JPWO2013027771A1 - Method for producing vinylidene fluoride polymer - Google Patents
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Abstract
本発明は、フッ化ビニリデン系重合体を懸濁重合により製造する際に発生する、排水中の浮遊物質の量を従来の製法よりも減少させることが可能な製造方法を提供することを目的とする。本発明のフッ化ビニリデン系重合体の製造方法は、少なくともフッ化ビニリデンを含むモノマーを、重合開始剤存在下で懸濁重合する製法において、一般式Ｒ1‐Ｏ‐Ｒ2（Ｒ1、Ｒ2はアルキル基または、フッ化アルキル基であり、Ｒ1、Ｒ2の少なくとも片方がフッ化アルキル基）で表わされる分子量が１００〜８００であるハイドロフルオロエーテルおよび環状ハイドロフルオロカーボンから選択される少なくとも１種のフッ素系化合物存在下で懸濁重合を行うこと、前記フッ素系化合物を、重合開始剤１００質量％に対して１０〜１０００質量％用いること、前記重合開始剤を、懸濁重合に使用する全モノマー１００質量部に対して０．０１〜５質量部用いることを特徴とする。An object of the present invention is to provide a production method capable of reducing the amount of suspended solids in waste water generated when producing a vinylidene fluoride polymer by suspension polymerization, as compared with a conventional production method. To do. The method for producing a vinylidene fluoride polymer according to the present invention is a method in which a monomer containing at least vinylidene fluoride is subjected to suspension polymerization in the presence of a polymerization initiator, wherein R 1 —O—R 2 (R 1 and R 2 are alkyl groups) Or the presence of at least one fluorine-based compound selected from hydrofluoroethers and cyclic hydrofluorocarbons having a molecular weight of 100 to 800 represented by a fluorinated alkyl group and at least one of R 1 and R 2 is a fluorinated alkyl group) Suspension polymerization is performed, the fluorine compound is used in an amount of 10 to 1000% by mass with respect to 100% by mass of the polymerization initiator, and the polymerization initiator is added to 100 parts by mass of all monomers used for the suspension polymerization. In contrast, 0.01 to 5 parts by mass is used.
Description
本発明はフッ化ビニリデン系重合体の製造方法に関する。 The present invention relates to a method for producing a vinylidene fluoride polymer.
フッ化ビニリデン系重合体は様々な重合法により合成することができるが、工業的生産では、乳化重合法や懸濁重合法により合成されている。乳化重合法では、０．２〜０．５μｍ程度の小粒径のラテックスが生成するため、重合後、凝集剤を用いた造粒処理が施されているが、乳化剤や凝集剤等を十分に除去する為には複雑な後処理が必要となる。一方、懸濁重合法では５０〜３００μｍ程度の粒径のビーズが生成し、簡易な洗浄処理で不純物の少ない重合体が得られる。 A vinylidene fluoride polymer can be synthesized by various polymerization methods, but in industrial production, it is synthesized by an emulsion polymerization method or a suspension polymerization method. In the emulsion polymerization method, a latex having a small particle size of about 0.2 to 0.5 μm is formed. Therefore, after polymerization, granulation treatment using a flocculant is performed. In order to remove, complicated post-processing is required. On the other hand, in the suspension polymerization method, beads having a particle size of about 50 to 300 μm are generated, and a polymer with few impurities is obtained by a simple washing treatment.
しかし、懸濁重合においては、重合反応中に水相に微粉が発生し、排水中の浮遊物質量が高くなりやすい。浮遊物質量が高くなれば環境負荷も大きくなる為、排水から浮遊物質を除去する為の排水処理設備（浮上分離など）が必要となる。一般に、浮遊物質の増大を防ぐ手段としては、重合禁止剤の添加や攪拌条件の最適化がなされるが、効果が不充分な場合や、重合反応の遅延、製品色調の変化が発生する問題があった。 However, in suspension polymerization, fine powder is generated in the aqueous phase during the polymerization reaction, and the amount of suspended solids in the wastewater tends to be high. If the amount of suspended solids increases, the environmental load increases, and wastewater treatment facilities (such as floating separation) are required to remove suspended solids from the wastewater. In general, as a means of preventing the increase of suspended solids, the addition of a polymerization inhibitor and the optimization of stirring conditions are made, but there are problems in that the effect is insufficient, the polymerization reaction is delayed, and the product color changes. there were.
浮遊物質の生成については様々な原因が考えられるが、重合開始剤と懸濁剤の反応や、正常に形成されたモノマー懸濁粒子の外で重合開始剤とモノマーが反応した場合等に形成されると考えられる。 There are various possible causes for the generation of suspended solids, but they are formed when the polymerization initiator reacts with the suspending agent or when the polymerization initiator reacts with the monomer outside the normally formed monomer suspension particles. It is thought.
ところで、懸濁重合は通常重合開始剤存在下で行われるが、重合開始剤の重合系内での分散性や混和性の向上、ハンドリングの向上、輸送・保管時の安全性の向上等の見地から、重合開始剤を適当な溶媒と併用若しくは溶解して用いられる事が一般的であるが、フッ化ビニリデンの重合においては成長ラジカルの強い水素引き抜き作用のため、使用溶媒が限定され、連鎖移動や副反応を抑制する為にフッ素系溶媒がしばしば用いられてきた。 By the way, suspension polymerization is usually carried out in the presence of a polymerization initiator. From the standpoint of improving the dispersibility and miscibility of the polymerization initiator in the polymerization system, improving handling, and improving safety during transportation and storage. In general, a polymerization initiator is used in combination with or dissolved in a suitable solvent. However, in the polymerization of vinylidene fluoride, the solvent used is limited due to the strong hydrogen abstraction action of the growing radical, and chain transfer is limited. Fluorine-based solvents have often been used to suppress side reactions.
フッ化ビニリデン系重合体の懸濁重合においては、例えば水性媒体１００質量部に対して、モノヒドロペンタフルオロジクロロプロパン等の特定のハロゲン化炭化水素溶剤を１０〜５０質量部用いる方法が提案されている（例えば、特許文献１参照）。該方法は、熱安定性に優れたフッ化ビニリデン系重合体を製造することを目的としており、懸濁重合における排水中の浮遊物質量については検討されていない。 In suspension polymerization of a vinylidene fluoride polymer, for example, a method using 10 to 50 parts by mass of a specific halogenated hydrocarbon solvent such as monohydropentafluorodichloropropane is proposed with respect to 100 parts by mass of an aqueous medium. (For example, refer to Patent Document 1). This method is intended to produce a vinylidene fluoride polymer excellent in thermal stability, and the amount of suspended solids in waste water in suspension polymerization has not been studied.
ところで、重合媒体として特定のヒドロフルオロアルキルエーテルを用い、フッ素モノマーを重合することにより含フッ素重合体を製造する方法が提案されている（例えば、特許文献２、３参照）。該フッ素重合体の製造方法は、オゾン層破壊の原因物質であるクロロフルオロカーボンを代替することを目的としており、オゾン層破壊係数が小さく、重合速度が大きい重合媒体を用いることを特徴としている。該フッ素重合体の製造方法は、重合媒体として特定のヒドロフルオロアルキルエーテルを用いるため、その使用量が多量であり、フッ素重合体の製造コストの増加、フッ素重合体中に該ヒドロフルオロアルキルエーテルが残留するとの問題があった。 By the way, a method for producing a fluoropolymer by polymerizing a fluorine monomer using a specific hydrofluoroalkyl ether as a polymerization medium has been proposed (for example, see Patent Documents 2 and 3). The production method of the fluoropolymer is intended to replace chlorofluorocarbon which is a causative substance of ozone layer destruction, and is characterized by using a polymerization medium having a low ozone layer destruction coefficient and a high polymerization rate. Since the method for producing the fluoropolymer uses a specific hydrofluoroalkyl ether as a polymerization medium, the amount used thereof is large, increasing the production cost of the fluoropolymer, and the hydrofluoroalkyl ether is contained in the fluoropolymer. There was a problem of remaining.
