JPS6024878B2 - sheet - Google Patents
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- Publication number
- JPS6024878B2 JPS6024878B2 JP51034166A JP3416676A JPS6024878B2 JP S6024878 B2 JPS6024878 B2 JP S6024878B2 JP 51034166 A JP51034166 A JP 51034166A JP 3416676 A JP3416676 A JP 3416676A JP S6024878 B2 JPS6024878 B2 JP S6024878B2
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- Japan
- Prior art keywords
- pulp
- paper
- weight
- polycarbonate
- sheet
- 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.)
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- Paper (AREA)
- Organic Insulating Materials (AREA)
- Nonwoven Fabrics (AREA)
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、譲露率、誘電正援、含浸性、機械的性質
等に優れた露気絶箱象紙、特に高圧送電ケーブル用電気
絶系粛紙に関したシートに関する。本発明の特徴は、ポ
リプロピレン短繊維とポリカーボネートのパルプ状物質
とを特定割合に混合抄紙し、乾燥の後加熱加圧すること
であり更には、該ポリカーボネートのパルプ状物質とし
て、特定の方法によりたパルプ状物質を使用することで
ある従来、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、送電ケーブル用絶糸教紙と
しても、天然パルプからの紙が多く使われている。More specifically, the present invention relates to a dew-proofing paper that is excellent in yield rate, dielectric support, impregnability, mechanical properties, etc., particularly a sheet related to electrical insulation-proofing paper for high-voltage power transmission cables. A feature of the present invention is that polypropylene short fibers and a polycarbonate pulp material are mixed in a specific ratio to make paper, and then heated and pressurized after drying. Conventionally, natural pulp is the most well-known pulp particle used in paper, and paper made from natural pulp is often used as cutting paper for power transmission cables.
しかし、天然パルプからの紙はその化学的主成分がセル
ロスであるため誘電的性質、耐熱性が悪く、電力需要の
増大に応えるべく近年釆検討されている。500KV以
上の送電ケーブル用の絶蕪象限としてはほとんど使用で
きないとされている。However, since the main chemical component of paper made from natural pulp is cellulose, it has poor dielectric properties and heat resistance, and in recent years, paper made from natural pulp has been studied in order to meet the increasing demand for electricity. It is said that it can hardly be used as an absolute quadrant for power transmission cables of 500 KV or more.
セルロース誘電的性質の悪さを補うものとして、最近に
至りポリカーボネート、ポリプロレン、ポリエチレン、
ポリフエニレンオキサイド、ポリスルホン、ポリ(26
−ジフエニルーパラーフェニレンオキサィド)等の素材
が検討されている。Recently, polycarbonate, polyprolene, polyethylene,
Polyphenylene oxide, polysulfone, poly(26
- Diphenyluparaphenylene oxide) and other materials are being considered.
これら素材の誘電的性質は500KVの以上の送電ケー
ブル用絶織紙として、充分その目的すなわち、低議電損
失化を果し得るものであることは良く知られている。例
えば、我々は先に特公昭48一23961号公報におい
てポリカーボネート短繊維{a)及びポリカーボネート
を沸点が90こ0以下のハロゲン化炭化水素に溶解した
濃度2〜2の重量%の溶液を、使用したハロゲン化炭化
水素の沸点より高い温度に保持された熱水中に注入又は
噴射することによって得たパルプ状物質‘bーをa,b
が1:2〜5:1(重量比)になる割合で混合してシー
トを作り、該シートを140〜170o0の温度で加熱
加圧することを特徴とするポリカーボネート紙の製造法
を提案した。この方法によって得られたポリカーボネー
ト紙の誘電的性質は非常に優れたものであったが、一方
次のような欠点もあった。It is well known that the dielectric properties of these materials are sufficient to serve the purpose of woven paper for power transmission cables of 500 KV or higher, that is, to reduce electrostatic loss. For example, in Japanese Patent Publication No. 48-23961, we previously used short polycarbonate fibers {a) and a solution of polycarbonate dissolved in a halogenated hydrocarbon having a boiling point of 90% or less at a concentration of 2 to 2% by weight. A pulp-like material 'b- obtained by injecting or injecting it into hot water maintained at a temperature higher than the boiling point of the halogenated hydrocarbon.
