Powders of tetrafluoroethylene copolymer and process for preparing the same

The present invention relates to a powder of tetrafluoroethylene (TFE) copolymer having a non-spherical particle shape and an average particle size of 5 to 500 µm which is useful for powder coating, and a process for preparing the same.

Study and development of powders of TFE copolymer used for powder coating are proceeded on the basis of the theory that such powders preferably have spherical particle shape in a viewpoint of their flowability (JP-A-240 713/1985).

EP-A-0 041 687 discloses powders of TFE copolymers having a non-spherical particle shape and an average particle size of 450 to 1400 µm, wherein the tetrafluoroethylene copolymers consist of a very small amount, i.e. 0,004 to 0,075 % by mole of units of a perfluoroalkylvinyl ether and for the rest of units of tetrafluoroethylene. This polymer is not melt-processable as is also a TFE homopolymer.

To roto-molding or roto-lining which has been recently utilized as a method of powder coatings, however, the above theory and powders can not be fully applied. For instance, there are some problems such that a coating formed on a mold surface partially falls off to yield coating defects on a surface of the molded article, that a coating surface largely undulates and has continuous ball-like projects, and that a coating contains bubbles or cells because gas content cannot be sufficiently removed.

As a result of the inventors' intensive study, it has been found out that the above-mentioned problems can be solved by using powders of TFE copolymers having particular composition and powder properties.

According to a first aspect the present invention relates to a powder of TFE copolymer having a non-spherical particle shape, and an average particle size of 5 to 500 µm which is characterized in that

said tetrafluoroethylene copolymer is a copolymer of tetrafluoroethylene and hexafluoropropylene or a fluoro(vinyl ether) containing tetrafluoroethylene units in an amount of from 85 to 99,5 % by mole and

it has a frictional packing ratio of 20 to 100 %, calculated from the formula Frictional Packing Ratio (%)=

wherein

ρ₁

is the bulk density of the powder measured according to JIS K 6891 and

ρ₂

is the bulk density of the packed powder measured according to JIS K 6891.

According to a preferred embodiment of the present invention the average particle size (µ) and the bulk density (ρ₁) of the powder of the present invention satisfy the following equation:

$\text{log µ < 2.45 ρ₁ + 0.75.}$

According to a second aspect the present invention relates to a process for preparing the powder of tetrafluoroethylene copolymer as defined above which comprises producing a sheet of a tetrafluoroethylene/hexafluoropropylene copolymer or of a tetrafluoroethylene/fluoro(vinyl ether) copolymer with rolls, and pulverizing the sheet.

According to a preferred embodiment of the present process the tetrafluoroethylene copolymer in the form of sheet or in the pulverized form is subjected to a fluorine gas treatment.

According to an other preferred embodiment of the present process the powder of tetrafluoroethylene copolymer is a powder which satisfies the following equation:

$\text{log µ < 2.45 ρ₁ + 0.75}$

wherein µ represents the average particle size of the powder and ρ₁ represents the bulk density of the powder.

The invention is illustrated below in detail making reference to the enclosed drawing.

Fig. 1 is a scanning-type electromicroscopic photograph (100 magnitudes) of a powder prepared in Preparation Example 4 described below.

In the present invention, the powders have a non-spherical particle shape. This property is important for obtaining an appropriate friction in the powder coating step, as explained hereinbelow.

Film forming operation of the roto-molding and roto-lining is carried out by externally heating a mold charged with a powder in such an amount to give a desired thickness while rotating the mold biaxially or uniaxially. In the course of the film formation, the powder is heated by contacting with the inner surface of heated mold, and gradually adheres onto the mold surface to form a molten thin film, from which air present between the powder particles is released by itself. The adhesion and melting of the remaining heated powder is gradually and continuously proceeded to produce a film having a desired thickness without bubbles or cells. For performing such a good film formation, it is necessary to contact a powder with a heated mold surface for an appropriate period of time. Namely, when the contacting time is shorter, an adherent powder partially falls off from a mold surface, or on the contrary a powder is wholly and homogeneously heated, and then the homogeneously heated powder wholely adheres onto the mold surface and is melted for a very short time to form a film without releasing bubbles.

Such an appropriate contacting time cannot be obtained by using spherical particles, but can be obtained by using non-spherical particles which have a large friction. The word "non-spherical shape" as used in the specification means a shape having at least a linear profile when a particle is cut along an optional line, even if the remaining profile is round. The sectional profile should not be a smooth circle.

