JP2022179573A - Production method of fluororesin particles containing fluorine-containing aliphatic ring structure - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a production method of fluororesin particles containing a fluorine-containing aliphatic ring structure, which is excellent in productivity and can remove an extraneous material.

SOLUTION: There is provided a production method of fluororesin particles containing a fluorine-containing aliphatic ring structure, which contains a precipitation process of precipitating particles of a fluororesin (A) by reducing a temperature of a solution relative to a fluororesin (A) solution in which the fluororesin (A) containing a fluorine-containing aliphatic ring structure is dissolved in a solvent (B).

SELECTED DRAWING: None

COPYRIGHT: (C)2023,JPO&INPIT

Description

TECHNICAL FIELD The present invention relates to a method for producing fluororesin particles having a fluorine-containing alicyclic structure, which is excellent in productivity and capable of removing foreign matters.

A fluororesin containing a fluorine-containing alicyclic structure (hereinafter referred to as the fluororesin) exhibits amorphous properties and is excellent in transparency, liquid repellency, durability, electrical properties, etc., so it is used in various fields such as optics and electronics. used for purposes.

As the fluororesin, for example, in Patent Document 1, a cyclized polymer of perfluoro(4-vinyloxy-1-butene), in Non-Patent Document 1, poly(perfluoro-2-methylene-4-methyl-1,3 -dioxolanes) have been reported.

The fluororesin is generally provided in the form of a solution in many cases, but in the case of melt molding, it is possible to continuously supply the resin to the inside of the molding machine, so the resin is preferably in the form of particles. Desired. In addition, in other wide-ranging applications, the resin is required to be in the form of particles from the viewpoint of handleability and solubility.

In Patent Document 1, suspension polymerization is exemplified as a method for obtaining particles of the fluororesin. However, dispersants and emulsifiers used as polymerization aids remain inside the resin particles and become foreign matter or cause coloration when heated. could have been lost. Further, according to the present inventors, particles cannot be obtained in suspension polymerization without using a dispersant.

In addition, in order to ensure the strict cleanliness required in the fields of optics and electronics, it is desirable to filter the fluororesin solution to remove foreign substances before granulating. For this purpose, it is necessary to once dissolve the fluororesin in a good solvent to form a solution. However, according to the present inventors, in a method generally known as a reprecipitation method, in which a polymer solution dissolved in a good solvent is added dropwise to a poor solvent to obtain a powder, the fluororesin is in the form of strands or cotton. etc., there is a problem that it is difficult to take out as particles.

WO2014/156996 publication Macromolecules, 2005, 38, 4237-4245

The present invention has been made in view of the above problems, and an object of the present invention is to provide a method for producing fluororesin particles containing a fluorine-containing alicyclic structure, which is excellent in productivity and capable of removing foreign matters.

The inventors of the present invention have made intensive studies to achieve the above objects, and found that a specific method for producing fluororesin particles containing a fluorine-containing alicyclic structure can solve the above problems. Arrived.

That is, the present invention is as follows.

A fluororesin (A) containing a fluorine-containing alicyclic structure is dissolved in a solvent (B) in a fluororesin (A) solution, and the temperature of the solution is lowered to precipitate particles of the fluororesin (A). A method for producing fluororesin particles containing a fluorine-containing alicyclic structure, comprising a precipitation step of allowing the

The structure of the fluororesin containing a fluorine-containing alicyclic structure (hereinafter referred to as "fluororesin (A)") is not limited as long as it contains a fluorine-containing alicyclic structure. 1), cyclized polymers and copolymers of perfluoro(4-vinyloxy-1-butene), polymers of perfluoro(2,2-dimethyl-1,3-dioxole) and copolymers, copolymers of perfluoro(2,2-dimethyl-1,3-dioxole) and tetrafluoroethylene, 2,2,4-trifluoro-5-trifluoromethoxy-1,3-dioxole At least one of the group consisting of polymers and copolymers, and copolymers of 2,2,4-trifluoro-5-trifluoromethoxy-1,3-dioxole and tetrafluoroethylene can be exemplified.