また、特定のハイドロフルオロエーテルと水とを含む重合媒質中で、フッ素化モノマーを重合させてフルオロポリマーを得る方法が提案されている（例えば、特許文献４参照）。特許文献４には、該ハイドロフルオロエーテルは、地球温暖化およびオゾン層破壊の可能性が小さいこと、容易に入手できることが開示されている。該フルオロポリマーの製造方法は、ハイドロフルオロエーテルとして、比較的炭素数の大きなフッ素化アルキル基を有するものを用いていた。該フルオロポリマーの製造方法では、未だ重合開始剤の分散性・混和性が劣っており、改善が望まれていた。 Further, a method has been proposed in which a fluoropolymer is obtained by polymerizing a fluorinated monomer in a polymerization medium containing a specific hydrofluoroether and water (see, for example, Patent Document 4). Patent Document 4 discloses that the hydrofluoroether has a low possibility of global warming and ozone layer destruction and can be easily obtained. In the production method of the fluoropolymer, a hydrofluoroether having a fluorinated alkyl group having a relatively large carbon number is used. In the method for producing the fluoropolymer, the dispersibility and miscibility of the polymerization initiator is still inferior, and improvement has been desired.
本発明は、上記従来技術の有する課題を鑑みてされたものであり、フッ化ビニリデン系重合体を懸濁重合により製造する際に発生する、排水中の浮遊物質の量を従来の製法よりも減少させることが可能なフッ化ビニリデン系重合体の製造方法を提供することを目的とする。本発明のフッ化ビニリデン系重合体の製造方法は、浮遊物質量を低減することが可能であるため、廃水処理コストの低減および生産性の向上が可能である。 The present invention has been made in view of the above-described problems of the prior art, and the amount of suspended solids in waste water generated when a vinylidene fluoride polymer is produced by suspension polymerization is more than the conventional production method. It is an object of the present invention to provide a method for producing a vinylidene fluoride polymer that can be reduced. Since the method for producing a vinylidene fluoride polymer of the present invention can reduce the amount of suspended solids, it is possible to reduce wastewater treatment costs and improve productivity.
本発明者らは上記課題を達成するために鋭意研究を重ねた結果、特定のフッ素系化合物が特定量存在する条件で懸濁重合を行うことにより、排水中の浮遊物質の量を低減することが可能であることを見出し、本発明を完成させた。 As a result of intensive studies to achieve the above-mentioned problems, the present inventors reduced the amount of suspended solids in wastewater by performing suspension polymerization under the condition that a specific amount of a specific fluorine compound exists. The present invention has been completed.
すなわち、本発明のフッ化ビニリデン系重合体の製造方法は、少なくともフッ化ビニリデンを含むモノマーを、重合開始剤存在下で懸濁重合するフッ化ビニリデン系重合体の製造方法において、一般式Ｒ1‐Ｏ‐Ｒ2（ここでＲ1およびＲ2はそれぞれ独立に、アルキル基または、アルキル基の水素原子の一部もしくは全部がフッ素化されたフッ化アルキル基であり、Ｒ1およびＲ2の少なくとも片方が前記フッ化アルキル基である）で表わされる分子量が１００〜８００であるハイドロフルオロエーテルおよび環状ハイドロフルオロカーボンから選択される少なくとも１種のフッ素系化合物存在下で懸濁重合を行うこと、前記フッ素系化合物を、前記重合開始剤１００質量％に対して１０〜１０００質量％用いること、前記重合開始剤を、懸濁重合に使用する全モノマー１００質量部に対して０．０１〜５質量部用いることを特徴とする。That is, the method of manufacture of vinylidene fluoride polymers present invention, a monomer containing at least vinylidene fluoride, in the manufacturing method of the vinylidene fluoride polymer to suspension polymerization in the presence of a polymerization initiator of the general formula R 1 the -O-R 2 (wherein R 1 and R 2 are each independently an alkyl group, or a part or all of the hydrogen atoms of the alkyl group are fluorinated fluoroalkyl group, R 1 and R 2 Carrying out suspension polymerization in the presence of at least one fluorine-based compound selected from hydrofluoroethers having a molecular weight of 100 to 800 and cyclic hydrofluorocarbons, at least one of which is the fluorinated alkyl group, The fluorine-based compound is used in an amount of 10 to 1000% by mass with respect to 100% by mass of the polymerization initiator, and the polymerization initiator is suspended. Which comprises using 0.01 to 5 parts by weight with respect to total monomer 100 parts by weight used in the polymerization.
前記アルキル基が、炭素数１〜２のアルキル基であり、前記フッ化アルキル基が炭素数１〜４のフッ化アルキル基であることが好ましい。
前記フッ素系化合物が、ＣＦ3ＣＨ2ＯＣＦ2ＣＨＦ2、ＣＨＦ2ＣＦ2ＣＨ2ＯＣＦ2ＣＨＦ2、ＣＦ3ＣＦ2ＣＨ2ＯＣＦ2ＣＨＦ2から選択される少なくとも１種のフッ素系化合物であることが好ましく、ＣＦ3ＣＨ2ＯＣＦ2ＣＨＦ2であることがより好ましい。The alkyl group is preferably an alkyl group having 1 to 2 carbon atoms, and the fluorinated alkyl group is preferably a fluorinated alkyl group having 1 to 4 carbon atoms.
The fluorine compound is at least one fluorine compound selected from CF 3 CH 2 OCF 2 CHF 2 , CHF 2 CF 2 CH 2 OCF 2 CHF 2 , and CF 3 CF 2 CH 2 OCF 2 CHF 2. Is preferable, and CF 3 CH 2 OCF 2 CHF 2 is more preferable.
前記重合開始剤が、前記フッ素系化合物に溶解した状態で懸濁重合が行われることが好ましい。
前記重合開始剤を、重合系外で前記フッ素系化合物に溶解させ、得られた溶液を重合系内に添加することが好ましい。It is preferable that suspension polymerization is performed in a state where the polymerization initiator is dissolved in the fluorine-based compound.
It is preferable to dissolve the polymerization initiator in the fluorine compound outside the polymerization system, and add the resulting solution into the polymerization system.
本発明のフッ化ビニリデン系重合体の製造方法は、フッ化ビニリデン系重合体を懸濁重合により製造する際に発生する、排水中の浮遊物質の量を従来の製法よりも減少させることが可能である。このため本発明のフッ化ビニリデン系重合体の製造方法は、廃水処理コストの低減および生産性の向上が可能である。 The method for producing a vinylidene fluoride polymer according to the present invention can reduce the amount of suspended solids in waste water generated when a vinylidene fluoride polymer is produced by suspension polymerization, compared to the conventional production method. It is. For this reason, the manufacturing method of the vinylidene fluoride polymer of the present invention can reduce wastewater treatment costs and improve productivity.
次に本発明について具体的に説明する。
本発明のフッ化ビニリデン系重合体の製造方法は、少なくともフッ化ビニリデンを含むモノマーを、重合開始剤存在下で懸濁重合するフッ化ビニリデン系重合体の製造方法において、一般式Ｒ1‐Ｏ‐Ｒ2（ここでＲ1およびＲ2はそれぞれ独立に、アルキル基または、アルキル基の水素原子の一部もしくは全部がフッ素化されたフッ化アルキル基であり、Ｒ1およびＲ2の少なくとも片方が前記フッ化アルキル基である）で表わされる分子量が１００〜８００であるハイドロフルオロエーテルおよび環状ハイドロフルオロカーボンから選択される少なくとも１種のフッ素系化合物存在下で懸濁重合を行うこと、前記フッ素系化合物を、前記重合開始剤１００質量％に対して１０〜１０００質量％用いること、前記重合開始剤を、懸濁重合に使用する全モノマー１００質量部に対して０．０１〜５質量部用いることを特徴とする。Next, the present invention will be specifically described.
The method of manufacturing a vinylidene fluoride polymer present invention, a monomer containing at least vinylidene fluoride, in the manufacturing method of the vinylidene fluoride polymer to suspension polymerization in the presence of a polymerization initiator of the general formula R 1 -O -R 2 (wherein R 1 and R 2 are each independently an alkyl group or a fluorinated alkyl group in which part or all of the hydrogen atoms of the alkyl group are fluorinated, and at least one of R 1 and R 2 Is a fluorinated alkyl group), and suspension polymerization is carried out in the presence of at least one fluorine-based compound selected from hydrofluoroethers having a molecular weight of 100 to 800 and cyclic hydrofluorocarbons; The compound is used in an amount of 10 to 1000% by mass based on 100% by mass of the polymerization initiator, and the polymerization initiator is used for suspension polymerization. Which comprises using 0.01 to 5 parts by weight with respect to total monomers 100 parts by mass.