The frictional packing ratio of the powder of the invention defined by the following equation (I) must be within a range from 20 to 100 %.

wherein

ρ₁:

bulk density of powder measured according to JIS K 6891

ρ₂:

bulk density of packed powder measured according to JIS K 6891. Packing operation is as follows: a 100 mℓ SUS container (diameter: 40 mm, height: 79.6 mm) is charged with a powder, and the container is vibrated by touching a vibrator (Panabrator EV234 available from Matsushita Electric Industrial Co., Ltd.) on a central side portion of the container for one minute. This vibration operation is repeated by adding a powder to the container until reducing volume becomes lower than 5 % by volume of the container. Finaly the container is filled with an additional powder, and then a bulk density of the packed powder is measured.

This frictional packing ratio shows degrees of both friction and packing density of powder. A small value means a low friction of a powder, and a large value means a high friction of a powder.

A frictional packing ratio of the powder according to the invention is 20 to 100 %. When the ratio is less than 20 %, the above-mentioned problems cannot be solved due to its low friction. A TFE copolymer powder having a spherical shape generally has a frictional packing ratio of 5 to 15 %. When more than 100 %, a uniform coating cannot be obtained due to its high friction.

An average particle size of the powder according to the invention is 5 to 500 µm. In case of a powder for roto-molding and roto-lining, the powder preferably has an average particle size of 100 to 150 µm, and in case for electrostatic powder coating the powder preferably has an average particle size of 5 to 150 µm.

Average particle sizes of powders are measured according to ASTM D-1457-69. Sieves of 1,2 to 0,033 mm (16 to 400 mesh) are provided on the basis of wet sieve method. Among them, by using five sieves so that a sieve having a pore opening size almost the same as an expected average particle size of a powder to be measured is a central sieve, the powder is sieved. An average particle size is determined by using a logarithm probability paper described in the ASTM on the basis of relationship between cumulative residual percentage and pore opening size of the sieve. A powder having an average particle size of not more than 400 mesh (not more than 33 µm) is measured as follows: a beaker of 100 mℓ is charged with 50 mℓ of chlorotrifluoroethylene telomer oil (Daifloil S-519 available from Daikin Industries, Ltd.), and 0.1 g of a powder to be measured is added thereto. After dispersing the powder with a supersonic dispersing apparatus for one minute, a sample is introduced to a spectral cell, and then an average particle size is measured by centrifugal transmittance method (with CAPA-500 manufactured by HORIBA, LTD.)

Particle size distribution as well as particle shape influences the packing density of powder. For instance, when a particle size distribution is wide, an amount of air between particles can be reduced because packing state becomes near closest packing. However, even in such a case, it is necessary to regulate the frictional packing ratio within the above-mentioned range.

The powder having a preferable flowability satisfies the flowing equation (II):

$\text{log µ < 2.45 ρ₁ + 0.75}$

wherein

µ:

average particle size

ρ₁:

bulk density as defined in the equation (I).

The TFE copolymer used in the invention is a TFE/hexafluoropropylene copolymer or a TFE/fluoro(vinyl ether) copolymer. The both of the copolymers preferably contain TFE units in an amount of from 85 to 99.5 % by mole. Preferred fluoro(vinyl ether) is a compound of the formula:

        CF₂ = CF(OCF₂CF(CF₃))mO(CF₂)nCF₂X

wherein X is hydrogen atom or fluorine atom, m is 0 or an integer of 1 to 4, n is 0 or an integer of 1 to 7. Examples of the fluoro(vinyl ether) are, for instance, perfluoro(methyl vinyl ether), perfluoro(ethyl vinyl ether), perfluoro(propyl vinyl ether),

CF₂ = CFOCF₂CF(CF₃)OCF₂CF₃,

CF₂ = CFOCF₂CF(CF₃)O(CF₂)₂CF₃,

CF₂ = CFOCF₂CF(CF₃)O(CF₂)₃CF₃,

CF₂ = CF(OCF₂CF(CF₃))₂OCF₂CF₃,

CF₂ = CF(OCF₂CF(CF₃))₂O(CF₂)₂CF₃, and

CF₂ = CF(OCF₂CF(CF₃))₂O(CF₂)₃CF₃,

A TFE/fluoro(vinyl ether) copolymer can be prepared, for example, by dispersion polymerization described in JP-A-189210/1983, or by emulsion polymerization described in JP-A-20788/1983.

The powder of the present invention can be prepared by producing a sheet with rolls from a TFE copolymer raw powder, and then pulverizing the sheet.

