JP4039079B2 - Fluorine-containing diene compound, process for producing the same, and polymer - Google Patents
Fluorine-containing diene compound, process for producing the same, and polymer Download PDFInfo
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- JP4039079B2 JP4039079B2 JP2002046013A JP2002046013A JP4039079B2 JP 4039079 B2 JP4039079 B2 JP 4039079B2 JP 2002046013 A JP2002046013 A JP 2002046013A JP 2002046013 A JP2002046013 A JP 2002046013A JP 4039079 B2 JP4039079 B2 JP 4039079B2
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Description
【0001】
【発明の属する技術分野】
本発明は、新規な含フッ素ジエン化合物、その製造方法および重合体に関する。
【0002】
【従来の技術】
含フッ素ジエン化合物については、特開2000−247914公報に記載のRfCF=CHCH=CH2が知られている。該含フッ素ジエン化合物を用いて得られる重合体は、撥水性および撥油性に優れるが、原料である化合物を得るためには、取扱いが困難である亜鉛等の触媒を使用するか、または多段階の反応を経由する必要があった。
【0003】
【発明が解決しようとする課題】
本発明は、従来技術が有する前述の欠点を解決するものである。すなわち、本発明は、取扱いが困難な亜鉛等の触媒を使用することなく、または多段階の反応を経由することなく製造できる、含フッ素ジエン化合物を提供することを目的とする。また、該含フッ素ジエン化合物の製造方法および重合体の提供を目的とする。
【0004】
【課題を解決するための手段】
本発明は、RfCH=CFCH=CH2で表される含フッ素ジエン化合物(以下、化合物1と記す。)を提供する。ただし、本明細書においてRfは炭素数1〜12のポリフルオロアルキル基(以下、Rf基と記す。)を示す。
【0005】
本発明は、RfCH2CF2CH2CH2X(ただし、Xはヨウ素原子を示す。以下においても同様。)で表される化合物(以下、化合物2と記す。)を、塩基性化合物の存在下に脱HX反応および脱HF反応させる化合物1の製造方法を提供する。
【0006】
本発明は、−CH2CH=CFCHRf−で表される繰り返し単位(以下、繰り返し単位Aと記す。)および/または−CH2CH(CF=CHRf)−で表される繰り返し単位(以下、繰り返し単位Bと記す。)を含み、かつ質量平均分子量が2×103〜5×106である重合体を提供する。
【0007】
【発明の実施の形態】
本発明においてRf基としては、対応するアルキル基における水素原子の数にして60%以上がフッ素原子に置換された基が好ましく、特に80%以上がフッ素原子に置換された基が好ましい。また、残余の水素原子の一部または全部が、塩素原子等の他のハロゲン原子に置換されていてもよい。
【0008】
Rf基の炭素数が3以上の場合は、Rf基は分岐状でも直鎖状でもよく、直鎖状が好ましい。Rf基の炭素数は、重合体におけるフッ素原子の含有量を多くし、重合体の耐熱性、耐油性、撥水性等を向上できるため、4〜10が好ましい。
【0009】
本発明の化合物1は、前記化合物2を塩基性化合物の存在下に脱HX反応および脱HF反応させることにより製造するのが好ましい。たとえば、化合物1は、化合物2を塩基性化合物の存在下に脱HX反応させてRfCH2CF2CH=CH2で表される化合物(以下、化合物3と記す。)とし、さらに塩基性化合物の存在下に脱HF反応させることにより製造するのが好ましい。
【0010】
