Patent Grant
9695263
This application is a 35 U.S.C. §371 national phase filing of International Patent Application No. PCT/JP2014/055820, filed Mar. 6, 2014, which claims priority under 35 U.S.C. §119 to Japanese Patent Application Nos. 2013-044078, filed Mar. 6, 2013 and 2013-044080, filed Mar. 6, 2013, the entire disclosure of each of which is hereby expressly incorporated by reference.
The present invention relates to a fluorine-containing oligomer, nano-silica composite particles using the same, and methods for producing both. More particularly, the present invention relates to a fluorine-containing oligomer obtained by a copolymerization reaction without using a fluorine-based peroxide initiator, and relates to nano-silica composite particles using the same, and methods for producing both.
Patent Document 1 discloses a nano-substance containing a fluorine-containing compound represented, for example, by the general formula:
Rf[CH2CH(Si(OR)3)]nRf.
Patent Document 1 also discloses a nano-composite obtained by further incorporating a specific silane coupling agent into the nano-substance. Patent Document 1 indicates that the fluorine-containing compound is produced by a method comprising reacting a corresponding olefin monomer in the presence of an organic peroxide having an Rf group (perfluoroalkyl group).
Moreover, Patent Document 2 discloses a method for obtaining polyaniline-containing nano-composite particles by oxidizing aniline in the presence of a fluoroalkyl group-containing oligomer represented by the general formula:
R1[CH2CR3(COZ)]nR2.
Patent Document 2 indicates that the fluoroalkyl group-containing oligomer is obtained by reacting a fluoroalkanoyl peroxide compound and an acrylic acid, etc.
However, perfluoroalkanoyl peroxides used in these methods are very unstable, and have the risk of decomposition or explosion; therefore, special safety measures are required. Patent Document 3 also indicates that a method using a fluorine-based peroxide is not suitable for mass production. Further, since the fluorine-containing functional groups of the fluorine-containing oligomer become bound only to both ends of the oligomer as groups derived from the perfluoroalkanoyl peroxide, which is a polymerization initiator, there are problems that it is difficult to control the fluorine group content, and that the oil-repellent performance derived from fluorine is less likely to be exhibited.
Furthermore, Patent Document 3 discloses fluorine-containing silica composite particles comprising a mixture of silica nanoparticles, a fluorine-containing surfactant represented by the general formula:
QOSO2Rft,
and a hydrolysate mixture of a functional alkoxysilane or a dehydration condensate thereof, without using a fluorine-based peroxide. Patent Document 3 indicates that the silica composite particles serve as a material that utilizes the chemical and thermal stability of silica, and the excellent water- and oil-repellency, antifouling properties, and catalytic characteristics of the fluorine compound.
However, the fluorine compound used in Patent Document 3 is a surfactant containing a sulfone group SO2, and is produced by electrolytic fluorination method. In the electrolytic fluorination method, a large amount of anhydrous hydrogen fluoride is used in the reaction, which thus requires sufficient safety measures. Other problems are that this method is not suitable for mass production in terms of the characteristics of the reaction, and that the resulting fluorine compounds are very expensive.
Patent Document 1: JP-A-2010-138156
Patent Document 2: JP-A-2011-190291
Patent Document 3: JP-A-2010-209280
Patent Document 4: WO 2009/034773 A1
An object of the present invention is to provide a fluorine-containing oligomer obtained by a copolymerization reaction without using a fluorine-based peroxide initiator, and to provide nano-silica composite particles using the same, and methods for producing both.
The present invention provides a fluorine-containing oligomer comprising a copolymer of a fluoroalkyl alcohol (meth)acrylic acid derivative represented by the general formula:
CnF2n+1(CH2)dOCOCR═CH2 [I]
wherein R is a hydrogen atom or a methyl group, n is an integer of 1 to 10, and d is an integer of 1 to 6; and a (meth)acrylic acid derivative represented by the general formula:
(CH2═CRCO)mR′ [II]
wherein R is a hydrogen atom or a methyl group, m is 1, 2, or 3; and when m is 1, R′ is an —OH group, an NH2 group that is unsubstituted or mono- or di-substituted with an alkyl group having 1 to 6 carbon atoms, or a monovalent group derived from an alkylene glycol or polyalkylene glycol group containing an alkylene group having 2 or 3 carbon atoms; when m is 2 or 3, R′ is a divalent or trivalent organic group derived from a diol or triol.
