JP2001277264A - Polyimide seamless tube and method for preparing it - Google Patents

Polyimide seamless tube and method for preparing it

Info

Publication number
JP2001277264A
JP2001277264A JP2000094413A JP2000094413A JP2001277264A JP 2001277264 A JP2001277264 A JP 2001277264A JP 2000094413 A JP2000094413 A JP 2000094413A JP 2000094413 A JP2000094413 A JP 2000094413A JP 2001277264 A JP2001277264 A JP 2001277264A
Authority
JP
Japan
Prior art keywords
polyimide
seamless tube
tube
mass
less
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
Application number
JP2000094413A
Other languages
Japanese (ja)
Other versions
JP4693956B2 (en
Inventor
Norihiko Miki
規彦 三木
Shigeki Imamura
茂樹 今村
Yoshiaki Echigo
良彰 越後
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Unitika Ltd
Original Assignee
Unitika Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Unitika Ltd filed Critical Unitika Ltd
Priority to JP2000094413A priority Critical patent/JP4693956B2/en
Publication of JP2001277264A publication Critical patent/JP2001277264A/en
Application granted granted Critical
Publication of JP4693956B2 publication Critical patent/JP4693956B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Reinforced Plastic Materials (AREA)
  • Moulding By Coating Moulds (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a polyimide seamless tube in which degree of orientation of the molecular chain in the longer direction and in the peripheral direction is low and anisotropic properties are not substantially exhibited and which has high elastic moduli and has a low water absorption and a method for preparing it. SOLUTION: The polyimide seamless tube comprising a polyimide shown by general formula (1) (wherein n is an integer of 1-20) and having a tensile elastic modulus in the longer direction of at least 480 kg/mm2 is provided. The method for preparing the polyimide seamless tube wherein a polyimide precursor solution in which a polyimide precursor to be changed to the polyimide shown in the above described general formula (l) is dissolved as a solute in a solvent is molded to imidize the polyimide precursor, is provided.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、高弾性率を有し、
吸水率の低いポリイミドシームレスチューブ及びその製
造方法に関するものである。
TECHNICAL FIELD The present invention has a high elastic modulus,
The present invention relates to a polyimide seamless tube having a low water absorption and a method for producing the same.

【0002】[0002]

【従来の技術】全芳香族系ポリイミドは、その優れた耐
熱性、耐摩擦、耐摩耗特性、機械的特性から、近年様々
な産業分野においてその需要が増加してきたエンジニア
リングプラスチックの一つであり、特に、OA機器産業
においては、その耐熱性や耐摩耗性に優れている点で様
々な部材に用いられ、その用途範囲が急速に伸びてい
る。
2. Description of the Related Art Due to its excellent heat resistance, friction resistance, abrasion resistance and mechanical properties, wholly aromatic polyimides are one of engineering plastics whose demand has been increasing in various industrial fields in recent years. In particular, in the OA equipment industry, it is used for various members because of its excellent heat resistance and wear resistance, and its application range is rapidly expanding.

【0003】中でもプリンター、複写機の熱定着ユニッ
トにおいては、従来用いられていたゴム被覆金属性円筒
状ヒーターは消費電力が大きいので、ポリイミドシーム
レスチューブを用いた小型線状ヒーターを備えた熱定着
ユニットの研究、開発が急速に進んでいる。この熱定着
ユニットは複数本の回転体によって、その内部から支
持、駆動されており、チューブの蛇行による位置ずれを
抑えるために端部は軸受けによって抑えられている。
In particular, in a thermal fixing unit of a printer or a copying machine, a conventionally used rubber-coated metallic cylindrical heater consumes a large amount of power, and therefore has a small linear heater using a polyimide seamless tube. Research and development are progressing rapidly. The heat fixing unit is supported and driven from the inside by a plurality of rotating bodies, and its end is suppressed by a bearing in order to suppress the displacement due to the meandering of the tube.

【0004】[0004]

【発明が解決しようとする課題】しかし、一般的にポリ
マー製シームレスチューブは金属製シームレスチューブ
に較べ機械的特性の面で劣り、位置ずれが極度に進行し
た場合には軸受けと接する端部が捲れ返る、たわむなど
して正常な動作ができなくなるといった問題が有った。
特に高速機種においては一定期間内に印刷、複写される
枚数が通常の機種に比べ多くなる可能性が高く、わずか
な支持・駆動ローラーの位置ずれでも短期間に上記の問
題を生じる。これを回避するには短期間毎のメンテナン
スが必要となり、維持費用が非常に高価となってしまう
といった問題が有った。
However, in general, polymer seamless tubes are inferior in mechanical properties as compared with metal seamless tubes, and when the displacement is extremely advanced, the ends in contact with the bearings are turned up. There was a problem that normal operation could not be performed due to return or bending.
Particularly in a high-speed model, the number of sheets printed and copied in a certain period is likely to be larger than that in a normal model, and even a slight displacement of the supporting / driving roller causes the above problem in a short time. In order to avoid this, maintenance has to be performed every short period, and there has been a problem that the maintenance cost is extremely high.

【0005】この問題を解決する手段として、特開平10
-83122号公報には、350kg/mm2 以上の弾性率を
有するポリイミドシームレスチューブを用いることが開
示されているが、高速化が進んだ場合には、単位期間中
の片側へ蛇行が大きく、単位期間中の安定した使用に関
しては長手方向にはこれ以上の弾性率を有するものが必
要となる。また特開平8-80580 号公報には弾性率が70
0kg/mm2 のシームレスチューブが示されている
が、含まれる無機物粒子が絶縁物であるため、OA機器
に適用した場合には帯電し、プリンター、複写機に用い
た場合にはトナーの付着を招き、印画像が乱れる上、ブ
レンド物である為に別途に原料を調製する必要が有り、
コスト的に高価になるという問題が有った。
As means for solving this problem, Japanese Patent Application Laid-Open
JP-83122 discloses that a polyimide seamless tube having an elastic modulus of 350 kg / mm 2 or more is used. However, when the speed is increased, meandering to one side during a unit period is large, and For stable use during the period, one having a higher elastic modulus in the longitudinal direction is required. Japanese Patent Application Laid-Open No. 8-80580 discloses that the elastic modulus is 70%.
Although a 0 kg / mm 2 seamless tube is shown, the inorganic particles contained therein are insulators, so they are charged when applied to OA equipment and adhere to toner when used in printers and copiers. In addition, the stamp image is disturbed, and it is necessary to prepare raw materials separately because it is a blend,
There was a problem that it became expensive in terms of cost.