We have proposed a method for producing polycarbonate paper, which is characterized in that a sheet is prepared by mixing in a ratio of 1:2 to 5:1 (weight ratio), and the sheet is heated and pressurized at a temperature of 140 to 170°C. Although the dielectric properties of the polycarbonate paper obtained by this method were very excellent, it also had the following drawbacks.
【11機械的性質特に、引張強度が低い。[11] Mechanical properties, especially low tensile strength.
【2’前記の方法で製造されたパルプ状物質の形状が悪
いためか、抄紙機において連続的に抄造することが困難
であった。[2' Perhaps because of the poor shape of the pulp-like material produced by the above method, it was difficult to continuously produce the paper using a paper machine.
潮 水と混和性の少し、ハロゲン化炭化水素を溶媒とし
て使用しているため、パルプ状物質中に徴量残存するハ
ロゲン化炭化水素の除去が面倒である。Since halogenated hydrocarbons, which are slightly miscible with tide water, are used as solvents, it is difficult to remove the halogenated hydrocarbons that remain in the pulp-like material.
更に、特公昭48一26801号公報には、ポリカーボ
ネートのジメチルーホルムアミド溶液とポリエステル、
短繊維との混合物を薄膜状にして、この薄膜を水中に浸
潰し、析出した重合体のマトリックスとその中に含有さ
れた短繊維とから成るシートを形成し、加熱加圧下にカ
レンダーロールがけして軍気絶材料に通した合成紙を製
造する方法がZ記載されている。Furthermore, Japanese Patent Publication No. 48-26801 discloses a dimethyl-formamide solution of polycarbonate and polyester,
The mixture with short fibers is formed into a thin film, this thin film is immersed in water to form a sheet consisting of a precipitated polymer matrix and the short fibers contained therein, and then rolled with a calendar roll under heat and pressure. A method of manufacturing synthetic paper passed through military stunning material is described in Z.
この方法により得られた合成紙の誘電的性質は優れたも
のであるが、重合体溶液中へ短繊維を均一に混合するの
がむつかしく、又厚薄斑の少し、均一な紙を得るのが困
難である。などの欠点を有している。我々はこれらの欠
点を除Z去すべ〈、鋭意検討を続けた結果次の様な諸事
実を知見し、本発明を完成したものである。‘1’ボリ
カーボネートは、水と混和性のあるN−メチル−2−ピ
ロリドンに良く溶け、溶液の安定性は良好である。Although the dielectric properties of the synthetic paper obtained by this method are excellent, it is difficult to uniformly mix the short fibers into the polymer solution, and there are some thickness and thin spots, making it difficult to obtain a uniform paper. It is. It has drawbacks such as: In order to eliminate these drawbacks, we have made the following findings as a result of intensive studies and have completed the present invention. '1' polycarbonate dissolves well in N-methyl-2-pyrrolidone, which is miscible with water, and the stability of the solution is good.
‘2’前記溶液を、Nーメチル−2ーピロリドンと水と
から成る沈澱剤中に導入し、微細な粒子として沈澱せし
めることによって、良好な形状を有するパルプ状物質が
得られる。'2' By introducing the solution into a precipitating agent consisting of N-methyl-2-pyrrolidone and water and precipitating it as fine particles, a pulp-like material with good shape is obtained.
【31 このパルプ状物質は抄紙性が良く、短繊維と混
合して、例えば、長網式抄紙機によって連続的に抄造す
る場合にみ断紙等のトラブルは全くない。[31] This pulp-like material has good paper-making properties, and there are no problems such as paper breakage when it is mixed with short fibers and continuously produced, for example, in a Fourdrinier paper machine.
t4’(3’項における短繊維としてポリプロピレン短
繊維を特定割合に使用して得たシートの性能は誘電的性
質はもちろんのこと、機械的性質含浸性等申し分のない
ものであった。The properties of the sheet obtained by using a specific proportion of polypropylene short fibers as the short fibers in t4' (section 3') were satisfactory in terms of not only dielectric properties but also mechanical properties and impregnation properties.
