JPH02110156A - Fluororesin molding - Google Patents
Fluororesin moldingInfo
- Publication number
- JPH02110156A JPH02110156A JP26352188A JP26352188A JPH02110156A JP H02110156 A JPH02110156 A JP H02110156A JP 26352188 A JP26352188 A JP 26352188A JP 26352188 A JP26352188 A JP 26352188A JP H02110156 A JPH02110156 A JP H02110156A
- Authority
- JP
- Japan
- Prior art keywords
- fluororesin
- liquid crystal
- resistance
- polymer
- molding
- 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.)
- Granted
Links
- 238000000465 moulding Methods 0.000 title abstract description 18
- 229920000642 polymer Polymers 0.000 claims abstract description 22
- 229920001577 copolymer Polymers 0.000 claims abstract description 19
- -1 polychlorotrifluoroethylene Polymers 0.000 claims abstract description 14
- 229920000139 polyethylene terephthalate Polymers 0.000 claims abstract description 5
- 239000005020 polyethylene terephthalate Substances 0.000 claims abstract description 5
- 239000004417 polycarbonate Substances 0.000 claims description 8
- 229920000515 polycarbonate Polymers 0.000 claims description 7
- 230000001747 exhibiting effect Effects 0.000 claims description 5
- 229920001230 polyarylate Polymers 0.000 claims description 4
- 229920000106 Liquid crystal polymer Polymers 0.000 abstract description 39
- 239000004977 Liquid-crystal polymers (LCPs) Substances 0.000 abstract description 39
- 239000000126 substance Substances 0.000 abstract description 8
- FJKROLUGYXJWQN-UHFFFAOYSA-N 4-hydroxybenzoic acid Chemical compound OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 abstract description 5
- 238000005299 abrasion Methods 0.000 abstract description 5
- 239000000203 mixture Substances 0.000 abstract description 5
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 abstract description 5
- 229920002493 poly(chlorotrifluoroethylene) Polymers 0.000 abstract description 3
- 239000005023 polychlorotrifluoroethylene (PCTFE) polymer Substances 0.000 abstract description 3
- 229940090248 4-hydroxybenzoic acid Drugs 0.000 abstract description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract description 2
- 239000005977 Ethylene Substances 0.000 abstract description 2
- 229920001774 Perfluoroether Polymers 0.000 abstract description 2
- 230000003247 decreasing effect Effects 0.000 abstract 2
- 238000010186 staining Methods 0.000 abstract 2
- 239000011347 resin Substances 0.000 description 14
- 229920005989 resin Polymers 0.000 description 14
- 229920000728 polyester Polymers 0.000 description 10
- 125000003118 aryl group Chemical group 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 239000008188 pellet Substances 0.000 description 6
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 5
- 229910052731 fluorine Inorganic materials 0.000 description 5
- 239000011737 fluorine Substances 0.000 description 5
- 239000004973 liquid crystal related substance Substances 0.000 description 5
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 4
- 238000004898 kneading Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 229920003232 aliphatic polyester Polymers 0.000 description 3
- 206010061592 cardiac fibrillation Diseases 0.000 description 3
- 229920000840 ethylene tetrafluoroethylene copolymer Polymers 0.000 description 3
- 230000002600 fibrillogenic effect Effects 0.000 description 3
- 238000001746 injection moulding Methods 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004642 Polyimide Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 2
- HJJVPARKXDDIQD-UHFFFAOYSA-N bromuconazole Chemical compound ClC1=CC(Cl)=CC=C1C1(CN2N=CN=C2)OCC(Br)C1 HJJVPARKXDDIQD-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical group FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 229920000343 polyazomethine Polymers 0.000 description 2
- 229920001721 polyimide Polymers 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- XKZQKPRCPNGNFR-UHFFFAOYSA-N 2-(3-hydroxyphenyl)phenol Chemical compound OC1=CC=CC(C=2C(=CC=CC=2)O)=C1 XKZQKPRCPNGNFR-UHFFFAOYSA-N 0.000 description 1
- 239000005711 Benzoic acid Substances 0.000 description 1
- 229920002430 Fibre-reinforced plastic Polymers 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- 229920006367 Neoflon Polymers 0.000 description 1
- RSPISYXLHRIGJD-UHFFFAOYSA-N OOOO Chemical compound OOOO RSPISYXLHRIGJD-UHFFFAOYSA-N 0.000 description 1
- 239000004419 Panlite Substances 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 235000010233 benzoic acid Nutrition 0.000 description 1
- 238000000071 blow moulding Methods 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical compound FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000032798 delamination Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 238000000635 electron micrograph Methods 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 125000000219 ethylidene group Chemical group [H]C(=[*])C([H])([H])[H] 0.000 description 1
- 239000011151 fibre-reinforced plastic Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 125000004957 naphthylene group Chemical group 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 125000000843 phenylene group Chemical group C1(=C(C=CC=C1)*)* 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000002076 thermal analysis method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、熱膨張率の低減され、且つ優れた機械的物性
および成形加工性を有するふりS系楕脂成形体に関する
。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a Furi S-based ellipsoid molded article having a reduced coefficient of thermal expansion and excellent mechanical properties and moldability.
(従来の技術)
ポリクロロ三ふっ化エチレン、エチレン−四ふつ化エチ
レン共重合体、四ふっ化エチレンー六ぶつ化プロピレン
共重合体、ノ曵−フルオロアルフキシふっ素樹脂等のふ
っ素系樹脂は第1表に示す如き広い使用温度を有し、成
形性が良く。(Prior art) Fluorine resins such as polychlorotrifluoroethylene, ethylene-tetrafluoroethylene copolymer, tetrafluoroethylene-hexabutylene propylene copolymer, and non-fluoroalfoxy fluororesin are shown in Table 1. It can be used over a wide range of temperatures as shown in Figure 2, and has good moldability.