The fluorine-containing oligomer is produced by copolymerizing the above fluoroalkyl alcohol (meth)acrylic acid derivative [I] and (meth)acrylic acid derivative [II] in the presence of a hydrocarbon-based organic peroxide or azo compound polymerization initiator.
The term (meth)acrylic acid used herein refers to acrylic acid or methacrylic acid.
Further, the present invention provides nano-silica composite particles formed as a condensate of the above fluorine-containing oligomer and an alkoxysilane with nano-silica particles.
The nano-silica composite particles are produced by reacting the above fluorine-containing oligomer and an alkoxysilane in the presence of nano-silica particles using an alkaline or acidic catalyst.
The fluorine-containing oligomer according to the present invention can be produced without using a fluorine-based peroxide initiator, and can be effectively used in the production of nano-silica composite particles, etc. Moreover, the use of a fluorine-containing monomer having a polymerizable functional group as a monomer has the advantage of easily controlling the fluorine content of the fluorine-containing oligomer and the fluorine content of the nano-silica composite particles.
Furthermore, fluorine-containing nano-silica composite particles produced by using the fluorine-containing oligomer have effects in not only that the average particle diameter and its variation range are small, but also that the particles are excellent in terms of heat-resistant weight loss.
The fluorine-containing oligomer is produced by copolymerizing a fluoroalkyl alcohol (meth)acrylic acid derivative represented by the general formula:
CnF2n+1(CH2)dOCOCR═CH2 [I]
The fluoroalkyl alcohol (meth)acrylic acid derivative [I] is described, for example, in Patent Document 4, and is synthesized through the following series of steps.
First, a fluoroalkyl iodide represented by the general formula:
CnF2n+1(CF2CF2)b(CH2CH2)cI
CF3(CH2CH2)I
C2F5(CH2CH2)I
C2F5(CH2CH2)2I
C3F7(CH2CH2)I
C3F7(CH2CH2)2I
C4F9(CH2CH2)I
C4F9(CH2CH2)2I
C2F5(CF2CF2)(CH2CH2)I
C2F5(CF2CF2)(CH2CH2)2I
C2F5(CF2CF2)2(CH2CH2)I
C2F5(CF2CF2)2(CH2CH2)2I
C2F5(CF2CF2)3(CH2CH2)I
C4F9(CF2CF2)(CH2CH2)I
C4F9(CF2CF2)2(CH2CH2)I
C4F9(CF2CF2)(CH2CH2)2I
C4F9(CF2CF2)2(CH2CH2)2I
C4F9(CF2CF2)3(CH2CH2)I
The (meth)acrylic acid derivative of the formula: (CH2═CRCO)mR′ [II], which is to be copolymerized with the fluoroalkyl alcohol (meth)acrylic acid derivative [I], is, when m is 1, a compound represented by the general formula:
CH2═CRCOOH
CH2═CRCONR1R2
The copolymerization reaction of both derivatives is performed by a solution-polymerization method in an organic solvent, such as methanol, ethanol, isopropanol, acetone, methyl ethyl ketone, tetrahydrofuran, ethyl acetate, chloroform, 1,2-dichloroethane, or AK-225, which is described later, in the presence of a hydrocarbon-based peroxide or azo compound polymerization initiator, such as tertiary-butyl peroxide, diisopropylbenzene hydroperoxide, cumene hydroperoxide, 2,2′-azobis(2,4-dimethylvaleronitrile), or azobis(isobutyronitrile). Such a polymerization initiator is used at a ratio of about 0.1 to 50 wt. %, preferably about 5 to 20 wt. %, based on the weight of the monomer mixture.
The amount of copolymerized fluorine-containing monomer [I] in the obtained fluorine-containing oligomer is about 0.1 to 50 mol %, preferably about 1 to 20 mol %. The oligomer has a number average molecular weight Mn of about 5,000 or less, preferably about 100 to 3,000, and has a particle diameter of 200 nm or less. The dispersibility of fluorine-containing oligomer white powder when dispersed in various solvents is also excellent, except in hydrocarbon solvents.
The thus-obtained fluorine-containing oligomer is reacted with an alkoxysilane in the presence of nano-silica particles using an alkaline or acidic catalyst, thereby forming nano-silica composite particles.