As the raw powder of TFE copolymer used in the process of the invention, there may be employed a dry powder prepared by dispersion polymerization described in JP-A-189210/1983 or prepared by emulsion polymerization described in JP-A-20788/1973. Since a dry powder prepared by emulsion polymerization contains an emulsifier or a coagulant, a dry powder prepared by dispersion polymerization is preferred in view of contaminant. Production of sheet with rolls is operative so that a sheet has a thickness of 0.05 to 5 mm, preferablly 0.1 to 3 mm.

The roll used in the present invention preferablly comprises two or more rolls which are arranged in perpendicular, inverted L, or Z position. Examples are, for instance, a calender roll or mixing roll. It is preferable to regulate a roll distance, rotation speed, pressure, and temperature. According to this method, since a large slide shearing force is applied to the copolymer, bubbles and cells in the copolymer can be released out of the copolymer to give a uniform and homogeneus sheet. The sheet produced by the method is uniform both in the surface and inner regions in comparison with a sheet produced by other press methods as described in U.S.-A-4,312,961, and can give the powder which satisfies the powder properties of the invention by the subsequent pulverizing step. The main defect of the press method is contamination of the TFE copolymer by a small amount of metal powder which is yielded due to abrasion between metal molds at the pressing operation. This contaminated TFE copolymer cannot be used for coatings or containers utilized in semiconductor industry because contamination gives serious damages to semiconductors. In addition, since release of bubbles or cells in the raw powder particles requires a very high pressure according to the press method, a special equipment is needed.

As operation conditions for production of sheet, there is preferably employed such conditions that an operation temperature is 0° to 250°C, particularly 30° to 200°C, and the resulting sheet is transparent or translucent.

Thickness of the sheet is preferably 0.05 to 5 mm. When more than 5 mm a uniform sheet is hard to obtain because a shearing force to the outer surface portion is different from that to the inner portion. A sheet thinner than 0.05 mm has a problem of productivity. The pulverizing step is carried out by applying impact force, shearing force and compression force to the sheet with machines such as cutter mill, hammer mill or jet mill. Operation temperature is generally -200° to 100°C.

Thermal stability of TFE copolymers can be improved by known methods desclosed in JP-B-23245/1971. Those methods may be employed in the present invention. Preferred thermally stabilizing method to be applied to the invention is fluorine gas treatment, which can be applied either to the copolymer obtained from the sheet production step or the copolymer obtained from the pulverizing step. As conditions of the fluorine gas treatment, there may be employed a fluorine gas concentration of 5 to 30 % by volume (the other gas being an inert gas such as nitrogen gas), a pressure of 0,1 to 1 MPa (0 to 10 kgf/cm²G), and a reaction temperature of 50° to 250°C.

Thermal stability ratio of a copolymer is calculated according to the equation (III):

wherein

MI(a):

melt index of a sample without heat treatment measured at 372°C according to ASTM D-2166

MI(b):

melt index of an sample which is subjected to heat treatment at 380°C for 5 hours.

The fluorine gas treatment is preferably carried out until a thermal stability ratio becomes 20 % or lower.

The TFE copolymer powder of the present invention is suitably used as material for molded articles such as pipes, parts, lining container or tank utilized for production of semiconductors which are seriously impared by contamination. Also the powder can be utilized for usual corrosion resistive lining, rotomolding (e.g. for containers), and roto-lining (e.g. for inner lining of pipes or joints). Those articles can be produced by various processing methods such as electrostatic powder coating method, fluidized dip coating method, roto-molding method and roto-lining method.

The present invention is more specifically described and explained by means of the following Examples.

PREPARATION EXAMPLE 1

A dry powder of TFE/perfluoro(propyl vinyl ether) copolymer (98.5/1.5 molar ratio) was prepared according to the dispersion polymerization described in JP-B-189210/1983. From the dry powder (bulk density: 0.57 g/cm³, average particle size: 400 to 600 µm), a translucent sheet having a thickness of 1 mm was produced by using special compression rolls (Roller Compactor "MINI" manufactured by Freund Industries, Co., Ltd.) under the following conditions: a roll rotation speed of 10 rpm, a feeder rotation speed of 20 rpm, a compression pressure of 15,1 MPa (150 kg/cm²G) and a roll surface temperature of 50°C.

The sheet was pulverized by using an atomizer (manufactured by Fuji Paudal Co., Ltd.) under the following conditions: a rotation speed of 1300 rpm, and a pore opening size of screen of 1.5 mm.

The resulting powder was sieved with a sieve of 0,50 mm (35 mesh) to give a non-spherical TFE copolymer powder having a frictional packing ratio of 35.5 %, a bulk density (ρ₁) of 0.92 g/cm³, an average particle size of 205 µm, and a thermal stability ratio of 75 %.

