JP3124348B2 - Tetrafluoroethylene copolymer - Google Patents
Tetrafluoroethylene copolymerInfo
- Publication number
- JP3124348B2 JP3124348B2 JP35383691A JP35383691A JP3124348B2 JP 3124348 B2 JP3124348 B2 JP 3124348B2 JP 35383691 A JP35383691 A JP 35383691A JP 35383691 A JP35383691 A JP 35383691A JP 3124348 B2 JP3124348 B2 JP 3124348B2
- Authority
- JP
- Japan
- Prior art keywords
- copolymer
- polymerization
- tetrafluoroethylene
- mol
- tetrafluoroethylene copolymer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Description
【0001】[0001]
【産業上の利用分野】本発明は、溶融成形可能なテトラ
フルオロエチレン共重合体に関する。 The present invention relates to related to a melt-moldable tetrafluoroethylene copolymer.
【0002】[0002]
【従来の技術】ポリテトラフルオロエチレンは優れた耐
薬品性、耐熱性、電気特性を有しているが、溶融成形で
きないため、溶融成形可能なテトラフルオロエチレン−
ヘキサフルオロプロピレン共重合体(FEP)やテトラ
フルオロエチレン−パーフルオロアルコキシエチレン共
重合体(PFA)などが開発され、市販されている。し
かしFEPやPFAは高温での機械特性に優れ、特に弾
性率が低く、高温弾性率の高い樹脂が望まれている。2. Description of the Related Art Polytetrafluoroethylene has excellent chemical resistance, heat resistance and electrical properties, but cannot be melt-molded.
Hexafluoropropylene copolymer (FEP) and tetrafluoroethylene-perfluoroalkoxyethylene copolymer (PFA) have been developed and are commercially available. However, FEP and PFA have excellent mechanical properties at high temperatures, and particularly, resins having low elastic modulus and high elastic modulus at high temperature are desired.
【0003】また、特開平1−131215では式1又
は式2で示される含フッ素熱可塑性重合体が開示され、
また米国特許第3978030号では式3で示されるモ
ノマーを重合した重合体が開示されている。Further, JP-A-1-131215 discloses a fluorinated thermoplastic polymer represented by the formula ( 1) or ( 2),
U.S. Pat. No. 3,978,030 discloses a polymer obtained by polymerizing a monomer represented by the formula ( 3).
【0004】[0004]
【化1】 Embedded image
【0005】[0005]
【0006】[0006]
【0007】これらの重合体は非結晶性でしかもガラス
転移温度が高く、ガラス転移温度以下では高弾性率であ
る。しかし、これらの重合体は特殊なモノマーの重合体
であり経済的に不利である。These polymers are non-crystalline and have a high glass transition temperature, and have a high elastic modulus below the glass transition temperature. However , these polymers are polymers of special monomers and are economically disadvantageous.
【0008】また、特公昭63−18964には、テト
ラフルオロエチレンとパーフルオロ(2,2−ジメチル
−1,3−ジオキソール)すなわちR 1 、R 2 がともにト
リフルオロメチル基である式3で示されるモノマー(以
下、PDDと略記する)との無定形共重合体の開示があ
るが、この共重合体はPDDのホモポリマーに比べてガ
ラス転移温度が低下し、高温での機械物性は低下する。 Further, in JP-B 63-18964, tetrafluoroethylene and perfluoro (2,2-dimethyl
-1,3-dioxole), that is, both R 1 and R 2
There is disclosed an amorphous copolymer with a monomer represented by the formula 3 which is a trifluoromethyl group (hereinafter abbreviated as PDD), but this copolymer has a lower glass transition temperature than a homopolymer of PDD. However, mechanical properties at high temperatures are reduced.
【0009】[0009]
【0010】[0010]
【発明が解決しようとする課題】本発明は、従来知られ
ていなかった高温での機械特性の優れた樹脂を新規に提
供することを目的とする。 SUMMARY OF THE INVENTION It is an object of the present invention shall be the object of providing excellent resin mechanical properties at high temperature has not been known to the new.
【0011】[0011]
【課題を解決するための手段】本発明は、テトラフルオ
ロエチレンに基づく単位95〜99モル%と、下記式
(1)で表されるモノマーに基づく単位1〜5モル%か
らなり、溶融成形が可能であり、容量流速が0.2〜5
0mm 3 /秒である、高温での機械特性の優れたテトラ
フルオロエチレン共重合体を提供する。 CF2 =CFO(CF2 )n CF=CF2 (1) (ここで、nは1〜6の整数である。)Means for Solving the Problems The present invention includes a unit 95 to 99 mol% based on Te tetrafluoroethylene consists unit 1-5 mol% based on the monomer represented by the following formula (1), melt molding And the volume flow rate is 0.2-5
Provided is a tetrafluoroethylene copolymer having excellent mechanical properties at a high temperature of 0 mm 3 / sec . CF 2 = CFO (CF 2) n CF = CF 2 (1) ( wherein, n represents an integer from 1 to 6.)