なお、本明細書では、一般式Ｒ1‐Ｏ‐Ｒ2（ここでＲ1およびＲ2はそれぞれ独立に、アルキル基または、アルキル基の水素原子の一部もしくは全部がフッ素化されたフッ化アルキル基であり、Ｒ1およびＲ2の少なくとも片方が前記フッ化アルキル基である）で表わされる分子量が１００〜８００であるハイドロフルオロエーテルおよび環状ハイドロフルオロカーボンから選択される少なくとも１種のフッ素系化合物を、特定のフッ素系化合物とも記す。In this specification, the general formula R 1 —O—R 2 (wherein R 1 and R 2 are each independently an alkyl group or a fluorinated fluorinated part or all of the hydrogen atoms of the alkyl group). At least one fluorine-based compound selected from hydrofluoroethers and cyclic hydrofluorocarbons having a molecular weight of 100 to 800, which is an alkyl group and at least one of R 1 and R 2 is the fluorinated alkyl group) Is also referred to as a specific fluorine-based compound.
〔少なくともフッ化ビニリデンを含むモノマー〕
本発明のフッ化ビニリデン系重合体の製造方法では、少なくともフッ化ビニリデンを含むモノマーを原料として用いる。[Monomer containing at least vinylidene fluoride]
In the method for producing a vinylidene fluoride polymer of the present invention, a monomer containing at least vinylidene fluoride is used as a raw material.
なお、本発明のフッ化ビニリデン系重合体の製造方法では、モノマーとして少なくともフッ化ビニリデンを用い、他のモノマーを合わせて用いてもよい。
本発明のフッ化ビニリデン系重合体の製造方法では、全モノマー（フッ化ビニリデンおよび他のモノマー）の合計１００モル％あたりフッ化ビニリデンが、通常は５０モル％以上であり、好ましくは８０モル％以上であり、より好ましくは８５モル％以上である。また、フッ化ビニリデン系重合体として、フッ化ビニリデン単独重合体を得る場合にはモノマーが全てフッ化ビニリデンである。In the method for producing a vinylidene fluoride polymer of the present invention, at least vinylidene fluoride may be used as a monomer, and other monomers may be used in combination.
In the method for producing a vinylidene fluoride polymer of the present invention, vinylidene fluoride is usually 50 mol% or more, preferably 80 mol% per 100 mol% of all monomers (vinylidene fluoride and other monomers) in total. It is above, More preferably, it is 85 mol% or more. Further, when a vinylidene fluoride homopolymer is obtained as the vinylidene fluoride polymer, all the monomers are vinylidene fluoride.
本発明のフッ化ビニリデン系重合体の製造方法では前述のように、フッ化ビニリデン以外のモノマー（他のモノマー）を用いてもよい。本発明のフッ化ビニリデン系重合体の製造方法では、全モノマーの合計１００モル％あたり他のモノマーが、通常は５０モル％以下であり、好ましくは２０モル％以下であり、より好ましくは１５モル％以下である。 In the method for producing a vinylidene fluoride polymer of the present invention, as described above, a monomer other than vinylidene fluoride (another monomer) may be used. In the method for producing a vinylidene fluoride polymer of the present invention, the other monomer is usually 50 mol% or less, preferably 20 mol% or less, more preferably 15 mol per 100 mol% in total of all monomers. % Or less.
前記他のモノマーとしては、例えばフッ化ビニリデンと共重合可能なフッ素系単量体あるいはエチレン、プロピレン等の炭化水素系単量体、カルボキシル基含有モノマー、カルボン酸無水物基含有モノマーが挙げられる。なお、他のモノマーは、一種単独でも、二種以上でもよい。 Examples of the other monomers include fluorine monomers copolymerizable with vinylidene fluoride, hydrocarbon monomers such as ethylene and propylene, carboxyl group-containing monomers, and carboxylic anhydride group-containing monomers. The other monomers may be used alone or in combination of two or more.
前記フッ化ビニリデンと共重合可能なフッ素系単量体としては、フッ化ビニル、トリフルオロエチレン、テトラフルオロエチレン、クロロトリフルオロエチレン、ヘキサフルオロプロピレン、ペルフルオロメチルビニルエーテルに代表されるペルフルオロアルキルビニルエーテル等を挙げることができる。 Examples of the fluorine-based monomer copolymerizable with vinylidene fluoride include vinyl fluoride, trifluoroethylene, tetrafluoroethylene, chlorotrifluoroethylene, hexafluoropropylene, and perfluoroalkyl vinyl ethers typified by perfluoromethyl vinyl ether. Can be mentioned.
前記カルボキシル基含有モノマーとしては、不飽和一塩基酸、不飽和二塩基酸、不飽和二塩基酸のモノエステル等が好ましい。
前記不飽和一塩基酸としては、アクリル酸、メタクリル酸、２−カルボキシエチルアクリレート、２−カルボキシエチルメタクリレート等が挙げられる。前記不飽和二塩基酸としては、マレイン酸、シトラコン酸等が挙げられる。また、前記不飽和二塩基酸のモノエステルとしては、炭素数５〜８のものが好ましく、例えばマレイン酸モノメチルエステル、マレイン酸モノエチルエステル、シトラコン酸モノメチルエステル、シトラコン酸モノエチルエステル等を挙げることができる。中でも、カルボキシル基含有モノマーとしては、アクリル酸、メタクリル酸、マレイン酸、シトラコン酸、マレイン酸モノメチルエステル、シトラコン酸モノメチルエステルが好ましい。また、カルボキシル基含有モノマーとしてはアクリロイロキシエチルコハク酸、メタクリロイロキシエチルコハク酸、アクリロイロキシエチルフタル酸、メタクリロイロキシエチルフタル酸等を用いてもよい。
前記カルボン酸無水物基含有モノマーとしては、前記不飽和二塩基酸の酸無水物、具体的には、無水マレイン酸、無水シトラコン酸が挙げられる。As the carboxyl group-containing monomer, unsaturated monobasic acid, unsaturated dibasic acid, monoester of unsaturated dibasic acid and the like are preferable.
Examples of the unsaturated monobasic acid include acrylic acid, methacrylic acid, 2-carboxyethyl acrylate, 2-carboxyethyl methacrylate and the like. Examples of the unsaturated dibasic acid include maleic acid and citraconic acid. The unsaturated dibasic acid monoester preferably has 5 to 8 carbon atoms, and examples thereof include maleic acid monomethyl ester, maleic acid monoethyl ester, citraconic acid monomethyl ester, and citraconic acid monoethyl ester. Can do. Among these, acrylic acid, methacrylic acid, maleic acid, citraconic acid, maleic acid monomethyl ester, and citraconic acid monomethyl ester are preferable as the carboxyl group-containing monomer. As the carboxyl group-containing monomer, acryloyloxyethyl succinic acid, methacryloyloxyethyl succinic acid, acryloyloxyethyl phthalic acid, methacryloyloxyethyl phthalic acid, or the like may be used.
Examples of the carboxylic acid anhydride group-containing monomer include acid anhydrides of the unsaturated dibasic acid, specifically maleic anhydride and citraconic anhydride.
〔重合開始剤〕
本発明のフッ化ビニリデン系重合体の製造方法では、重合開始剤存在下で前記モノマーの懸濁重合を行う。(Polymerization initiator)
In the method for producing a vinylidene fluoride polymer according to the present invention, the monomer is subjected to suspension polymerization in the presence of a polymerization initiator.
重合開始剤としては、１０時間半減期温度が３０〜９０℃のものが好ましく用いられ、その好ましい例としてはジイソプロピルパーオキシジカーボネート、ジノルマルプロピルパーオキシジカーボネート、ｔ‐ブチルパーオキシピバレートが挙げられ、重合開始剤と特定のフッ素系化合物との親和性の観点からジイソプロピルパーオキシジカーボネートおよびジノルマルプロピルパーオキシジカーボネートがより好ましく、ジイソプロピルパーオキシジカーボネートが最も好ましい。重合開始剤の使用量は、懸濁重合に使用する全モノマーを１００質量部とすると、０．０１〜５質量部、好ましくは０．０５〜２質量部、特に好ましくは０．１〜１．５質量部の範囲で用いられる。重合開始剤の使用量が０．０１質量部より小さいと重合時間が極端に長くなってしまう。重合開始剤の使用量が５質量部より大きくなると、製品が黄褐色に着色したり、浮遊物質量が増大する。この為、前記範囲で重合開始剤を使用することが好ましい。 As the polymerization initiator, those having a 10-hour half-life temperature of 30 to 90 ° C. are preferably used, and preferred examples thereof include diisopropyl peroxydicarbonate, dinormal propyl peroxydicarbonate, and t-butyl peroxypivalate. From the viewpoint of the affinity between the polymerization initiator and the specific fluorine-based compound, diisopropyl peroxydicarbonate and dinormalpropyl peroxydicarbonate are more preferable, and diisopropyl peroxydicarbonate is most preferable. The amount of the polymerization initiator used is 0.01-5 parts by mass, preferably 0.05-2 parts by mass, particularly preferably 0.1-1. It is used in the range of 5 parts by mass. If the amount of the polymerization initiator used is less than 0.01 parts by mass, the polymerization time will be extremely long. When the amount of the polymerization initiator used is greater than 5 parts by mass, the product is colored yellowish brown or the amount of suspended solids increases. For this reason, it is preferable to use a polymerization initiator in the said range.
