JPS5947080B2 - sheet - Google Patents
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- JPS5947080B2 JPS5947080B2 JP10253875A JP10253875A JPS5947080B2 JP S5947080 B2 JPS5947080 B2 JP S5947080B2 JP 10253875 A JP10253875 A JP 10253875A JP 10253875 A JP10253875 A JP 10253875A JP S5947080 B2 JPS5947080 B2 JP S5947080B2
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- pulp
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Description
【発明の詳細な説明】 本発明はシートに関する。[Detailed description of the invention] The present invention relates to sheets.
更に詳しくは、特定の芳香族ポリアミドイミドから成る
パルプ粒子に耐熱性を有する短繊維を特定割合混合し、
加圧加熱して得られる耐熱性、電気絶縁性にすぐれ、か
つ力学的性質の改善されたシート特に、電気絶縁用に適
したシートに関する。従来、紙に用いられるパルプ粒子
としては、天然パルプが最も良く知られており、電気絶
縁紙としても天然パルプからの紙が多く使われている。More specifically, pulp particles made of a specific aromatic polyamide-imide are mixed with a specific proportion of short fibers having heat resistance,
The present invention relates to a sheet obtained by pressurizing and heating that has excellent heat resistance, electrical insulation, and improved mechanical properties, and in particular, a sheet suitable for electrical insulation. Conventionally, natural pulp is the most well-known pulp particle used in paper, and paper made from natural pulp is often used as electrically insulating paper.
しかし、天然パルプからの紙は、耐熱性に欠けるという
大きな欠点があり、電動機、変圧器等の電気機器の小型
化、軽量化に際して要求される耐熱性にはほど遠いもの
である。最近に至り、合成重合体から得られるパルプ粒
子が、耐熱性、電気絶縁性等にすぐれているため、電気
絶縁紙の素材として注目されるようになつた。例えば、
特公昭拐−11816号公報にはある種の芳香族ポリア
ミドの溶液中にLiCl、LiBrおよびCaCl2か
ら選ばれた化合物を芳香族ポリアミドに対して、1〜2
0重量%添加せしめ、ついで該溶液を沈澱剤中に分散せ
しめて、電気絶縁紙用パルプ状物体を製造する方法が記
載されている。この方法で得られたパルプ状物体からの
紙は、耐熱性には、すぐれているものの、絶縁破壊電圧
は未だ不充分であり、力学的性質、吸湿性も満足できる
水準にあるとは言えない。又、特公昭47−14761
号公報には、アスベスト繊維と芳香族ポリアミドとから
なるパルプ状粒子についての記載が見られるが、このパ
ルプ状粒子からの紙もやはり、力学的性質、電気絶縁性
は充分でなく、従つて、性能に対する、高度の信頼性が
要求される電気絶縁紙としては、その性能は必ずしも充
分であるとは言えない。However, paper made from natural pulp has a major drawback of lacking heat resistance, and is far from meeting the heat resistance required to reduce the size and weight of electrical equipment such as electric motors and transformers. Recently, pulp particles obtained from synthetic polymers have attracted attention as materials for electrically insulating paper because of their excellent heat resistance and electrical insulation properties. for example,
Japanese Patent Publication No. 11816 discloses that a compound selected from LiCl, LiBr, and CaCl2 is added to a solution of a certain type of aromatic polyamide in a ratio of 1 to 2 to the aromatic polyamide.
A method is described for producing an electrically insulating paper pulp by adding 0% by weight and then dispersing the solution in a precipitant. Although the paper made from the pulp-like material obtained by this method has excellent heat resistance, the dielectric breakdown voltage is still insufficient, and the mechanical properties and hygroscopicity cannot be said to be at a satisfactory level. . In addition, special public service No. 47-14761
Although the publication describes pulp-like particles made of asbestos fibers and aromatic polyamide, paper made from these pulp-like particles also does not have sufficient mechanical properties and electrical insulation properties, and therefore, As an electrically insulating paper that requires a high degree of reliability, its performance cannot necessarily be said to be sufficient.
更に、特公昭43−20421号公報には、粒状雲母と
、実質上溶融されていない、芳香族ポリアミドフイブリ
ドのもつれあつた混合物からなる電気絶縁用に適した耐
高温性シート状構造物が記載されている。Furthermore, Japanese Patent Publication No. 43-20421 discloses a high-temperature-resistant sheet-like structure suitable for electrical insulation consisting of an entangled mixture of granular mica and substantially unmelted aromatic polyamide fibrids. Are listed.
しかしながらここに記載されたシート状構造物も、小型
化、軽量化されるべき電気機器の電気絶縁材料としては
、特に力学的性質、含浸性、が不充分である。更にかか
るシート状構造物を製造する際、雲母とフイブリドが分
離するために、抄紙作業が極めて困難であるという欠点
を有している。更にかかるシート状構造物は、摩擦によ
り、雲母が容易に剥離するという欠点をも有する。我々
はこれらの欠点の克服、すなわち、
等を達成できるものとして、先に特開昭48一1004
50号公報において、雲母粒子30〜90重量%と、含
窒素ポリ複素環状化合物またはその前駆体50〜10重
量?とからなり、前記雲母粒子を含窒素ポリ複素環状化
合物または、その前駆体で被い且つ連結してなるパルプ
粒子20〜80重量%と、短繊維80〜20重量%とを
混合し、加圧加熱してなるシートを提案した。However, the sheet-like structure described herein also has insufficient mechanical properties and impregnability, especially as an electrical insulating material for electrical equipment that is to be made smaller and lighter. Furthermore, when producing such a sheet-like structure, the mica and fibrids separate, which makes the papermaking process extremely difficult. Furthermore, such a sheet-like structure has the disadvantage that the mica easily peels off due to friction. We have previously proposed Japanese Patent Application Laid-Open No. 48-1004 to overcome these shortcomings, i.e., to achieve the following.