【0012】重合方法としてはラジカル重合が用いられ
る。すなわち重合方法としては、ラジカル的に進行する
ものであれば手段は何ら制限されず、例えば有機ラジカ
ル開始剤、無機ラジカル開始剤、光、電離放射線または
熱による重合などが挙げられる。ラジカル重合の方法も
バルク重合、溶液重合、懸濁重合並びに乳化重合を用い
ることができる。分子量はモノマー濃度、温度、開始剤
の濃度、連鎖移動剤の濃度などにより制御できる。Radical polymerization is used as the polymerization method. That As the polymerization method, means as long as it proceeds radically is not limited by any means, for example, an organic radical initiator, inorganic radical initiator, light, ionizing radiation or the like thermal polymerization. As the method of radical polymerization, bulk polymerization, solution polymerization, suspension polymerization, and emulsion polymerization can be used. The molecular weight can be controlled by the monomer concentration, temperature, initiator concentration, chain transfer agent concentration, and the like.
【0013】共重合体の重合組成は各々のモノマーの仕
込割合により制御できる。本発明の共重合体中のCF2
=CFO(CF2 )n CF=CF2 に基づく単位の量は
1〜5モル%である。1モル%未満では溶融成形性が悪
く、5モル%超では結晶性が低下し高温での機械特性が
低下する。The polymerization composition of the copolymer can be controlled by the proportion of each monomer charged. CF 2 in the copolymer of the present invention
= Amount of CFO (CF 2) n CF = CF 2 in based units is 1 to 5 mol%. If it is less than 1 mol%, the melt formability is poor, and if it exceeds 5 mol%, the crystallinity is reduced and the mechanical properties at high temperatures are reduced.
【0014】また、容量流速は溶融成形性の指標であ
り、0.2〜50mm 3 /秒である。0.2mm 3 /秒未
満では成形性が悪く、50mm 3 /秒超では機械特性が
低下する。なお、本明細書における容量流速は、島津製
作所製高化式フローテスターを用い、共重合体を内径
9.5mmのシリンダーに入れ、温度380℃で5分間
保った後、7kgのピストン荷重下に内径2.1mm,
長さ8mmのオリフィスを通して押し出し、このときの
押出速度(mm3/秒)である。The volume flow rate is an index of melt moldability, and is 0.2 to 50 mm 3 / sec . 0.2 mm 3 / sec Not <br/> Mitsurude has poor moldability, mechanical characteristics is lowered by 50 mm 3 / sec greater. The volume flow rate in the present specification was measured by using a high flow type flow tester manufactured by Shimadzu Corporation, placing the copolymer in a cylinder having an inner diameter of 9.5 mm, maintaining the temperature at 380 ° C. for 5 minutes, and then applying a 7 kg piston load. Inner diameter 2.1mm,
It is extruded through an orifice having a length of 8 mm and the extrusion speed (mm 3 / sec) at this time.
【0015】また、1種類以上の共重合可能なモノマー
を5モル%を超えない範囲で共重合させることもでき
る。[0015] One or more copolymerizable monomers
May be copolymerized within a range not exceeding 5 mol%.Can
You.
【0016】[0016]
【実施例】実施例1 内容積が1200mlの撹拌機付オートクレーブを脱気
し、1,1,2−トリクロロ−1,2,2−トリフルオ
ロエタン(以下、R113と略記する。)1440g、
メタノール0.9g、CF2 =CFO(CF2 )2 CF
=CF2 (以下、BVEと略記する。)44.4g、テ
トラフルオロエチレン(以下、TFEと略記する。)7
8gを仕込み、50℃に昇温し、ビス(パーフルオロブ
タノイル)パーオキシドの1%R113溶液を1ml添
加し、重合を開始させた。TFEの追加仕込みを行い圧
力を一定に保った。また、TFEの追加仕込量に対して
5.5重量%のBVEを追加仕込みした。ビス(パーフ
ルオロブタノイル)パーオキシドの1%R113溶液
を、重合開始10分後と20分後で各々1ml、40分
後、60分後、70分後、100分後に各々0.5ml
ずつ計4ml後仕込みをした。TFE追加仕込量が82
gになったところで重合を停止した。重合時間は3時間
であった。Example 1 An autoclave equipped with a stirrer having an internal volume of 1200 ml was degassed, and 1,440 g of 1,1,2-trichloro-1,2,2-trifluoroethane (hereinafter abbreviated as R113 ) was used.
0.9 g of methanol, CF 2 CFCFO (CF 2 ) 2 CF
= CF 2 (hereinafter, abbreviated as BVE.) 44.4 g, tetrafluoroethylene (hereinafter referred to as TFE.) 7
8 g was charged, the temperature was raised to 50 ° C., and 1 ml of a 1% R113 solution of bis (perfluorobutanoyl) peroxide was added to initiate polymerization. An additional charge of TFE was made to keep the pressure constant. Further, 5.5% by weight of BVE was additionally charged with respect to the added amount of TFE. 0.5 ml each of 1% R113 solution of bis (perfluorobutanoyl) peroxide was added 10 minutes and 20 minutes after the start of polymerization, 1 ml each, 40 minutes, 60 minutes, 70 minutes, and 100 minutes.