耐薬品性、耐アルカリ性、耐酸性、耐水性、耐摩
候性、耐食性、耐耗性、電気絶縁性等がすぐれているの
でノ曵イブ、パルプ、ポンプ等のライニング材、フレキ
シブルチューブ、フィルム、クエハーバスケット、ポン
プインペラー、機械部品、化学実験器具など広い用途に
使用されている。It has excellent chemical resistance, alkali resistance, acid resistance, water resistance, weather resistance, corrosion resistance, abrasion resistance, electrical insulation, etc., so it can be used as a lining material for pumps, flexible tubes, films, etc. It is used in a wide range of applications such as hearth baskets, pump impellers, mechanical parts, and chemical laboratory equipment.
第 1
麦
しかし、ふっ素系樹脂は線膨張系数が大きいため、温度
変化の激しい条件下あるいは高温領域での使用によって
熱的に変化する場合がある。However, since fluororesin has a large linear expansion coefficient, it may undergo thermal changes when used under conditions of rapid temperature changes or in high-temperature areas.
従ってふっ素系樹脂成形体は、特にエレクトロニクス分
野において高精度が要求される部品、化学装置に使用さ
れる/曵イブやライニング材に応用することは困難であ
る。Therefore, it is difficult to apply fluororesin molded bodies to parts that require high precision, especially in the electronics field, and to eaves and lining materials used in chemical equipment.
成形体の線膨張係数を低減するため(、石綿等との複合
成形体とすること、金属材や繊維強化プラスチック(F
RP )との積層体とすること等が考えられる。しかし
ながら、このような複合成形体は、たとえ大量の充填材
を使用してもふっ素系樹脂の線膨張係数が充分には低減
されず、逆にふっ素系樹脂が有していた優れた表面特性
(摩擦特性や摩耗特性)が損なわれる。In order to reduce the linear expansion coefficient of the molded product (to make it a composite molded product with asbestos, etc.), use metal materials and fiber reinforced plastics (F
It is conceivable to form a laminate with RP). However, in such composite molded bodies, even if a large amount of filler is used, the coefficient of linear expansion of the fluororesin cannot be sufficiently reduced, and on the contrary, the excellent surface properties ( (friction and wear characteristics) are impaired.
他方、積層体の場合は、物性的には解決されるが、積層
化による重量の増加、線膨張係数の追いによる層間剥離
、成形加工性の自由度低下等の新たな問題が新たに発生
する。On the other hand, in the case of laminates, although this is solved physically, new problems arise, such as an increase in weight due to lamination, delamination due to increasing coefficient of linear expansion, and reduced flexibility in molding processability. .
(本発明が解決しようとする問題点)
本発明が上記従来の問題点を解決するものであり、その
目的とするところは、ふつ巣系樹脂の優れた耐候性、耐
薬品性、耐摩耗性、耐汚染性等の特性を損なうこと無く
、線膨張係数が大幅に低減され、更に優れた機械的物性
および成形加工性をも併せ持つふっ素系樹脂成形体を提
供することにある。(Problems to be Solved by the Present Invention) The present invention solves the above-mentioned conventional problems, and its purpose is to improve the excellent weather resistance, chemical resistance, and abrasion resistance of the fuss-based resin. The object of the present invention is to provide a fluororesin molded article which has a significantly reduced coefficient of linear expansion without impairing properties such as stain resistance, and also has excellent mechanical properties and moldability.
(問題を解決するための手段)
本発明で使用されるふっ素系樹脂は、ポリクロロ三ふっ
化エチレン、エチレン−四ぶつ化エチレン共重合体、四
ふつ化エチレンー六ふつ化グロビレン共11合体及ヒノ
I −7ルオo 7 tしニア キシふっ素樹脂よりな
る群から選ばれたものである0
上記ポリクロロ三ふつ化エチレンは通常の溶融成形が可
断なものであればよく、その重合度は500〜3000
程度のものが好ましい。(Means for solving the problem) The fluororesin used in the present invention is polychlorotrifluoroethylene, ethylene-tetrafluoroethylene copolymer, tetrafluoroethylene-hexafluoroglobylene co-11 polymer, and Hino I The above polychlorotrifluoroethylene may be one that can be broken by ordinary melt molding, and its degree of polymerization is from 500 to 3,000.
It is preferable that the degree of
上記エチレン−四ふつ化エチレン共重合体は、エチレン
と四ふつ化エチレンの共重合体であり、共重合比率は8
:2〜2:8のものが好ましい。The above ethylene-tetrafluoroethylene copolymer is a copolymer of ethylene and tetrafluoroethylene, and the copolymerization ratio is 8.
:2 to 2:8 is preferred.
上記四ふっ化エチレンー六ぶつ化プロピレン共重合体は
、四ふつ化エチレンと六ふつ化プロピレンの共重合体で
あり、六ふつ化プロピレンの含量はlO〜20mo1%
が好ましい。The above-mentioned tetrafluoroethylene-hexafluoropropylene copolymer is a copolymer of tetrafluoroethylene and hexafluoropropylene, and the content of hexafluoropropylene is 10 to 20 mo1%.
is preferred.
上E/’−フルオロアルコキシふっ素樹脂は四ふつ化エ
チレンと/(−フルオロアルキルビニルエーテルの共重
合体であり、)曵−フルオロアルキルビニルエーテルの
含量は1〜10mo1%が好ましく、アルキル基は炭素
数1〜lOのものが好ましい。The above E/'-fluoroalkoxyfluororesin is a copolymer of tetrafluoroethylene and/(-fluoroalkyl vinyl ether), and the content of the fluoroalkyl vinyl ether is preferably 1 to 10 mo1%, and the alkyl group has 1 carbon number. ~10 is preferred.