No. 50, 30 to 90% by weight of mica particles and 50 to 10% by weight of a nitrogen-containing polyheterocyclic compound or its precursor. 20 to 80% by weight of pulp particles formed by covering and connecting the mica particles with a nitrogen-containing polyheterocyclic compound or a precursor thereof, and 80 to 20% by weight of short fibers are mixed, and then pressurized. We proposed a sheet that can be heated.
前記特開昭48−100450号公報において、含窒素
ポリ複素環状化合物の例の1つとして、芳香族ポリアミ
ドイミドを挙げている。In JP-A-48-100450, aromatic polyamideimide is mentioned as one example of the nitrogen-containing polyheterocyclic compound.
特開昭48−100450号公報で記した芳香族ポリア
ミドイミドからのシートは耐熱性、含浸性、電気絶縁性
、耐吸湿性等にはすぐれているが、力学的性質は未だ不
充分であつた。その後、本発明者は特に力学的性質の改
善を目的として、芳香族ポリアミドイミドの特徴を損わ
ない範囲で、更に検討を進めた結果、特定のイミドジカ
ルボン酸とイソフタル酸および/又はテレフタル酸から
なる特定割合のカルボン酸混合物と特定のジイソシアネ
ートとを加熱反応せしめて得られる、イミド結合よりア
ミド結合の多い特定の芳香族ポリアミドイミドのN−メ
チル−2−ピロリドンの溶液を沈澱剤中に導入し、微細
な粒子として沈澱せしめることによつて、抄紙性の良い
パルプ粒子が得られこのパルプ粒子と短繊維とを特定割
合に混合し、加圧加熱して得たシートは、耐熱性、含浸
性、電気絶縁性等にすぐれているのはもちろんのこと、
力学的性質の改善できることを知見し本発明を完成した
ものである。The sheet made of aromatic polyamideimide described in JP-A No. 48-100450 has excellent heat resistance, impregnation properties, electrical insulation properties, moisture absorption resistance, etc., but its mechanical properties are still insufficient. . After that, the present inventor conducted further studies with the aim of improving the mechanical properties, within a range that does not impair the characteristics of aromatic polyamideimide. A solution of N-methyl-2-pyrrolidone of a specific aromatic polyamide-imide having more amide bonds than imide bonds, which is obtained by heat-reacting a carboxylic acid mixture in a specific proportion with a specific diisocyanate, is introduced into a precipitant. By precipitating it as fine particles, pulp particles with good paper-making properties are obtained. These pulp particles and short fibers are mixed in a specific ratio and heated under pressure to produce a sheet that has good heat resistance and impregnation properties. It not only has excellent electrical insulation properties, but also
The present invention was completed by discovering that the mechanical properties could be improved.
すなわち、本発明は、4.4′−ビス(トリメリトイミ
ド)ジフエニルメタン及び/又は4.4′−ビス−(ト
リメリトイミド)ジフエニルエーテルとイソフタル酸お
よび/又はテレフタル酸で構成されその組成が第1図の
斜線で示された範囲内のカルボン酸混合物と4.4′
−ジフエニルメタンジイソシアネート及び/又は4.4
′−ジフエニルエーテルジイソシアネートとを加熱反応
せしめて得られる芳香族ポリアミドイミドを主たる樹脂
成分とするパルプ粒子20〜95重量部と短繊維5〜8
0重量部とを混合抄紙し、加圧加熱してなるシートであ
る。That is, the present invention is composed of 4,4'-bis(trimellitimido)diphenylmethane and/or 4,4'-bis(trimellitimido)diphenyl ether and isophthalic acid and/or terephthalic acid, and the composition thereof is as shown in FIG. Carboxylic acid mixture within the shaded range and 4.4'
- diphenylmethane diisocyanate and/or 4.4
20 to 95 parts by weight of pulp particles whose main resin component is aromatic polyamideimide obtained by heating reaction with '-diphenyl ether diisocyanate and 5 to 8 parts by weight of short fibers.
This sheet is made by mixing 0 parts by weight and pressurizing and heating.
本発明において、使用するイミドジカルボン酸は4.4
′−ビス(トリメリトイミド)ジフエニルメタンおよび
/又は4.4′−ビス(トリメリトイミド)ジフエニル
エーテルであり、例えば特公昭38−21500号公報
、特公昭41−19302号公報等に記載の方法によつ
て製造することができる。In the present invention, the imidodicarboxylic acid used is 4.4
'-bis(trimellitimide) diphenylmethane and/or 4,4'-bis(trimellitimide) diphenyl ether, produced by the method described in, for example, Japanese Patent Publication No. 38-21500, Japanese Patent Publication No. 41-19302, etc. can do.
又、本発明で用いられるジイソシアネートは4.4′−
ジフエニルメタンジイソシアネートおよび/又は4.4
′−ジフエニルエーテルジイソシアネートであり、本発
明の実施例では就中4.4′一ジフエニルメタンジイソ
シアネートが好んで用いられる。Furthermore, the diisocyanate used in the present invention is 4.4'-
diphenylmethane diisocyanate and/or 4.4
'-diphenyl ether diisocyanate, in particular 4,4'-diphenylmethane diisocyanate, is preferably used in the embodiments of the present invention.