化合物2は、Rf−Xで表される化合物にフッ化ビニリデンおよびエチレンをラジカル反応により付加して得られる。該ラジカル反応は、フッ化ビニリデンを付加した後に、エチレンを付加するのが好ましい。
【0011】
化合物2と塩基性化合物との反応は、溶媒の存在下で行われるのが好ましい。溶媒としては、tert−ブタノール(以下、t−BuOHと記す。)、メタノール(以下、MeOHと記す。)、水等が好ましく挙げられる。特に、t−BuOHが好ましい。
【0012】
塩基性化合物としては、アルカリ金属水酸化物、アルカリ土類金属水酸化物、アルカリ金属アルコキシド、有機アミン化合物等が好ましく用いられる。具体的には、水酸化カリウム(以下、KOHと記す。)、水酸化ナトリウム、水酸化カルシウム、水酸化マグネシウム、tert−ブトキシカリウム(以下、t−BuOKと記す。)、トリエチルアミン、ピリジン等が好ましい。
【0013】
塩基性化合物としては、化合物2との反応においては、反応率、生成物の選択性等の観点からt−BuOKが好ましく、化合物3との反応においては、比較的塩基性の弱いKOHが好ましい。また、該反応は、相間移動触媒を添加して行ってもよい。相間移動触媒としては、アルキルアンモニウム塩等が好ましく挙げられる。
塩基性化合物の存在下での脱HX反応および脱HF反応において、反応温度は40〜100℃が好ましく、反応時間は1〜100時間が好ましい。
【0014】
本発明の化合物1は、高い重合性を有し、化合物1に基づく重合単位を有する重合体が得られる。本発明の重合体は、前記繰り返し単位Aおよび/または前記繰り返し単位Bを有し、かつ質量平均分子量は2×103〜5×106であるのが好ましい。質量平均分子量が大きすぎると重合体の製造が困難となり、小さすぎると重合体の熱安定性が低くなり、分解しやすくなる。
【0015】
繰り返し単位Aは、化合物1が1,4−重合様式で重合した構造であり、繰り返し単位Bは、1,2−重合様式で重合した構造である。本発明の重合体は、繰り返し単位Aおよび繰り返し単位Bの両方が含まれる重合体でもよく、繰り返し単位Aのみまたは繰り返し単位Bのみが含まれる重合体でもよい。
【0016】
本発明の重合体は、上記の繰り返し単位以外に、他の単量体に基づく繰り返し単位を含んでいてもよい。他の単量体としては、テトラフルオロエチレン、クロロトリフルオロエチレン、フッ化ビニリデン、フッ化ビニル、ヘキサフルオロプロピレン、エチレン、プロピレン、メチル(メタ)アクリレート、フルオロアルキル(メタ)アクリレート、(メタ)アクリロニトリル、炭素数14以上の飽和炭化水素基含有(メタ)アクリレート、スチレンおよびその誘導体等が好ましく挙げられる。特に、炭素数14以上の飽和炭化水素基含有(メタ)アクリレートが好ましい。重合体において、他の単量体に基づく繰り返し単位の割合は90モル%以下が好ましい。
【0017】
本発明の重合体は、イオン重合法、ラジカル重合法等の重合方法を用いて得ることができる。本発明においては、ラジカル開始剤を用いて特に穏和な条件で重合できるラジカル重合法を用いて重合体を得るのが好ましい。具体的には、懸濁重合、溶液重合、バルク重合、乳化重合等の重合方法が好ましく採用できる。
【0018】
ラジカル開始剤としては、水溶性開始剤または油溶性開始剤が重合方法に応じて使用できる。たとえば、乳化重合においては、水溶性過酸化物が好ましく用いられ、たとえば、過硫酸カリウム、過硫酸アンモニウム、ジコハク酸パーオキシド等が好ましく用いられる。懸濁重合、溶液重合またはバルク重合においては、非フッ素系過酸化物、フッ素系過酸化物、アゾ化合物が好ましく用いられ、たとえば、ジイソプロピルパーオキシジカーボネート、ベンゾイルパーオキシド、パーフルオロブタン酸パーオキシド、アゾビスイソブチロニトリル(以下、AIBNと記す。)等が好ましく用いられる。
【0019】
溶液重合においては、溶剤として、Cl(CF2)2CHClF、F(CF2)8F、H(CF2)6F等のフッ素系溶剤が好ましく用いられる。重合体を得る反応の温度は、ラジカル重合においては50〜100℃が好ましい。
【0020】
【実施例】
以下、本発明について実施例を挙げて詳細に説明する。しかし、本発明はこれらに限定されない。