本発明で使用される異方性溶融形態を示す重合体(b)
(以下液晶ポリマーと称す)としては、芳香族−脂肪族
ポリエステル、全芳香族ポリエステル、芳香族ポリアゾ
メチン、ポリイミドエステル等が挙げられ、これらのう
ち異方性溶融形態を示す化合物が選択される。芳香族−
脂肪族ポリエステルとしては、例えばポリエチレンテレ
フタレートとパラヒドロキシ安息香酸との共重合体があ
る。全芳香族ポリエステルとしては、例えばバラヒドロ
キシ安息香酸と6−ヒドロキシ−2−す7トエ酸との共
重合体;又はノ曵うヒドロキシ安息香酸、テレフタル酸
及び6−ヒドロキシ−2−す7トールの共重合体がある
。Polymer (b) exhibiting anisotropic melt morphology used in the present invention
Examples of the liquid crystal polymer (hereinafter referred to as liquid crystal polymer) include aromatic-aliphatic polyesters, wholly aromatic polyesters, aromatic polyazomethines, polyimide esters, and among these, compounds exhibiting an anisotropic melt morphology are selected. Aromatic-
Examples of aliphatic polyesters include copolymers of polyethylene terephthalate and parahydroxybenzoic acid. Examples of wholly aromatic polyesters include copolymers of hydroxybenzoic acid and 6-hydroxy-2-7-toic acid; There are copolymers.
芳香族ポリアゾメチンとしては、例えばポリにトリロー
2−メチル−1,4−フェニレンニトロエチリテイン−
1,4−7二二レンエチリデイン)等がある。ポリイミ
ドエステルとしては、例えば2.6−す7タレンジカル
ポン酸、テレフタル酸及び4(4′−ヒドロキシフタル
イミド)フェノールの共重合体、又はジフェノールト4
− (4’−ヒドロキシ7タルイミド)安息香酸から誘
導される共重合体等がある。As the aromatic polyazomethine, for example, polytrilo-2-methyl-1,4-phenylenenitroethyriteine-
1,4-7 22lene ethylidene), etc. As the polyimide ester, for example, a copolymer of 2,6-s7tale dicarboxylic acid, terephthalic acid and 4(4'-hydroxyphthalimide)phenol, or a diphenol 4
- Copolymers derived from (4'-hydroxy 7-talimide) benzoic acid, etc.
これらの共重合体が液晶ポリマーであることを判別する
には、液晶ポリマーが溶融状態で光学的異方性を示しえ
ることを利用するとよい。In order to determine whether these copolymers are liquid crystal polymers, it is preferable to utilize the fact that liquid crystal polymers can exhibit optical anisotropy in a molten state.
光学的異方性t1、通常の偏光!lll−鏡を用いるこ
とによって確認しうる。例えば加熱ステージ上に1關以
下の厚さに調整さhた試験片を置き、窒素雰囲気下で2
℃/始程度の昇温速度で加熱してゆく。この状態で偏光
顕微鏡の偏光子と検光子を直交させ、40倍もしくは1
00倍の倍率で観測することにより容易にa11駆する
ことができる。このような方法では、また同時に、これ
ら共重合体が液晶相に転移する温度も測定し得る。この
ことは熱分析(例えばDSC%TMA等)によっても測
定可能な場合がある。Optical anisotropy t1, normal polarization! This can be confirmed by using a lll-mirror. For example, place a test piece adjusted to a thickness of 1 inch or less on a heating stage, and heat it for 2 hours under a nitrogen atmosphere.
Heating is continued at a temperature increase rate of approximately ℃/starting temperature. In this state, the polarizer of the polarizing microscope and the analyzer are crossed at right angles, and
A11 drive can be easily detected by observing at a magnification of 00x. In such a method, it is also possible to simultaneously measure the temperature at which these copolymers transition to a liquid crystal phase. This may also be measurable by thermal analysis (eg, DSC%TMA, etc.).
上記液晶ポリマーとしては、第1表に示したふっ素系欄
gr1−の成形温度範囲で異方性溶融形態を示す重合体
が好適に使用される。As the liquid crystal polymer, a polymer exhibiting an anisotropic melt morphology in the molding temperature range of the fluorine column gr1- shown in Table 1 is preferably used.
換言すると、本発明の成形体はふっ素系樹脂と、それが
熱分解を起こさずに溶融する温度範囲と部分的に重複す
る湿度範囲内で異方性溶融形態を示しえる(即ち溶融可
能である)液晶ポリマーとで構成されているのが好まし
い。In other words, the molded article of the present invention can exhibit an anisotropic melt morphology (i.e., can be melted) within a humidity range that partially overlaps the temperature range in which the fluororesin melts without thermal decomposition. ) is preferably composed of a liquid crystal polymer.
なぜなら、本発明における成形体の製造手段としては、
一般に、上記組成物を溶融状態で互いに分散させる工程
を包含する方法が用いられるためである。このような方
法に於て、組成物を構成するふっ素系樹脂と液晶ポリマ
ーとのうちいずれか一方が熱分解を起こすような場合に
は、得られた成形体の物理的特性が低下するため好まし
くない。前述の通り、ふっ素系樹脂の成形温度は300
〜400’Cとされているので、このような温度範囲で
成形可能な液晶ポリマーを選ぶことが好ましい。従って
、上記の液晶ポリマーのうち、特に、芳香族−脂肪族ポ
リエステル、および全芳香族ポリエステルが好適である
。This is because, as a means for producing a molded article in the present invention,
This is because a method is generally used that includes a step of dispersing the above compositions in a molten state. In such a method, if either the fluororesin or the liquid crystal polymer constituting the composition undergoes thermal decomposition, the physical properties of the obtained molded product will deteriorate, so this is not preferred. do not have. As mentioned above, the molding temperature of fluororesin is 300
~400'C, so it is preferable to select a liquid crystal polymer that can be molded in this temperature range. Therefore, among the above liquid crystal polymers, aromatic-aliphatic polyesters and wholly aromatic polyesters are particularly suitable.