〔特定のフッ素系化合物〕
本発明のフッ化ビニリデン系重合体の製造方法は、前述のように一般式Ｒ1‐Ｏ‐Ｒ2（ここでＲ1およびＲ2はそれぞれ独立に、アルキル基または、アルキル基の水素原子の一部もしくは全部がフッ素化されたフッ化アルキル基であり、Ｒ1およびＲ2の少なくとも片方が前記フッ化アルキル基である）で表わされる分子量が１００〜８００であるハイドロフルオロエーテルおよび環状ハイドロフルオロカーボンから選択される少なくとも１種のフッ素系化合物存在下で懸濁重合を行うことを特徴とする。[Specific fluorinated compounds]
As described above, the method for producing the vinylidene fluoride polymer of the present invention has the general formula R 1 —O—R 2 (wherein R 1 and R 2 are each independently an alkyl group or a hydrogen atom of an alkyl group). Hydrofluoroethers and cyclic hydrofluorocarbons having a molecular weight of 100 to 800, which are partially or fully fluorinated alkyl groups and at least one of R 1 and R 2 is the fluorinated alkyl group) Suspension polymerization is performed in the presence of at least one fluorine-based compound selected from:
本発明のフッ化ビニリデン系重合体の製造方法は、特定のフッ素系化合物の存在下で懸濁重合を行うことにより、フッ化ビニリデン系重合体を懸濁重合により製造する際に発生する、排水中の浮遊物質の量を従来の製法よりも減少させることが可能であり、このため本発明のフッ化ビニリデン系重合体の製造方法は、廃水処理コストの低減および生産性の向上が可能である。 The method for producing a vinylidene fluoride polymer of the present invention is a wastewater generated when a vinylidene fluoride polymer is produced by suspension polymerization by performing suspension polymerization in the presence of a specific fluorine compound. It is possible to reduce the amount of suspended solids in the process compared to the conventional production method. Therefore, the method for producing a vinylidene fluoride polymer of the present invention can reduce wastewater treatment costs and improve productivity. .
前記ハイドロフルオロエーテルの分子量は１００〜８００であるが、１５０〜５００であることが好ましい。また、前記ハイドロフルオロエーテルのフッ素含有率が３０〜９０ｗｔ％であることが好ましく、フッ素含有率が５０〜７５ｗｔ％であることがより好ましい。なおフッ素含有率とは、フッ素系化合物分子を占めるフッ素原子の質量の割合である。 The hydrofluoroether has a molecular weight of 100 to 800, preferably 150 to 500. Moreover, it is preferable that the fluorine content rate of the said hydrofluoroether is 30-90 wt%, and it is more preferable that the fluorine content rate is 50-75 wt%. The fluorine content is the ratio of the mass of fluorine atoms occupying the fluorine compound molecules.
また、前記一般式において、アルキル基は炭素数１〜２のアルキル基であることが好ましく、前記フッ化アルキル基が炭素数１〜４のフッ化アルキル基であることが好ましい。前記アルキル基の炭素数が１〜２であり、フッ化アルキル基の炭素数が１〜４であると、重合開始剤に対する溶解力が優れると共に、フッ化ビニリデンモノマーの重合反応時に水素引き抜きが起こり難いため好ましい。 In the general formula, the alkyl group is preferably an alkyl group having 1 to 2 carbon atoms, and the fluorinated alkyl group is preferably a fluorinated alkyl group having 1 to 4 carbon atoms. When the alkyl group has 1 to 2 carbon atoms and the alkyl fluoride group has 1 to 4 carbon atoms, it has excellent solubility in the polymerization initiator and hydrogen abstraction occurs during the polymerization reaction of the vinylidene fluoride monomer. It is preferable because it is difficult.
前記ハイドロフルオロエーテルとしては、１，１，２，２−テトラフルオロエチル２，２，２−トリフルオロエチルエーテル（ＣＦ3ＣＨ2ＯＣＦ2ＣＨＦ2）、１，１，２，２−テトラフルオロエチル２，２，３，３−テトラフルオロプロピルエーテル（ＣＨＦ2ＣＦ2ＣＨ2ＯＣＦ2ＣＨＦ2）、１，１，２，２−テトラフルオロエチル２，２，３，３，３−ペンタフルオロプロピルエーテル（ＣＦ3ＣＦ2ＣＨ2ＯＣＦ2ＣＨＦ2）、ヘプタフルオロプロピルメチルエーテル、ノナフルオロブチルメチルエーテル、ノナフルオロブチルエチルエーテル、１，１，１，２，３，４，４，５，５，５−デカフルオロ−３−メトキシ−２−（トリフルオロメチル）ペンタン等が挙げられる。Examples of the hydrofluoroether include 1,1,2,2-tetrafluoroethyl 2,2,2-trifluoroethyl ether (CF 3 CH 2 OCF 2 CHF 2 ), 1,1,2,2-tetrafluoroethyl. 2,2,3,3-tetrafluoropropyl ether (CHF 2 CF 2 CH 2 OCF 2 CHF 2 ), 1,1,2,2-tetrafluoroethyl 2,2,3,3,3-pentafluoropropyl ether (CF 3 CF 2 CH 2 OCF 2 CHF 2 ), heptafluoropropyl methyl ether, nonafluorobutyl methyl ether, nonafluorobutyl ethyl ether, 1,1,1,2,3,4,4,5,5,5 -Decafluoro-3-methoxy-2- (trifluoromethyl) pentane and the like.
前記環状ハイドロフルオロカーボンとしては、通常は炭素数が４〜１０、フッ素含有率が３０％〜９０％であるものが用いられる。環状ハイドロフルオロカーボンとしては、炭素数が５〜８、フッ素含有率が５０％〜７５％で有るものを用いることが好ましい。 As the cyclic hydrofluorocarbon, one having usually 4 to 10 carbon atoms and 30 to 90% fluorine content is used. As the cyclic hydrofluorocarbon, those having 5 to 8 carbon atoms and a fluorine content of 50% to 75% are preferably used.
前記環状ハイドロフルオロカーボンとしては、１，１，２，２，３，３，４−ヘプタフルオロシクロペンタン、オクタフルオロシクロペンテン等が挙げられる。
本発明に用いる前記特定のフッ素系化合物としては、１種または２種以上のハイドロフルオロエーテルでもよく、１種または２種以上の環状ハイドロフルオロカーボンでもよく、ハイドロフルオロエーテルと環状ハイドロフルオロカーボンとの２種以上の混合物であってもよい。Examples of the cyclic hydrofluorocarbon include 1,1,2,2,3,3,4-heptafluorocyclopentane and octafluorocyclopentene.
The specific fluorine-based compound used in the present invention may be one type or two or more types of hydrofluoroethers, one type or two or more types of cyclic hydrofluorocarbons, and two types of hydrofluoroethers and cyclic hydrofluorocarbons. A mixture of the above may also be used.
本発明に用いる特定のフッ素系化合物としては、ＣＦ3ＣＨ2ＯＣＦ2ＣＨＦ2、ＣＨＦ2ＣＦ2ＣＨ2ＯＣＦ2ＣＨＦ2、ＣＦ3ＣＦ2ＣＨ2ＯＣＦ2ＣＨＦ2から選択される少なくとも１種のフッ素系化合物が好ましく、ＣＦ3ＣＨ2ＯＣＦ2ＣＨＦ2がより好ましい。The specific fluorine compound used in the present invention is at least one selected from CF 3 CH 2 OCF 2 CHF 2 , CHF 2 CF 2 CH 2 OCF 2 CHF 2 , and CF 3 CF 2 CH 2 OCF 2 CHF 2 . A fluorine-based compound is preferable, and CF 3 CH 2 OCF 2 CHF 2 is more preferable.