本発明において使用する芳香族ポリアミドイミドを得る
に際しては、イミドジカルボン酸とジイソシアネートと
を溶融状態で反応せしめる事も出来るが、イミドジカル
ボン酸および得られる芳香族ポリアミドイミドは高融点
であり、均一状態で反応が進行しない場合もあるので、
不活性有機極性溶媒の存在下に反応を行うことが望まし
い。In order to obtain the aromatic polyamide-imide used in the present invention, imidodicarboxylic acid and diisocyanate can be reacted in a molten state, but the imidodicarboxylic acid and the resulting aromatic polyamide-imide have a high melting point, Since the reaction may not proceed,
It is desirable to carry out the reaction in the presence of an inert organic polar solvent.
反応溶媒としては、イミドジカルボン酸、イソフタル酸
、および/又はテレフタル酸からなるカルボン酸混合物
及びジイソシアネートの少なく共一方、好ましくは両方
を溶解するとともに、反応途中で生成する低量重合体を
充分高分子量の芳香族ポリアミドイミドが得られるまで
活性が失われない程度に少なくとも膨潤、好ましくは溶
解し得るものであることが要求され、好適な反応溶媒の
例としては、N−メチル−2−ピロリドン、N.N′
一ジメチルアセトアミド、ジメチルホルムアミド、ヘキ
サメチルホスホルアミド等があげられる。Nーメチル−
2−ピロリドンが特に好適である。有機溶媒の存在下で
重縮合を行なう場合、反応溶媒にイミドジカルボン酸と
イソフタル酸および/又はテレフタル酸を溶解せしめ、
次いでジイソシアネートを添加する方法が良い。カルボ
ン酸混合物とジイソシアネートとは等モルないしジイソ
シアネートが約10モル%まで過剰で反応させるのが好
ましい。反応温度は100℃から180℃の範囲が好適
であり、反応中に発生した炭酸ガスは充分に除去しなけ
ればならない。反応終了後、得られた重合体は反応混合
物を非溶剤に投入することにより、再沈分離する事もで
きるが、反応終了時において、反応溶液が均一に得られ
る場合には、それをそのまま或いは適当な溶媒で希釈し
たり、添加剤を加えたりして、パルプ製造用の原液とし
て使用することが好ましい。本発明において使用する重
合体を製造するに際し、カルボン酸混合物の組成が第1
図斜線で示した範囲外の時は、反応途中の低量重合体が
反応溶媒に溶解せず、固型分が析出してきて、反応が均
一に進行しなくなり、充分高分子量の重合体を得るのが
困難となる。The reaction solvent should dissolve at least one, preferably both, of a carboxylic acid mixture consisting of imidodicarboxylic acid, isophthalic acid, and/or terephthalic acid and diisocyanate, and at the same time dissolve low polymers produced during the reaction with a sufficiently high molecular weight. The reaction solvent is required to be able to swell, preferably dissolve, at least to the extent that the activity is not lost until the aromatic polyamideimide is obtained. Examples of suitable reaction solvents include N-methyl-2-pyrrolidone, N-methyl-2-pyrrolidone, .. N'
Examples include monodimethylacetamide, dimethylformamide, hexamethylphosphoramide, and the like. N-methyl-
2-pyrrolidone is particularly preferred. When polycondensation is carried out in the presence of an organic solvent, imidodicarboxylic acid and isophthalic acid and/or terephthalic acid are dissolved in the reaction solvent,
A preferred method is to then add diisocyanate. It is preferred that the carboxylic acid mixture and diisocyanate are reacted in an equimolar to an excess of about 10 mol % of the diisocyanate. The reaction temperature is preferably in the range of 100°C to 180°C, and carbon dioxide gas generated during the reaction must be sufficiently removed. After the completion of the reaction, the obtained polymer can be reprecipitated and separated by pouring the reaction mixture into a non-solvent, but if a uniform reaction solution is obtained at the end of the reaction, it can be used as it is or It is preferable to dilute it with a suitable solvent or add additives and use it as a stock solution for pulp production. When producing the polymer used in the present invention, the composition of the carboxylic acid mixture is
When the range is outside the shaded range in the figure, the low-weight polymer in the middle of the reaction will not dissolve in the reaction solvent, solid matter will precipitate, and the reaction will not proceed uniformly, resulting in a sufficiently high molecular weight polymer. becomes difficult.
例えば第1図点A)すなわちイミドジカルボン酸45モ
ル%、イソフタル酸5モル%、テレフタル酸50モル%
などテレフタル酸が30モル%を越える領域や点Bすな
わち、イミドジカルボン酸10モル%、イソフタル酸8
0モル%、テレフタル酸10モル%など、イソフタル酸
が75モル%を越える領域更には、点Cすなわち、イミ
ドジカルボン酸5モル%、イソフタル酸70モル%、テ
レフタル酸25モル%などイミドジカルボン酸が10モ
ル%より少ない領域では充分高分子量の重合体を得るの
が困難であり、この預域のカルボン酸混合物とジイソシ
アネートとから得られた芳香族ポリアミドイミドを用い
て製造したパルプ粒子からのシートは、力学的性質が不
満足なものとなる。更には、未溶解物が存在し、この為
電気絶縁性が悪くなる場合が多い。従つて、カルボン酸
混合物の組成が、第1図斜線で示した範囲内にある時に
限つて、力学的性質等のすぐれたシートが得られるので
ある。本発明に使用するパルプ粒子の製造に際しては、
重合体溶液を沈澱剤中に導入し、微細な粒子として沈澱
させ、パルプ粒子となす方法を適用できる。For example, point A in Figure 1: 45 mol% imidodicarboxylic acid, 5 mol% isophthalic acid, 50 mol% terephthalic acid.