上述した液晶ポリマー単独の成形体は、通常優れた機械
的物性(例えば強度、弾性率、および衝撃強度)を有す
る。更に射出成形や押し出し成形によって得られた成形
体は、溶融時にポリマー分子が梼脂の流れ方向に対して
平行に配向することにより、増強された機械的物性を示
す。これは液晶ポリマーが異方性溶融形態を示すが故の
自己補強効果であり、その増強度はポリマー分子の配向
程度によって支配されている。The above-mentioned molded body made of liquid crystal polymer alone usually has excellent mechanical properties (eg, strength, elastic modulus, and impact strength). Furthermore, molded bodies obtained by injection molding or extrusion molding exhibit enhanced mechanical properties due to the orientation of the polymer molecules parallel to the flow direction of the resin during melting. This is a self-reinforcing effect because the liquid crystal polymer exhibits an anisotropic melt morphology, and the degree of reinforcement is controlled by the degree of orientation of the polymer molecules.
即ち液晶ポリマーの溶融成形体の機械的物性は、成形の
方法および/または成形体の形状によってしばしば異な
る。また同じ理由により液晶ポリマーの成形体は、機械
的物性に関して顕著な異方性を示す。加えて液晶ポリマ
ーはその分子構造が線状であるため、通常極めて小さな
線膨張係数(熱膨張率)を有する。しかも成形体におい
ては流動に平行な方向に対しては、更に小さい値を示す
ことも認められている。本発明のふっ素系樹脂成形体は
、このような特性を有する液晶ポリマーとふっ素系樹脂
とな含有するため、ふっ素系樹脂のみからなる成形体に
比べて線膨張係数が低減され、しかも、この成形体は機
械的物性と成形加工性にも優れる。That is, the mechanical properties of a melt molded body of a liquid crystal polymer often differ depending on the molding method and/or the shape of the molded body. Furthermore, for the same reason, molded bodies of liquid crystal polymers exhibit significant anisotropy in terms of mechanical properties. In addition, since the liquid crystal polymer has a linear molecular structure, it usually has an extremely small coefficient of linear expansion (coefficient of thermal expansion). Moreover, it has been recognized that in molded bodies, the value is even smaller in the direction parallel to the flow. Since the fluororesin molded article of the present invention contains a liquid crystal polymer having such characteristics and a fluororesin, the coefficient of linear expansion is lower than that of a molded article made only of fluororesin. The body also has excellent mechanical properties and moldability.
本発明のふっ素系樹脂成形体を構成するふっ素系樹脂(
a)と液晶ポリマー(blの重量割合は6゜:40〜9
7:3であり、好ましくは70:30〜95:5である
。液晶ポリマーが5重量%を下回ると線膨張係数の低減
効果が期待できない。また、40重量%近くになるとそ
の効果がほば一定値に収束し、40重量%を越えると、
液晶ポリ!−のフィブリルが微細化し難く、成形体の物
理的な緻密さが得られなくなるからである。Fluorine resin (
The weight ratio of a) and liquid crystal polymer (bl is 6°:40-9
The ratio is 7:3, preferably 70:30 to 95:5. If the content of the liquid crystal polymer is less than 5% by weight, no effect of reducing the coefficient of linear expansion can be expected. In addition, when it approaches 40% by weight, the effect converges to a constant value, and when it exceeds 40% by weight,
LCD poly! This is because the fibrils of - are difficult to miniaturize, making it impossible to obtain physical compactness of the molded article.
又、2番目の発明においては、さらにポリアリレート、
ポリエチレンテレフタレート及びポリカーボネートより
なる群から選ばれた一種以上のポリマー(clを含有す
る。ポリマー(c)はふっ素系樹脂と液晶ポリマーの相
溶性を向上させる。Furthermore, in the second invention, polyarylate,
One or more polymers (containing Cl) selected from the group consisting of polyethylene terephthalate and polycarbonate. Polymer (c) improves the compatibility between the fluororesin and the liquid crystal polymer.
ふっ素系樹脂と液晶ポリマーはその界面における親和性
が小さいが上記ポリマーを添加すると相溶性が向上し、
成形体が緻密になり表面の平滑性や機械的物性が向上す
る。The compatibility between fluororesin and liquid crystal polymer is small at the interface, but adding the above polymer improves the compatibility.
The molded product becomes denser and its surface smoothness and mechanical properties improve.
上記ポリアリレートとはビスフェノールAとテレフタル
酸もしくはイソフタル酸の共重合体である。ポリアリレ
ートは通常の溶融成形が可能なものであればよいが、そ
の分子量は1000〜40. OOO程度であることが
好ましい。The above polyarylate is a copolymer of bisphenol A and terephthalic acid or isophthalic acid. The polyarylate may be of any type as long as it can be melt-molded, but its molecular weight is between 1000 and 40. It is preferable that it is about OOO.
上記ポリエチレンテレフタレートとは下式で示される線
状ポリエステルであって、分子量が1000〜40.
OOOOものが好ましい。The above-mentioned polyethylene terephthalate is a linear polyester represented by the following formula, and has a molecular weight of 1000 to 40.
OOOO is preferable.
又、上記ポリカーボネートとは主鎖にカーボであり、次
式で示される高分子化合物が好適に使用され、特にビス
フェノールAとホスゲンの反応から得られるものが好ま
しい。又、分子量は2000〜40.000のものが好
ましい。The above-mentioned polycarbonate has carbon in its main chain, and polymer compounds represented by the following formula are preferably used, and those obtained from the reaction of bisphenol A and phosgene are particularly preferred. Further, the molecular weight is preferably 2000 to 40,000.
(式中 R1はフェニレン基、)・ロダンもしくはアル
キル置換フェニレン基又はナフチレン基を示し、R1は
水素もしくは炭素飲10以下のアルキル基を示す。)
上記ポリマー(clの割合はふっ素yF、m脂!a)と
液晶ポリマーfblの合計量100重量部に対し、1〜
20重量部であり、好ましくは2〜10重量部である。(In the formula, R1 is a phenylene group,) represents a rhodane or alkyl-substituted phenylene group or a naphthylene group, and R1 represents hydrogen or an alkyl group having 10 or less carbon atoms. ) 1 to 100 parts by weight of the total amount of the above polymer (Cl ratio is fluorine yF, m fat!a) and liquid crystal polymer fbl.
The amount is 20 parts by weight, preferably 2 to 10 parts by weight.