(In the formula (1), Rf ₁ , Rf ₂ , Rf ₃ and Rf ₄ are each independently a fluorine atom or a C 1-7 etheric oxygen atom which may be linear, branched or (Rf ₁ , Rf ₂ , Rf ₃ and Rf ₄ may be linked to each other to form a ring having 4 to 8 carbon atoms.)
Each of Rf ₁ , Rf ₂ , Rf ₃ and Rf ₄ groups in the residue unit represented by formula (1) in the present invention independently has a fluorine atom or an etheric oxygen atom having 1 to 7 carbon atoms. one of the group consisting of linear, branched or cyclic perfluoroalkyl groups which may be substituted. Also, Rf ₁ , Rf ₂ , Rf ₃ and Rf ₄ may be linked to each other to form a ring having 4 or more and 8 or less carbon atoms. Examples of linear perfluoroalkyl groups having 1 to 7 carbon atoms include trifluoromethyl group, pentafluoroethyl group, heptafluoropropyl group, nonafluorobutyl group, undecafluoropentyl group, tridecafluorohexyl group, pentadecafluoroheptyl group and the like, and examples of branched perfluoroalkyl groups having 3 to 7 carbon atoms include heptafluoroisopropyl group, nonafluoroisobutyl group, nonafluorosec-butyl group, nonafluorotert-butyl group and the like. Examples of the cyclic perfluoroalkyl group having 3 to 7 carbon atoms include heptafluorocyclopropyl group, nonafluorocyclobutyl group, tridecafluorocyclohexyl group and the like. Linear perfluoroalkyl groups having 1 to 7 carbon atoms which may have an etheric oxygen atom include, for example, -CF ₂ OCF ₃ group, -(CF ₂ ) ₂ OCF ₃ group, -(CF ₂ ) ₂ OCF ₂ CF ₃ groups and cyclic perfluoroalkyl groups having 3 to 7 carbon atoms which may have an etheric oxygen atom include, for example, 2-(2,3,3,4,4,5, 5,6,6-decafluoro)-pyrinyl group, 4-(2,3,3,4,4,5,5,6,6-decafluoro)-pyrinyl group, 2-(2,3,3, 4,4,5,5-heptafluoro)-furanyl group and the like.

At least one of Rf ₁ , Rf ₂ , Rf ₃ and Rf ₄ is preferably a linear, branched or cyclic perfluoroalkyl group having 1 to 7 carbon atoms in order to obtain excellent heat resistance.

Specific examples of residue units represented by general formula (1) include the following residue units.

Among them, since a fluororesin having excellent heat resistance can be obtained, a fluororesin containing a perfluoro(4-methyl-2-methylene-1,3-dioxolane) residue unit represented by the following general formula (3) is preferably

The fluororesin (A) of the present invention may contain other monomer residue units, and other monomer residue units include tetrafluoroethylene (TFE) and hexafluoropropylene (HFP). , chlorotrifluoroethylene (CTFE), trifluoroethylene, hexafluoroisobutylene, perfluoroalkylethylene, fluorovinyl ether, and the like.

The solvent (B) in the present invention dissolves the fluororesin (A) at the temperature before the temperature is lowered in the precipitation step, and the fluororesin (A) is precipitated by lowering the temperature in the precipitation step. Just do it.

Here, the expression that the fluororesin (A) is dissolved in the solvent (B) means that at least a part of the fluororesin (A) is dissolved in the solvent (B). In addition to the method of confirming whether the If this occurs, it can be confirmed by a method such as judging that at least a part of the fluororesin (A) is dissolved in the fluororesin (A) solution before it is added to the poor solvent. The state of the solution may be a stirrable state, and examples include a uniform liquid state, a cloudy liquid state, and a gel state.

In the precipitation step, the solubility of the fluororesin (A) in the solvent (B) at the temperature before lowering the temperature is 50 wt. % or more, more preferably 70% by weight or more, and particularly preferably 80% by weight or more.

The solubility of the fluororesin (A) in the solvent (B) at the temperature after the temperature is lowered in the particle precipitation step is excellent in productivity, and particles excellent in handleability as powder are obtained. It is preferably less than 50% by weight, preferably less than 30% by weight, particularly preferably less than 20% by weight.

The solvent (B) in the present invention dissolves the fluororesin (A) at the temperature before lowering the temperature in the precipitation step, and if the fluororesin (A) is precipitated by lowering the temperature in the precipitation step. Often, the component can be a single solvent or a composition comprising multiple solvents. The solvent (B) is a good solvent (b-1) for the fluororesin (A) and a poor solvent for the fluororesin (A), since particles with excellent productivity and excellent handleability as powder can be obtained. A composition containing (b-2) is preferred.

Here, the good solvent (b-1) is an organic solvent capable of dissolving the fluororesin (A) at the temperature before the temperature is lowered in the precipitation step, preferably at 50°C. It is an organic solvent.

For example, a powdery or flocculent fluororesin (A) is immersed in an organic solvent at the same temperature as the resin solution to be subjected to the precipitation step for 5 hours or more, and a solvent in which the resin dissolves can be judged as a good solvent. can. Here, the temperature of the resin solution to be subjected to the precipitation step refers to the temperature before the temperature is lowered.

The good solvent (b-1) preferably has a solubility of 80 wt % or more, more preferably 90 wt % or more, in the fluororesin (A).

The good solvent (b-1) is preferably at least one selected from the group consisting of perfluorocarbons, hydrochlorofluorocarbons, hydrofluorocarbons, hydrofluoroethers, hydrofluoroolefins and aromatic fluorine compounds, more preferably perfluorohexane. , perfluoro-N-methylmorpholine, perfluoro-N-propylmorpholine, perfluorotriethylamine, perfluoromethyldibutylamine, perfluorotributylamine, CF ₃ CF ₂ CHCl ₂ , CF ₃ CHFCHFCF ₂ CF ₃ , CF ₃ CF _{2 CF2CF2CF2CF2H , CF3 ( CF2 ) 5CH2CH3 , C4F9OCH3 , C4F9OC2H5 , C2F5CF ( OCH3 ) C3F _ _ _ 7} ), preferably at least one of the group consisting of hexafluorobenzene.