すなわち、本発明は10〜9広重量%のポリプロピレン
短繊維{a}およびポリカーボネートをN−メチル−2
ーピロリドンに溶解した溶液を、N−メチル−2ーピロ
リドンと水とから成る沈澱剤中に導入することによって
得たパルプ状物質他90〜iの重量%とを混合抄紙し乾
燥の後加熱加圧してなるシートである。That is, the present invention combines 10 to 9% by weight of short polypropylene fibers {a} and polycarbonate with N-methyl-2
A pulp-like material obtained by introducing a solution dissolved in pyrrolidone into a precipitant consisting of N-methyl-2-pyrrolidone and water and 90 to 90% by weight of the material is mixed to make paper, dried, and then heated and pressurized. This is a sheet.
本発明におし、言うポリカーボネートとは、ビス(4ー
ヒドロキシフエニル)メタン、1.1ービス(4一ヒド
ロキシーフエニル)エタン、ビス(4−ヒドロキシフエ
ニル)プロパン、ビス(4…ヒドロキシー3.5−ジク
ロロフヱニル)メタン、ピス(4ーヒドロキシフエニル
)フエニルメタン、2.2ービス(4ーヒドロキシ−3
.5ージブロムフエニル)プロパワ等をジオキシ成分と
して使用し、これとホスゲンあるいは、ジフェニルカー
ポネートとの反応によって得られる。In the present invention, the polycarbonate refers to bis(4-hydroxyphenyl)methane, 1.1-bis(4-hydroxyphenyl)ethane, bis(4-hydroxyphenyl)propane, bis(4...hydroxy-3 .5-dichlorophenyl)methane, pis(4-hydroxyphenyl)phenylmethane, 2.2-bis(4-hydroxy-3
.. It is obtained by using 5-dibromophenyl) propawa as a dioxy component and reacting it with phosgene or diphenyl carbonate.
いわゆるホスゲン法ポリカーボネートあるいはェステル
交換法ポリカーボネートであり、その平均分子量は10
000〜5,00政序ましくは20,000〜35,0
00である。本発明においてて使用するパルプ状物質を
製造するに際しては、ポリカーボネートのNーメチルー
2ーピロリドン溶液を、水とN−メチル−2ーピロリド
ンとからなる沈澱剤中に導入し、微細な粒子として沈澱
せしめるパルプ状物質となす方と適用する。ポリカーボ
ネートのNーメチルー2−ピロリドン溶液中のポリカー
ポネートの濃度はポリカーボネートの重合度、種類等に
よって異なるが、概略2〜2重量%が望ましく更に好ま
しくは6〜1り重量%である。This is the so-called phosgene method polycarbonate or ester exchange method polycarbonate, and its average molecular weight is 10.
000-5,00 government order or 20,000-35,00
It is 00. In producing the pulp-like material used in the present invention, a solution of polycarbonate in N-methyl-2-pyrrolidone is introduced into a precipitant consisting of water and N-methyl-2-pyrrolidone, and the pulp-like material is precipitated as fine particles. Apply to matter and what it does. The concentration of polycarbonate in the N-methyl-2-pyrrolidone solution of polycarbonate varies depending on the degree of polymerization, type, etc. of the polycarbonate, but is preferably approximately 2 to 2% by weight, and more preferably 6 to 1% by weight.
又、沈澱に供する際の溶液の温度は10〜90oo特に
好ましく20〜60qoである。又、溶液中に少量の水
を含有しても差支えない。更に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、必ずしも必要でないが含浸性、耐熱性
、電気絶縁性、抄紙性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、雲母
類、アスベルト、ガラスフレークス、石英粉末、タルク
カオリン、アルミナなどの一種又は二種以上が利用でき
る。The temperature of the solution during precipitation is 10 to 90 qo, particularly preferably 20 to 60 qo. Moreover, there is no problem even if a small amount of water is contained in the solution. Furthermore, it is not necessary to add and mix into the solution a minute solid inorganic substance that does not substantially react with or dissolve in the solution, but it can further improve impregnating properties, heat resistance, electrical insulation properties, and paper-making properties. The above is preferable. In this case, as the solid inorganic substance, one or more of micas, asvert, glass flakes, quartz powder, talcum kaolin, alumina, etc. can be used.