PREPARATION EXAMPLE 2

A translucent sheet having a thickness of 1 mm was produced according to the same procedures and by using the same TFE copolymer as in Preparation Example 1, and then was pulverized with an atomizer (manufactured by Fuji Paudal Co., Ltd.) under the following conditions: a rotation speed of 3900 rpm and a pore opening size of screen of 0.5 mm.

The resulting powder was sieved with a sieve of 0,25 mm (60 mesh) to give a non-spherical TFE copolymer powder having a frictional packing ratio of 60.0 %, a bulk density (ρ₁) of 0.55 g/cm³, an average particle size of 40 µm, and a thermal stability ratio of 72.5 %.

PREPARATION EXAMPLE 3

A dry powder (bulk density: 0.48 g/cm³, average particle size: 400 to 800 µm) of TFE/hexafluoropropylene copolymer (92/8 molar ratio) was prepared by dispersion polymerization. From the dry powder a translucent sheet having a thickness of 1.5 mm was produced by using special compression rolls (Roller Compactor "MINI" manufactured by Freund Industries, Co., Ltd.) under the following conditions: a roll rotation speed of 10 rpm, a feeder rotation speed of 20 rpm, a compression pressure of 15,1 MPa (150 kg/cm²G) and a roll surface temperature of 80°C.

The sheet was pulverized by using an atomizer (manufactured by Fuji Paudal Co., Ltd.) under the following conditions: a rotation speed of 1300 rpm, and a pore opening size of screen of 1.5 mm.

The resulting powder was sieved with a sieve of 0,50 mm (35 mesh) to give a non-spherical TFE copolymer powder having a frictional packing ratio of 40.2 %, a bulk density (ρ₁) of 0.90 g/cm³, an average particle size of 185 µm, and a thermal stability ratio of 120.5 %.

PREPARATION EXAMPLE 4

A cylindrical container of monel (inner diameter: 200 mm, height: 600 mm) having a heater wound therearound and also having a set of disc-like pans (outer diameter: 185 mm, height: 20 mm, 12 stages) arranged in the center of the container by means of a guide was used for fluorine gas treatment. Each pan was charged with 100 g of the TFE copolymer powder prepared in Preparation Example 1. After installing the set of pans in the container, the container was washed with nitrogen gas to remove oxygen gas, and then heated to 250°C. Subsequently, a fluorine gas diluted with nitrogen gas (fluorine gas content: 10 % by volume) was introduced to the container and maintained for 120 minutes. After cooling, nitrogen gas was exhausted to obtain a thermally stabilized powder having a thermal stability ratio of 2 %. As a result of observing the powder by means of scanning type electronmicroscopy, the powder particle was non-spherical. The electronmicroscopic photograph (magnification: 100) is shown in Fig. 1.

PREPARATION EXAMPLE 5

The TFE copolymer powder prepared in Preparation Example 1 was subject to the same fluorine gas treatment as in Preparation Example 4 except that the treatment was carried out at 200°C for 120 minutes by using a fluorine gas (fluorine gas content: 10 % by volume) to give a powder having a thermal stability ratio of 5 %.

PREPARATION EXAMPLE 6

The TFE copolymer powder prepared in Preparation Example 1 was subject to the same fluorine gas treatment as in Preparation Example 4 except that the treatment was carried out at 250°C for 180 minutes by using a fluorine gas (fluorine gas content: 5 % by volume) to give a powder having a thermal stability ratio of 11%.

PREPARATION EXAMPLE 7

The production of sheet and pulverization in Preparation Example 1 were repeated by using the fluorine-gas-treated TFE copolymer powder prepared in Preparation Example 4 to obtain a podwer. The powder was sieved with a sieve of 35 mesh to give a non-spherical TFE copolymer powder having a frictional packing ratio of 32.3 %, a bulk density (ρ₁) of 0.95 g/ml, an average particle size of 190 µm, and a thermal stability ratio of 2 %.

PREPARATION EXAMPLE 8

The TFE copolymer powder prepared in Preparation Example 2 was subjected to the same fluorine gas treatment as in Preparation Example 4 except that the treatment was carried out at 200°C for 120 minutes by using a fluorine gas (fluorine gas content: 10 % by volume) to give a powder having a thermal stability ratio of 9 %.

COMPARATIVE PREPARATION EXAMPLE 1

By using the TFE copolymer raw powder used in Preparation Example 1, tablets (diameter: 11 mm, thickness: 3 mm, weight: 0.8 g) were prepared by means of an automatic molding machine under a compression pressure of 70,1 MPa (700 kg/cm²G.)