前記特定のフッ素系化合物は、前記重合開始剤を１００質量％とすると、１０〜１０００質量％用いることが好ましく、２５〜５００質量％用いることがより好ましく、５０〜３００質量％用いることが特に好ましい。重合開始剤を１００質量％とした時の特定のフッ素化合物の添加量が１０％より小さいと、重合開始剤の分散性・混和性が劣り、重合開始剤の利用効率が低下する。特定のフッ素化合物を１０００質量％を超えて添加しても、重合開始剤の分散・混和性の改善幅は小さく、製品コストの増大につながるため好ましくない。 The specific fluorine-based compound is preferably used in an amount of 10 to 1000% by mass, more preferably 25 to 500% by mass, and particularly preferably 50 to 300% by mass when the polymerization initiator is 100% by mass. . When the addition amount of the specific fluorine compound when the polymerization initiator is 100% by mass is less than 10%, the dispersibility / miscibility of the polymerization initiator is inferior and the utilization efficiency of the polymerization initiator is lowered. Even if the specific fluorine compound is added in excess of 1000% by mass, the improvement in the dispersion / miscibility of the polymerization initiator is small, which leads to an increase in product cost, which is not preferable.
本発明の特定のフッ素系化合物は、懸濁重合を行う際に使用する全モノマー１００質量部とすると、０．００１〜４．８質量部であることが好ましく、０．００５〜３．０質量部であることがより好ましく、０．０１〜１．２質量部であることが特に好ましい。前記範囲では重合開始剤の分散性・混和性に優れると共に、製品コスト面から好ましい。 The specific fluorine-based compound of the present invention is preferably 0.001 to 4.8 parts by mass, and preferably 0.005 to 3.0 parts by mass, based on 100 parts by mass of all monomers used for suspension polymerization. Part is more preferable, and 0.01 to 1.2 parts by mass is particularly preferable. Within this range, the polymerization initiator is excellent in dispersibility and miscibility, and is preferred from the viewpoint of product cost.
〔懸濁剤〕
本発明のフッ化ビニリデン系重合体の製造方法は、通常前記モノマーを、懸濁剤を含む水性媒体中に分散し、重合開始剤および前記特定のフッ素系化合物存在下で懸濁重合することにより行われる。[Suspension]
In the method for producing a vinylidene fluoride polymer of the present invention, the monomer is usually dispersed in an aqueous medium containing a suspending agent, and suspension polymerization is performed in the presence of a polymerization initiator and the specific fluorine-based compound. Done.
本発明のフッ化ビニリデン系重合体の製造方法では、通常懸濁剤を用いる。
懸濁剤としては、特に限定はないが、メチルセルロース、メトキシ化メチルセルロース、プロポキシ化メチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルセルロース、ヒドロキシプロピルメチルセルロース、ヒドロキシエチルメチルセルロース等のセルロース誘導体、ポリビニルアルコール、ポリエチレンオキシド、ゼラチン等を用いることができる。In the method for producing a vinylidene fluoride polymer of the present invention, a suspending agent is usually used.
The suspending agent is not particularly limited, but includes cellulose derivatives such as methylcellulose, methoxylated methylcellulose, propoxylated methylcellulose, hydroxyethylcellulose, hydroxypropylcellulose, hydroxypropylmethylcellulose, hydroxyethylmethylcellulose, polyvinyl alcohol, polyethylene oxide, gelatin and the like. Can be used.
懸濁剤としてはセルロース誘導体を用いることが好ましく、メチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルメチルセルロース等が好ましい。
懸濁剤の使用量としては、懸濁重合を行う際に使用する全モノマー１００質量部に対して０．０２質量部以上、０．２５質量部未満存在することが好ましく、０．０３質量部以上、０．２質量部未満存在することがより好ましく、０．０５質量部以上、０．１５質量部以下存在することが特に好ましい。前記範囲内では、モノマーの懸濁粒子が安定であり、気泡の発生も少なく好ましい。As the suspending agent, a cellulose derivative is preferably used, and methylcellulose, hydroxyethylcellulose, hydroxypropylmethylcellulose and the like are preferable.
The amount of the suspending agent used is preferably 0.02 parts by mass or more and less than 0.25 parts by mass with respect to 100 parts by mass of the total monomers used for suspension polymerization, and 0.03 parts by mass. As mentioned above, it is more preferable that it exists less than 0.2 mass part, and it is especially preferable that it exists 0.05 mass part or more and 0.15 mass part or less. Within the above range, the suspended particles of the monomer are stable, and the generation of bubbles is preferable.
〔水性媒体〕
本発明のフッ化ビニリデン系重合体の製造方法では、前述のように水性媒体中に前記フッ化ビニリデンを主成分とするモノマーを分散させ、懸濁重合を行う。[Aqueous medium]
In the method for producing a vinylidene fluoride polymer of the present invention, as described above, the monomer containing vinylidene fluoride as a main component is dispersed in an aqueous medium, and suspension polymerization is performed.
水性媒体としては、イオン交換水、純水等の精製された水を用いることが好ましい。
懸濁重合を行う際の水性媒体の使用量としては、使用する全モノマー１００質量部に対して１００〜１０００質量部であることが好ましく、より好ましくは２００〜５００質量部である。As the aqueous medium, purified water such as ion exchange water or pure water is preferably used.
As the usage-amount of the aqueous medium at the time of performing suspension polymerization, it is preferable that it is 100-1000 mass parts with respect to 100 mass parts of all the monomers to be used, More preferably, it is 200-500 mass parts.
〔懸濁重合〕
本発明のフッ化ビニリデン系重合体の製造方法は、前述のように前記少なくともフッ化ビニリデンを含むモノマーを、前記特定のフッ素系化合物および重合開始剤存在下で懸濁重合することにより、フッ化ビニリデン系重合体を得る。また、該製造方法は、通常懸濁剤を含む水性媒体中で行われる。(Suspension polymerization)
As described above, the method for producing a vinylidene fluoride polymer according to the present invention includes the above-mentioned monomer containing at least vinylidene fluoride by suspension polymerization in the presence of the specific fluorine compound and a polymerization initiator. A vinylidene polymer is obtained. Moreover, this manufacturing method is normally performed in the aqueous medium containing a suspending agent.
本発明のフッ化ビニリデン系重合体の製造方法では、前記特定のフッ素系化合物は、重合開始剤の溶媒として作用することが好ましい。すなわち、前記重合開始剤が、前記特定のフッ素系化合物に溶解した状態で懸濁重合が行われることが好ましい。 In the method for producing a vinylidene fluoride polymer according to the present invention, the specific fluorine compound preferably acts as a solvent for a polymerization initiator. That is, it is preferable that suspension polymerization is performed in a state where the polymerization initiator is dissolved in the specific fluorine-based compound.
本発明の製法方法により、排水中の浮遊物質の量が低減される機構は明らかではないが、本発明者らは以下のように推測した。重合開始剤の溶媒として従来使用されてきたハイドロクロロフルオロカーボン等のフッ素系溶媒と、前記ハイドロフルオロエーテル、環状ハイドロフルオロカーボン等の特定のフッ素系化合物とを比べると、前記懸濁剤、水性媒体、モノマー、重合開始剤の親和性が異なり、該親和性の違いが浮遊物質量の低減につながっていると推測した。浮遊物質の生成においては、重合開始剤と懸濁剤の反応、モノマー懸濁粒子外での開始剤とモノマーとの反応が寄与していると考えられ、開始剤を溶解する溶媒の選択が浮遊物質の形成に影響すると本発明者らは推測した。 Although the mechanism by which the amount of suspended solids in the wastewater is reduced by the production method of the present invention is not clear, the present inventors speculated as follows. When the fluorinated solvent such as hydrochlorofluorocarbon conventionally used as a solvent for the polymerization initiator is compared with the specific fluorinated compound such as hydrofluoroether and cyclic hydrofluorocarbon, the suspending agent, aqueous medium, monomer It was speculated that the affinity of the polymerization initiator was different and that the difference in affinity led to a reduction in the amount of suspended solids. In the generation of suspended solids, the reaction between the polymerization initiator and the suspending agent and the reaction between the initiator and the monomer outside the monomer suspension particles are thought to contribute, and the choice of the solvent that dissolves the initiator is floating. We speculated that it would affect the formation of the material.