Areas where terephthalic acid exceeds 30 mol%, such as point B, i.e., imidodicarboxylic acid 10 mol%, isophthalic acid 8 mol%
Furthermore, in areas where isophthalic acid exceeds 75 mol%, such as 0 mol%, terephthalic acid 10 mol%, point C, imidodicarboxylic acid 5 mol%, isophthalic acid 70 mol%, terephthalic acid 25 mol%, etc. It is difficult to obtain a polymer with a sufficiently high molecular weight in a region of less than 10 mol%, and a sheet made from pulp particles produced using an aromatic polyamideimide obtained from a carboxylic acid mixture and a diisocyanate in this region is , the mechanical properties become unsatisfactory. Furthermore, undissolved substances are present, which often results in poor electrical insulation. Therefore, only when the composition of the carboxylic acid mixture is within the shaded range in FIG. 1 can a sheet with excellent mechanical properties be obtained. When producing pulp particles used in the present invention,
A method can be applied in which a polymer solution is introduced into a precipitant and precipitated as fine particles to form pulp particles.
重合体溶液中の重合体濃度は、重合体種類、重合体の重
合度等によつて異なるが、概略2〜15重量%が望まし
い。又、溶液中に1〜10重量%好ましくは3〜9重量
%の水を含有しても差支えない。又、溶液中に溶液と実
質上反応せず、又、溶液に溶解しない微小な固体無機物
質を添加混合することは、シートの含浸性、耐熱性、耐
炎性、電気的性質をより一層向上せしめる上で好ましい
ことである。この場合固体無機物質としては、電気絶縁
性、耐熱性にすぐれている雲母類が好ましく、更にアス
ベスト、ガラスプレークズ、石英粉末、タルク、カオリ
ン、アルミナ、硫酸カルシウムなどが利用できる。固体
無機物質を混合する場合は、前記重合体の5〜900重
量弊好ましくは20〜400重量%である。又、二種以
上の固体無機物質を同時に添加混合しても差し支えない
。前記した固体無機物質を溶液中に混合する際、できる
だけ均一に分散させるのが好ましく、装置として例えば
、アトライター(三井三池製作所製)、T・K・ホモミ
クサー(特殊機化学工業製)などが有効である。次に本
発明において使用するパルプ粒子を製造する際に用いる
沈澱剤としては、重合体溶液の溶媒とは混和性であるが
、重合体に対しては非溶媒である液体又は溶液が望まし
い。The concentration of the polymer in the polymer solution varies depending on the type of polymer, the degree of polymerization of the polymer, etc., but is preferably approximately 2 to 15% by weight. Further, the solution may contain 1 to 10% by weight, preferably 3 to 9% by weight of water. Additionally, adding and mixing a minute solid inorganic substance that does not substantially react with or dissolve in the solution further improves the impregnation properties, heat resistance, flame resistance, and electrical properties of the sheet. The above is preferable. In this case, the solid inorganic substance is preferably mica, which has excellent electrical insulation and heat resistance, and furthermore, asbestos, glass flakes, quartz powder, talc, kaolin, alumina, calcium sulfate, etc. can be used. When a solid inorganic substance is mixed, the amount is 5 to 900% by weight, preferably 20 to 400% by weight of the polymer. Furthermore, two or more types of solid inorganic substances may be added and mixed at the same time. When mixing the solid inorganic substance described above into a solution, it is preferable to disperse it as uniformly as possible, and effective devices include Attritor (manufactured by Mitsui Miike Manufacturing Co., Ltd.) and T.K. Homomixer (manufactured by Tokushu Kikagaku Kogyo Co., Ltd.). It is. Next, as the precipitant used in producing the pulp particles used in the present invention, a liquid or solution that is miscible with the solvent of the polymer solution but is a non-solvent for the polymer is desirable.
重合体の溶媒として、有機溶媒を用いた場合に使用でき
る沈澱剤は、水単独或いは水有機溶媒混合液、グリセリ
ン、グリセリンー水混合液、エチレングリコール等でも
良いし、或いは又式MXnで表わされる塩類の1種又は
2種以上を溶解している水溶液であつても良い。沈澱剤
は高速攪拌を行ない、導入した溶液から脱溶媒すると同
時に剪断作用又は叩解作用を生ぜしめるように操作する
。When an organic solvent is used as the solvent for the polymer, the precipitant that can be used may be water alone, a water-organic solvent mixture, glycerin, a glycerin-water mixture, ethylene glycol, or a salt represented by the formula MXn. It may be an aqueous solution in which one or more of these are dissolved. The precipitant is stirred at high speed and operated to remove the solvent from the introduced solution and at the same time to produce a shearing or beating action.
本発明において、短繊維と混合するパルプ粒子の量はシ
ートに対して20〜95重量%でなければならない。In the present invention, the amount of pulp particles mixed with staple fibers should be 20-95% by weight based on the sheet.