【0006】また耐荷重の絶対値を向上させるにはある
一定以上の厚みが必要となるが、一般的にポリイミドフ
ィルム状成型物はその厚みが厚くなるにつれ、弾性率が
低下するという問題があった。また気候の変動により、
湿度が上昇した場合には、定着チューブが大気中の水分
を吸収し、寸法が変化する懸念が有る。このような寸法
変化はチューブの回転中の偏りの原因となる。またポリ
イミドシームレスチューブは特開平6-23770 号公報に開
示されているように円筒状金型を用いて成形されること
が多いが、ポリイミド成形体は一般にその前駆体を成形
し、これをイミド化することにより得られ、このイミド
化過程中に大きな収縮を生じる。円筒状の金型を用いて
成形した場合には、長手方向にポリイミド分子が配向を
起こし易く、周方向よりも長手方向の方が大きな弾性率
を示すことが多い。これにより長手方向には十分な機械
的特性を有しながらも、周方向には不十分であるという
現象を生じ易い。
In order to improve the absolute value of the withstand load, a certain thickness or more is required. In general, a polyimide film-shaped molded article has a problem that the elastic modulus decreases as the thickness increases. Was. Also, due to climate change,
When the humidity rises, there is a concern that the fixing tube absorbs moisture in the atmosphere and the dimensions change. Such a dimensional change causes a deviation during rotation of the tube. In addition, polyimide seamless tubes are often molded using a cylindrical mold as disclosed in JP-A-6-23770, but polyimide molded articles are generally formed by molding the precursor and imidizing the precursor. And a large shrinkage occurs during the imidization process. When molded using a cylindrical mold, the polyimide molecules tend to be oriented in the longitudinal direction, and often exhibit a larger elastic modulus in the longitudinal direction than in the circumferential direction. As a result, there is a tendency for a phenomenon in which sufficient mechanical properties are obtained in the longitudinal direction, but insufficient in the circumferential direction.

【0007】上記の事情に鑑み、本発明の課題は、長手
方向及び周方向における分子鎖の配向度が低く、実質的
に異方性を示さず、長手方向及び周方向においても高い
弾性率を有し、吸水率の低いポリイミドシームレスチュ
ーブ及びその製造方法を提供することにある。
In view of the above circumstances, an object of the present invention is to reduce the degree of molecular chain orientation in the longitudinal and circumferential directions, exhibit substantially no anisotropy, and achieve a high elastic modulus in the longitudinal and circumferential directions. An object of the present invention is to provide a polyimide seamless tube having a low water absorption and a method of manufacturing the same.

【0008】[0008]

【課題を解決するための手段】本発明者らは、特定の化
学構造を有するポリイミド前駆体溶液を成形して得られ
るポリイミドシームレスチューブは、長手方向及び周方
向における配向度がほぼ等しく、高弾性率を示し、吸水
率が低く、かつ従来用いられてきたものよりも厚くする
ことができ、飛躍的に耐久性が向上することを見いだ
し、かかる知見に基づき本発明に到達した。
Means for Solving the Problems The present inventors have found that a polyimide seamless tube obtained by molding a polyimide precursor solution having a specific chemical structure has substantially the same degree of orientation in the longitudinal direction and the circumferential direction, and has high elasticity. It has been found that the water absorption rate is low, the water absorption rate is low, and the thickness can be made thicker than that conventionally used, and the durability is dramatically improved.

【0009】すなわち、本発明の要旨は、第1に、一般
式(1)に示すポリイミドからなり、長手方向における
引張弾性率が480kg/mm2 以上であることを特徴
とするポリイミドシームレスチューブである。〔式中、
nは1〜20の整数を示す。〕
That is, the gist of the present invention is, firstly, a polyimide seamless tube comprising a polyimide represented by the general formula (1) and having a tensile modulus in the longitudinal direction of 480 kg / mm 2 or more. . (In the formula,
n shows the integer of 1-20. ]

【0010】[0010]

【化3】 Embedded image

【0011】第2に、24時間浸水後の吸水率が2質量
%未満であって、長手方向及び周方向における寸法変化
率が0.1%未満であることを特徴とする前記のポリイ
ミドシームレスチューブであり、第3に、長手方向及び
周方向における分子鎖の配向度が0.1未満であること
を特徴とする前記のポリイミドシームレスチューブであ
り、第4に、カーボンブラックを0.1質量%以上5質
量%未満含有することを特徴とする前記のポリイミドシ
ームレスチューブであり、第5に、長さが4mm未満の
炭素繊維を0.1〜10質量%含有することを特徴とす
る前記のポリイミドシームレスチューブであり、第6
に、下記一般式(2)に示すカルボン酸と下記一般式
(3)に示すジアミンとからなる塩が溶質として溶媒中
に溶解しているポリイミド前駆体溶液を成形し、ポリイ
ミド前駆体をイミド化することを特徴とするポリイミド
シームレスチューブの製造方法である。〔式中、lは0
〜20の整数を表し、mは0〜20の整数を表し、l+
mは1〜20である。〕
Second, the polyimide seamless tube is characterized in that the water absorption after water immersion for 24 hours is less than 2% by mass and the dimensional change in the longitudinal and circumferential directions is less than 0.1%. Thirdly, the polyimide seamless tube is characterized in that the degree of molecular chain orientation in the longitudinal direction and the circumferential direction is less than 0.1, and fourthly, 0.1% by mass of carbon black. Fifth, the polyimide seamless tube is characterized by containing less than 5% by mass, and fifth, 0.1 to 10% by mass of a carbon fiber having a length of less than 4 mm. 6th seamless tube
Next, a polyimide precursor solution in which a salt comprising a carboxylic acid represented by the following general formula (2) and a diamine represented by the following general formula (3) is dissolved in a solvent as a solute is formed, and the polyimide precursor is imidized. A method for producing a polyimide seamless tube. [Where l is 0
Represents an integer of 0 to 20; m represents an integer of 0 to 20;
m is 1-20. ]

【0012】[0012]

【化4】 Embedded image

【0013】[0013]

【発明の実施の形態】以下、本発明について詳細に説明
する。まず、本発明で用いる用語について説明する。 (1)ポリイミド ポリマー鎖の繰り返し単位の80モル%以上がイミド構
造を有する有機ポリマーをいう。そして、この有機ポリ
マーは耐熱性を示す。 (2)ポリイミド前駆体 加熱又は、化学的作用により閉環してポリイミドとなる
有機化合物をいう。ここで、閉環とはイミド環構造が形
成されることをいう。 (3)ポリイミド前駆体溶液 ポリイミド前駆体が溶媒に溶解しているものである。こ
こで溶媒とは、25℃で液状の化合物をいう。 (4)粘度 (株)トキメック社製、DVL−BII型デジタル粘度計
(B型粘度計)を用い、20℃における回転粘度を測定
したものである。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. First, terms used in the present invention will be described. (1) Polyimide An organic polymer in which 80 mol% or more of the repeating unit of the polymer chain has an imide structure. And this organic polymer shows heat resistance. (2) Polyimide precursor An organic compound that becomes a polyimide by ring closure by heating or chemical action. Here, ring closure means that an imide ring structure is formed. (3) Polyimide precursor solution The polyimide precursor is dissolved in a solvent. Here, the solvent refers to a compound which is liquid at 25 ° C. (4) Viscosity The rotational viscosity at 20 ° C. was measured using a DVL-BII type digital viscometer (B type viscometer) manufactured by Tokimec Co., Ltd.