このような観点から、開始剤として、ジイソプロピルパーオキシジカーボネートを用いた場合には、前記特定のフッ素系化合物として、１，１，２，２‐テトラフルオロエチル２，２，２‐トリフルオロエチルエーテルを用いることが特に好ましい。該組み合わせでは排水中の浮遊物質の量を特に好適に低減することができるため好ましい。 From this point of view, when diisopropyl peroxydicarbonate is used as an initiator, 1,2,2,2-tetrafluoroethyl 2,2,2-trifluoroethyl is used as the specific fluorine compound. It is particularly preferable to use ether. This combination is preferable because the amount of suspended solids in the waste water can be particularly suitably reduced.
本発明のフッ化ビニリデン系重合体の製造方法では、重合系内で、前記水性媒体、特定のフッ素系化合物、重合開始剤を分散・混合することにより、特定のフッ素系化合物に重合開始剤を溶解させてもよいが、前記重合開始剤を、重合系外で前記特定のフッ素系化合物に溶解させ、得られた溶液を重合系内に添加することが特定のフッ素系化合物中に含まれる重合開始剤濃度が均一化し、重合開始剤の利用効率が向上するため好ましい。 In the method for producing a vinylidene fluoride polymer of the present invention, the polymerization initiator is added to the specific fluorine compound by dispersing and mixing the aqueous medium, the specific fluorine compound, and the polymerization initiator in the polymerization system. The polymerization may be dissolved, but the polymerization initiator is dissolved in the specific fluorine compound outside the polymerization system, and the resulting solution is added to the polymerization system. This is preferable because the initiator concentration becomes uniform and the utilization efficiency of the polymerization initiator is improved.
特定のフッ素系化合物と重合開始剤とを混合すると、重合開始剤が溶解され、重合開始剤が均一的に懸濁重合に利用されることを補助するが、重合系内に過剰量の特定のフッ素系化合物が存在しても、重合開始剤の分散・混和性の改善幅は小さく、製品コストの増大につながるため好ましくない。 When a specific fluorine-based compound and a polymerization initiator are mixed, the polymerization initiator is dissolved and assists the polymerization initiator to be uniformly used for suspension polymerization. Even if a fluorine-based compound is present, the range of improvement in dispersion and miscibility of the polymerization initiator is small, which leads to an increase in product cost, which is not preferable.
本発明のフッ化ビニリデン系重合体の製造方法においては、前記特定のフッ素系化合物存在下で懸濁重合を行う以外、好ましくは重合開始剤を重合系外で前記特定のフッ素系化合物に溶解し、得られた溶液をフッ化ビニリデン系重合体の製造に用いる以外は、従来の懸濁重合と同様の方法で行うことができる。なお、本発明のフッ化ビニリデン系重合体の製造方法において用いる、少なくともフッ化ビニリデンを含むモノマー、重合開始剤、特定のフッ素系化合物、懸濁剤、水性媒体の種類や使用量としては、前述の通りである。 In the method for producing a vinylidene fluoride polymer of the present invention, except that suspension polymerization is performed in the presence of the specific fluorine compound, a polymerization initiator is preferably dissolved in the specific fluorine compound outside the polymerization system. The obtained solution can be used in the same manner as conventional suspension polymerization except that it is used for the production of a vinylidene fluoride polymer. The types and amounts of the monomers, polymerization initiators, specific fluorine compounds, suspending agents, and aqueous media that contain at least vinylidene fluoride used in the method for producing the vinylidene fluoride polymer of the present invention are as described above. It is as follows.
また、酢酸エチル、酢酸メチル、炭酸ジエチル、アセトン、エタノール、ｎ−プロパノール、アセトアルデヒド、プロピルアルデヒド、プロピオン酸エチル、四塩化炭素等の連鎖移動剤を添加して、得られるフッ化ビニリデン系重合体の重合度を調節することも可能である。その使用量は、通常は、懸濁重合に使用する全モノマーを１００質量部とすると、０．０１〜５質量部、好ましくは０．０２〜４質量部である。 Further, a vinylidene fluoride polymer obtained by adding a chain transfer agent such as ethyl acetate, methyl acetate, diethyl carbonate, acetone, ethanol, n-propanol, acetaldehyde, propyl aldehyde, ethyl propionate, carbon tetrachloride, etc. It is also possible to adjust the degree of polymerization. The amount of use is usually 0.01 to 5 parts by mass, preferably 0.02 to 4 parts by mass, when the total amount of monomers used for suspension polymerization is 100 parts by mass.
また、懸濁重合における重合温度Ｔは、重合開始剤の１０時間半減期温度Ｔ10に応じて適宜選択され、通常はＴ10−２５℃≦Ｔ≦Ｔ10＋２５℃の範囲で選択される。例えば、ｔ‐ブチルパーオキシピバレートおよびジイソプロピルパーオキシジカーボネートのＴ10はそれぞれ、５４．６℃および４０．５℃である。したがって、ｔ‐ブチルパーオキシピバレートおよびジイソプロピルパーオキシジカーボネートを重合開始剤として用いた重合では、その重合温度Ｔはそれぞれ２９．６℃≦Ｔ≦７９．６℃および１５．５℃≦Ｔ≦６５．５℃の範囲で適宜選択される。重合時間は特に制限されないが、生産性等を考慮すると１００時間以下であることが好ましい。重合時の圧力は通常加圧下で行われ、好ましくは１．０〜８．０ＭＰａ‐Ｇである。The polymerization temperature T in suspension polymerization is appropriately selected according to the 10-hour half-life temperature T 10 of the polymerization initiator, and is usually selected in the range of T 10 −25 ° C. ≦ T ≦ T 10 + 25 ° C. For example, T 10 for t-butyl peroxypivalate and diisopropyl peroxydicarbonate are 54.6 ° C. and 40.5 ° C., respectively. Therefore, in the polymerization using t-butyl peroxypivalate and diisopropyl peroxydicarbonate as polymerization initiators, the polymerization temperatures T are 29.6 ° C. ≦ T ≦ 79.6 ° C. and 15.5 ° C. ≦ T ≦, respectively. It is appropriately selected within the range of 65.5 ° C. The polymerization time is not particularly limited, but is preferably 100 hours or less in consideration of productivity and the like. The pressure at the time of superposition | polymerization is normally performed under pressurization, Preferably it is 1.0-8.0 MPa-G.
上記の条件で前記モノマーの懸濁重合を行うことにより、フッ化ビニリデン系重合体を得ることができる。
本発明のフッ化ビニリデン系重合体の製造方法は、フッ化ビニリデン系重合体を懸濁重合により製造する際に発生する、排水中の浮遊物質の量を従来の製法よりも減少させることが可能であり、廃水処理コストの低減および生産性の向上が可能である。A vinylidene fluoride polymer can be obtained by suspension polymerization of the monomer under the above conditions.
The method for producing a vinylidene fluoride polymer according to the present invention can reduce the amount of suspended solids in waste water generated when a vinylidene fluoride polymer is produced by suspension polymerization, compared to the conventional production method. Therefore, it is possible to reduce wastewater treatment costs and improve productivity.
〔フッ化ビニリデン系重合体〕
本発明の製造方法で得られるフッ化ビニリデン系重合体としては、従来の製法により得られるフッ化ビニリデン系重合体が用いられる各種用途に用いることが可能である。すなわち、本発明の製造方法で得られるフッ化ビニリデン系重合体は、溶融成型して各種フィルムや成形品を製造するための材料として用いてもよく、塗料やバインダー樹脂として用いてもよい。[Vinylidene fluoride polymer]
As a vinylidene fluoride polymer obtained by the production method of the present invention, it can be used for various applications in which a vinylidene fluoride polymer obtained by a conventional production method is used. That is, the vinylidene fluoride polymer obtained by the production method of the present invention may be used as a material for producing various films and molded products by melt molding, or may be used as a paint or a binder resin.
本発明の製造方法で得られるフッ化ビニリデン系重合体の平均粒径としては、特に限定はないが、通常は８０〜２５０μｍであり、好ましくは１３０〜２３０μｍである。
また、本発明の製造方法で得られるフッ化ビニリデン系重合体のインヘレント粘度（樹脂４ｇを１リットルのＮ，Ｎ−ジメチルホルムアミドに溶解させた溶液の３０℃における対数粘度。以下、同様）は、０．５〜５．０ｄｌ／ｇの範囲内の値であることが好ましく、０．８〜４．０ｄｌ／ｇの範囲内の値であることがより好ましく、１．０〜３．５ｄｌ／ｇの範囲内の値であることが最も好ましい。Although there is no limitation in particular as an average particle diameter of the vinylidene fluoride polymer obtained by the manufacturing method of this invention, Usually, it is 80-250 micrometers, Preferably it is 130-230 micrometers.