パルプ粒子の量が20重量%より少いとシートの絶縁破
壊電圧、力学的性質が低下するので好ましくない。また
、パルプ粒子の量が95重量%より多い場合は含浸性、
力学的性質共に悪くなる。パルプ粒子と短繊維からの抄
紙は、従来の天然パルプから製紙する場合と同様、長網
式、或いは円網式の製紙機を用いて、湿式法により抄紙
するのが良い。この際使用する短繊維としては耐熱性の
良い繊維であれば何れでも良く、芳香族ポリアミドから
なる繊維(例えば帝人社製コーネツクス一登録商標−)
や芳香族ポリアミドイミドからなる繊維(例えばフラン
ス国ローヌ・プーラン社製、ケルメル)などが好適であ
る。更に、ガラス繊維等の無機化合物からなる短繊維も
使用できる。又2種以上の短繊維を同時に添加混合して
も良い。短繊維の繊度は0.5〜10デニール特に1.
0〜3.0デニールが好ましい。更に短繊維の長さは短
繊維の繊度によつても異なるが、1〜15u好ましくは
5〜10m7nが良い。前記の如くして得られたシート
は乾燥後熱プレス又は熱ロール等の手段で、加圧下加熱
することにより、すぐれた性能を付与することができる
。加圧する時の温度は、重合体種類、短繊維の種類等に
よつて異なるが、11『C〜350℃が適当である。圧
力は温度と同様、重合体種類等によつて異なるが、40
0kg/d以下が望ましい。かくして得られたシートは
、均一に分散したパルプ粒子と短繊維とのからみ合い、
接着が充分に行なわれており、満足できる水準の力学的
性質、電気絶縁性を発現するのである。以下本発明にお
ける主要な測定値について測定方法を説明する。If the amount of pulp particles is less than 20% by weight, the dielectric breakdown voltage and mechanical properties of the sheet will decrease, which is not preferable. In addition, if the amount of pulp particles is more than 95% by weight, impregnating property,
Both mechanical properties deteriorate. Paper made from pulp particles and short fibers is preferably made by a wet method using a fourdrinier or cylinder type paper making machine, similar to the conventional paper making from natural pulp. The short fibers used at this time may be any fibers that have good heat resistance, such as fibers made of aromatic polyamide (for example, Teijin Co., Ltd.'s Cornex I registered trademark).
Fibers made of aromatic polyamideimide (for example, Kermel, manufactured by Rhône-Poulenc, France) are suitable. Furthermore, short fibers made of inorganic compounds such as glass fibers can also be used. Also, two or more types of short fibers may be added and mixed at the same time. The fineness of short fibers is 0.5 to 10 deniers, especially 1.
A denier of 0 to 3.0 is preferred. Further, the length of the short fibers varies depending on the fineness of the short fibers, but is preferably 1 to 15 m and preferably 5 to 10 m and 7 n. After drying, the sheet obtained as described above can be imparted with excellent performance by heating under pressure using a hot press, a hot roll, or the like. The temperature during pressurization varies depending on the type of polymer, the type of short fibers, etc., but a temperature of 11°C to 350°C is appropriate. Like the temperature, the pressure varies depending on the type of polymer, etc., but
Desirably 0 kg/d or less. The sheet thus obtained is made up of uniformly dispersed pulp particles and short fibers,
Adhesion is sufficient, and it exhibits satisfactory mechanical properties and electrical insulation properties. The method for measuring the main measured values in the present invention will be explained below.
以下実施例により本発明を詳述する。The present invention will be explained in detail with reference to Examples below.
実施例 1
重合体溶液の作成
4.4′−ビス(トリメリトイミド)ジフエニルメノン
80モル%、イソフタル酸49モル%、テレフタル酸2
1モル?よりなるカルボン酸混合物と、4.4′−ジフ
エニルメタンジイソシアネートとを、N−メチル−2−
ピロリドン中でジイソシアネート4.0モル%過剰で反
応せしめてポリアミドイミド(N−メチル−2−ピロリ
ドン中対数粘度0.61)を25重量%含む溶液を得た
。Example 1 Preparation of polymer solution 4.4'-bis(trimellitimido)diphenylmenone 80 mol%, isophthalic acid 49 mol%, terephthalic acid 2
1 mole? A carboxylic acid mixture consisting of N-methyl-2-
The reaction was carried out in pyrrolidone with a 4.0 mol% excess of diisocyanate to obtain a solution containing 25% by weight of polyamideimide (logarithmic viscosity in N-methyl-2-pyrrolidone, 0.61).
(溶液A)別にN−メチル−2−ピロリドン2350重
量部にイオン交換水190重量部を加えた後、アンドレ
アゼンピペット法で測定した粒子径が、400〜100
0メツシユ相当の雲母粉末418重量部を加え、次いで
T.Kホモミクサーで40分間攪拌して、N−メチル−
2−ピロリドン、水、雲母からなる混合液を得た。(混
合液B)次に混合液B2985重量部に溶液A9OO重
量部を加えて均一になるまで攪拌し、沈澱に供する為の
溶液を得た。(溶液C)沈澱剤の作成
N−メチル−2−ピロリドン55重量部と水45重量部
とを混合し沈澱剤とした。(Solution A) Separately, 190 parts by weight of ion-exchanged water was added to 2350 parts by weight of N-methyl-2-pyrrolidone, and the particle size measured by the Andreasen pipette method was 400 to 100.
418 parts by weight of mica powder equivalent to 0 mesh was added, and then T. Stir with a K homomixer for 40 minutes to prepare N-methyl-
A mixed solution consisting of 2-pyrrolidone, water, and mica was obtained. (Mixed solution B) Next, 900 parts by weight of solution A were added to 2985 parts by weight of mixed solution B, and the mixture was stirred until it became homogeneous to obtain a solution to be used for precipitation. (Solution C) Preparation of precipitant 55 parts by weight of N-methyl-2-pyrrolidone and 45 parts by weight of water were mixed to prepare a precipitant.