The tablets were pulverized under the same conditions as in Preparation Example 1 and sieved to give a non-spherical TFE copolymer powder having a frictional packing ratio of 125 %, a bulk density (ρ₁) of 0.62 g/cm³, an average particle size of 233 µm, and a thermal stability ratio of 76.5 %.

COMPARATIVE PREPARATION EXAMPLE 2

Tablets were prepared in the same manner as in Comparative Preparation Example 1, and then pulverized in the same manner as in Preparation Example 2 to give a non-spherical TFE copolymer powder having a frictional packing ratio of 150 %, a bulk density (ρ₁) of 0.32 g/cm³, an average particle size of 55 µm, and a thermal stability ratio of 73 %.

EXAMPLES 1 TO 5 AND COMPARATIVE EXAMPLE 1

A mold of 3000 mℓ with a mold bumping was cleaned, and a silicone type mold-release compound was applied to the mold, and then dried. The mold was charged with 600 g of the powder prepared in Preparation Example 1, and sealed. After setting the mold to a roto-molding machine, the molding machine was heated from room temperature to 360°C for 40 minutes while rotating biaxially at a revolution speed of 9 rpm and an autorotation speed of 23 rpm, and maintained at 360°C for 60 minutes, following by air cooling for 30 minutes to mold a container. The outer and inner surfaces of the molded container were observed in viewpoints of appearance and foaming. The results are shown in Table 1.

The represented evalution in Table 1 are based on the following standard.

(Appearance of outer surface)

X

: Partial surface defects

○

: Beautiful appearance

(Appearance of inner surface)

X

: Great undulation having continuous ball-like projections

△

: Modelate undulation

○

: Good leveling property

(Foaming)

X

: Many bubbles or cells

△

: Some bubbles or cells

○

: No bubble or cell

EXAMPLE 6

A container was molded in the same manner as in Example 1 except that the powder prepared in Preparation Example 9 was used and the mold was heated at 340°C. The molded container was observed to evaluate its appearance and foaming. The results are shown in Table 1.

COMPARATIVE EXAMPLE 2

A container was molded in the same manner as in Example 1 except that a spherical powder having a frictional packing ratio of 13.5 %, a bulk density of 0.98 g/cm³, an average particle size of 320 µm and a thermal stability ratio of 3 %. The molded container was observed to evaluate its appearance and foaming. The results are shown in Table 1.

EXAMPES 7 TO 8 AND COMPARATIVE EXAMPLE 3

To the powders prepared in Preparation Examples 1 and 3 and Comparative Preparation Example 1 was added potassium hydrogen-sulfate as a melting agent. The powder was melted and decomposed in a platinum basin, and then an ash content was dissolved in deionized water to prepare a sample solution. The sample solutions were analyzed by means of atomic absorption analysis (flameless) to determine amounts of iron, chromium and nickel present in the powders. The results are shown in Table 2.

As is clear from Table 2, according to the press method the powder is contaminated with metals used in the mold.

EXAMPLE 9

To a blast-treated stainless steel plate were applied two prymers for fluorine resin coating (EK-1083GB and EK-1883GB, both avairable from Daikin Industries, Ltd.) to form a double layer primer coating, and then was baked. The primer coating was electrostatically coated with the powder prepared in Preparation Example 8 at a base plate temperature of 300°C with a electrostatic powder coating machine (GX3300 Type manufactured by Iwata Aircompressor Manufacturing, Co., Ltd.), and the resulting coating was baked at 340°C.

After repeating the electrostatic powder coating operation three times one above the other while shifting the application area so that a surface of each coating could be observed, the resulting three-layer coating was baked at 340°C for 120 minutes to obtain a sample. The appearance of each coating surface was observed and evaluated according to the following standard. The result are shown in Table 3.

X

: Many bubbles or cells

△

: Some bubbles or cells

○

: No bubble or cell

COMPARATIVE EXAMPLE 4

By using the TFE copolymer powder of Comparative Preparation Example 2, the same coating and baking procedures as in Example 9 were repeated to prepare a coating, and then the appearance of the coating surfaces were observed. The results are shown in Table 3.

Example No.

TFE Copolymer Powder

First Coating (thickness)

Second Coating (thickness)

Third Coating (thickness)

9

Prep.Ex.8

○ (500 µm)

○ (900 µm)

○ (1200 µm)

Comp. Ex. No.

4

Comp. Prep. Ex. 2

○ (200 µm)

X (400 µm)

-