Further, the inherent viscosity of the vinylidene fluoride polymer obtained by the production method of the present invention (the logarithmic viscosity at 30 ° C. of a solution obtained by dissolving 4 g of resin in 1 liter of N, N-dimethylformamide. The same applies hereinafter). A value in the range of 0.5 to 5.0 dl / g is preferable, a value in the range of 0.8 to 4.0 dl / g is more preferable, and 1.0 to 3.5 dl / g. Most preferably, the value is within the range.
次に本発明について実施例を示してさらに詳細に説明するが、本発明はこれらによって限定されるものではない。
実施例、比較例で得られたフッ化ビニリデン系重合体粉末の物性は以下の方法で測定した。EXAMPLES Next, although an Example is shown and this invention is demonstrated further in detail, this invention is not limited by these.
The physical properties of the vinylidene fluoride polymer powders obtained in Examples and Comparative Examples were measured by the following methods.
〔インヘレント粘度〕
１リットルのＮ，Ｎ−ジメチルホルムアミドに、フッ化ビニリデン系重合体粉末４ｇを添加し、８０℃で８時間かけて溶解させた溶液を調製した。この溶液および溶媒であるＮ，Ｎ−ジメチルホルムアミドを３０℃に保持してウベローデ粘度計でそれぞれの流出時間を測定し、下式によりインヘレント粘度を求めた。
［η］＝ｌｎ（ηrel）／Ｃ
ここでηrelは、試料溶液の流出時間／溶媒の流出時間、Ｃは試料溶液の濃度（０．４ｇ／ｄｌ）を表す。[Inherent viscosity]
A solution was prepared by adding 4 g of vinylidene fluoride polymer powder to 1 liter of N, N-dimethylformamide and dissolving it at 80 ° C. for 8 hours. This solution and the solvent N, N-dimethylformamide were kept at 30 ° C., and each outflow time was measured with an Ubbelohde viscometer, and the inherent viscosity was determined by the following equation.
[Η] = ln (η rel ) / C
Here, η rel is the sample solution outflow time / solvent outflow time, and C is the sample solution concentration (0.4 g / dl).
〔平均粒径〕
フッ化ビニリデン系重合体粉末の粒度分布を、（株）平工製作所製ロータップ式ＩＩ型ふるい振とう機Ｄ型を用い、ＪＩＳ Ｋ ００６９−３．１に従って、乾式ふるい分け法により測定した。平均粒径の算出は、粒度分布の測定結果を元に、対数正規分布法にて求めた。平均粒径は、粒度累積分布において、５０％累積値（Ｄ５０）を示す粒径とした。[Average particle size]
The particle size distribution of the vinylidene fluoride polymer powder was measured by a dry sieving method according to JIS K 0069-3.1 using a low tap type II type sieve shaker D type manufactured by Hiraiko Seisakusho. The average particle size was calculated by the log normal distribution method based on the measurement result of the particle size distribution. The average particle size was a particle size showing a 50% cumulative value (D50) in the particle size cumulative distribution.
〔浮遊物質量の測定〕
重合完了後、重合体スラリーを遠心脱水して排水を回収した。遠心脱水においては通気性（ＪＩＳ Ｌ１０９６）が７０ｃｍ3／ｃｍ2・ｓｅｃのろ布を用いた。得られた排水について、ＪＩＳ Ｋ０１０２記載の懸濁物質の測定方法に従い得られた懸濁物質量を浮遊物質量（ＳＳ）とした。[Measurement of suspended solids]
After the polymerization was completed, the polymer slurry was centrifuged and dewatered to collect the waste water. In the centrifugal dehydration, a filter cloth having an air permeability (JIS L1096) of 70 cm 3 / cm 2 · sec was used. About the obtained waste_water | drain, the amount of suspended solids obtained according to the measuring method of the suspended solids of JISK0102 was made into the amount of suspended solids (SS).
〔比較例１〕
内容積１４．５リットルのオートクレーブに、７４２０ｇのイオン交換水、４．６ｇのメチルセルロース、３０５０ｇのフッ化ビニリデン、３０．７ｇのマレイン酸モノメチルエステル、ジイソプロピルパーオキシジカーボネートを１，３‐ジクロロ‐１，１，２，２，３‐ペンタフルオロプロパン（旭硝子（株）製）（以下、２２５ｃｂとも記す）に５０ｗｔ％の濃度で溶解した開始剤溶液６６．２ｇ、６．２ｇの酢酸エチルを仕込み、２９℃で２６時間懸濁重合を進めた時点で４５℃まで昇温し、合計２８時間２０分懸濁重合を行った。重合完了時の圧力は１．７ＭＰａ、重合収率は８９．４％、平均粒子径は１６５μｍであった。[Comparative Example 1]
To an autoclave having an internal volume of 14.5 liters, 7420 g of ion-exchanged water, 4.6 g of methylcellulose, 3050 g of vinylidene fluoride, 30.7 g of maleic acid monomethyl ester, and diisopropyl peroxydicarbonate were added to 1,3-dichloro-1 , 1,2,2,3-pentafluoropropane (Asahi Glass Co., Ltd.) (hereinafter also referred to as 225cb) was charged with 66.2 g of an initiator solution dissolved at a concentration of 50 wt%, 6.2 g of ethyl acetate, When suspension polymerization proceeded at 29 ° C. for 26 hours, the temperature was raised to 45 ° C., and suspension polymerization was performed for a total of 28 hours and 20 minutes. The pressure at the completion of the polymerization was 1.7 MPa, the polymerization yield was 89.4%, and the average particle size was 165 μm.
重合完了後、重合体スラリーを遠心脱水し、排水を浮遊物質量の測定に供した。遠心脱水した重合体は水に再分散し、９５℃で３０分間熱処理した後、遠心脱水、水洗し、さらに８０℃で２０時間乾燥してフッ化ビニリデン系重合体粉末（ｃ１）を得た。得られたフッ化ビニリデン系重合体粉末（ｃ１）のインヘレント粘度は１．０８ｄｌ／ｇであった。
結果を表１に示す。After completion of the polymerization, the polymer slurry was centrifugally dehydrated, and the wastewater was subjected to measurement of the amount of suspended solids. The centrifugally dehydrated polymer was re-dispersed in water, heat-treated at 95 ° C. for 30 minutes, centrifuged, washed with water, and further dried at 80 ° C. for 20 hours to obtain a vinylidene fluoride polymer powder (c1). The inherent viscosity of the obtained vinylidene fluoride polymer powder (c1) was 1.08 dl / g.
The results are shown in Table 1.
〔実施例１〕
１，３‐ジクロロ‐１，１，２，２，３‐ペンタフルオロプロパンを１，１，２，２‐テトラフルオロエチル２，２，２‐トリフルオロエチルエーテル（旭硝子（株）製）（以下、ＡＥ３０００とも記す）に代えた以外は、比較例１と同様に行い、フッ化ビニリデン系重合体粉末（１）を得た。[Example 1]
1,1,2-Dichloro-1,1,2,2,3-pentafluoropropane is converted to 1,1,2,2-tetrafluoroethyl 2,2,2-trifluoroethyl ether (Asahi Glass Co., Ltd.) The vinylidene fluoride polymer powder (1) was obtained in the same manner as in Comparative Example 1 except that it was replaced with AE3000.
なお、懸濁重合は合計２８時間００分行った。重合完了時の圧力は１．７ＭＰａ、重合収率は８９．３％、平均粒子径は１６２μｍであった。得られたフッ化ビニリデン系重合体粉末（１）のインヘレント粘度は１．０７ｄｌ／ｇであった。
結果を表１に示す。The suspension polymerization was carried out for a total of 28 hours and 00 minutes. The pressure at the completion of the polymerization was 1.7 MPa, the polymerization yield was 89.3%, and the average particle size was 162 μm. The inherent viscosity of the obtained vinylidene fluoride polymer powder (1) was 1.07 dl / g.
The results are shown in Table 1.