【0021】
[例1]
撹拌機、ジムロート、滴下ロート付き1Lの三つ口フラスコに、3,3,5,5,6,6,7,7,8,8,8−ウンデカフルオロ−1−ヨードオクタンの200gおよびMeOHの100gを入れ、KOHの28gをMeOHの150gに溶解させた溶液を室温にて1時間かけて滴下した。
【0022】
その後、加熱して還流させ、還流開始から3時間後に、KOHの11gをMeOHの80gに溶解させた溶液を添加し、さらに5時間反応させた。反応後、得られたC4F9CH2CF2CH=CH2を含む反応混合物を、蒸留水にて洗浄し、反応液を得た。
【0023】
撹拌機、ジムロート、滴下ロート付き1Lの三つ口フラスコに、得られた反応液の143gおよびt−BuOHの50gを入れ、t−BuOKの39gとテトラブチルアンモニウム(以下、TBABと記す。)の11gをt−BuOHの150gに溶解させた溶液を室温にて1時間かけて滴下した。
【0024】
その後、加熱して還流させ、還流開始から12時間後に、t−BuOKの20gをt−BuOHの100gに溶解させた溶液を添加し、さらに4時間反応させた。反応後、得られた反応粗液を蒸留水で洗浄し、減圧蒸留して、目的とする生成物1であるC4F9CH=CFCH=CH2(沸点65℃/200torr)の23g(生成物1の単離収率は17%。)を得た。得られた生成物1はトランス体のみであった。19F−NMRおよび1H−NMRの測定結果を示す。
【0025】
19F−NMR(溶媒:CDCl3)δ(ppm):−81.8(3F,CF3−)、−107.9(2F,−CF2−CH=)、−108.4(1F,−CH=CF−(trans))、−124.9〜−126.3(4F,−CF2−)。
【0026】
1H−NMR(溶媒:CDCl3)δ(ppm):5.01(1H,−CH=CF−)、5.55〜5.93(2H,CH2=)、6.16(1H,=CF−CH=)。
【0027】
[例2]
撹拌機、ジムロート、滴下ロート付き1Lの三つ口フラスコに、3,3,5,5,6,6,7,7,8,8,9,9,10,10,10−ペンタデカフルオロ−1−ヨードデカンの400gおよびMeOHの200gを入れ、これにKOHの47gをMeOHの200gに溶解させた溶液を室温にて1時間かけて滴下した。
【0028】
その後、加熱して還流させ、還流開始から3時間後にKOHの12gをMeOHの100gに溶解させた溶液を添加し、さらに5時間反応させた。反応後、得られたC6F13CH2CF2CH=CH2を含む反応混合物を、蒸留水にて洗浄し、反応液を得た。
【0029】
撹拌機、ジムロート、滴下ロート付き1Lの三つ口フラスコに、得られた反応液の298gおよびt−BuOHの100gを入れ、t−BuOKの60gとTBABの17gをt−BuOHの250gに溶解させた溶液を室温にて1時間かけて滴下した。
【0030】
その後、加熱して還流させ、還流開始から12時間後に、t−BuOKの45gをt−BuOHの200gに溶解させた溶液を添加し、さらに8時間反応させた。反応後、得られた反応粗液を蒸留水で洗浄し、減圧蒸留して、目的とする生成物2であるC6F13CH=CFCH=CH2(沸点66℃/30torr)の65g(生成物2の単離収率は23%。)を得た。得られた生成物はトランス体のみであった。19F−NMRおよび1H−NMRの測定結果を示す。
【0031】
19F−NMR(溶媒:CDCl3)δ(ppm):−81.5(3F、CF3−)、−107.6(2F、−CF2−CH=)、−108.4(1F、−CH=CF−(trans))、−122.1〜126.5(8F、−CF2−)、
(溶媒:CDCl3)δ(ppm):5.01(1H、−CH=CF−)、5.55〜5.93(2H、CH2=)、6.15(1H、=CF−CH=)。
【0032】
[例3]
100mLのガラス製アンプルに、生成物1の9g、AK−225(旭硝子社製、商品名)の51gおよびAIBNの0.36gを入れ、液体窒素を用いて凍結脱気を3回繰り返した後、65℃にて12時間重合反応を行い、重合体を得た。反応終了後の溶液をガスクロマトグラフィーにより分析したところ、未反応の生成物1は実質的に検出されなかった。得られた重合体の質量平均分子量は9300であり、該重合体における繰り返し単位Aと繰り返し単位Bの割合は約1:1であった。