Examples of these solvents include perfluorocarbons such as Fluorinert FC-5052, FC-72, FC-770, FC-3283, FC-40, and FC-43 (all manufactured by 3M Japan); Asahiklin AK-225 (Asahi Glass Hydrochlorofluorocarbons such as Vertrel XF (manufactured by Mitsui Chemours), Asahiklin AC-2000, AC-6000 (both manufactured by Asahi Glass Co., Ltd.), etc.; Novec7100, Novec7200, Novec7300 (manufactured by 3M Japan) ); hydrofluoroolefins such as Opteon SF10 (manufactured by Mitsui Chemours); aromatic fluorine-containing solvents such as hexafluorobenzene; The good solvent (b-1) is preferably a fluorine-containing solvent, such as hydrofluorocarbons, hydrofluoroethers, hydrochlorofluorocarbons, hydro Aliphatic fluorinated solvents having hydrogen atoms in the molecule such as fluoroolefins; is even more preferred, and hydrofluoroethers are particularly preferred. Here, the aliphatic fluorine-containing solvent having hydrogen atoms may be saturated or unsaturated, and may be linear or cyclic.

Here, the poor solvent (b-2) is an organic solvent that precipitates the fluororesin (A) at a temperature after the temperature is lowered in the precipitation step, preferably at 25 ° C., the fluororesin (A) is It is an organic solvent for precipitation. An organic solvent in which the fluororesin (A) precipitates when the good solvent (b-1) in which the fluororesin (A) is dissolved can be dropped into an organic solvent can be judged as a poor solvent.

The poor solvent (b-2) preferably has a solubility of less than 20 wt%, more preferably less than 10 wt%, in the fluororesin (A).

Examples of the poor solvent (b-2) include 1,1,2,2-tetrafluoroethyl-2,2,2-trifluoroethyl ether, 2,2,2-trifluoroethanol, 1,1,1 , 3,3,3-hexafluoroisopropanol, 1,2,2,3,3,4,4-heptafluorocyclopentane and other fluorine-containing solvents having a hydrogen atom in the molecule; fluorine-containing alcohols such as trifluoroethanol at least one selected from the group consisting of fluorine-free organic solvents such as hexane, toluene, acetone, methanol, ethyl acetate and chloroform; The organic solvent is preferably a fluorine-containing solvent, more preferably a fluorine-containing solvent having a hydrogen atom in the molecule, since particles having excellent productivity and excellent handleability as powder can be obtained. , 1,1,2,2-tetrafluoroethyl-2,2,2-trifluoroethyl ether, 2,2,2-trifluoroethanol, 1,1,1,3,3,3-hexafluoroisopropanol, More preferred is at least one of the group consisting of 1,2,2,3,3,4,4-heptafluorocyclopentane.

In the solvent (B) subjected to the precipitation step, the ratio of the good solvent (b-1) and the poor solvent (b-2) is excellent in productivity, and particles excellent in handleability as powder are obtained. The weight ratio of good solvent: poor solvent is preferably 10:90 to 99:1, more preferably 20:80 to 95:5, still more preferably 30:70 to 95:5, and 30:70 to 90:10. is more preferred, and 30:70 to 80:20 is even more preferred.

In the precipitation step, the concentration of the fluororesin (A) solution is preferably 1 to 30 wt%, more preferably 2 to 20 wt%, since particles having excellent productivity and excellent handleability as powder can be obtained. , 5 to 15 wt % are particularly preferred.

In the precipitation step, the temperature of the fluororesin (A) solution to be subjected to the precipitation step, that is, the solution temperature before lowering the temperature (hereinafter referred to as “T ₁ ”) is preferably 30° C. or higher, more preferably 40° C. or higher. On the other hand, in the precipitation step, the solution temperature (hereinafter referred to as “T ₂ ”) after the temperature is lowered is preferably 30° C. or lower, more preferably 25° C. or lower. Thereby, the fluororesin (A) is sufficiently deposited.

In addition, T ₁ −T ₂ is preferably 5° C. or higher, more preferably 10° C. or higher, since particles having excellent productivity and excellent handleability as powder can be obtained.

In the precipitation step, since particles with excellent productivity and excellent handleability as powder are obtained, it is preferable to lower the temperature in 1 to 600 minutes, and it is more preferable to lower the temperature in 5 to 300 minutes. preferable.

In the precipitation step, it is preferable to lower the temperature at a rate of 0.05 to 20 ° C. per minute, since particles with excellent productivity and excellent handleability as powder can be obtained, and the temperature is preferably decreased at a rate of 0.1 to 0.1 per minute. Decreasing the temperature at a rate of 5°C is particularly preferred.