パルプ粒子の製造
バツスルのついているステーターとタービン翼型ロータ
との組み合せからなり、かつ沈澱剤、溶液の供給口およ
び沈澱後のパルプ粒子スラリーの排出口を備えた管路撹
拌連続沈澱機に溶液CO.5kg/駆、沈澱剤5kg/
駆の流量で同時に供給しパルプ粒子スラリーを排出口か
らとり出した。Production of Pulp Particles A solution of CO is introduced into a conduit-stirring continuous precipitator, which consists of a combination of a stator with a battlement and a turbine blade-shaped rotor, and is equipped with a precipitant, a solution supply port, and a discharge port for the pulp particle slurry after precipitation. .. 5kg/driver, precipitant 5kg/
The slurry of pulp particles was simultaneously supplied at a flow rate of 100 liters and taken out from the outlet.
この際沈澱剤の温度は33℃、溶液Cは20℃に調節し
た。又、ローターの回転数は7100r.p.m.とし
た。得られたパルプ粒子スラリーを遠心分離機に入れ大
部分の沈澱剤をf液としてとり出した。次いでイオン交
換水を供給し充分に洗浄を行なつた。製紙
かくして得られたパルプ粒子2.161(固型分)と7
mmに切断した。At this time, the temperature of the precipitant was adjusted to 33°C, and the temperature of solution C was adjusted to 20°C. Also, the rotation speed of the rotor is 7100r. p. m. And so. The obtained pulp particle slurry was put into a centrifuge, and most of the precipitant was taken out as an f-liquid. Next, ion-exchanged water was supplied to perform thorough washing. Papermaking Pulp particles thus obtained 2.161 (solid content) and 7
It was cut into mm.
芳香族ポリアミド繊維(帝人社製、コーネツクス)0.
54gを含む水分散液からタツピースタンダードシート
マシンを用いて抄紙したところ、抄紙性は良好で地合の
良好なシートを得た。このシートを270℃、2001
<g/0IILの条件で熱プレスして厚さ110μの紙
を得た。この紙の引張強度は5.4kg/Udl伸度は
4.0%であり、良好であつた。又、絶縁破壊強度は2
9Kv/Tnnであつた。更に、この紙をシリコーン油
中に浸漬し240℃で1000時間放置したが、引張強
伸度はほとんど変らず耐熱性も良好であつた。Aromatic polyamide fiber (manufactured by Teijin Co., Ltd., Cornex) 0.
When paper was made from an aqueous dispersion containing 54 g using a Tatsupi standard sheet machine, a sheet with good paper-making properties and good texture was obtained. This sheet was heated to 270℃ in 2001.
A paper having a thickness of 110 μm was obtained by hot pressing under the condition of <g/0IIL. The tensile strength of this paper was 5.4 kg/Udl and the elongation was 4.0%, which was good. Also, the dielectric breakdown strength is 2
It was 9Kv/Tnn. Further, this paper was immersed in silicone oil and left at 240°C for 1000 hours, but the tensile strength and elongation hardly changed and the heat resistance was good.
カルボン酸混合物が本発明パルプ粒子を製造する場合と
は異なる時の例を比較として次に示す。比較例 1
実施例1において、4.4’ −ビス(トリメリトイミ
ド)ジフエニルメタン33モル%およびトリメリト酸無
水物67モル%からなるカルボン酸混合物を使う以外は
同様に実施し、対数粘度0.7のポリアミドイミドを得
た。For comparison, an example in which the carboxylic acid mixture is different from that used in producing the pulp particles of the present invention is shown below. Comparative Example 1 The same procedure as in Example 1 was carried out except that a carboxylic acid mixture consisting of 33 mol% of 4.4'-bis(trimellitimido)diphenylmethane and 67 mol% of trimellitic anhydride was used, and a polyamide with a logarithmic viscosity of 0.7 was used. I got imide.
次いで、沈澱剤としてN−メチル−2−ピロリドン67
重量部と水33重量とからなる混合液を使う以外は実施
例1と全く同様にパルプ粒子を製造、製紙した。Then, N-methyl-2-pyrrolidone 67 was used as a precipitant.
Pulp particles were produced and paper was made in exactly the same manner as in Example 1, except that a mixed solution consisting of 33 parts by weight and 33 parts by weight of water was used.
かくして得られた紙の絶縁破壊強度は良好であつたが、
引張強伸度はそれぞれ3.6kg/一、1.3%と悪く
、満足出来る水準ではなかつた。実施例 2〜9
4.4’ −ビス(トリメリトイミド)ジフエニルメタ
ン、イソフタル酸およびテレフタル酸の割合を種々に変
えて、実施例1と同様にしてパルプ粒子を得た。Although the dielectric breakdown strength of the paper thus obtained was good,
The tensile strength and elongation were poor at 3.6 kg/1 and 1.3%, respectively, which were not at a satisfactory level. Examples 2 to 9 Pulp particles were obtained in the same manner as in Example 1, with various proportions of 4.4'-bis(trimellitimido)diphenylmethane, isophthalic acid, and terephthalic acid.
このパルプ粒子からやはり実施例1と同様にして紙を得
た。カルボン酸混合物の組成と得られた紙の引張強伸度
との関係は第1表のとおりであつた。いずれの場合も絶
縁破壊強度は27〜30KV/ Mynで良好であり、
力学的性質も第1表に示したとおり良好である。Paper was obtained from the pulp particles in the same manner as in Example 1. Table 1 shows the relationship between the composition of the carboxylic acid mixture and the tensile strength and elongation of the paper obtained. In either case, the dielectric breakdown strength is good at 27-30KV/Myn,
The mechanical properties are also good as shown in Table 1.