【0033】
重合体を含む溶液に蒸留水を加えて、重合体の濃度が5質量%となるように希釈し、試験液とした。試験液の1mLを、7cm四方のガラス板に滴下し、3000回転で30秒間スピンコートした後、110℃にて1時間キュアリングを行ってサンプルを作製した。得られたサンプルの表面の、水に対する接触角は110.4度であり、ヘキサデカンに対する接触角は68.5度であった。
【0034】
[例4]
生成物1の代わりに生成物2を用いる以外は、例3と同様に重合反応を行った。得られた重合体の質量平均分子量は10300であり、該重合体における繰り返し単位Aと繰り返し単位Bの割合は約1:1であった。さらに、例3と同様にしてサンプルを作製した。得られたサンプルの表面の、水に対する接触角は109度であり、ヘキサデカンに対する接触角は66.7度であった。
【0035】
[例5]
100mLガラス製重合アンプルに、生成物1の8.11g、ステアリルアクリレートの12.25g、ヒドロキシエチルアクリレートの0.42g、ポリオキシアルキレングリコールモノメタクリレートの0.3g、ポリオキシエチレンオクチルフェニルエーテルの1.68g、ステアリルトリエチルアンモニウムクロライドの0.42g、水の26.20g、アセトンの10.5g、分子量調整剤としてステアリルメルカプタンの0.11g、開始剤として2,2’−アゾビス(2−メチルプロピオンアミジン)2塩酸塩の0.04gを入れた。
【0036】
窒素置換を行い、55℃にて12時間重合反応を行い、重合体の固形分濃度が38.4質量%であるエマルションを得た。得られた重合体の質量平均分子量は45800であり、重合体における生成物1に基づく重合単位の割合は39.9モル%であった。
【0037】
得られたエマルションの3gをメタノールの27gに滴下し、重合体を沈殿させた。得られた重合体を30℃にて一晩真空乾燥させた後、AK−225を用いて重合体の濃度が5質量%である溶液を得た。
【0038】
得られた溶液を用いて、例3と同様にしてサンプルを作製した。得られたサンプルの表面の、水に対する接触角は107.2度であり、ヘキサデカンに対する接触角は66.7度であった。
【0039】
[例6]
生成物1の代わりに生成物2を用いる以外は、例5と同様に重合反応を行い、重合体の固形分濃度が39.1質量%であるエマルションを得た。得られた重合体の質量平均分子量は47000であり、重合体における生成物2に基づく重合単位の割合は33.1モル%であった。
【0040】
さらに、例5と同様にしてサンプルを作製した。得られたサンプルの、水に対する接触角は109.4度であり、ヘキサデカンに対する接触角は69.4度であった。
【0041】
【発明の効果】
本発明の含フッ素ジエン化合物は新規な化合物である。該化合物の合成は、取扱いが困難である亜鉛等の触媒を使用せず、多段階の反応を経由せずに行える。また、該化合物は重合性に優れ、質量平均分子量の大きな重合体を得ることができる。
【0042】
本発明の重合体は、柔軟性に優れ、Rf基を有することにより耐熱性、撥水性、撥油性に優れる。また、二重結合を有する炭素原子にフッ素原子が結合しているため、熱的に安定である。また、該重合体はフッ素系溶剤に可溶であるため、耐候性、撥水性、非粘着性に優れた塗料またはコーティング材として有用である。さらに、フッ素原子を多く含むことから誘電率が低く、低誘電率被膜としての用途にも有用である。
【0043】
また、本発明の重合体は二重結合を有することから、さらに架橋反応が行え、また重合体に官能基を容易に導入できる。さらに、ポリブタジエン、ニトリルゴム、スチレン・ブタジエン共重合体などの樹脂に、Rf基を容易に導入でき、樹脂の改質が容易に行える。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a novel fluorine-containing diene compound, a production method thereof and a polymer.