ボIJ−r−の添加量が少なくなるとふっ素系樹脂と液
晶ポリマーの相溶性を向上させる効果がなくなり、20
重量部を越えると、ふっ素系樹脂が有する優れた耐薬品
性、耐候性等の特性が損なわれる。When the amount of IJ-r- added decreases, the effect of improving the compatibility between the fluororesin and the liquid crystal polymer disappears, and 20
If the amount exceeds 1 part by weight, the excellent properties of the fluororesin, such as chemical resistance and weather resistance, will be impaired.
又、本発明においては若干の物性改良、および成形性の
安定化を目的とし、ガラス繊維、無機充填剤、改質剤、
滑剤、熱安定剤、可暖剤等が添加されてもよい。In addition, in the present invention, for the purpose of slightly improving physical properties and stabilizing moldability, glass fibers, inorganic fillers, modifiers,
A lubricant, a heat stabilizer, a warming agent, etc. may be added.
本発明のふっ素系樹脂成形体は、−膜内に溶融成形によ
って製造される。このような製造方法としては、ふっ素
系樹脂、液晶ポリマー およびポリマーのポリマーブレ
ンドの溶融物を成形する任意の成形方法が挙げられる。The fluororesin molded article of the present invention is produced by melt molding into a membrane. Such manufacturing methods include any molding method that molds a melt of a polymer blend of a fluororesin, a liquid crystal polymer, and a polymer.
例えば、ふっ素系樹脂、液晶ポリ!−及びポリマーを溶
融、混疎し、引き続いて押し出し成形、プロー成形、射
出成形、カレンダー成形等rこよって成形される。For example, fluorine resin, liquid crystal polyester! - and polymers are melted, mixed, and subsequently molded by extrusion molding, blow molding, injection molding, calender molding, etc.
このような成形時に於て液晶ポリマーは、溶融状態で伸
張流動や剪断流動を受けることにより容易tこフィブリ
ル形態を形成し、しかも実質的にその長軸が互いに平行
に配列することがしばしば認められる。かかるフィブリ
ルの配向程度は線膨張係数を低減させるのに効果的であ
る。During such molding, it is often observed that the liquid crystal polymer easily forms a fibrillar shape by being subjected to extensional flow or shear flow in the molten state, and that the long axes of the polymers are substantially aligned parallel to each other. . This degree of fibril orientation is effective in reducing the coefficient of linear expansion.
従って、液晶ポリマーのフィブリル化を促進させ、フィ
ブリルの配向度を高める手段を用いることが有用である
。例えば押し出し成形では、成形機にスタテイクミルを
直列に配置させると効果的である。これは押し出し機中
で充分に分散したブレンド体がスタテイクミル内を通過
する際に液晶状態にある液晶ポリマーtこ対して効率的
に伸張流動や剪断流動を付加させる為である。同じ理由
で押し出し機のヘッド部分に比較的小径の通路を有する
プレーカーを設けること、目間き径約IJrl11以下
のメツシュを設けることが有用である。これは溶融樹脂
の流路に絞り込まれた通路を設け、流体が該通路を通過
する時に圧力勾配を発生させ、特tこ流線方向に速度分
布を与えることで伸張力を高める手法である。更には成
形物が冷却固化する迄に1軸もしくは2軸方向に延伸さ
せることは、液晶ポリ!−のフィブリル化が著しくなる
ため、極めて有効な手段である。また射出成形tこおい
ては、−膜内な方法でも液晶ポリマーのフィブリル化は
ある程度期待できるが、さらに向上を期待する場合は、
金型内での樹脂のせん断速度を大きくすること(例えば
射出速度を上げること、ノズルやスプールをコニカル形
状にすること、金型の長さ/厚み比(L/T)を大きく
すること)等が有効である。Therefore, it is useful to use a means to promote fibrillation of the liquid crystal polymer and increase the degree of fibril orientation. For example, in extrusion molding, it is effective to arrange a static mill in series with the molding machine. This is in order to efficiently add elongation flow and shear flow to the liquid crystal polymer t which is in a liquid crystal state when the blend sufficiently dispersed in the extruder passes through the static mill. For the same reason, it is useful to provide the extruder head with a breaker having relatively small diameter passages, and to provide a mesh with a mesh diameter of about IJrl11 or less. This is a method of increasing the tensile force by providing a constricted passage in the flow path of the molten resin, generating a pressure gradient when the fluid passes through the passage, and giving a velocity distribution, especially in the streamline direction. Furthermore, stretching the molded product in one or two axes until it cools and solidifies is the best way to use liquid crystal polyester! This is an extremely effective means because the fibrillation of - becomes significant. In addition, in injection molding, fibrillation of liquid crystal polymer can be expected to some extent even with the in-film method, but if further improvement is expected,
Increasing the shear rate of the resin within the mold (e.g. increasing the injection speed, making the nozzle or spool conical, increasing the length/thickness ratio (L/T) of the mold), etc. is valid.
このよう「こして得られる成形体においては、ふっ素系
樹脂中に液晶ポリマーの長繊維(フィブリル)が均一に
分散しているために、ふっ素系樹脂のみからなる成形体
と比較して小さい線膨張係数を示す。しかも、成形体は
改善された機械的物性を有する。なぜなら液晶ポリマー
はフィブリル形態を取るとぎに、そのポリマーの分子が
最も高い配向状WAにあるため、より大きい弾性率とよ
り小さい(時には負の値をも示す)線膨張係数を併せ持
ち、液晶ポリマーを含存する成形体の線膨張係数を低減
するのに特に効果的と考えられるからである。上記液晶
ポリマーのフィブリルは、好ましくは、その直径が10
0μmまたはそれ以下である。特にこのフィブリルの平
均長さ/直径比(L/D )が大きいほど効果的で、好
ましくは10またはそれ以上、さらに好ましくは100
またはそれ以上である。In the molded product obtained by straining, the long fibers (fibrils) of the liquid crystal polymer are uniformly dispersed in the fluororesin, so the linear expansion is smaller than that of a molded product made only of fluororesin. Moreover, the molded body has improved mechanical properties because when the liquid crystal polymer takes the fibrillar form, the molecules of the polymer are in the highest oriented WA, resulting in a larger elastic modulus and a smaller This is because it has a coefficient of linear expansion (sometimes showing a negative value) and is considered to be particularly effective in reducing the coefficient of linear expansion of a molded article containing a liquid crystal polymer.The fibrils of the liquid crystal polymer are preferably , whose diameter is 10
0 μm or less. In particular, the larger the average length/diameter ratio (L/D) of the fibrils, the more effective it is, preferably 10 or more, more preferably 100
or more.