【0014】(5)厚み (株)ミツトヨ製デジマチックマイクロメーターを用
い、ポリイミド被膜の厚みを10箇所で測定し、その平
均値として求めたものである。 (6)引張弾性率 JISK−7127に準拠して測定したものである。 (7)寸法変化率 水への浸漬前後における寸法の変化量を原寸との割合で
求めた。 (8)吸水率 25℃に保たれた純水中に24時間浸漬した後の吸水率
によって示される。 (9)配向度 X線透過法により観察された結晶性の回折ピークにおい
て、2θ角を固定して、θ角を変化させて得られるθ−
回折強度曲線より得られる半価幅Hに対し、下記の式に
より算出されるΠをさす。 Π=(180−H)/180
(5) Thickness The thickness of the polyimide film was measured at 10 locations using a Digimatic Micrometer manufactured by Mitutoyo Corporation, and the average value was obtained. (6) Tensile modulus Measured in accordance with JIS K-7127. (7) Dimensional change rate The amount of dimensional change before and after immersion in water was determined as a ratio to the original size. (8) Water absorption The water absorption is shown by the water absorption after immersion in pure water kept at 25 ° C. for 24 hours. (9) Degree of orientation In the crystalline diffraction peak observed by the X-ray transmission method, θ− obtained by fixing the 2θ angle and changing the θ angle is obtained.
The half-width H obtained from the diffraction intensity curve indicates Π calculated by the following equation. Π = (180−H) / 180

【0015】さらに本発明について説明する。本発明の
ポリイミドシームレスチューブは、一般式(1)に示す
化学構造を有し、厚みが55μm以上であることが好ま
しい。シームレスとは目視上継目が確認されないだけで
なく、折曲げ試験によって特性値の異なる点が長手方向
に1列状に生じないものをいう。本発明において、長手
方向の引張弾性率の値は、シームレスチューブの使用環
境、予張力などの使用状況により異なるが、中間転写ベ
ルト、搬送転写ベルトなどの用途を兼ねる場合を考慮す
ると、480kg/mm2 以上である。500kg/m
2 以上が好ましく、550kg/mm2 以上であれば
実用上の色ズレが殆ど生じないので特に好ましい。
Further, the present invention will be described. The polyimide seamless tube of the present invention has a chemical structure represented by the general formula (1), and preferably has a thickness of 55 μm or more. The term "seamless" means not only that the seam is not visually confirmed, but also that points having different characteristic values do not occur in a line in the longitudinal direction in the bending test. In the present invention, the value of the tensile modulus in the longitudinal direction varies depending on the use environment of the seamless tube, the use condition such as pretension, etc., but in consideration of the case where the seamless tube is also used as an intermediate transfer belt or a transfer belt, it is 480 kg / mm. 2 or more. 500kg / m
m 2 or more is preferable, and 550 kg / mm 2 or more is particularly preferable because practical color shift hardly occurs.

【0016】本発明のポリイミドシームレスチューブに
は、導電性の観点からカーボンブラックを0.1質量%
以上5質量%未満含有させることが好ましい。0.1質
量%未満では導電性の効果が発揮されず、安定的に導電
性を発現させ、破談強度等機械的物性を維持させるため
には2質量%以上5質量%未満が好ましい。本発明のポ
リイミドシームレスチューブでは引張弾性率をさらに高
くする方法として断面の直径が1μm以上で長さが4m
m未満の炭素繊維を配合すると弾性率が向上することが
知見として得られた。炭素繊維の配合量としては0.1
〜10質量%が好ましい。炭素繊維の断面径が1μm未
満のものを用いた場合は面方向に対し平行に分散され難
い。長さが4mm以上の場合は原料溶液への分散が困難
となり、均一に分散されたポリイミドシームレスチュー
ブが得られないことがある。炭素繊維の配合量が0.1
質量%未満では配合効果が発揮されず、10質量%を超
えると成形が困難となる。配合量は1〜5質量%がより
好ましい。また、炭素繊維を配合することにとって導電
性効果も発揮される。
The polyimide seamless tube of the present invention contains 0.1% by mass of carbon black from the viewpoint of conductivity.
It is preferred that the content be at least 5 mass%. If it is less than 0.1% by mass, the effect of conductivity is not exhibited, and in order to stably exhibit conductivity and maintain mechanical properties such as breaking strength, the content is preferably 2% by mass or more and less than 5% by mass. In the polyimide seamless tube of the present invention, as a method for further increasing the tensile modulus, the cross-sectional diameter is 1 μm or more and the length is 4 m.
It has been found that the addition of a carbon fiber of less than m improves the elastic modulus. The compounding amount of carbon fiber is 0.1
-10% by mass is preferred. When a carbon fiber having a cross-sectional diameter of less than 1 μm is used, it is difficult to disperse the carbon fiber parallel to the plane direction. When the length is 4 mm or more, dispersion in the raw material solution becomes difficult, and a uniformly dispersed polyimide seamless tube may not be obtained. The amount of carbon fiber is 0.1
When the amount is less than 10% by mass, the compounding effect is not exhibited, and when the amount exceeds 10% by mass, molding becomes difficult. The amount is more preferably 1 to 5% by mass. In addition, a conductive effect is exhibited by blending carbon fibers.

【0017】本発明のポリイミドシームレスチューブは
外部の影響によって中間転写ベルト、搬送転写ベルトの
機能を損なわないためには、24時間浸水後の吸水率が
2質量%未満であることが好ましく、1質量%以下がさ
らに好ましい。また同様に長手方向及び周方向における
寸法変化率が0.1未満であることが好ましく、0.0
5未満であることがさらに好ましい。
The polyimide seamless tube of the present invention preferably has a water absorption of less than 2% by mass after being immersed for 24 hours in order to prevent the function of the intermediate transfer belt and the transfer belt from being impaired by external influences. % Is more preferable. Similarly, the dimensional change rate in the longitudinal direction and the circumferential direction is preferably less than 0.1, and 0.0
More preferably, it is less than 5.

【0018】本発明のポリイミドシームレスチューブ
は、下記一般式(2)に示すカルボン酸と下記一般式
(3)に示すジアミンとからなる塩が溶質として溶媒中
に溶解しているポリイミド前駆体溶液を成形し、ポリイ
ミド前駆体をイミド化することによって得られる。成形
方法としては、公知の方法が採用され、例えば樹脂環状
体製造遥遠等の内側表面に回転成形などの方法を利用し
て塗布し、同時、あるいは次いで、加熱することによ
り、溶媒除去とイミド化を行うことにより製造すること
ができる。なお、一般式(2)において、R3 は水素又
は炭素数7以下の1価の有機基を示し、1価の有機基と
しては、メチル基、エチル基、プロピル基、イソプロピ
ル基等が挙げられる。また、lは0〜20の整数を示
し、mは0〜20の整数を示し、l+mは1〜20の整
数である。
The polyimide seamless tube of the present invention comprises a polyimide precursor solution in which a salt comprising a carboxylic acid represented by the following general formula (2) and a diamine represented by the following general formula (3) is dissolved as a solute in a solvent. It is obtained by molding and imidizing a polyimide precursor. As a molding method, a known method is adopted, for example, by applying a method such as rotational molding to an inner surface of a resin ring body far and the like, and simultaneously or subsequently, by heating, solvent removal and imidization. Can be produced. In the general formula (2), R 3 represents hydrogen or a monovalent organic group having 7 or less carbon atoms, and examples of the monovalent organic group include a methyl group, an ethyl group, a propyl group, and an isopropyl group. . Also, l represents an integer of 0 to 20, m represents an integer of 0 to 20, and l + m is an integer of 1 to 20.