[0002]
[Prior art]
As for the fluorine-containing diene compound, R f CF═CHCH═CH 2 described in JP-A No. 2000-247914 is known. The polymer obtained using the fluorine-containing diene compound is excellent in water repellency and oil repellency. However, in order to obtain a compound as a raw material, a catalyst such as zinc, which is difficult to handle, is used. It was necessary to go through the reaction.
[0003]
[Problems to be solved by the invention]
The present invention solves the aforementioned drawbacks of the prior art. That is, an object of the present invention is to provide a fluorine-containing diene compound that can be produced without using a catalyst such as zinc, which is difficult to handle, or without going through a multistage reaction. Another object is to provide a method for producing the fluorine-containing diene compound and a polymer.
[0004]
[Means for Solving the Problems]
The present invention provides a fluorine-containing diene compound represented by R f CH═CFCH═CH 2 (hereinafter referred to as compound 1). In the present specification, R f represents a C 1-12 polyfluoroalkyl group (hereinafter referred to as R f group).
[0005]
The present invention relates to a compound represented by R f CH 2 CF 2 CH 2 CH 2 X (where X represents an iodine atom, the same shall apply hereinafter) (hereinafter referred to as compound 2) as a basic compound. The present invention provides a method for producing Compound 1 in which deHX reaction and deHF reaction are performed in the presence of
[0006]
The invention, -CH 2 CH = CFCHR f - represented by the repeating units (. Hereinafter referred to as repeating unit A) and / or -CH 2 CH (CF = CHR f ) - repeating units (hereinafter represented by And a repeating unit B.), and a polymer having a mass average molecular weight of 2 × 10 3 to 5 × 10 6 .
[0007]
DETAILED DESCRIPTION OF THE INVENTION
In the present invention, the R f group is preferably a group in which 60% or more of hydrogen atoms in the corresponding alkyl group are substituted with fluorine atoms, and particularly preferably a group in which 80% or more is substituted with fluorine atoms. Further, some or all of the remaining hydrogen atoms may be substituted with other halogen atoms such as chlorine atoms.
[0008]
When the number of carbon atoms in the R f group is 3 or more, the R f group may be branched or linear, and is preferably linear. The number of carbon atoms in the R f group is preferably 4 to 10 because the content of fluorine atoms in the polymer can be increased and the heat resistance, oil resistance, water repellency and the like of the polymer can be improved.
[0009]
Compound 1 of the present invention is preferably produced by subjecting Compound 2 to a deHX reaction and a deHF reaction in the presence of a basic compound. For example, compound 1 is obtained by subjecting compound 2 to de-HX reaction in the presence of a basic compound to give a compound represented by R f CH 2 CF 2 CH═CH 2 (hereinafter referred to as compound 3), and further basic. It is preferably produced by deHF reaction in the presence of the compound.
[0010]
Compound 2 is obtained by adding vinylidene fluoride and ethylene to the compound represented by R f -X by radical reaction. In the radical reaction, it is preferable to add ethylene after adding vinylidene fluoride.
[0011]
The reaction between compound 2 and the basic compound is preferably carried out in the presence of a solvent. Preferred examples of the solvent include tert-butanol (hereinafter referred to as t-BuOH), methanol (hereinafter referred to as MeOH), water and the like. In particular, t-BuOH is preferable.
[0012]
As the basic compound, an alkali metal hydroxide, an alkaline earth metal hydroxide, an alkali metal alkoxide, an organic amine compound, or the like is preferably used. Specifically, potassium hydroxide (hereinafter referred to as KOH), sodium hydroxide, calcium hydroxide, magnesium hydroxide, tert-butoxypotassium (hereinafter referred to as t-BuOK), triethylamine, pyridine and the like are preferable. .
[0013]
The basic compound is preferably t-BuOK in the reaction with the compound 2 from the viewpoint of the reaction rate, the selectivity of the product, etc., and the reaction with the compound 3 is preferably KOH having a relatively weak basicity. In addition, the reaction may be performed by adding a phase transfer catalyst. Preferred examples of the phase transfer catalyst include alkyl ammonium salts.