このような形状を有する液晶ポリマーのフィブリルが分
散されていることrこより、ふっ素系樹脂成形体の線膨
張係数が、ふっ素系樹脂のみからなる成形体に比べて充
分に低い値を示す。また、フィブリルが成形体中におい
て実質的に一軸配向していれば、該方向の線膨張係数は
選択的に低減され好ましい。Because the fibrils of the liquid crystal polymer having such a shape are dispersed, the coefficient of linear expansion of the fluororesin molded article exhibits a sufficiently lower value than that of a molded article made only of fluororesin. Further, it is preferable that the fibrils are substantially uniaxially oriented in the molded article because the coefficient of linear expansion in this direction is selectively reduced.
本発明のふっ素系樹脂成形体は、シート状、棒状、フィ
ルム状、パイプ状、繊維状、塊状など所望の形状に成形
される。本発明の成形体は、各種の強酸や溶剤下で使用
されるパイプ、チューブ、フィルム、ライニング材、バ
ルブシート、フィルター等のプラント部材、機械部品、
電子部品等として幅広い用途に応用される。The fluororesin molded article of the present invention is molded into a desired shape such as a sheet, rod, film, pipe, fiber, or block. The molded product of the present invention can be used in plant parts such as pipes, tubes, films, lining materials, valve seats, filters, etc. used under various strong acids and solvents, machine parts, etc.
It is used in a wide range of applications such as electronic components.
(実施例) 次に本発明の詳細な説明する。(Example) Next, the present invention will be explained in detail.
実施例1〜4、比較例1.2
第−表に示した所定量のポリクロロ三ふっ化エチレン(
ダイキン社製:ダイ70ンCTFE、表中ΩCTFE)
、全芳香族ポリエステル+!晶ポリマー(ポリプラスチ
ックス社製: VECTRA A950、表中LCP
)、及びポリカーボネート(帝人化成社製:)へンライ
トL−1225、表中pc)を充分に乾燥した後、二軸
混練押し出し機に供給し、樹脂温度330℃にて2成分
もしくは3成分の溶融混練を充分に行った後約3闘径の
ストランド状成形物として押し出し、それをペレタイザ
ーを用いて長さ約4鰭に切断してベレットを得た。得ら
れたベレットを25朋単軸押し出し機に供給しシート状
成形体に成形した。ここで、押し出し機シリンダー内に
おける樹脂温度は330℃、スクリュー回転数は40r
pmであった。又、押し出し機の成形ダイの開口寸法は
厚み3關、幅50 m s設定温度は290℃であった
。押し出し機の、押し出す方向の延長線上「こ、成形体
を冷却する水槽、および成形体を引き取るロール引き取
り機をそれぞれ設置し、引き取り機の引き取り速度を変
えて成形体を延伸した。Examples 1 to 4, Comparative Example 1.2 A predetermined amount of polychlorotrifluoroethylene (
Manufactured by Daikin: Dai70-inch CTFE, ΩCTFE in the table)
, fully aromatic polyester+! Crystalline polymer (manufactured by Polyplastics: VECTRA A950, LCP in the table)
), and polycarbonate (manufactured by Teijin Kasei Co., Ltd.: Henrite L-1225, pc in the table) were sufficiently dried, then fed to a twin-screw kneading extruder, and the two or three components were melted at a resin temperature of 330°C. After thorough kneading, the mixture was extruded into a strand-like molded product with a length of about 3 diameters, and cut into lengths of about 4 fins using a pelletizer to obtain pellets. The obtained pellets were fed into a 25 mm single screw extruder and molded into a sheet-like molded product. Here, the resin temperature in the extruder cylinder is 330°C, and the screw rotation speed is 40r.
It was pm. Further, the opening dimensions of the molding die of the extruder were 3 mm thick, 50 ms wide, and the set temperature was 290°C. A water tank for cooling the molded body and a roll take-up machine for taking up the molded body were installed on the extension line of the extruder in the extrusion direction, and the molded body was stretched by changing the take-up speed of the take-off machine.
尚、延伸比は次式で計算した。Note that the stretching ratio was calculated using the following formula.
得られたシート状成形体をジメチルアセトアミドで溶解
し、伐ったフィブリルの偏光顕微鏡写真(100倍)か
ら液晶ポリマーのフィブリルの平均長さ(L)を測定し
、成形体の断面の電子顕微鏡写真(1000倍)からフ
ィブリルの直径(D)を測定し、L/Dを求めた。The obtained sheet-like molded body was dissolved in dimethylacetamide, and the average length (L) of the liquid crystal polymer fibrils was measured from a polarized light micrograph (100x magnification) of the cut fibrils, and an electron micrograph of the cross section of the molded body ( The diameter (D) of the fibril was measured from a magnification of 1000 times, and L/D was determined.
得られたシート状成形体の押出し方向の弓張試M(AS
TM D 638に準拠)を行うと共に、同方向の
線膨張係数(ASTM D696に準拠)を測定した
。得られた結果を第2表に示した。Bow tension test M (AS
TM D 638), and the coefficient of linear expansion in the same direction (based on ASTM D696) was measured. The results obtained are shown in Table 2.