After a total of 4 ml, the mixture was charged. 82 additional TFE charge
When the amount reached g, the polymerization was stopped. The polymerization time was 3 hours.
【0017】得られたスラリー状の共重合体をR113
で洗浄し、100℃で10時間乾燥し87.6gの共重
合体が得られた。この共重合体の組成は酸素の蛍光X線
分析により得られ、TFEに基づく単位/BVEに基づ
く単位=98.5/1.5(モル比)であった。また容
量流速は2.6mm3/秒であった。200℃での引張
破断強度は131kg/cm2、動的粘弾性測定装置
(レオバイブロンDDV、東洋ボールドウィン社製)で
測定した200℃での動的弾性率は7.0×107dy
n/cm2であった。The slurry-like copolymer obtained was R113
And dried at 100 ° C. for 10 hours to obtain 87.6 g of a copolymer. The composition of this copolymer was obtained by X-ray fluorescence analysis of oxygen, and the ratio of units based on TFE / units based on BVE was 98.5 / 1.5 (molar ratio). The volume flow rate was 2.6 mm 3 / sec. The tensile rupture strength at 200 ° C. is 131 kg / cm 2 , and the dynamic elastic modulus at 200 ° C. measured by a dynamic viscoelasticity measuring device (Leo Vibron DDV, manufactured by Toyo Baldwin) is 7.0 × 10 7 dy.
n / cm 2 .
【0018】実施例2〜4、比較例1〜4 実施例1の重合方法で仕込量だけを表1のように変更し
て重合を行った。表2に得られた共重合体の物性を示
す。本発明の共重合体は200℃での引張破断強度及び
200℃での動的弾性率が高いことがわかった。Examples 2 to 4 and Comparative Examples 1 to 4 Polymerization was carried out by the polymerization method of Example 1 except that only the charged amounts were changed as shown in Table 1. Table 2 shows the physical properties of the obtained copolymer. It was found that the copolymer of the present invention had a high tensile strength at break at 200 ° C. and a high dynamic modulus at 200 ° C.
【0019】[0019]
【表1】 [Table 1]
【0020】[0020]
【表2】 [Table 2]
【0021】[0021]
【発明の効果】本発明のテトラフルオロエチレン共重合
体は高温での機械特性が優れていて、高温で使用される
成形品やフィルム、シート、ライニング、電線被覆材料
として用いることができる。Industrial Applicability The tetrafluoroethylene copolymer of the present invention has excellent mechanical properties at high temperatures and can be used as a molded article, a film, a sheet, a lining and a wire covering material used at high temperatures.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C08F 214/26 C08F 216/12 - 216/20 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) C08F 214/26 C08F 216/12-216/20
Claims (1)
〜99モル%と、下記式(1)で表されるモノマーに基
づく単位1〜5モル%からなり、溶融成形が可能であ
り、容量流速が0.2〜50mm 3 /秒である、高温で
の機械特性の優れたテトラフルオロエチレン共重合体。 CF2 =CFO(CF2 )n CF=CF2 (1) (ここで、nは1〜6の整数である。)1. Unit 95 based on tetrafluoroethylene
And 99 mol% consists of units 1-5 mol% based on the monomer represented by the following formula (1), is capable of melt molding, volume flow rate is 0.2 to 50 mm 3 / sec, the hot so
A tetrafluoroethylene copolymer having excellent mechanical properties . CF 2 = CFO (CF 2) n CF = CF 2 (1) ( wherein, n represents an integer from 1 to 6.)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP35383691A JP3124348B2 (en) | 1991-12-18 | 1991-12-18 | Tetrafluoroethylene copolymer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP35383691A JP3124348B2 (en) | 1991-12-18 | 1991-12-18 | Tetrafluoroethylene copolymer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05170834A JPH05170834A (en) | 1993-07-09 |
JP3124348B2 true JP3124348B2 (en) | 2001-01-15 |
Family
ID=18433546
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP35383691A Expired - Fee Related JP3124348B2 (en) | 1991-12-18 | 1991-12-18 | Tetrafluoroethylene copolymer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3124348B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4466002B2 (en) * | 2002-12-06 | 2010-05-26 | 旭硝子株式会社 | Tetrafluoroethylene copolymer, process for producing the same, and paste extrusion molding |
CN1295259C (en) * | 2002-12-06 | 2007-01-17 | 旭硝子株式会社 | Tetrafluoroethylene copolymer, method for producing the same and paste extrusion molded product |
-
1991
- 1991-12-18 JP JP35383691A patent/JP3124348B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH05170834A (en) | 1993-07-09 |
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