比較例 2
カルボン酸混合物の組成が第1図斜線で示した範囲より
はずれている場合の例を比較として次に示す。Comparative Example 2 An example in which the composition of the carboxylic acid mixture deviates from the shaded range in FIG. 1 is shown below for comparison.
4.4’ −ビス(トリメリトイミド)ジフエニルメタ
ン55モル%、テレフタル酸45モル%よ ・りなるカ
ルボン酸混合物と、4.4’ −ジフエニルメタンジイ
ソシアネートとを、N−メチル−2−ピロリドン中でジ
イソシアネート5モル%過剰で反応せしめたところ、微
細な未溶解物が多数浮遊していた。A carboxylic acid mixture consisting of 55 mol% of 4.4'-bis(trimellitimido)diphenylmethane and 45 mol% of terephthalic acid and 4.4'-diphenylmethane diisocyanate were diisocyanate-treated in N-methyl-2-pyrrolidone. When the reaction was carried out in excess of 5 mol %, many fine undissolved substances were suspended.
フイルタープレスで未溶解物を除去した後、対数粘度を
測定したところ0.41であつた。沈澱剤中のN−メチ
ル−2−ピロリドン濃度を60重量%として、他は実施
例1と同様にしてパルプ粒子を製造したが、得られたパ
ルプ粒子は大きさが非常に小さく、遠心分離機による洗
浄中沢布からの漏洩が多く好ましくなかつた。次いで、
実施例1と同様にして紙を得たが、この紙は強伸度はそ
れぞれ2.5kg/一、0.9%であり、悪かつた。After removing undissolved matter using a filter press, the logarithmic viscosity was measured and found to be 0.41. Pulp particles were produced in the same manner as in Example 1 except that the concentration of N-methyl-2-pyrrolidone in the precipitant was 60% by weight. There was a lot of leakage from the washed cloth, which was not desirable. Then,
Paper was obtained in the same manner as in Example 1, but the strength and elongation of this paper were 2.5 kg/1 and 0.9%, respectively, which were poor.
又、フイルタープレスで除き得なかつた未溶解物の為か
、絶縁破壊強度も2/ Mmと低目であつた。In addition, the dielectric breakdown strength was low at 2/Mm, probably due to undissolved substances that could not be removed by the filter press.
比較例 3
比較例2と同様カルボン酸混合物の組成が第1図斜線で
示した範囲よりはずれている場合の例である。Comparative Example 3 Similar to Comparative Example 2, this is an example in which the composition of the carboxylic acid mixture deviates from the range shown by diagonal lines in FIG.
4.4′−ビス(トリメリトイミド)ジフエニルエーテ
ル100モル%と4.4′−ジフエニルエーテルジイソ
シアネートとを、N−メチル−2−ピロリドン中でジイ
ソシアネート4モル%過剰で反応せしめて、ポリアミド
イミド(対数粘度0.70)を25重量%含む溶液を得
た。Polyamideimide ( A solution containing 25% by weight of viscosity (logarithmic viscosity 0.70) was obtained.
次いで、沈澱剤中のN−メチル−2−ピロリドン濃度を
68%とする以外は実施例1と同様にしてパルプ粒子を
得た。このパルプ粒子を用いて、やはり、実施例1と同
様にして厚さ115μの紙を得た。この紙の引張強度は
、3.1kg/Md、伸度は1.4%であり、満足でき
る水準のものではなかつた。実施例 10
4.4′−ビス(トリメリトイミド)ジフエニルメタン
70モル%、イソフタル酸15モル%、テレフタル酸1
5モル%よりなるカルボン酸混合物と4.4′−ジフエ
ニルメタンジイソシアネートとを、N−メチル−2−ピ
ロリドン中でジイソシアネート4.0モル%過剰で反応
せしめた後更にN−メチル−2−ピロリドンを加えて希
釈し、ポリアミドイミド(対数粘度0.68)を8.8
重量%含む溶液を得た。Next, pulp particles were obtained in the same manner as in Example 1 except that the concentration of N-methyl-2-pyrrolidone in the precipitant was 68%. Using these pulp particles, a paper having a thickness of 115 μm was obtained in the same manner as in Example 1. The tensile strength of this paper was 3.1 kg/Md, and the elongation was 1.4%, which were not at a satisfactory level. Example 10 4.4'-bis(trimellitimido)diphenylmethane 70 mol%, isophthalic acid 15 mol%, terephthalic acid 1
5 mol % of a carboxylic acid mixture and 4.4'-diphenylmethane diisocyanate are reacted in N-methyl-2-pyrrolidone in a 4.0 mol % excess of diisocyanate, followed by further N-methyl-2-pyrrolidone. diluted by adding polyamideimide (logarithmic viscosity 0.68) to 8.8
A solution containing % by weight was obtained.
(溶液A)一方、沈澱剤として、N−メチル−2−ピロ
リドン61重量%と水39重量?とから成る混合液を用
意した。(凝固価34)次いで実施例1とほぼ同様の方
法によりパルプ粒子を得た。かくして得られたパルプ粒
子1.62g(固型分)と7uに切断した芳香族ポリア
ミド繊維(帝人社製コーネツクス繊維1.5デニール)
1.08f!を含む水分散液からタツピースタンダード
シートマシンを用いて抄紙したところ、抄紙性は良好で
、地合の良好なシートを得た。(Solution A) On the other hand, as a precipitant, 61% by weight of N-methyl-2-pyrrolidone and 39% by weight of water were used. A mixed solution consisting of was prepared. (Coagulation value: 34) Pulp particles were then obtained in substantially the same manner as in Example 1. 1.62 g (solid content) of the thus obtained pulp particles and an aromatic polyamide fiber cut into 7 u pieces (1.5 denier Cornex fiber manufactured by Teijin)
1.08f! When paper was made from an aqueous dispersion containing the following using a Tatsupi standard sheet machine, a sheet with good paper-making properties and good texture was obtained.