【0019】本発明において、溶媒としては一般式
(2)に示すカルボン酸と一般式(3)に示すジアミン
からなる塩を溶かす溶媒であればいかなる溶媒も用いる
ことができる。例えば、非プロトン性極性溶媒である、
N−メチルピロリドン、N,N−ジメチルホルムアミ
ド、N,N−ジメチルアセトアミド、ジメチルスルホキ
シド、ヘキサメチルフォスフォラアミド、エーテル系化
合物である、2−メトキシエタノール、2−エトキシエ
タノール、2−(メトキシメトキシ)エトキシエタノー
ル、2−イソプロポキシエタノール、2−ブトキシエタ
ノール、テトラヒドロフルフリルアルコール、ジエチレ
ングリコール、ジエチレングリコールモノメチルエーテ
ル、ジエチレングリコールモノエチルエーテル、ジエチ
レングリコールモノブチルエーテル、トリエチレングリ
コール、トリエチレングリコールモノエチルエーテル、
テトラエチレングリコール、1−メトキシ−2−プロパ
ノール、1−エトキシ−2−プロパノール、ジプロピレ
ングリコール、ジプロピレングリコールモノメチルエー
テル、ジプロピレングリコールモノエチルエーテル、ト
リプロピレングリコールモノメチルエーテル、ポリエチ
レングリコール、ポリプロピレングリコール、テトラヒ
ドロフラン、ジオキサン、1,2−ジメトキシエタン、
ジエチレングリコールジメチルエーテル、ジエチレング
リコールジエチルエーテル、水溶性アルコール系化合物
である、メタノール、エタノール、1−プロパノール、
2−プロパノール、tert−ブチルアルコール、エチ
レングリコール、1,2−プロパンジオール、1,3−
プロパンジオール、1,3−ブタンジオール、1,4−
ブタンジオール、2,3−ブタンジオール、1,5−ペ
ンタンジオール、2−ブテン−1,4−ジオール、2−
メチル−2,4−ペンタンジオール、1,2,6−ヘキ
サントリオール、ジアセトンアルコール等が、非水溶性
アルコール系化合物ではベンジルアルコールが、ケトン
系化合物では1,5,5−トリメチル−3−シクロヘキ
サノンが、その他ではγ―ブチロラクトンが挙げられ、
上記各化合物を単独、もしくは二種以上を混合して用い
ることができる。このうち特に好ましい例としては、単
独溶媒としてN−メチルピロリドン、N,N−ジメチル
ホルムアミド、N,N−ジメチルアセトアミド、ジエチ
レングリコールモノメチルエーテル、混合溶媒として
は、N−メチルピロリドンとジエチレングリコールモノ
メチルエーテル、N−メチルピロリドンとメタノール、
N−メチルピロリドンと2―メトキシエタノール等の組
み合わせがあげられる。
In the present invention, any solvent may be used as long as it dissolves a salt comprising a carboxylic acid represented by the general formula (2) and a diamine represented by the general formula (3). For example, an aprotic polar solvent,
N-methylpyrrolidone, N, N-dimethylformamide, N, N-dimethylacetamide, dimethylsulfoxide, hexamethylphosphoramide, ether compounds, 2-methoxyethanol, 2-ethoxyethanol, 2- (methoxymethoxy) Ethoxyethanol, 2-isopropoxyethanol, 2-butoxyethanol, tetrahydrofurfuryl alcohol, diethylene glycol, diethylene glycol monomethyl ether, diethylene glycol monoethyl ether, diethylene glycol monobutyl ether, triethylene glycol, triethylene glycol monoethyl ether,
Tetraethylene glycol, 1-methoxy-2-propanol, 1-ethoxy-2-propanol, dipropylene glycol, dipropylene glycol monomethyl ether, dipropylene glycol monoethyl ether, tripropylene glycol monomethyl ether, polyethylene glycol, polypropylene glycol, tetrahydrofuran , Dioxane, 1,2-dimethoxyethane,
Diethylene glycol dimethyl ether, diethylene glycol diethyl ether, water-soluble alcohol-based compounds, methanol, ethanol, 1-propanol,
2-propanol, tert-butyl alcohol, ethylene glycol, 1,2-propanediol, 1,3-
Propanediol, 1,3-butanediol, 1,4-
Butanediol, 2,3-butanediol, 1,5-pentanediol, 2-butene-1,4-diol, 2-
Methyl-2,4-pentanediol, 1,2,6-hexanetriol, diacetone alcohol, etc., benzyl alcohol for water-insoluble alcohol compounds, and 1,5,5-trimethyl-3-cyclohexanone for ketone compounds However, in others, γ-butyrolactone is mentioned,
Each of the above compounds can be used alone or in combination of two or more. Among them, particularly preferred examples include N-methylpyrrolidone, N, N-dimethylformamide, N, N-dimethylacetamide, diethylene glycol monomethyl ether as a single solvent, and N-methylpyrrolidone and diethylene glycol monomethyl ether, N-methylpyrrolidone as a mixed solvent. Methylpyrrolidone and methanol,
Examples include a combination of N-methylpyrrolidone and 2-methoxyethanol.

【0020】本発明におけるポリイミド前駆体溶液の粘
度は50ポイズ以上が好ましく、より好ましくは200
ポイズ以上である。本発明のポリイミドシームレスチュ
ーブの長手方向及び周方向における分子鎖の配向度は
0.1未満であり、実質的に長手方向及び周方向には異
方性を示さない。これは一般式(2)示すカルボン酸と
一般式(3)示すジアミンからなる塩であるポリイミド
前駆体は一般に分子量が低く、ポリイミド前駆体状態で
成形される際に加えられる外力に対して分子鎖の配向を
起こし難く、またイミド化段階においては同時に重合反
応を生じるために、分子内閉環反応により収縮しようと
するチューブ被膜と金型表面間の摩擦による延伸が、高
分子化しようとする分子の動きに阻害される。このた
め、長手方向及び周方向ににおいては特定の方向にポリ
イミド分子が配向することはない。したがって、本発明
のポリイミドシームレスチューブは長手方向及び周方向
における弾性率がほぼ同じ値を示す。
The viscosity of the polyimide precursor solution in the present invention is preferably 50 poise or more, more preferably 200 poise.
More than poise. The degree of orientation of molecular chains in the longitudinal direction and the circumferential direction of the polyimide seamless tube of the present invention is less than 0.1, and does not substantially show anisotropy in the longitudinal direction and the circumferential direction. This is a salt of a carboxylic acid represented by the general formula (2) and a diamine represented by the general formula (3). A polyimide precursor generally has a low molecular weight, and a molecular chain against an external force applied when molded in a polyimide precursor state. It is difficult for the molecules to be polymerized due to friction between the tube coating and the mold surface, which tend to shrink due to the intramolecular ring closure reaction, because the polymerization reaction occurs at the same time during the imidization step. Inhibited by movement. Therefore, the polyimide molecules are not oriented in a specific direction in the longitudinal direction and the circumferential direction. Therefore, the polyimide seamless tube of the present invention has substantially the same elastic modulus in the longitudinal direction and the circumferential direction.

【0021】[0021]

【実施例】以下実施例により本発明を具体的に説明する
が、本発明はこれらの実施例により限定されるものでは
ない。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples.