〔比較例２〕
内容積１４．５リットルのオートクレーブに、８１７０ｇのイオン交換水、１．６ｇのメチルセルロース、２８７０ｇのフッ化ビニリデン、３２０ｇのヘキサフルオロプロピレン、ジイソプロピルパーオキシジカーボネートを１，３‐ジクロロ‐１，１，２，２，３‐ペンタフルオロプロパンに５０ｗｔ％の濃度で溶解した開始剤溶液１２．８ｇ、３０ｇの酢酸エチルを仕込み、２９℃で１７時間４５分懸濁重合を行った。重合完了時の圧力は１．９ＭＰａ、重合収率は８４．５％、平均粒子径は１６２μｍであった。[Comparative Example 2]
To an autoclave with an internal volume of 14.5 liters, 8170 g of ion-exchanged water, 1.6 g of methylcellulose, 2870 g of vinylidene fluoride, 320 g of hexafluoropropylene, and diisopropyl peroxydicarbonate were added to 1,3-dichloro-1,1, 12.8 g of an initiator solution dissolved in 2,2,3-pentafluoropropane at a concentration of 50 wt% and 30 g of ethyl acetate were charged, and suspension polymerization was performed at 29 ° C. for 17 hours and 45 minutes. The pressure at the completion of the polymerization was 1.9 MPa, the polymerization yield was 84.5%, and the average particle size was 162 μm.
重合完了後、重合体スラリーを遠心脱水し、排水を浮遊物質量の測定に供した。遠心脱水した重合体は水に再分散し、９５℃で３０分間熱処理した後、脱水、水洗し、さらに８０℃で２０時間乾燥してフッ化ビニリデン系重合体粉末（ｃ２）を得た。得られたフッ化ビニリデン系重合体粉末のインヘレント粘度は１．９０ｄｌ／ｇであった。
結果を表２に示す。After completion of the polymerization, the polymer slurry was centrifugally dehydrated, and the wastewater was subjected to measurement of the amount of suspended solids. The centrifugally dehydrated polymer was re-dispersed in water, heat-treated at 95 ° C. for 30 minutes, dehydrated, washed with water, and further dried at 80 ° C. for 20 hours to obtain a vinylidene fluoride polymer powder (c2). The inherent viscosity of the obtained vinylidene fluoride polymer powder was 1.90 dl / g.
The results are shown in Table 2.
〔実施例２〕
１，３‐ジクロロ‐１，１，２，２，３‐ペンタフルオロプロパンを１，１，２，２‐テトラフルオロエチル２，２，２‐トリフルオロエチルエーテルに代えた以外は、比較例２と同様に行い、フッ化ビニリデン系重合体粉末（２）を得た。[Example 2]
Comparative Example 2 except that 1,3-dichloro-1,1,2,2,3-pentafluoropropane was replaced with 1,1,2,2-tetrafluoroethyl 2,2,2-trifluoroethyl ether In the same manner as above, a vinylidene fluoride polymer powder (2) was obtained.
なお、懸濁重合は合計１７時間２０分行った。重合完了時の圧力は１．９ＭＰａ、重合収率は８４．６％、平均粒子径は１６６μｍであった。得られたフッ化ビニリデン系重合体粉末（２）のインヘレント粘度は１．８９ｄｌ／ｇであった。
結果を表２に示す。The suspension polymerization was carried out for a total of 17 hours and 20 minutes. The pressure at the completion of the polymerization was 1.9 MPa, the polymerization yield was 84.6%, and the average particle size was 166 μm. The inherent viscosity of the obtained vinylidene fluoride polymer powder (2) was 1.89 dl / g.
The results are shown in Table 2.
〔比較例３〕
内容積１４．５リットルのオートクレーブに、８１７０ｇのイオン交換水、１．６ｇのメチルセルロース、３１９０ｇのフッ化ビニリデン、ジイソプロピルパーオキシジカーボネートを１，３‐ジクロロ‐１，１，２，２，３‐ペンタフルオロプロパンに５０ｗｔ％の濃度で溶解した開始剤溶液２５．４ｇ、１２７ｇの酢酸エチルを仕込み、２６℃で１２時間重合を進めた時点で４０℃まで昇温し、合計１７時間３０分懸濁重合を行った。重合完了時の圧力は１．４ＭＰａ、重合収率は９２．０％、平均粒子径は１５３μｍであった。[Comparative Example 3]
To an autoclave with an internal volume of 14.5 liters, 8170 g of ion-exchanged water, 1.6 g of methylcellulose, 3190 g of vinylidene fluoride, and diisopropylperoxydicarbonate were added to 1,3-dichloro-1,1,2,2,3- An initiator solution of 25.4 g dissolved in pentafluoropropane at a concentration of 50 wt% and 127 g of ethyl acetate were charged, and when polymerization was carried out at 26 ° C. for 12 hours, the temperature was raised to 40 ° C. and suspended for a total of 17 hours 30 minutes. Polymerization was performed. The pressure at the completion of the polymerization was 1.4 MPa, the polymerization yield was 92.0%, and the average particle size was 153 μm.
重合完了後、重合体スラリーを遠心脱水し、排水を浮遊物質量の測定に供した。遠心脱水した重合体は水に再分散し、９５℃で３０分間熱処理した後、脱水、水洗し、さらに８０℃で２０時間乾燥してフッ化ビニリデン系重合体粉末（ｃ３）を得た。得られたフッ化ビニリデン系重合体粉末（ｃ３）のインヘレント粘度は１．００ｄｌ／ｇであった。
結果を表３に示す。After completion of the polymerization, the polymer slurry was centrifugally dehydrated, and the wastewater was subjected to measurement of the amount of suspended solids. The centrifugally dehydrated polymer was redispersed in water, heat-treated at 95 ° C. for 30 minutes, dehydrated, washed with water, and further dried at 80 ° C. for 20 hours to obtain a vinylidene fluoride polymer powder (c3). The inherent viscosity of the obtained vinylidene fluoride polymer powder (c3) was 1.00 dl / g.
The results are shown in Table 3.
〔実施例３〕
１，３‐ジクロロ‐１，１，２，２，３‐ペンタフルオロプロパンを１，１，２，２‐テトラフルオロエチル２，２，２‐トリフルオロエチルエーテルに代えた以外は、比較例３と同様に行い、フッ化ビニリデン系重合体粉末（３）を得た。Example 3
Comparative Example 3 except that 1,3-dichloro-1,1,2,2,3-pentafluoropropane was replaced with 1,1,2,2-tetrafluoroethyl 2,2,2-trifluoroethyl ether In the same manner as above, a vinylidene fluoride polymer powder (3) was obtained.
なお、懸濁重合は合計１７時間００分行った。重合完了時の圧力は１．４ＭＰａ、重合収率は９１．３％、平均粒子径は１５２μｍであった。得られたフッ化ビニリデン系重合体粉末（３）のインヘレント粘度は１．０２ｄｌ／ｇであった。 The suspension polymerization was carried out for a total of 17:00 hours. The pressure at the completion of the polymerization was 1.4 MPa, the polymerization yield was 91.3%, and the average particle size was 152 μm. The inherent viscosity of the obtained vinylidene fluoride polymer powder (3) was 1.02 dl / g.
結果を表３に示す。 The results are shown in Table 3.
Claims (6)
一般式Ｒ1‐Ｏ‐Ｒ2（ここでＲ1およびＲ2はそれぞれ独立に、アルキル基または、アルキル基の水素原子の一部もしくは全部がフッ素化されたフッ化アルキル基であり、Ｒ1およびＲ2の少なくとも片方が前記フッ化アルキル基である）で表わされる分子量が１００〜８００であるハイドロフルオロエーテルおよび環状ハイドロフルオロカーボンから選択される少なくとも１種のフッ素系化合物存在下で懸濁重合を行うこと、
前記フッ素系化合物を、前記重合開始剤１００質量％に対して１０〜１０００質量％用いること、
前記重合開始剤を、懸濁重合に使用する全モノマー１００質量部に対して０．０１〜５質量部用いることを特徴とするフッ化ビニリデン系重合体の製造方法。In the method for producing a vinylidene fluoride-based polymer in which a monomer containing at least vinylidene fluoride is subjected to suspension polymerization in the presence of a polymerization initiator,
Each general formula R 1 -O-R 2 (wherein R 1 and R 2 are independently an alkyl group, or a part or all of the hydrogen atoms of the alkyl group are fluorinated fluoroalkyl group, R 1 And at least one of R 2 is the above-mentioned fluorinated alkyl group). Suspension polymerization is carried out in the presence of at least one fluorine-based compound selected from hydrofluoroethers having a molecular weight of 100 to 800 and cyclic hydrofluorocarbons. What to do,
10 to 1000% by mass of the fluorine-based compound is used with respect to 100% by mass of the polymerization initiator,
0.01-5 mass parts of said polymerization initiator is used with respect to 100 mass parts of all the monomers used for suspension polymerization, The manufacturing method of the vinylidene fluoride polymer characterized by the above-mentioned.
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