In the deHX reaction and the deHF reaction in the presence of a basic compound, the reaction temperature is preferably 40 to 100 ° C., and the reaction time is preferably 1 to 100 hours.
[0014]
The compound 1 of the present invention has high polymerizability, and a polymer having a polymer unit based on the compound 1 is obtained. The polymer of the present invention preferably has the repeating unit A and / or the repeating unit B, and has a mass average molecular weight of 2 × 10 3 to 5 × 10 6 . When the mass average molecular weight is too large, it is difficult to produce the polymer, and when it is too small, the thermal stability of the polymer is lowered and the polymer is easily decomposed.
[0015]
The repeating unit A has a structure in which the compound 1 is polymerized in a 1,4-polymerization mode, and the repeating unit B has a structure in which the compound 1 is polymerized in a 1,2-polymerization mode. The polymer of the present invention may be a polymer containing both the repeating unit A and the repeating unit B, or may be a polymer containing only the repeating unit A or only the repeating unit B.
[0016]
The polymer of this invention may contain the repeating unit based on another monomer other than said repeating unit. Other monomers include tetrafluoroethylene, chlorotrifluoroethylene, vinylidene fluoride, vinyl fluoride, hexafluoropropylene, ethylene, propylene, methyl (meth) acrylate, fluoroalkyl (meth) acrylate, (meth) acrylonitrile Preferred examples include saturated hydrocarbon group-containing (meth) acrylates having 14 or more carbon atoms, styrene and derivatives thereof. In particular, a saturated hydrocarbon group-containing (meth) acrylate having 14 or more carbon atoms is preferred. In the polymer, the proportion of repeating units based on other monomers is preferably 90 mol% or less.
[0017]
The polymer of the present invention can be obtained using a polymerization method such as an ionic polymerization method or a radical polymerization method. In the present invention, it is preferable to obtain a polymer by using a radical polymerization method that can be polymerized under a particularly mild condition using a radical initiator. Specifically, polymerization methods such as suspension polymerization, solution polymerization, bulk polymerization, and emulsion polymerization can be preferably employed.
[0018]
As the radical initiator, a water-soluble initiator or an oil-soluble initiator can be used depending on the polymerization method. For example, in emulsion polymerization, a water-soluble peroxide is preferably used, and for example, potassium persulfate, ammonium persulfate, disuccinic acid peroxide and the like are preferably used. In suspension polymerization, solution polymerization or bulk polymerization, non-fluorine peroxide, fluorine peroxide, and azo compound are preferably used. For example, diisopropyl peroxydicarbonate, benzoyl peroxide, perfluorobutanoic acid peroxide, Azobisisobutyronitrile (hereinafter referred to as AIBN) and the like are preferably used.
[0019]
In the solution polymerization, a fluorine-based solvent such as Cl (CF 2 ) 2 CHClF, F (CF 2 ) 8 F, H (CF 2 ) 6 F is preferably used as the solvent. The reaction temperature for obtaining the polymer is preferably 50 to 100 ° C. in radical polymerization.
[0020]
【Example】
Hereinafter, the present invention will be described in detail with reference to examples. However, the present invention is not limited to these.
[0021]
[Example 1]
In a 1 L three-necked flask equipped with a stirrer, Dimroth and dropping funnel, 200 g of 3,3,5,5,6,7,7,8,8,8-undecafluoro-1-iodooctane and MeOH A solution prepared by dissolving 28 g of KOH in 150 g of MeOH was added dropwise at room temperature over 1 hour.
[0022]
Thereafter, the mixture was heated to reflux, and after 3 hours from the start of reflux, a solution prepared by dissolving 11 g of KOH in 80 g of MeOH was added, and further reacted for 5 hours. After the reaction, the resulting reaction mixture containing C 4 F 9 CH 2 CF 2 CH═CH 2 was washed with distilled water to obtain a reaction solution.