(以下余白)
ロンETFE、表中ETFE)、全芳香族ポリエステル
液晶ポリ!−(ポリプラスチックス社製: VECTR
A A950、表中LCP)及びポリカーボネート(今
人化成社製:)曵ンライトL−1225、表中pc)を
充分に乾燥した後、二軸混練押し出し機を用い、樹脂温
度310℃にて2成分もしくは3成分の溶融混線を充分
に行って約3B径のストランド状成形物として押し出し
、それをペレタイザーを用いて長さ約4 vrs C切
断してベレットを得た。得られたベレットを使用し、押
し出し機シリンダー内における樹脂温度を330℃にし
、成形ダイの設定温度を300℃にした以外は実施例1
で行ったと同様にしてシート状成形体を得、物性を測定
し、結果を第3表に示した。(Left below) Ron ETFE, ETFE in the table), fully aromatic polyester liquid crystal poly! - (Manufactured by Polyplastics: VECTR
After thoroughly drying A950 (LCP in the table) and polycarbonate (manufactured by Konjin Kasei Co., Ltd.) and Hannrite L-1225 (pc in the table), the two components were mixed at a resin temperature of 310°C using a twin-screw kneading extruder. Alternatively, the three components were sufficiently melt-mixed and extruded as a strand-like molded product with a diameter of about 3B, which was then cut into a length of about 4vrsC using a pelletizer to obtain a pellet. Example 1 except that the obtained pellet was used, the resin temperature in the extruder cylinder was 330°C, and the temperature setting of the molding die was 300°C.
A sheet-like molded product was obtained in the same manner as in Example 1, and its physical properties were measured. The results are shown in Table 3.
(以下余白)
実施例5〜8、比較例3.4
第(2)表に示した所定量のエチレン
化エチレン共重合体(ダイキン社製、
四ふっ
ネオ7
製、ネオフロンFEP%表中FEP )、全芳香族ポリ
エステル液晶ポリマー(ポリプラスチックス社製、VE
CTRA、A950. 表中LCP )及びポリカー
ボネート(今人化成社製:)電ンライトL−1225、
表中PC)を充分に乾燥した後、二軸混練押し出し機を
用い、樹脂温度350℃ζて2成分もしくは3成分の溶
融混線を充分に行って約3餌径のストランド状成形物と
して押し出し、それをペレタイザーを用いて長さ約4f
iに切断してペレットを得た。得られたベレットを使用
し、押し出し機シリンダー内の樹脂温度を340℃にし
、成形ダイの設定温度を320℃にした以外は、実施例
1で行ったと同様にしてシート状成形体を得、物性を測
定し、結果を第4表に示した。(Margins below) Examples 5 to 8, Comparative Example 3.4 Ethylated ethylene copolymer in a predetermined amount shown in Table (2) (manufactured by Daikin Co., Ltd., Yofu Neo 7, Neoflon FEP% FEP in the table) , fully aromatic polyester liquid crystal polymer (manufactured by Polyplastics, VE
CTRA, A950. LCP in the table) and polycarbonate (manufactured by Konjin Kasei Co., Ltd.:) Denlight L-1225,
After thoroughly drying the PC in the table, using a twin-screw kneading extruder, the two or three components were sufficiently melt mixed at a resin temperature of 350°C and extruded as a strand-shaped molded product with a feed diameter of about 3. Using a pelletizer, it was made into a length of about 4f.
i to obtain pellets. Using the obtained pellet, a sheet-shaped molded product was obtained in the same manner as in Example 1, except that the resin temperature in the extruder cylinder was set at 340°C and the temperature set in the molding die was set at 320°C. was measured and the results are shown in Table 4.
(以下余白)
実施例9〜12、比較例5.6
第■表に示した所定量の四ふつ化エチレン六フっ化7’
ロビレン共重合体(ダイキン社ンPFA、表中PFA)
、全芳香族ポリエステル液晶ポリマー(ポリプラスチッ
クス社製、VECTRA A950、表中LCP)及
びポリカーボネート(量大化成社製、パンライトL−1
225、表中pc)を用い、実施例9で行ったと同11
1Cしてベレットを得た。得られたベレットを使用し、
押し出し機シリンダー内の樹脂温度を350℃にし、成
形グイの設定温度を333℃にした以外は実施例1で行
ったと同様にしてシート状成形体を得、物性を測定し、
結果を第5表に示した。(Left space below) Examples 9 to 12, Comparative Example 5.6 Predetermined amount of tetrafluoroethylene hexafluoride 7' shown in Table ■
Robylene copolymer (Daikin PFA, PFA in the table)
, fully aromatic polyester liquid crystal polymer (manufactured by Polyplastics Co., Ltd., VECTRA A950, LCP in the table) and polycarbonate (manufactured by Ryotai Kasei Co., Ltd., Panlite L-1
225, pc in the table), and the same 11 as carried out in Example 9.
1C to obtain a beret. Using the resulting beret,
A sheet-shaped molded product was obtained in the same manner as in Example 1, except that the resin temperature in the extruder cylinder was 350°C and the temperature of the molding guide was 333°C, and the physical properties were measured.
The results are shown in Table 5.
(以下余白)
実施例13〜16、比較例7.8
第i0表に示した所定量のパーフルオロアルコキシふっ
素樹脂(グイ
キン社製、
ネオ70
耐薬品性、耐摩耗性、耐汚染性などの特性を損なうこと
無く、線膨張係数が大幅に低減され、表面性がすぐれ且
つ優れた機械的物性および成形加工性を有している。(Leaves below) Examples 13 to 16, Comparative Example 7.8 A predetermined amount of perfluoroalkoxy fluororesin shown in Table i0 (manufactured by Guikin, Neo 70) Characteristics such as chemical resistance, abrasion resistance, stain resistance, etc. It has a significantly reduced coefficient of linear expansion, excellent surface properties, and excellent mechanical properties and moldability without impairing the properties.
従って本発明の成形体は各種の強酸や溶剤下で使用され
る)曵イブ、チューブ、フィルム、ライニング材、バル
ブシート、フィルターなどのプラント部材、機械部品、
電子部品等の幅広い用途r:FI5.用される。Therefore, the molded product of the present invention can be used under various strong acids and solvents), plant parts such as tubes, films, lining materials, valve seats, filters, etc., machine parts, etc.