In the precipitation step, it is preferable to perform stirring because it is possible to obtain particles having excellent productivity and excellent handleability as a powder.

In the precipitation process, particles with excellent productivity and excellent handleability as powder are obtained ^. It is preferable ^to deposit a particulate ^solid by lowering the temperature while stirring so that 0.5 to 10 kW/m ³ are particularly preferred. Here, the Pv value (kW/m ³ ) can be calculated by the following formula (5).

(Here, Np: power number, ρ: density of solution (kg/m ³ ), n: rotation speed of stirring blade (rpm), d: diameter of stirring blade (mm), V: amount of solution (L) show.)
Np in Equation (5) is a dimensionless number called power number, which varies depending on the shape of the stirring blade. This Np is obtained from known documents such as "Kagaku Kiseki, August 1995, pp. 71-79" and "Shinko Faudler Giho vol.28, No. 8 (October 1984), pp. 13-16". be able to. At this time, when the ratio b/d of the blade width b to the stirring blade diameter d is different from the stirring blade described in the literature, it can be calculated by the following formula (6).

Actual Np = Literature Np x (Actual b/d)/(Literature b/d) (6)
(Here, Np: power number, b: width of stirring blade (mm), d: diameter of stirring blade (mm).)
In the fluororesin (A) solution in which the particles are precipitated, obtained in the precipitation step, mutual adhesion of the obtained particles is prevented, and particles with excellent handleability are obtained, so the poor solvent (b-2) It is preferable to perform a poor solvent addition step of adding. The amount of the poor solvent (b-2) added in the poor solvent addition step is excellent in productivity, prevents mutual adhesion of particles, and provides particles with excellent handleability as powder. It is preferable to add the poor solvent in an amount of 0.1 times or more, more preferably 0.5 to 1 time, with respect to the weight of the fluororesin (A) solution obtained.

Since the productivity is excellent, the particles are prevented from sticking to each other, and particles with excellent handleability as powder are obtained, the good solvent after adding the poor solvent (b-2) in the poor solvent addition step: poor The weight ratio of the solvents is preferably 10:90-90:10, more preferably 20:80-80:20, even more preferably 30:70-70:30, and particularly preferably 30:70-60:40.

In the present invention, any other process may be added, but in order to ensure the strict cleanliness required in the field of optics and electronics, the fluororesin (A) solution is filtered before the deposition process to remove foreign matter. It is preferable to have a filtration step to remove the The filtration method is not particularly limited, and examples thereof include pressure filtration, vacuum filtration, centrifugal filtration, and the like. Although the size of the filter to be used is not limited, for example, a filter having a capture particle size of 1 μm or less can be used. The material of the filter to be used is not limited, but examples thereof include polypropylene, polyethylene, polyethylene terephthalate, nylon, PTFE, and PES.

In the present invention, any other step may be added, and a separation step of taking out a particulate solid by solid-liquid separation may be included after the precipitation step or the poor solvent addition step. The solid-liquid separation method is not particularly limited, and examples thereof include pressure filtration, vacuum filtration, centrifugation, and centrifugal filtration. Although the size of the filter to be used is not limited, for example, a filter having a capture particle size of 10 μm or less can be used. The material of the filter to be used is not limited, but examples thereof include polypropylene, polyethylene, polyethylene terephthalate, nylon, PTFE, and PES.

In the present invention, any other step may be added, and a drying step for drying the particles of the fluororesin (A) may be included. The drying method is not particularly limited, and examples thereof include vacuum drying, reduced pressure drying, normal pressure drying, air drying, shaking drying, warm air drying, heat drying and the like.

The weight average molecular weight Mw of the fluororesin (A) may be any value, for example, the weight average molecular weight Mw measured using gel permeation chromatography (GPC) is 10,000 to 1,000,000. mentioned.

The fluororesin (A) in the present invention may be produced by any method. For example, it can be obtained by polymerizing a monomer represented by the following general formula (4) in the presence of a radical polymerization initiator. can.

(In the formula (4), Rf ₅ , Rf ₆ , Rf ₇ and Rf ₈ each independently have a fluorine atom or an etheric oxygen atom having 1 to 7 carbon atoms, may be linear, branched or (Rf ₅ , Rf ₆ , Rf ₇ and Rf ₈ may be linked to each other to form a ring having 4 to 8 carbon atoms.)
Examples of radical polymerization initiators for radical polymerization include benzoyl peroxide, lauryl peroxide, octanoyl peroxide, acetyl peroxide, di-tetr-butyl peroxide, tetr-butylcumyl peroxide, dicumyl peroxide, oxide, tetr-butyl peroxyacetate, perfluoro(di-tetr-butyl peroxide), bis(2,3,4,5,6-pentafluorobenzoyl) peroxide, tetr-butyl peroxybenzoate, tetr-butyl Organic peroxides such as perpivalate; 2,2′-azobis(2,4-dimethylvaleronitrile), 2,2′-azobis(2-butyronitrile), 2,2′-azobisisobutyronitrile, Examples include azo initiators such as dimethyl-2,2'-azobisisobutyrate and 1,1'-azobis(cyclohexane-1-carbonitrile).