[0023]
143 g of the obtained reaction solution and 50 g of t-BuOH were placed in a 1 L three-necked flask equipped with a stirrer, a Dimroth, and a dropping funnel, and 39 g of t-BuOK and tetrabutylammonium (hereinafter referred to as TBAB). A solution prepared by dissolving 11 g in 150 g of t-BuOH was added dropwise at room temperature over 1 hour.
[0024]
Thereafter, the mixture was heated to reflux, and 12 hours after the start of reflux, a solution in which 20 g of t-BuOK was dissolved in 100 g of t-BuOH was added, and the mixture was further reacted for 4 hours. After the reaction, the obtained reaction crude liquid was washed with distilled water and distilled under reduced pressure to obtain 23 g (formation of C 4 F 9 CH═CFCH═CH 2 (boiling point 65 ° C./200 torr) which is the target product 1 The isolated yield of product 1 was 17%.). The obtained product 1 was only a trans form. The measurement results of 19 F-NMR and 1 H-NMR are shown.
[0025]
19 F-NMR (solvent: CDCl 3 ) δ (ppm): −81.8 (3F, CF 3 —), −107.9 (2F, —CF 2 —CH═), −108.4 (1F, − CH = CF- (trans)), - 124.9~-126.3 (4F, -CF 2 -).
[0026]
1 H-NMR (solvent: CDCl 3 ) δ (ppm): 5.01 (1H, —CH═CF—), 5.55-5.93 (2H, CH 2 =), 6.16 (1H, = CF-CH =).
[0027]
[Example 2]
3, 3, 5, 5, 6, 6, 7, 7, 8, 8, 9, 9, 10, 10, 10-pentadecafluoro-into a 1 L three-necked flask equipped with a stirrer, Dimroth, and dropping funnel 400 g of 1-iododecane and 200 g of MeOH were added, and a solution in which 47 g of KOH was dissolved in 200 g of MeOH was added dropwise at room temperature over 1 hour.
[0028]
Thereafter, the mixture was heated to reflux, and after 3 hours from the start of reflux, a solution in which 12 g of KOH was dissolved in 100 g of MeOH was added, and further reacted for 5 hours. After the reaction, the resulting reaction mixture containing C 6 F 13 CH 2 CF 2 CH═CH 2 was washed with distilled water to obtain a reaction solution.
[0029]
Into a 1 L three-necked flask equipped with a stirrer, Dimroth and dropping funnel, 298 g of the obtained reaction solution and 100 g of t-BuOH were put, and 60 g of t-BuOK and 17 g of TBAB were dissolved in 250 g of t-BuOH. The solution was added dropwise at room temperature over 1 hour.
[0030]
Thereafter, the mixture was heated to reflux, and after 12 hours from the start of reflux, a solution prepared by dissolving 45 g of t-BuOK in 200 g of t-BuOH was added, and further reacted for 8 hours. After the reaction, the obtained reaction crude liquid was washed with distilled water and distilled under reduced pressure to obtain 65 g of the desired product 2 (C 6 F 13 CH═CFCH═CH 2 (boiling point 66 ° C./30 torr)) The isolated yield of product 2 was 23%.). The product obtained was only the trans isomer. The measurement results of 19 F-NMR and 1 H-NMR are shown.
[0031]
19 F-NMR (solvent: CDCl 3 ) δ (ppm): −81.5 (3F, CF 3 —), −107.6 (2F, —CF 2 —CH═), −108.4 (1F, − CH = CF- (trans)), - 122.1~126.5 (8F, -CF 2 -),
(Solvent: CDCl 3 ) δ (ppm): 5.01 (1H, —CH═CF—), 5.55-5.93 (2H, CH 2 =), 6.15 (1H, ═CF—CH═) ).
[0032]
[Example 3]
In a 100 mL glass ampule, 9 g of product 1, 51 g of AK-225 (trade name, manufactured by Asahi Glass Co., Ltd.) and 0.36 g of AIBN were added, and freeze deaeration was repeated three times using liquid nitrogen. A polymerization reaction was carried out at 65 ° C. for 12 hours to obtain a polymer. When the solution after completion of the reaction was analyzed by gas chromatography, the unreacted product 1 was not substantially detected. The obtained polymer had a mass average molecular weight of 9,300, and the ratio of the repeating unit A to the repeating unit B in the polymer was about 1: 1.