As the nano-silica particles, organosilica sol having an average particle diameter (measured by a dynamic light scattering method) of 5 to 200 nm, preferably 10 to 100 nm, and having a primary particle diameter of 40 nm or less, preferably 5 to 30 nm, even more preferably 10 to 20 nm, is used. Practically used are commercial products of Nissan Chemical Industries, Ltd., such as Methanol Silica Sol, Snowtex IPA-ST (isopropyl alcohol dispersion), Snowtex EG-ST (ethylene glycol dispersion), Snowtex MEK-ST (methyl ethyl ketone dispersion), and Snowtex MIBK-ST (methyl isobutyl ketone dispersion).
Examples of the alkoxysilane include alkoxysilanes represented by the general formula:
(R1O)pSi(OR2)q(R3)r [III]
The proportion of these components are such that about 10 to 100 parts by weight, preferably about 20 to 80 parts by weight, of fluorine-containing oligomer, and about 0.1 to 100 parts by weight, preferably about 20 to 80 parts by weight, of alkoxysilane are used based on 100 parts by weight of nano-silica particles. When the amount of fluorine-containing oligomer used is less than this range, the water- and oil-repellency decreases. In contrast, when the amount of fluorine-containing oligomer used is greater than this range, dispersibility in solvents decreases.
The reaction between these components is performed in the presence of a catalytic amount of an alkaline or acidic catalyst, such as aqueous ammonia, an aqueous solution of a hydroxide of an alkali metal or alkaline earth metal (e.g., sodium hydroxide, potassium hydroxide, or calcium hydroxide), or hydrochloric acid, or sulfuric acid, at a temperature of about 0 to 100° C., preferably about 10 to 50° C., for about 0.5 to 48 hours, preferably about 1 to 10 hours.
In the nano-silica composite particles obtained from the reaction, it is considered that the fluorine-containing oligomer becomes bound to a hydroxyl group present on the surface of the nano-silica particles via a siloxane bond, or that the fluorine-containing oligomer is included in a shell having a siloxane skeleton. Therefore, the chemical and thermal stability of silica, and the excellent water- and oil-repellency, antifouling properties, etc., of the fluorine-containing oligomer are effectively exhibited. In fact, the nano-silica composite particles have the effect of reducing weight loss at 800° C. Moreover, the particle size of the nano-silica composite particles and the variation of the particle size also show small values. The nano-silica composite particles are thus formed by a condensation reaction of a fluorine-containing oligomer and a silane derivative with nano-silica particles; however, mixing of other components is allowed, as long as the object of the present invention is not impaired.
The following describes the present invention with reference to Examples.
In 50 ml of isopropanol,
The reaction mixture was supplied in n-hexane, and the generated fluorine-containing oligomer was separated by filtration, thereby obtaining 30 g (yield: 90.0%) of white powder fluorine-containing oligomer. When the molecular weight of the fluorine-containing oligomer was measured by GPC, the number average molecular weight Mn was 801, and Mn/Mw, which indicates molecular weight distribution, was 1.74. Further, when the copolymerization ratio of the obtained fluorine-containing oligomer was measured by 1H-NMR, FAAC-4:DMAA was 2:98 (mol %).
In Example 1, the types and amounts (unit: g) of the fluorine-containing monomer [I] and its comonomer [II], and the amount (unit: g) of the polymerization initiator (V-65) were changed in various ways. The results shown in Table 1 (Examples) and Table 2 (Reference Examples) below were obtained. Table 1 also shows the results of Example 1. The Mn of fluorine-containing oligomers in which PDE 100 is copolymerized cannot be measured because they are insoluble in the GPS mobile phase.
(Fluorine-Containing Monomers)
(Comonomers)
Tables 1 and 2 also show the particle diameter (unit: nm) of the produced fluorine-containing oligomer white powders measured by a dynamic light scattering method, the particle diameter distribution, and the dispersibility of the powders. The dispersibility was visually observed when 1 wt. % of each powder was dispersed in various solvents, and evaluated according to the following evaluation criteria. Regarding the solvent dispersibility, dispersibility in water, methanol, ethanol, isopropanol, and dimethylsulfoxide is ◯, while dispersibility in toluene and n-hexane is x; therefore, their descriptions are omitted.