The fluororesin (A) may be produced by any method, and examples thereof include methods such as bulk polymerization and solution polymerization.

The fluororesin solution (A) may be prepared by any method, but since it is excellent in productivity, a method of dissolving the solid of the fluororesin (A) in a solvent or a method of dissolving the fluororesin (A) in a solvent It is preferable to prepare the fluororesin solution (A) in the solution preparation step of obtaining the fluororesin solution (A) by any of the methods including using the solution obtained by performing the polymerization reaction of A) as it is.

In the method of dissolving the fluororesin (A) resin in a solvent, the method of dissolving the solid of the fluororesin (A) in the composition of the good solvent (b-1) and the poor solvent (b-2), the fluororesin (A) A method of dissolving the solid in the good solvent (b-1) is preferred, and a method of dissolving the fluororesin (A) in a composition of the good solvent (b-1) and the poor solvent (b-2) is particularly preferred. At this time, the obtained solution may be used as it is, or the composition of the good solvent (b-1) and the poor solvent (b-2), or the concentration may be adjusted by adding the poor solvent (b-2). good.

In the method using the solution in which the fluororesin (A) has been polymerized, the fluororesin (A) is polymerized using a composition of the good solvent (b-1) and the poor solvent (b-2) as the polymerization solvent. A method of using a solution and a method of using a solution in which the fluororesin (A) has been polymerized using the good solvent (b-1) as a polymerization solvent are preferred. At this time, the resulting solution may be used as it is, or a composition of a good solvent (b-1) and a poor solvent (b-2), or a poor solvent (b-2) is added to the fluororesin (A ) concentration may be adjusted.

The particle diameter of the fluororesin particles containing a fluorine-containing alicyclic structure of the present invention is not particularly limited, but the volume average particle diameter is 1 to 10,000 μm because it is excellent in handleability during molding. preferably 1 to 1000 μm, more preferably 10 to 1000 μm.

ADVANTAGE OF THE INVENTION According to this invention, it is excellent in productivity and can provide the manufacturing method of the fluororesin particle containing the fluorine-containing alicyclic structure which can remove a foreign material.

EXAMPLES The present invention will be described in more detail below with reference to Examples and Comparative Examples, but the present invention is not limited to these.
[Measurement of weight average molecular weight Mw]
Measurement was performed using gel permeation chromatography equipped with a column TSKgel SuperAWM-H manufactured by Tosoh Corporation and an RI detector. Using Agilent's standard polymethyl methacrylate as a standard sample, the weight average molecular weight Mw in terms of polymethyl methacrylate was calculated from the elution times of the sample and the standard sample.
[Measurement of volume average particle size]
The volume average particle size (unit: μm) was measured using MT3000 manufactured by Microtrac and using methanol as a dispersion medium.
[Calculation of Pv value]
The Pv value, which is the value of the stirrer motor power per unit stirring capacity, was calculated from the following formula. An Np of 1.25 was used when four diagonal paddle stirring blades (blade diameter 40 mm, blade width 8 mm, oblique angle 45°) were used.

(Here, Np: power number, ρ: density of solution (kg/m ³ ), n: rotation speed of stirring blade (rpm), d: diameter of stirring blade (mm), V: amount of solution (L) show.)

[Synthesis Example 1]
0.017 g of bis(2,3,4,5,6-pentafluorobenzoyl) peroxide as a radical polymerization initiator, perfluoro(4-methyl-2-methylene-1, 3-dioxolane) and 20 g of FC-72 (manufactured by 3M Japan Co., Ltd.) as a polymerization solvent were added, and after repeating nitrogen substitution and pressure release by freezing and degassing, the flask was sealed under reduced pressure. This ampoule was placed in a constant temperature bath at 55° C. and held for 24 hours to carry out radical solution polymerization. After cooling to room temperature, the ampoule was opened, and the resin solution was diluted with 25 g of FC-72 to adjust the viscosity to prepare a diluted resin solution. Hexane is added to a beaker equipped with a stirrer, and the diluted resin solution is added to the hexane while stirring to precipitate the resin. A fluororesin (A) (poly(perfluoro(4-methyl-2-methylene-1,3-dioxolane)) containing a structure was obtained. The obtained fluororesin (A) was composed of fibers having a length of 5 cm or more. When the resin diluted solution was added to hexane, the resin wound around the stirrer to a large extent, and had a weight average molecular weight Mw of 470,000.