【0022】実施例1 パラフェニレンジアミン10.27g(0.095mo
l)を、N,N−ジメチルアセトアミド355gに溶解
し、室温下で攪拌した。これにピロメリット酸二無水物
4.36g(0.02mol)およびビフェニルテトラ
カルボン酸二無水物23.54g(0.08mol)を
1分間で加え、室温下2時間攪拌した。メタノール0.
48g(0.015mol)およびジメチルアミノエタ
ノール0.024gを加え、70℃湯浴上で2時間攪拌
した。室温まで冷却した後、ジアミノジフェニルエーテ
ル1.001g(0.005mol)を加え、さらに1
時間撹拌を続けたところ、均一な黄橙色透明溶液が得ら
れた(溶質濃度10質量%)。こうして得られたポリイ
ミド前駆体溶液を円柱状金型にスプレーコートした。こ
れを窒素雰囲気下で段階的に昇温しながら300℃ま
で、5時間かけて昇温し、ポリイミド前駆体をイミド化
し、ポリイミドシームレスチューブを金型から脱型し
た。このポリイミドシームレスチューブを切り開き厚み
測定を行ったところ57μmであった。切り開かれたチ
ューブに対し、長手方向における引張弾性率の測定を行
ったところ500kg/mm2 以上の値を示した。また
切り開かれたチューブの吸水率を測定したところ1.1
質量%であり、長手方向及び周方向における寸法変化率
は0.1%未満であった。このチューブをX線透過回折
法測定したところ、2θ=11°付近に結晶性の回折が
見られたので、2θを固定してθ角を変化させた際の回
折強度分布を測定したが、強度の変化は見られず、配向
度は0であった。
Example 1 10.27 g of paraphenylenediamine (0.095 mol
l) was dissolved in 355 g of N, N-dimethylacetamide and stirred at room temperature. To this, 4.36 g (0.02 mol) of pyromellitic dianhydride and 23.54 g (0.08 mol) of biphenyltetracarboxylic dianhydride were added over 1 minute, and the mixture was stirred at room temperature for 2 hours. Methanol 0.
48 g (0.015 mol) and 0.024 g of dimethylaminoethanol were added, and the mixture was stirred on a 70 ° C. water bath for 2 hours. After cooling to room temperature, 1.001 g (0.005 mol) of diaminodiphenyl ether was added, and
When stirring was continued for a time, a uniform yellow-orange transparent solution was obtained (solute concentration: 10% by mass). The thus obtained polyimide precursor solution was spray-coated on a cylindrical mold. The temperature was raised to 300 ° C. over 5 hours while gradually raising the temperature in a nitrogen atmosphere to imidize the polyimide precursor, and the polyimide seamless tube was released from the mold. When this polyimide seamless tube was cut open and the thickness was measured, it was 57 μm. When the tensile elastic modulus in the longitudinal direction of the cut tube was measured, the value was 500 kg / mm 2 or more. The water absorption of the cut tube was measured.
% By mass, and the dimensional change rate in the longitudinal direction and the circumferential direction was less than 0.1%. When this tube was measured by X-ray transmission diffraction method, crystalline diffraction was observed around 2θ = 11 °. Therefore, the diffraction intensity distribution when the 2θ was fixed and the θ angle was changed was measured. No change was observed, and the degree of orientation was 0.

【0023】実施例2 パラフェニレンジアミン10.27g(0.095mo
l)を、N,N−ジメチルアセトアミド341gに溶解
し、室温下で攪拌した。これにピロメリット酸二無水物
8.72g(0.04mol)およびビフェニルテトラ
カルボン酸二無水物17.65g(0.06mol)を
1分間で加え、室温下2時間攪拌した。メタノール0.
48g(0.015mol)およびジメチルアミノエタ
ノール0.024gを加え、70℃湯浴上で2時間攪拌
した。室温まで冷却した後、ジアミノジフェニルエーテ
ル1.001g(0.005mol)を加え、さらに1
時間撹拌を続けたところ、均一な黄橙色透明溶液が得ら
れた(溶質濃度10質量%)。こうして得られたポリイ
ミド前駆体溶液を円柱状金型にスプレーコートした。こ
れを窒素雰囲気下で段階的に昇温しながら300℃ま
で、5時間かけて昇温することによりポリイミド前駆体
をイミド化し、ポリイミドシームレスチューブを金型か
ら脱型した。このポリイミドシームレスチューブを切り
開き厚み測定を行ったところ56μmであった。切り開
かれたチューブに対し、長手方向における弾性率の測定
を行ったところ500kg/mm2 以上の値を示した。
また切り開かれたチューブの吸水率を測定したところ
1.2質量%であり、長手方向及び周方向における寸法
変化率は0.1%未満であった。このチューブをX線透
過回折法測定したところ、2θ=11°付近に結晶性の
回折が見られたので、2θを固定してθ角を変化させた
際の回折強度分布を測定したが、強度の変化は見られ
ず、配向度は0であった。
Example 2 10.27 g of paraphenylenediamine (0.095 mol)
l) was dissolved in 341 g of N, N-dimethylacetamide and stirred at room temperature. To this, 8.72 g (0.04 mol) of pyromellitic dianhydride and 17.65 g (0.06 mol) of biphenyltetracarboxylic dianhydride were added over 1 minute, and the mixture was stirred at room temperature for 2 hours. Methanol 0.
48 g (0.015 mol) and 0.024 g of dimethylaminoethanol were added, and the mixture was stirred on a 70 ° C. water bath for 2 hours. After cooling to room temperature, 1.001 g (0.005 mol) of diaminodiphenyl ether was added, and
When stirring was continued for a time, a uniform yellow-orange transparent solution was obtained (solute concentration: 10% by mass). The thus obtained polyimide precursor solution was spray-coated on a cylindrical mold. This was heated to 300 ° C. over 5 hours while gradually raising the temperature under a nitrogen atmosphere to imidize the polyimide precursor, and the polyimide seamless tube was released from the mold. When this polyimide seamless tube was cut open and the thickness was measured, it was 56 μm. When the elastic modulus of the cut tube was measured in the longitudinal direction, it showed a value of 500 kg / mm 2 or more.
The water absorption of the cut tube was measured and found to be 1.2% by mass, and the dimensional change in the longitudinal and circumferential directions was less than 0.1%. When this tube was measured by X-ray transmission diffraction method, crystalline diffraction was observed around 2θ = 11 °. Therefore, the diffraction intensity distribution when the 2θ was fixed and the θ angle was changed was measured. No change was observed, and the degree of orientation was 0.