Wide range of applications such as electronic parts: FI5. used.
Claims (1)
ふっ化エチレン共重合体、四ふっ化エチレン−六ふっ化
プロピレン共重合体及びパーフルオロアルコキシふっ素
樹脂よりなる群から選ばれたふっ素系樹脂と(b)異方
性溶融形態を示す重合体よりなり、ふっ素系樹脂(a)
と重合体(b)の重量比が60:40〜97:3である
ふっ素系樹脂成形体。 2、(a)ポリクロロ三ふっ化エチレン、エチレン−四
ふっ化エチレン共重合体、四ふっ化エチレン−六ふっ化
プロピレン共重合体及びパーフルオロアルコキシふっ素
樹脂よりなる群から選ばれたふっ素系樹脂と、 (b)異方性溶融形態を示す重合体と、 (c)ポリアリレート、ポリエチレンテレフタレート及
びポリカーボネートよりなる群から選ばれた一種以上の
ポリマー よりなり、ふっ素系樹脂(a)と重合体(b)の重量比
が60:40〜97:3であり、ふっ素系樹脂(a)と
重合体(b)の合計量100重量部に対し、ポリマー(
c)の含有量が1〜20重量部であるふっ素系樹脂成形
体。[Claims] 1. (a) selected from the group consisting of polychlorotrifluoroethylene, ethylene-tetrafluoroethylene copolymer, tetrafluoroethylene-hexafluoropropylene copolymer, and perfluoroalkoxyfluororesin (b) a polymer exhibiting an anisotropic melt morphology, the fluororesin (a)
and a polymer (b) in a weight ratio of 60:40 to 97:3. 2, (a) a fluororesin selected from the group consisting of polychlorotrifluoroethylene, ethylene-tetrafluoroethylene copolymer, tetrafluoroethylene-hexafluoropropylene copolymer, and perfluoroalkoxyfluororesin; , (b) a polymer exhibiting an anisotropic melt morphology, and (c) one or more polymers selected from the group consisting of polyarylate, polyethylene terephthalate, and polycarbonate, comprising a fluororesin (a) and a polymer (b). ) is 60:40 to 97:3, and the polymer (
A fluororesin molded article containing 1 to 20 parts by weight of c).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63263521A JP2817922B2 (en) | 1988-10-19 | 1988-10-19 | Fluorine resin molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63263521A JP2817922B2 (en) | 1988-10-19 | 1988-10-19 | Fluorine resin molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02110156A true JPH02110156A (en) | 1990-04-23 |
JP2817922B2 JP2817922B2 (en) | 1998-10-30 |
Family
ID=17390694
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63263521A Expired - Lifetime JP2817922B2 (en) | 1988-10-19 | 1988-10-19 | Fluorine resin molding |
Country Status (1)
Country | Link |
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JP (1) | JP2817922B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0545308A2 (en) * | 1991-11-30 | 1993-06-09 | Hoechst Aktiengesellschaft | Mixtures of liquid crystalline copolymers and fluorinated thermoplastics, and their use |
WO1995029956A1 (en) * | 1994-04-28 | 1995-11-09 | Daikin Industries, Ltd. | Thermoplastic resin composition |
WO1999036473A1 (en) * | 1998-01-20 | 1999-07-22 | Asahi Glass Company Ltd. | Fluororesin composition |
WO2020008923A1 (en) | 2018-07-02 | 2020-01-09 | 清華大学 | Fluorine-containing resin composition and method for production thereof |
WO2021132341A1 (en) | 2019-12-24 | 2021-07-01 | ダイキン工業株式会社 | Composition, injection molded article, and molding auxiliary agent |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56115357A (en) * | 1979-11-30 | 1981-09-10 | Ici Ltd | Melt workable polymer composition having improved workability |
JPS63230756A (en) * | 1987-03-18 | 1988-09-27 | Polyplastics Co | Fluororesin composition |
JPH0232147A (en) * | 1988-07-20 | 1990-02-01 | Toray Ind Inc | Composite material of fluororesin and production thereof |
-
1988
- 1988-10-19 JP JP63263521A patent/JP2817922B2/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56115357A (en) * | 1979-11-30 | 1981-09-10 | Ici Ltd | Melt workable polymer composition having improved workability |
JPS63230756A (en) * | 1987-03-18 | 1988-09-27 | Polyplastics Co | Fluororesin composition |
JPH0232147A (en) * | 1988-07-20 | 1990-02-01 | Toray Ind Inc | Composite material of fluororesin and production thereof |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0545308A2 (en) * | 1991-11-30 | 1993-06-09 | Hoechst Aktiengesellschaft | Mixtures of liquid crystalline copolymers and fluorinated thermoplastics, and their use |
WO1995029956A1 (en) * | 1994-04-28 | 1995-11-09 | Daikin Industries, Ltd. | Thermoplastic resin composition |
US5767198A (en) * | 1994-04-28 | 1998-06-16 | Daikin Industries, Ltd. | Thermoplastic resin composition |
WO1999036473A1 (en) * | 1998-01-20 | 1999-07-22 | Asahi Glass Company Ltd. | Fluororesin composition |
WO2020008923A1 (en) | 2018-07-02 | 2020-01-09 | 清華大学 | Fluorine-containing resin composition and method for production thereof |
KR20210013115A (en) | 2018-07-02 | 2021-02-03 | 칭화대학교 | Fluorine-containing resin composition and its manufacturing method |
WO2021132341A1 (en) | 2019-12-24 | 2021-07-01 | ダイキン工業株式会社 | Composition, injection molded article, and molding auxiliary agent |
KR20220107235A (en) | 2019-12-24 | 2022-08-02 | 다이킨 고교 가부시키가이샤 | Compositions, Injection Molded Articles and Molding Aids |
Also Published As
Publication number | Publication date |
---|---|
JP2817922B2 (en) | 1998-10-30 |
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