[Reference example 1]
The fluororesin (A) was immersed in various organic solvents at 50° C. for 5 hours or more, and it was visually confirmed whether it was dissolved or not. The results are as follows.
Soluble: FC-72, FC-770, Novec7200, Novec7300, hexafluorobenzene When the solutions dissolved in these solvents were cooled to 25°C, they all remained dissolved. All of them had almost no undissolved residue and had a solubility of 90 wt % or more.
Not soluble: Zeorora H, AE-3000, trifluoroethanol, ethyl acetate, chloroform, acetone, hexane

[Reference example 2]
When the FC-72 solution in which the fluororesin (A) was dissolved was added dropwise at 25° C. to the following organic solvent, no solid precipitated.
FC-72, FC-770, Novec7200, Novec7300, Hexafluorobenzene

[Comparative Example 1]
When the FC-72 solution in which the fluororesin (A) was dissolved was added dropwise to the following organic solvent at 25°C, a solid precipitated. The obtained fluororesin (A) was flocculate with fibers having a length of 5 cm or longer.
For all of Zeorora H, AE-3000, trifluoroethanol, ethyl acetate, chloroform, acetone, and hexane, the recovery rate of fluororesin (A) after filtration and drying exceeds 80%, and the solubility is 20 wt% or less. rice field.

[Example 1]
5.0 g of fluororesin (A) in a 50 mL sample tube equipped with a stirrer, 21.31 g of Novec7200 (manufactured by 3M Japan) as a good solvent (b-1), and Zeorora H (Japan) as a poor solvent (b-2) Zeon Corporation) 14.21 g was taken, tightly stoppered, and stirred at 50° C. to dissolve the fluororesin (A) to prepare a solution. After adding the above solution that had been returned to room temperature to a separable flask with a capacity of 50 mL equipped with 4 diagonal paddle stirring blades (blade diameter 40 mm, blade width 8 mm, diagonal 45°), three-one motor, and water bath, the solution was stirred at 150 rpm with a zeorola. When 7.10 g of H was added, a massive solid precipitated. By heating to 50° C. while stirring at 150 rpm and holding for 10 minutes, a fluororesin (A) solution was obtained (Zeorolla H/Novec7200=50/50 (wt/wt)) (the steps up to this point are referred to as “ “solution preparation step”).

While stirring the fluororesin (A) solution at 500 rpm (Pv value: 4.4 kW/m ³ ), remove the water bath, allow to cool in the air, and cool to 30°C in about 10 to 20 minutes. A particulate solid was obtained (this process is referred to as the "precipitation process"). At this time, precipitation of particulate solids began at about 40°C.

Then, while stirring at 500 rpm, 18.27 g of Zeorora H was further added (Zeorolla H/Novec7200=65/35 (wt/wt)) (this process is referred to as a "poor solvent addition process").

The obtained solution is subjected to suction filtration and vacuum-dried under heating to obtain a fluororesin A containing a fluorine-containing alicyclic structure (poly(perfluoro(4-methyl-2-methylene-1,3-dioxolane )) particles were obtained (this step is referred to as the “separation step”).
The obtained particles were fine particles having a volume average particle diameter of 130 μm, and were substantially free of coarse particles.

[Example 2]
Particles of fluororesin A were obtained in the same manner as in Example 1 except that the fluororesin A solution was stirred at 250 rpm (Pv value: 0.54 kW/m ³ ) in the precipitation step. The obtained particles were fine particles having a volume average particle diameter of 270 μm, and were substantially free of coarse particles.

[Example 3]
In Example 1, 5.0 g of fluororesin (A) was placed in a 50 mL sample tube equipped with a stirrer, 21.32 g of Novec7200 (manufactured by 3M Japan) as a good solvent (b-1), and a poor solvent (b-2). Take 14.21 g of Zeorora H (manufactured by Nippon Zeon Co., Ltd.) as a seal, and stir at 50 ° C. to dissolve the fluororesin (A), prepare a solution, and then pressurize using a 1 μm PTFE membrane filter. The same operation as in Example 1 was performed except that a filtering step of filtering and removing foreign matter was performed. The obtained particles were fine particles having a volume average particle diameter of 150 μm, and were substantially free of coarse particles.

[Example 4]
The same operation as in Example 1 was performed except that AE-3000 (manufactured by Asahi Glass Co., Ltd.) was used as the poor solvent (b-2) instead of Zeorola H. The obtained particles were fine particles having a volume average particle diameter of 170 μm, and were substantially free of coarse particles.

[Example 5]
The same operation as in Example 1 was performed except that Novec7300 (manufactured by 3M Japan Ltd.) was used instead of Novec7200 as the good solvent (b-1). The obtained particles were fine particles having a volume average particle diameter of 40 μm, and were substantially free of coarse particles.

[Example 6]
5.0 g of fluororesin (A) and 21.31 g of hexafluorobenzene (manufactured by Tokyo Chemical Industry Co., Ltd.) as a good solvent (b-1) are placed in a 50 mL sample tube equipped with a stirrer, sealed, and stirred at 50°C. Thus, the fluororesin (A) was dissolved to prepare a solution. After the solution was returned to room temperature, it was poured into a 50 mL separable flask equipped with four diagonal paddle stirring blades (blade diameter 40 mm, blade width 8 mm, diagonal 45 °), three-one motor, and water bath. When 11.48 g of Zeorola H was added as the solvent (b-2), a massive solid precipitated. By heating to 50° C. with stirring at 150 rpm and holding for 10 minutes, most of the fluororesin (A) was dissolved in the organic solvent, and a cloudy solution was obtained (Zeorolla H/Hexafluorobenzene=35/ 65 (wt/wt)).