このシートを270℃、200kg/41177!の条
件で熱プレスして厚さ約130μの紙を得た。This sheet at 270℃, 200kg/41177! A paper having a thickness of about 130 μm was obtained by hot pressing under the following conditions.
この紙の性能は次のとおりでありいずれもすぐれていた
。実施例 11実施例1において、4.4′−ビス(ト
リメリトイミド)ジフエニルメタンの代りに、4.4′
−ビス(トリメリトイミド)ジフエニルエーテルを使い
、4.4′−ジフエニルメタンジイソシアネートの代り
に4.4′−ジフエニルエーテルジイソシアネートを使
う以外は、実施例1と全く同様にしてパルプ粒子を得た
。The performance of this paper was as follows, and all were excellent. Example 11 In Example 1, instead of 4.4'-bis(trimellitimido)diphenylmethane, 4.4'
Pulp particles were obtained in exactly the same manner as in Example 1, except that -bis(trimellitimide) diphenyl ether was used and 4,4'-diphenyl ether diisocyanate was used instead of 4,4'-diphenylmethane diisocyanate. .
このパルプ粒子を用いて、やはり、実施例1と同様に抄
紙したところ抄紙金網からの水切れが良く抄紙性は良好
であり、得られたシートの地合は良好であつた。このシ
ートを実施例1におけると同様にして熱プレスして得ら
れた紙の性能は次のとおりであり、いずれも申し分のな
いものであつた。When paper was made using these pulp particles in the same manner as in Example 1, the paper-making properties were good, with good water drainage from the paper-making wire mesh, and the resulting sheet had good texture. This sheet was hot pressed in the same manner as in Example 1, and the properties of the paper obtained were as follows, and all were satisfactory.
実施例 12
実施例1で得たパルプ粒子と7mnに切断した芳香族ポ
リアミド繊維(帝人社製コーネツクス)とを各種割合に
混合した水分散液を抄紙し、乾燥の後270℃200k
g/dの条件で熱プレスし紙を得た。Example 12 Paper was made from an aqueous dispersion in which the pulp particles obtained in Example 1 and aromatic polyamide fibers cut to 7 mm (Teijin Co., Ltd. Cornex) were mixed in various proportions, and after drying, the mixture was heated at 270°C and 200k.
Paper was obtained by hot pressing under the conditions of g/d.
得られた紙の性能を第2表に示した。The performance of the obtained paper is shown in Table 2.
表中▲B,cは本発明によるシートであり、引張強伸度
、絶縁破壊電圧は良好であつた。In the table, ▲B and c are sheets according to the present invention, and the tensile strength and elongation and dielectric breakdown voltage were good.
煮aはパルプ粒子の量が少ない場合で、絶縁破壊電圧、
引張強度が不良である。Boiling a is when the amount of pulp particles is small, and the dielectric breakdown voltage,
Tensile strength is poor.
Claims (1)
タン及び/又は4.4′−ビス(トリメリトイミド)ジ
フェニルエーテルとイソフタル酸および/又はテレフタ
ル酸で構成されその組成が第1図斜線で示された範囲内
のカルボン酸混合物と、4.4′−ジフェニルメタンジ
イソシアネート及び/又は4.4′−ジフェニルエーテ
ルジイソシアネートとを加熱反応せしめて得られる芳香
族ポリアミドイミドを主たる樹脂成分とするパルプ粒子
20〜95重量部と短繊維5〜80重量部とを混合抄紙
し、加圧加熱してなるシート。1 Carboxylic acid composed of 4.4'-bis(trimellitimide)diphenylmethane and/or 4.4'-bis(trimellitimide)diphenyl ether and isophthalic acid and/or terephthalic acid, the composition of which is within the shaded range in Figure 1. 20 to 95 parts by weight of pulp particles whose main resin component is aromatic polyamideimide obtained by subjecting an acid mixture to a heating reaction with 4.4'-diphenylmethane diisocyanate and/or 4.4'-diphenyl ether diisocyanate, and 5 parts by weight of short fibers. - 80 parts by weight are mixed together to make paper, and then heated under pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10253875A JPS5947080B2 (en) | 1975-08-26 | 1975-08-26 | sheet |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10253875A JPS5947080B2 (en) | 1975-08-26 | 1975-08-26 | sheet |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5227806A JPS5227806A (en) | 1977-03-02 |
JPS5947080B2 true JPS5947080B2 (en) | 1984-11-16 |
Family
ID=14330037
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10253875A Expired JPS5947080B2 (en) | 1975-08-26 | 1975-08-26 | sheet |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5947080B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5441500A (en) * | 1977-09-08 | 1979-04-02 | Mitsubishi Paper Mills Ltd | Oil-immersion insulating board |
JPS57183499A (en) * | 1981-05-06 | 1982-11-11 | Mitsui Toatsu Chemicals | Sheet like article |
-
1975
- 1975-08-26 JP JP10253875A patent/JPS5947080B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5227806A (en) | 1977-03-02 |
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