【0024】実施例3 パラフェニレンジアミン10.27g(0.095mo
l)を、N,N−ジメチルアセトアミド328gに溶解
し、室温下で攪拌した。これにピロメリット酸二無水物
13.1g(0.06mol)およびビフェニルテトラ
カルボン酸二無水物11.8g(0.04mol)を1
分間で加え、室温下2時間攪拌した。メタノール0.4
8g(0.015mol)およびジメチルアミノエタノ
ール0.024gを加え、70℃湯浴上で2時間攪拌し
た。室温まで冷却した後、ジアミノジフェニルエーテル
1.001g(0.005mol)を加え、さらに1時
間撹拌を続けたところ、均一な黄橙色透明溶液が得られ
た(溶質濃度10質量%)。得られたポリイミド前駆体
溶液を円柱状金型にスプレーコートした。これを窒素雰
囲気下で段階的に昇温しながら300℃まで、5時間か
けて昇温することによりポリイミド前駆体をイミド化
し、ポリイミドシームレスチューブを金型から脱型し
た。このポリイミドシームレスチューブを切り開き厚み
測定を行ったところ57μmであった。切り開かれたチ
ューブに対し、長手方向における弾性率の測定を行った
ところ520kg/mm2 以上の値を示した。また切り
開かれたチューブの吸水率を測定したところ1.1質量
%であり、長手方向及び周方向における寸法変化率は
0.1%未満であった。このチューブをX線透過回折法
測定したところ、2θ=11°付近に結晶性の回折が見
られたので、2θを固定してθ角を変化させた際の回折
強度分布を測定したが、強度の変化は見られず、配向度
は0であった。
Example 3 10.27 g of paraphenylenediamine (0.095 mol
l) was dissolved in 328 g of N, N-dimethylacetamide and stirred at room temperature. To this, 13.1 g (0.06 mol) of pyromellitic dianhydride and 11.8 g (0.04 mol) of biphenyltetracarboxylic dianhydride were added in 1 part.
And stirred at room temperature for 2 hours. Methanol 0.4
8 g (0.015 mol) and 0.024 g of dimethylaminoethanol were added, and the mixture was stirred on a 70 ° C. water bath for 2 hours. After cooling to room temperature, 1.001 g (0.005 mol) of diaminodiphenyl ether was added, and stirring was further continued for 1 hour to obtain a uniform yellow-orange transparent solution (solute concentration: 10% by mass). The obtained polyimide precursor solution was spray-coated on a cylindrical mold. This was heated to 300 ° C. over 5 hours while gradually raising the temperature under a nitrogen atmosphere to imidize the polyimide precursor, and the polyimide seamless tube was released from the mold. When this polyimide seamless tube was cut open and the thickness was measured, it was 57 μm. When the elastic modulus of the cut tube was measured in the longitudinal direction, the tube showed a value of 520 kg / mm 2 or more. The water absorption of the cut tube was measured to be 1.1% by mass, and the dimensional change in the longitudinal and circumferential directions was less than 0.1%. When this tube was measured by X-ray transmission diffraction method, crystalline diffraction was observed around 2θ = 11 °. Therefore, the diffraction intensity distribution when the 2θ was fixed and the θ angle was changed was measured. No change was observed, and the degree of orientation was 0.

【0025】実施例4 実施例1で得られたポリイミド前駆体溶液の固形分に対
しカーボンブラック2質量%加え、混練機を用いて分散
させた。こうして得られたカーボンブラックを分散させ
たポリイミド前駆体溶液を金型上にスプレーコートし、
窒素雰囲気下で段階的に昇温しながら300℃まで、5
時間かけて昇温してポリイミド前駆体をイミド化し、ポ
リイミドシームレスチューブを金型から脱型した。この
ポリイミドシームレスチューブを切り開き厚み測定を行
ったところ67μmであった。切り開かれたチューブに
対し、長手方向における弾性率の測定を行ったところ5
50kg/mm2 以上の値を示した。また切り開かれた
チューブの吸水率を測定したところ1.1質量%であ
り、長手方向及び周方向における寸法変化率は0.1%
未満であった。このチューブをX線透過回折法測定した
ところ、2θ=11°付近に結晶性の回折が見られたの
で、2θを固定してθ角を変化させた際の回折強度分布
を測定したが、強度の変化は見られず、配向度は0であ
った。
Example 4 2% by mass of carbon black was added to the solid content of the polyimide precursor solution obtained in Example 1 and dispersed using a kneader. The polyimide precursor solution obtained by dispersing the carbon black thus obtained is spray-coated on a mold,
Up to 300 ° C while gradually raising the temperature under a nitrogen atmosphere, 5
The temperature was raised over time to imidize the polyimide precursor, and the polyimide seamless tube was released from the mold. When this polyimide seamless tube was cut open and the thickness was measured, it was 67 μm. The elastic modulus in the longitudinal direction was measured for the cut-out tube.
It showed a value of 50 kg / mm 2 or more. The water absorption of the cut tube was measured to be 1.1% by mass, and the dimensional change in the longitudinal and circumferential directions was 0.1%.
Was less than. When this tube was measured by X-ray transmission diffraction method, crystalline diffraction was observed around 2θ = 11 °. Therefore, the diffraction intensity distribution when the 2θ was fixed and the θ angle was changed was measured. No change was observed, and the degree of orientation was 0.

【0026】実施例5 実施例1で得られたポリイミド前駆体溶液に固形分に対
し炭素繊維4質量%加え、混練機を用いて分散させた。
こうして得られた炭素繊維を分散しているポリイミド前
駆体溶液中に円柱状金型を浸漬し静かに引き上げた。こ
の円筒状金型に、金型外径よりも0.6mm大きい内径
を有するリング状ダイスを自由落下させて通過させた。
さらに、窒素雰囲気下で段階的に昇温しながら300℃
まで、5時間かけて昇温することによりポリイミド前駆
体のイミド化し、ポリイミドシームレスチューブを金型
から脱型した。このポリイミドシームレスチューブを切
り開き厚み測定を行ったところ56μmであった。切り
開かれたチューブに対し、長手方向における弾性率の測
定を行ったところ530kg/mm2 以上の値を示し
た。また切り開かれたチューブの吸水率を測定したとこ
ろ1.3質量%であり、長手方向及び周方向における寸
法変化率は0.1%未満であった。このチューブをX線
透過回折法測定したところ、2θ=11°付近に結晶性
の回折が見られたので、2θを固定してθ角を変化させ
た際の回折強度分布を測定したが、強度の変化は見られ
ず、配向度は0であった。
Example 5 To the polyimide precursor solution obtained in Example 1 was added 4% by mass of carbon fiber based on the solid content, and the mixture was dispersed using a kneader.
The cylindrical mold was immersed in the polyimide precursor solution in which the carbon fibers thus obtained were dispersed, and was gently pulled up. A ring-shaped die having an inner diameter 0.6 mm larger than the outer diameter of the mold was allowed to fall freely through the cylindrical mold and passed therethrough.
Further, the temperature is raised stepwise under a nitrogen atmosphere to 300 ° C.
The polyimide precursor was imidized by raising the temperature for 5 hours until the polyimide seamless tube was released from the mold. When this polyimide seamless tube was cut open and the thickness was measured, it was 56 μm. When the elastic modulus of the cut tube was measured in the longitudinal direction, it showed a value of 530 kg / mm 2 or more. The water absorption of the cut tube was measured to be 1.3% by mass, and the dimensional change in the longitudinal and circumferential directions was less than 0.1%. When this tube was measured by X-ray transmission diffraction method, crystalline diffraction was observed around 2θ = 11 °. Therefore, the diffraction intensity distribution when the 2θ was fixed and the θ angle was changed was measured. No change was observed, and the degree of orientation was 0.