Most of the fluororesin (A) is dissolved in the organic solvent, and the cloudy solution is stirred at 500 rpm (Pv value: 4.4 kW/m ³ ), removed from the water bath, and allowed to cool in the air. Cooling to 30° C. in about 10-20 minutes gave a particulate solid. After that, while stirring at 500 rpm, 9.84 g of Zeorora H was further added (Zeorolla H/hexafluorobenzene = 50/50 (wt/wt). Suction filtration was performed, and vacuum drying under heating was performed to obtain a fluororesin ( Particles A) were obtained, which were fine particles having a volume average particle diameter of 410 μm and almost no coarse particles.

[Example 7]
5.0 g of fluororesin (A) in a 50 mL sample tube equipped with a stirrer, 21.31 g of FC-72 (manufactured by 3M Japan) as a good solvent (b-1), and Zeorora H as a poor solvent (b-2) (manufactured by Nippon Zeon Co., Ltd.) 14.21 g was taken, sealed, and stirred at 50 ° C. to dissolve the fluororesin (A) to prepare a solution (Zeo Roller H / FC-72 = 40/60 (wt / wt )). After adding the above solution that had been returned to room temperature to a separable flask with a capacity of 50 mL equipped with 4 diagonal paddle stirring blades (blade diameter 40 mm, blade width 8 mm, diagonal 45°), three-one motor, and water bath, the solution was stirred at 150 rpm with a zeorola. When 21.31 g of H was added, a massive solid precipitated. By heating to 50 ° C. with stirring at 150 rpm and holding for 10 minutes, a solution in which the fluororesin (A) was separated in the form of a gel in an organic solvent was obtained (Zeorolla H/FC-72 = 62.5/37 .5 (wt/wt)).

Remove the water bath while stirring the solution of the fluororesin (A) separated in gel form in the organic solvent at 500 rpm (Pv value: 4.4 kW/m ³ ), allow to cool in the air, Cooling to 30° C. in ˜20 minutes gave a particulate solid. Then, while stirring at 500 rpm, 14.21 g of Zeorora H was further added (Zeorolla H/FC-72=70/30 (wt/wt)). Particles of fluororesin (A) were obtained by suction filtration and vacuum drying under heating. The obtained particles had an average particle diameter of about 1.5 mm as measured with a ruler, and included coarse particles having a diameter of about 5 to 10 mm.

[Example 8]
5.0 g of fluororesin (A) and 21.31 g of Novec7200 (manufactured by 3M Japan) as a good solvent (b-1) are placed in a 50 mL sample tube equipped with a stirrer, sealed, and stirred at 50°C. A solution was prepared by dissolving the fluororesin (A). After the solution was returned to room temperature, it was poured into a 50 mL separable flask equipped with four diagonal paddle stirring blades (blade diameter 40 mm, blade width 8 mm, diagonal 45 °), three-one motor, and water bath. When 2.37 g of ethyl acetate was added as the solvent (b-2), a lumpy solid precipitated. By heating to 50° C. with stirring at 150 rpm and holding for 10 minutes, a solution in which the fluororesin (A) was dissolved in the organic solvent (B) was obtained (ethyl acetate/Novec7200=10/90 (wt/wt When 1.39 g of ethyl acetate was further added and heated to 70° C., a solution in which fluororesin A was separated in a gel form was obtained (ethyl acetate/Novec7200=15/85 (wt/wt)). .

The solution in which the fluororesin (A) is separated in gel form is stirred at 500 rpm (Pv value: 4.4 kW/m ³ ), the water bath is removed, and the solution is allowed to cool in the air for about 10 to 20 minutes. A particulate solid was obtained by cooling to 30°C. Then, while stirring at 500 rpm, 3.34 g of ethyl acetate was further added (ethyl acetate/Novec7200=25/75 (wt/wt)). Particles of fluororesin (A) were obtained by suction filtration and vacuum drying under heating. The obtained particles had an average particle size of about 2 mm as measured with a ruler, and included coarse particles having a diameter of about 5 to 10 mm.

[Example 9]
0.017 g of bis(2,3,4,5,6-pentafluorobenzoyl) peroxide as a radical polymerization initiator, perfluoro(4-methyl-2-methylene-1, 3-dioxolane) and 20 g of Novec 7200 as a polymerization solvent were added, and after repeating nitrogen replacement by freeze degassing and depressurization, the flask was sealed under reduced pressure. This ampoule was placed in a constant temperature bath at 55° C. and held for 24 hours to carry out radical solution polymerization. As a result, a solution in which the fluororesin (A) was uniformly dissolved was obtained. After cooling to room temperature, the ampoule was opened, 20 g of AE-3000 was added, and the mixture was heated to 50°C while stirring with a magnetic stirrer. = 50/50 (wt/wt)).