[0033]
Distilled water was added to the solution containing the polymer to dilute the polymer to a concentration of 5% by mass to obtain a test solution. 1 mL of the test solution was dropped on a 7 cm square glass plate, spin-coated at 3000 rpm for 30 seconds, and then cured at 110 ° C. for 1 hour to prepare a sample. The contact angle with respect to water of the surface of the obtained sample was 110.4 degrees, and the contact angle with respect to hexadecane was 68.5 degrees.
[0034]
[Example 4]
A polymerization reaction was carried out in the same manner as in Example 3 except that the product 2 was used instead of the product 1. The obtained polymer had a mass average molecular weight of 10,300, and the ratio of the repeating unit A to the repeating unit B in the polymer was about 1: 1. Further, a sample was produced in the same manner as in Example 3. The contact angle with respect to water of the surface of the obtained sample was 109 degrees, and the contact angle with hexadecane was 66.7 degrees.
[0035]
[Example 5]
In a 100 mL glass polymer ampoule, 8.11 g of product 1, 12.25 g of stearyl acrylate, 0.42 g of hydroxyethyl acrylate, 0.3 g of polyoxyalkylene glycol monomethacrylate, 1. of polyoxyethylene octylphenyl ether. 68 g, 0.42 g of stearyl triethylammonium chloride, 26.20 g of water, 10.5 g of acetone, 0.11 g of stearyl mercaptan as a molecular weight regulator, 2,2′-azobis (2-methylpropionamidine) as an initiator 0.04 g of dihydrochloride was added.
[0036]
The emulsion was purged with nitrogen and subjected to a polymerization reaction at 55 ° C. for 12 hours to obtain an emulsion having a solid content concentration of 38.4% by mass. The weight average molecular weight of the obtained polymer was 45800, and the ratio of polymerized units based on the product 1 in the polymer was 39.9 mol%.
[0037]
3 g of the obtained emulsion was dropped into 27 g of methanol to precipitate a polymer. The obtained polymer was vacuum-dried at 30 ° C. overnight, and then a solution having a polymer concentration of 5% by mass was obtained using AK-225.
[0038]
A sample was prepared in the same manner as in Example 3 using the obtained solution. The contact angle with respect to water of the surface of the obtained sample was 107.2 degrees, and the contact angle with hexadecane was 66.7 degrees.
[0039]
[Example 6]
A polymerization reaction was carried out in the same manner as in Example 5 except that the product 2 was used in place of the product 1, and an emulsion having a solid content concentration of 39.1% by mass was obtained. The weight average molecular weight of the obtained polymer was 47000, and the ratio of polymerized units based on the product 2 in the polymer was 33.1 mol%.
[0040]
Further, a sample was produced in the same manner as in Example 5. The obtained sample had a contact angle with water of 109.4 degrees and a contact angle with hexadecane of 69.4 degrees.
[0041]
【The invention's effect】
The fluorine-containing diene compound of the present invention is a novel compound. The compound can be synthesized without using a catalyst such as zinc, which is difficult to handle, and without going through a multistage reaction. Moreover, this compound is excellent in polymerizability, and can obtain a polymer with a large mass average molecular weight.
[0042]
The polymer of the present invention is excellent in flexibility, and has excellent heat resistance, water repellency and oil repellency by having an R f group. Further, since a fluorine atom is bonded to a carbon atom having a double bond, it is thermally stable. Further, since the polymer is soluble in a fluorine-based solvent, it is useful as a paint or coating material excellent in weather resistance, water repellency and non-adhesiveness. Furthermore, since it contains a large amount of fluorine atoms, it has a low dielectric constant and is useful for applications as a low dielectric constant film.
[0043]
Further, since the polymer of the present invention has a double bond, it can further undergo a crosslinking reaction, and a functional group can be easily introduced into the polymer. Furthermore, Rf groups can be easily introduced into resins such as polybutadiene, nitrile rubber, styrene / butadiene copolymer, and the resin can be easily modified.
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