【0027】比較例1 パラフェニレンジアミン10.27g(0.095mo
l)を、N,N−ジメチルアセトアミド386gに溶解
し、室温下で攪拌した。これにピロメリット酸二無水物
17.4g(0.08mol)およびビフェニルテトラ
カルボン酸二無水物5.88g(0.02mol)を加
え、室温下2時間攪拌し、均一な黄橙色透明溶液を得た
(溶質濃度8質量%)。得られたポリイミド前駆体溶液
をスプレーコートした。適宜、80℃にて乾燥を行いな
がら所定の塗工厚み量になるまで、スプレーコートを行
い、これを窒素雰囲気下で段階的に昇温しながら300
℃まで、5時間かけて昇温することによりイミド化を行
った。イミド化されたチューブを金型から脱型し、ポリ
イミドシームレスチューブを得、これを切り開き厚み測
定を行ったところ50μmであった。切り開かれたチュ
ーブに対し、弾性率の測定を行ったところ430kg/
mm 2 と低い値を示した。
Comparative Example 1 10.27 g of paraphenylenediamine (0.095 mol
l) is dissolved in 386 g of N, N-dimethylacetamide
And stirred at room temperature. This is pyromellitic dianhydride
17.4 g (0.08 mol) and biphenyltetra
5.88 g (0.02 mol) of carboxylic dianhydride was added.
Then, the mixture was stirred at room temperature for 2 hours to obtain a uniform yellow-orange transparent solution.
(Solute concentration 8% by mass). The obtained polyimide precursor solution
Was spray coated. Do not dry at 80 ° C as appropriate.
Spray coat until the specified coating thickness is reached.
The temperature is raised stepwise under a nitrogen atmosphere by 300
Imidation was carried out by raising the temperature to 5 ° C over 5 hours.
Was. Remove the imidized tube from the mold,
Obtain an imide seamless tube, cut it out and measure its thickness.
As a result, it was 50 μm. The opened Ju
When the elastic modulus was measured for the probe, 430 kg /
mm TwoAnd a low value.

【0028】比較例2 パラフェニレンジアミン10.8g(0.1mol)
を、N,N−ジメチルアセトアミド359gに溶解し、
室温下で攪拌した。これにピロメリット酸二無水物4.
3g(0.02mol)およびビフェニルテトラカルボ
ン酸二無水物23.5g(0.08mol)を1分間で
加え、室温下2時間攪拌した。メタノール0.48g
(0.015mol)およびジメチルアミノエタノール
0.024gを加え、70℃湯浴場で2時間攪拌した。
室温まで冷却した後、ジアミノジフェニルエーテル1.
001g(0.005mol)を加え、さらに1時間撹
拌を続けたところ、均一な黄橙色透明溶液が得られた
(溶質濃度10質量%)。こうして得られたポリイミド
前駆体溶液を円柱状金型外側面に比較例1と同様にして
スプレーコートをおこなった。これを窒素雰囲気下で段
階的に昇温しながら300℃まで、5時間かけて昇温す
ることによりイミド化を行ったが被膜は破れ、チューブ
を得ることはできなかった。被膜片の厚みは55μmで
あった。
Comparative Example 2 10.8 g (0.1 mol) of paraphenylenediamine
Is dissolved in 359 g of N, N-dimethylacetamide,
The mixture was stirred at room temperature. This is followed by pyromellitic dianhydride.
3 g (0.02 mol) and 23.5 g (0.08 mol) of biphenyltetracarboxylic dianhydride were added over 1 minute, and the mixture was stirred at room temperature for 2 hours. 0.48 g of methanol
(0.015 mol) and 0.024 g of dimethylaminoethanol were added, and the mixture was stirred in a 70 ° C hot water bath for 2 hours.
After cooling to room temperature, diaminodiphenyl ether
001 g (0.005 mol) was added, and stirring was further continued for 1 hour to obtain a uniform yellow-orange transparent solution (solute concentration: 10% by mass). The thus obtained polyimide precursor solution was spray-coated on the outer surface of a cylindrical mold in the same manner as in Comparative Example 1. This was heated up to 300 ° C. over 5 hours while gradually raising the temperature under a nitrogen atmosphere to perform imidization. However, the coating was broken, and a tube could not be obtained. The thickness of the coated piece was 55 μm.

【0029】比較例3 パラフェニレンジアミン10.8g(0.1mol)
を、N,N−ジメチルアセトアミド211gに溶解し、
室温下で攪拌した。これにビフェニルテトラカルボン酸
二無水物29.4g(0.1mol)を加え、室温下2
時間攪拌し、均一な黄橙色透明溶液が得られた(溶質濃
度16質量%)こうして得られたポリイミド前駆体溶液
を円柱状金型外側面にはけで塗布し、これに金型外径よ
りも300μm大きい内径を有するリング状ダイスを通
すことで金型外面に均一に前駆体溶液を塗布した。これ
を窒素雰囲気下で段階的に昇温しながら300℃まで、
5時間かけて昇温することによりイミド化し、ポリイミ
ドシームレスチューブを金型から脱型した。このポリイ
ミドシームレスチューブを切り開き厚み測定を行ったと
ころ40μmであった。切り開かれたチューブに対し、
弾性率の測定を行ったところ周方向には440〜470
kg/mm2 の値を示したが、長手方向には420kg
/mm2 の値しか示さなかった。また切り開かれたチュ
ーブの吸水率を測定したところ0.9質量%であった。
このチューブをX線透過回折法測定したところ、2θ=
11°付近に結晶性の回折が見られたため2θを固定し
てθ角を変化させた際の回折強度分布を測定したとこ
ろ、強度の変化が見られ、配向度は周方向におよそ0.
4であった。上記ポリイミドシームレスチューブの特性
値についての結果を表1に示す。
Comparative Example 3 10.8 g (0.1 mol) of paraphenylenediamine
Is dissolved in 211 g of N, N-dimethylacetamide,
The mixture was stirred at room temperature. To this was added 29.4 g (0.1 mol) of biphenyltetracarboxylic dianhydride, and the mixture was added at room temperature for 2 hours.
After stirring for a time, a uniform yellow-orange transparent solution was obtained (solute concentration: 16% by mass). The polyimide precursor solution thus obtained was applied to the outer surface of the cylindrical mold with a brush. Further, the precursor solution was uniformly applied to the outer surface of the mold by passing through a ring-shaped die having an inner diameter larger by 300 μm. This is heated up to 300 ° C in a nitrogen atmosphere while increasing the temperature stepwise.
It was imidized by raising the temperature over 5 hours, and the polyimide seamless tube was released from the mold. When this polyimide seamless tube was cut open and the thickness was measured, it was 40 μm. For the cut tube,
When the elastic modulus was measured, it was found to be 440 to 470 in the circumferential direction.
kg / mm 2 , but 420 kg in the longitudinal direction.
/ Mm 2 only. The water absorption of the cut tube was measured and found to be 0.9% by mass.
When this tube was measured by the X-ray transmission diffraction method, 2θ =
Since diffraction of the crystallinity was observed at around 11 °, the diffraction intensity distribution when the θ was changed while fixing 2θ was measured. As a result, a change in the intensity was observed, and the degree of orientation was about 0. 0 in the circumferential direction.
It was 4. Table 1 shows the results of the characteristic values of the polyimide seamless tube.