This solution is heated to 50°C, and a separable flask with a capacity of 50 mL equipped with four diagonal paddle stirring blades (blade diameter 40 mm, blade width 8 mm, oblique 45°) heated to 50 ° C., three-one motor, and water bath. , heated to 50°C while stirring at 150 rpm, and held for 10 ^minutes . A particulate solid was obtained by cooling to 30° C. in 10-20 minutes. After that, while stirring at 500 rpm, 17.143 g of AE-3000 was further added (AE-3000/Novec7200=65/35 (wt/wt)). Particles of fluororesin (A) were obtained by suction filtration and vacuum drying under heating. The obtained particles were fine particles having a volume average particle diameter of 200 μm, and were substantially free of coarse particles.

[Example 10]
In Example 1, the fluororesin (A) solution was stirred at 500 rpm (Pv value: 4.4 kW/m ³ ), removed from the water bath, allowed to cool in the air, and cooled to 30°C in about 10 to 20 minutes. Instead of obtaining a particulate solid by ^cooling down to Cool and proceed as in Example 1 except that a particulate solid was obtained by cooling to 30° C. in about 150 minutes. The obtained particles were fine particles having a volume average particle diameter of 250 μm, and were substantially free of coarse particles.

[Comparative Example 2]
A resin solution was prepared by dissolving fluororesin A of Synthesis Example 1 in FC-72 so that the polymer concentration was 10 wt %. Hexane was added to a beaker equipped with a stirrer, and the resin was precipitated by adding the diluted resin solution to the hexane while stirring, and suction filtration was performed to obtain a solid. The obtained solid was flocculated with fibers having a length of 5 cm or longer, and was greatly wrapped around the stirrer when the resin solution was added to hexane.

ADVANTAGE OF THE INVENTION According to this invention, it is excellent in productivity and can provide the manufacturing method of the fluororesin particle containing the fluorine-containing alicyclic structure which can remove a foreign material. The resin particles obtained by the method for producing fluororesin particles containing a fluorine-containing alicyclic structure of the present invention can be applied to various applications such as the fields of optics and electronics.

Claims (10)

A fluororesin (A) containing a fluorine-containing alicyclic structure is dissolved in a solvent (B) in a fluororesin (A) solution, and the temperature of the solution is lowered to precipitate particles of the fluororesin (A). A method for producing fluororesin particles containing a fluorine-containing alicyclic structure, comprising a precipitation step of allowing the Claim 1, wherein the solvent (B) is a composition containing a good solvent (b-1) for the fluororesin (A) and a poor solvent (b-2) for the fluororesin (A). A method for producing fluororesin particles. 3. The method for producing fluororesin particles according to claim 2, wherein the good solvent (b-1) is an aliphatic fluorine-containing solvent or an aromatic fluorine-containing solvent having a hydrogen atom in the molecule. 4. The method for producing fluororesin particles according to any one of claims 2 and 3, wherein the poor solvent (b-2) is a fluorine-containing solvent having a hydrogen atom in its molecule. A poor solvent addition step of adding a poor solvent (b-2) to the fluororesin (A) solution obtained in the precipitation step, and a solid-liquid separation of the particles of the fluororesin (A) after the poor solvent addition step. 5. The method for producing fluororesin particles according to any one of claims 1 to 4, comprising the steps of: In the precipitation step, when the solution temperature T ₁ before lowering the temperature is 30° C. or higher and the solution temperature after lowering the temperature is T ₂ , T ₁ −T ₂ is 5° C. or higher. The method for producing fluororesin particles according to any one of claims 1 to 5, characterized in that 7. In the precipitation step, the temperature is lowered while stirring so that the Pv value, which is the value of the stirrer motor power per unit stirring capacity, is 0.2 to 50 kw/m ³ . A method for producing the fluororesin particles according to item 1. A solution preparation step of obtaining a fluororesin solution (A) by a method including either a method of dissolving the fluororesin (A) in a solvent or a method of using a solution in which the fluororesin (A) has undergone a polymerization reaction. 8. A method for producing fluororesin particles according to any one of 1 to 7. 9. The method for producing fluororesin particles according to any one of claims 1 to 8, further comprising a filtering step of removing foreign matters by filtering a solution in which the fluororesin (A) is dissolved in a solvent. 10. The method for producing fluororesin particles having a fluorinated alicyclic structure according to any one of claims 1 to 9, wherein the fluororesin contains a residue unit represented by the following general formula (1): .

(In the formula (1), Rf ₁ , Rf ₂ , Rf ₃ and Rf ₄ are each independently a fluorine atom or a C 1-7 etheric oxygen atom which may be linear, branched or (Rf ₁ , Rf ₂ , Rf ₃ and Rf ₄ may be linked to each other to form a ring having 4 to 8 carbon atoms.)