | Polymers of fluorinated monomers and hydrocarbon monomers |
| US7531611B2 (en) * | 2005-07-05 | 2009-05-12 | Gore Enterprise Holdings, Inc. | Copolymers of tetrafluoroethylene |
| WO2010123002A1 (ja) * | 2009-04-21 | 2010-10-28 | ダイキン工業株式会社 | エチレン/テトラフルオロエチレン共重合体、電線及び回転成形用フッ素樹脂粉末 |
| WO2017082417A1 (ja) * | 2015-11-13 | 2017-05-18 | 旭硝子株式会社 | 共重合体およびこれを含む組成物 |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49112977A (ja) * | 1973-03-02 | 1974-10-28 | ||
| JPS50156542A (ja) * | 1974-06-10 | 1975-12-17 | ||
| JPS51116849A (en) * | 1975-04-07 | 1976-10-14 | Du Pont Mitsui Fluorochem Co Ltd | Powdered copolymers from ethylene and fluorine containing olefin |
| JPS51127137A (en) * | 1975-04-30 | 1976-11-05 | Du Pont Mitsui Fluorochem Co Ltd | Method for electrostatic coating with coating powder containing fluoro resin |
| JPH01139657A (ja) * | 1987-11-26 | 1989-06-01 | Daikin Ind Ltd | フッ素ゴム粉体組成物 |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3624250A (en) * | 1970-01-20 | 1971-11-30 | Du Pont | Copolymers of ethylene/tetrafluoroethylene and of ethylene/chlorotrifluoroethylene |
| US4001360A (en) * | 1972-01-05 | 1977-01-04 | Davis William J | Method for preparing pulverulent polymers exhibiting an apparent increase in glass transition temperature and shaping the resultant polymer materials |
| US3960825A (en) * | 1973-10-15 | 1976-06-01 | Pennwalt Corporation | High-modulus thermoplastic ethylene-tetrafluoroethylene hexafluoropropene terpolymers |
| US4033939A (en) * | 1975-04-02 | 1977-07-05 | Allied Chemical Corporation | Stress-crack resistant ethylene-perhaloethylene terpolymers |
| US4123602A (en) * | 1976-05-24 | 1978-10-31 | Asahi Glass Company, Ltd. | Terpolymers of tetrafluoroethylene, ethylene and perfluoroalkyl vinyl monomer and process for producing the same |
| JPS5950162B2 (ja) * | 1977-05-20 | 1984-12-06 | 旭硝子株式会社 | 改良されたエチレン−四弗化エチレン系共重合体及びその製法 |
| DE3024450A1 (de) * | 1980-06-28 | 1982-01-28 | Hoechst Ag, 6000 Frankfurt | Verfahren zur herstellung von waessrigen, kolloidalen dispersionen von copolymerisaten des typs tetrafluorethylen-ethylen |
| EP0121073B1 (en) * | 1983-03-07 | 1987-07-22 | Ausimont, U.S.A., Inc. | A process of rotational molding fluoropolymers |
| DE3575566D1 (de) * | 1984-12-19 | 1990-03-01 | Ausimont Usa | Terpolymer aus chlortrifluorethylen oder tetrafluorethylen, ethylen und perfluorisoalkoxyperfluoralkylethylen. |
| EP0411214A1 (en) * | 1989-07-04 | 1991-02-06 | Sunrex Industry Co., Ltd | Fluororesin rotation molded articles and process for preparing same |
| EP0638596B1 (en) * | 1993-03-17 | 1999-10-06 | Asahi Glass Company Ltd. | Process for producing fluoropolymer |
| US6197904B1 (en) * | 1998-02-26 | 2001-03-06 | E. I. Du Pont De Nemours And Company | Low-melting tetrafluoroethylene copolymer |
| DE60019138T2 (de) * | 1999-09-13 | 2006-02-02 | Asahi Glass Co., Ltd. | Tetrafluorethylen / ethylen-copolymer und daraus hergestellter film |
-
1998
- 1998-03-20 JP JP07267098A patent/JP3951277B2/ja not_active Expired - Lifetime
-
1999
- 1999-03-17 US US09/646,100 patent/US6589597B1/en not_active Expired - Lifetime
- 1999-03-17 DE DE69929514T patent/DE69929514T2/de not_active Expired - Lifetime
- 1999-03-17 WO PCT/JP1999/001324 patent/WO1999048952A1/ja not_active Ceased
- 1999-03-17 EP EP99909204A patent/EP1069152B1/en not_active Expired - Lifetime
- 1999-03-17 ES ES99909204T patent/ES2257036T3/es not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49112977A (ja) * | 1973-03-02 | 1974-10-28 | ||
| JPS50156542A (ja) * | 1974-06-10 | 1975-12-17 | ||
| JPS51116849A (en) * | 1975-04-07 | 1976-10-14 | Du Pont Mitsui Fluorochem Co Ltd | Powdered copolymers from ethylene and fluorine containing olefin |
| JPS51127137A (en) * | 1975-04-30 | 1976-11-05 | Du Pont Mitsui Fluorochem Co Ltd | Method for electrostatic coating with coating powder containing fluoro resin |
| JPH01139657A (ja) * | 1987-11-26 | 1989-06-01 | Daikin Ind Ltd | フッ素ゴム粉体組成物 |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP1069152A4 * |
Also Published As
| Publication number | Publication date |
|---|---|
| US6589597B1 (en) | 2003-07-08 |
| DE69929514T2 (de) | 2006-09-07 |
| EP1069152A4 (en) | 2002-04-10 |
| JP3951277B2 (ja) | 2007-08-01 |
| ES2257036T3 (es) | 2006-07-16 |
| JPH11269274A (ja) | 1999-10-05 |
| DE69929514D1 (de) | 2006-04-06 |
| EP1069152A1 (en) | 2001-01-17 |
| EP1069152B1 (en) | 2006-01-18 |
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