【0030】[0030]

【表1】 [Table 1]

【0031】[0031]

【発明の効果】以上のように、本発明のポリイミドシー
ムレスチューブは長手方向及び周方向における分子鎖の
配向度が低く、実質的に異方性を示さず、長手方向及び
周方向においても高い弾性率を有しており、吸水率が低
いものである。中でもカーボンブラックを含有させたも
のは、導電性を有し、帯電性の問題を解決できるもので
あり、炭素繊維を含有するものは、導電性を有し、帯電
性の問題を解決できるものであるとともに、機械的特性
がより優れたものとなる。したがって、本発明のポリイ
ミドシームレスチューブは、複写機、プリンターの熱定
着チューブとして長時間安定走行できる。また、本発明
によれば、このようなポリイミドシームレスチューブを
容易に製造することができる。
As described above, the polyimide seamless tube of the present invention has a low degree of molecular chain orientation in the longitudinal and circumferential directions, does not substantially exhibit anisotropy, and has a high elasticity in the longitudinal and circumferential directions. It has a low water absorption rate. Among them, those containing carbon black have conductivity and can solve the problem of chargeability, and those containing carbon fibers have conductivity and can solve the problem of chargeability. As well as having better mechanical properties. Therefore, the polyimide seamless tube of the present invention can run stably for a long time as a heat fixing tube of a copying machine or a printer. Further, according to the present invention, such a polyimide seamless tube can be easily manufactured.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C08L 79/08 C08L 79/08 Z // B29K 79:00 B29K 79:00 B29L 23:00 B29L 23:00 Fターム(参考) 4F072 AA02 AA07 AB10 AB14 AD45 AE08 AF01 AK03 AL11 AL16 4F205 AA40A AG08 GA05 GA08 GB01 GC01 GE02 GF25 GN13 GN28 GN29 GW05 4J002 CM041 DA017 DA036 FA047 FD017 FD116 GM00 GQ00 4J043 PA02 PA04 PB08 PB14 QB26 QB31 RA35 SA06 SB01 SB03 TA14 TA22 TB01 TB03 UA121 UA122 UA131 UA132 UB121 XA15 XA16 XA19 XB36 YA06 YA13 ZA11 ZA32 ZA44 ZA60 ZB41 ZB47 ZB51 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) C08L 79/08 C08L 79/08 Z // B29K 79:00 B29K 79:00 B29L 23:00 B29L 23:00 F term (for reference) 4F072 AA02 AA07 AB10 AB14 AD45 AE08 AF01 AK03 AL11 AL16 4F205 AA40A AG08 GA05 GA08 GB01 GC01 GE02 GF25 GN13 GN28 GN29 GW05 4J002 CM041 DA017 DA036 FA047 FD017 FD116 GM00 GQB0404G04B04B04J04 TA22 TB01 TB03 UA121 UA122 UA131 UA132 UB121 XA15 XA16 XA19 XB36 YA06 YA13 ZA11 ZA32 ZA44 ZA60 ZB41 ZB47 ZB51

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 一般式(1)に示すポリイミドからな
り、長手方向における引張弾性率が480kg/mm2
以上であることを特徴とするポリイミドシームレスチュ
ーブ。〔式中、nは1〜20の整数を示す。〕 【化1】
1. A polyimide made of the general formula (1) having a tensile modulus in the longitudinal direction of 480 kg / mm 2.
A polyimide seamless tube characterized by the above. [In formula, n shows the integer of 1-20. [Formula 1]
【請求項2】 24時間浸水後の吸水率が2質量%未満
であって、長手方向及び周方向における寸法変化率が
0.1%未満であることを特徴とする請求項1記載のポ
リイミドシームレスチューブ。
2. The polyimide seamless according to claim 1, wherein the water absorption after immersion in water for 24 hours is less than 2% by mass, and the dimensional change in the longitudinal and circumferential directions is less than 0.1%. tube.
【請求項3】 長手方向及び周方向における分子鎖の配
向度が0.1未満であることを特徴とする請求項1記載
のポリイミドシームレスチューブ。
3. The polyimide seamless tube according to claim 1, wherein the degree of molecular chain orientation in the longitudinal direction and the circumferential direction is less than 0.1.
【請求項4】 カーボンブラックを0.1質量%以上5
質量%未満を含有することを特徴とする請求項1記載の
ポリイミドシームレスチューブ。
4. A carbon black containing at least 0.1% by mass
The seamless polyimide tube according to claim 1, wherein the polyimide seamless tube contains less than 10% by mass.
【請求項5】 長さが4mm未満の炭素繊維を0.1〜
10質量%含有することを特徴とする請求項1記載のポ
リイミドシームレスチューブ。
5. A carbon fiber having a length of less than 4 mm is 0.1 to
The polyimide seamless tube according to claim 1, which contains 10% by mass.
【請求項6】 下記一般式(2)に示すカルボン酸と下
記一般式(3)に示すジアミンとからなる塩が溶質とし
て溶媒中に溶解しているポリイミド前駆体溶液を成形
し、ポリイミド前駆体をイミド化することを特徴とする
請求項1記載のポリイミドシームレスチューブの製造方
法。〔式中、lは0〜20の整数を表し、mは0〜20
の整数を表し、l+mは1〜20である。〕 【化2】
6. A polyimide precursor solution in which a salt comprising a carboxylic acid represented by the following general formula (2) and a diamine represented by the following general formula (3) is dissolved in a solvent as a solute, 2. The method for producing a polyimide seamless tube according to claim 1, wherein [Wherein, l represents an integer of 0 to 20, and m represents 0 to 20.
And l + m is 1 to 20. [Chemical formula 2]
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Cited By (7)

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JP2004323834A (en) * 2003-04-10 2004-11-18 Gunze Ltd Method for manufacturing seamless tubular polyimide film
JP2005247987A (en) * 2004-03-03 2005-09-15 Gunze Ltd Semiconducting polyimide precursor composition and manufacturing method of semiconducting polyimide tubular product using the same
JP2005247988A (en) * 2004-03-03 2005-09-15 Gunze Ltd Semiconducting high-concentration polyimide precursor composition and semiconducting polyimide tubular product using the same
JP2005247986A (en) * 2004-03-03 2005-09-15 Gunze Ltd Semiconducting aromatic amic acid composition and manufacturing method of semiconducting endless tubular polyimide film using the same
JP2010255002A (en) * 2010-08-06 2010-11-11 Gunze Ltd Semiconducting aromatic amic acid composition and manufacturing method of semiconducting endless tubular polyimide film using the same
US8097693B2 (en) 2004-03-03 2012-01-17 Gunze Limited Endless tubular polyimide film
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JP2004323834A (en) * 2003-04-10 2004-11-18 Gunze Ltd Method for manufacturing seamless tubular polyimide film
JP2005247987A (en) * 2004-03-03 2005-09-15 Gunze Ltd Semiconducting polyimide precursor composition and manufacturing method of semiconducting polyimide tubular product using the same
JP2005247988A (en) * 2004-03-03 2005-09-15 Gunze Ltd Semiconducting high-concentration polyimide precursor composition and semiconducting polyimide tubular product using the same
JP2005247986A (en) * 2004-03-03 2005-09-15 Gunze Ltd Semiconducting aromatic amic acid composition and manufacturing method of semiconducting endless tubular polyimide film using the same
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JP2010255002A (en) * 2010-08-06 2010-11-11 Gunze Ltd Semiconducting aromatic amic acid composition and manufacturing method of semiconducting endless tubular polyimide film using the same
CN111764156A (en) * 2020-06-28 2020-10-13 东华大学 Preparation method of high-performance polyimide fiber
CN111764156B (en) * 2020-06-28 2021-09-21 东华大学 Preparation method of high-performance polyimide fiber

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