◯: Uniformly dispersed, and transparent dispersion
Δ: Slightly dispersed, and cloudy dispersion
x: Not dispersed, but precipitated in dispersion medium
To 0.25 g of the fluorine-containing oligomer (FAAC-8-DMAA copolymer) obtained in Example 3, 1.67 g (0.50 g as nano-silica) of silica sol (Methanol Silica Sol, a product of Nissan Chemical Industries, Ltd.; nano-silica content: 30 wt. %, average particle diameter: 11 nm) and 20 ml of methanol were added. Further, 0.25 ml of tetraethoxysilane (a product of Tokyo Chemical Industry Co., Ltd.; density: 0.93 g/ml) and 0.25 ml of 25 wt. % aqueous ammonium were added under stirring conditions, and the mixture was reacted for 5 hours.
The methanol and aqueous ammonium were removed from the reaction mixture, which was a white solution, using an evaporator, and the taken white powder was redispersed in 10 ml of methanol overnight. After centrifugation, the resultant was rinsed with methanol, and the obtained powder was dried in an oven at 70° C., and then vacuum dried at 50° C. As a result, 0.507 g (yield: 62%) of white powder, which was nano-silica composite particles, was obtained.
The particle diameter of the obtained white powder was measured by a dynamic light scattering (DLS) method in a state where 1 g of white powder was dispersed in 1 L of methanol. In addition, the weight loss of the powder was measured in the following manner. That is, the rate of weight loss (percentage of reduced weight to initial weight) when the powder was heated to 800° C. at a heating rate of 10° C./min was measured using TGA (TG-DTA2000SA, produced by Bruker AXS).
In Example 11, the same amount (0.25 g) of the fluorine-containing oligomer (FAAC-8-ACA copolymer oligomer) obtained in Example 5 was used as the fluorine-containing oligomer.
In Example 11, the same amount (0.25 g) of the fluorine-containing oligomer (DTFAC-DMAA copolymer oligomer) obtained in Reference Example 1 was used as the fluorine-containing oligomer.
In Example 11, the same amount (0.25 g) of the fluorine-containing oligomer (DTFAC-ACA copolymer oligomer) obtained in Reference Example 3 was used as the fluorine-containing oligomer.
In Example 11, the same amount (0.25 g) of the fluorine-containing oligomer (DTFMAC-ACA copolymer oligomer) obtained in Reference Example 4 was used as the fluorine-containing oligomer.
Table 3 below shows the measurement results obtained in Examples 11 and 12, and Reference Examples 11 to 13, together with the generation amount and yield of nano-silica composite particles.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2013-044078 | Mar 2013 | JP | national |
| 2013-044080 | Mar 2013 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2014/055820 | 3/6/2014 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2014/136895 | 9/12/2014 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 20040114248 | Hokazono | Jun 2004 | A1 |
| 20090148653 | Brown et al. | Jun 2009 | A1 |
| 20090149096 | Brown et al. | Jun 2009 | A1 |
| 20110009555 | Kurihara et al. | Jan 2011 | A1 |
| Number | Date | Country |
|---|---|---|
| 0 351 364 | Jun 1989 | EP |
| 2-70713 | Mar 1990 | JP |
| 2007-23180 | Feb 2007 | JP |
| 2008-297482 | Dec 2008 | JP |
| 2009-102570 | May 2009 | JP |
| 2010-138156 | Jun 2010 | JP |
| 2010-209280 | Sep 2010 | JP |
| 2011 039363 | Feb 2011 | JP |
| 2011-039363 | Feb 2011 | JP |
| 2011-506640 | Mar 2011 | JP |
| 2011-190291 | Sep 2011 | JP |
| 2012-214759 | Nov 2012 | JP |
| 2013-014125 | Jan 2013 | JP |
| 10-2009-0051068 | May 2009 | KR |
| WO 2008021153 | Feb 2008 | WO |
| WO 2009034773 | Mar 2009 | WO |
| WO 2012133622 | Oct 2012 | WO |
| Entry |
|---|
| JP 2011 039363 Machine translation (2011). |
| International Preliminary Report on Patentability and Written Opinion from corresponding PCT application No. PCT/JP2014/055820 filed Sep. 17, 2015 (7 pgs). |
| International Search Report from corresponding PCT application No. PCT/JP2014/055820 filed Jun. 10, 2014 (3 pgs). |
| Number | Date | Country | |
|---|---|---|---|
| 20160017072 A1 | Jan 2016 | US |