固体無機物質を混合する場合その量は、重合体の5〜4
0の重量%好ましくは10〜20の重量%である。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T・
K・ホモミクサー(特殊機化工業製)アトラィター(三
井、三池製作所製)などが有効である。When a solid inorganic substance is mixed, the amount should be 5 to 4 times the amount of the polymer.
0% by weight, preferably 10-20% by weight. When mixing the solid inorganic substance described above into a solution, it is preferable to disperse it as uniformly as possible.
K. Homo Mixer (manufactured by Tokushu Kika Kogyo), Attritor (manufactured by Mitsui, Miike Seisakusho), etc. are effective.
次に、本発明においてはパルプ状物質の製造に際して沈
澱剤として、水とN−メチル−2−ピロリドンとから成
る沈澱剤を使用する。Next, in the present invention, a precipitant consisting of water and N-methyl-2-pyrrolidone is used as a precipitant when producing a pulp-like material.
沈澱剤中のNーメチル−2ーピロリドン濃度は重合体種
類、重合体濃度、重合体重合度等によって多少異なるが
、15〜8の重量%が適当であり好ましくは30〜7の
重量%である。The concentration of N-methyl-2-pyrrolidone in the precipitant varies somewhat depending on the type of polymer, polymer concentration, degree of polymerization, etc., but is suitably 15 to 8% by weight, preferably 30 to 7% by weight.
8の重量%より大きいと、生成したパルプ状物質同志が
凝集溶着してしまいこのパルプ状物質を加工して得られ
るシートの引張強伸度、絶縁破壊電圧の低下を招く。If the content is greater than 8% by weight, the produced pulp-like substances will aggregate and weld together, resulting in a decrease in tensile strength and elongation and dielectric breakdown voltage of the sheet obtained by processing this pulp-like substance.
逆に15重量%より4・さい場合には、得られるパルプ
状物質の形状が粗大なものとなりパルプ状物質同志の絡
合性、パルプ状物質と短繊維との絡合性が少なくなり、
抄紙性が悪くなると共に、得られたシートの機械的性質
、絶縁破壊電圧も悪くなる。沈澱に供する際の沈澱剤の
温度は10〜70CO好ましくは20〜50o○である
。沈澱剤は高速蝿梓を行ない、導入した溶液から脱藩煤
すると同時に雛断又は叩解作用を生ぜしめる様に操作す
る。沈澱剤/溶液の流量比は5/1〜30ノ1が望まし
く、特に好ましくは8/1〜15ノ1である。On the other hand, if it is less than 15% by weight, the shape of the resulting pulp-like material becomes coarse, and the entanglement of the pulp-like materials with each other and the entanglement of the pulp-like material with short fibers decreases.
In addition to poor paper-making properties, the mechanical properties and dielectric breakdown voltage of the resulting sheet also deteriorate. The temperature of the precipitating agent during precipitation is 10 to 70°C, preferably 20 to 50°C. The precipitant is operated at high speed to remove soot from the introduced solution and at the same time produce a chick cutting or beating action. The precipitant/solution flow rate ratio is desirably 5/1 to 30/1, particularly preferably 8/1 to 15/1.
(重量比)かくして得たパルプ状物質は公知の方法によ
り充分水洗した後、ポリプロピレン短繊維と混合抄紙し
乾燥後加熱加圧して、すぐれたシートとすることができ
る。(Weight ratio) The pulp-like material thus obtained is thoroughly washed with water by a known method, mixed with polypropylene staple fibers, and then dried and heated and pressed to form an excellent sheet.
この時、シート中のパルプ状物質/ポリプロピレン短繊
維の割合は、重量比で90/1〜10/90でる必要が
ある。At this time, the ratio of pulp-like material/polypropylene short fibers in the sheet needs to be 90/1 to 10/90 by weight.
パルプ状物質の量が9の重量%より多いと、機械的性質
、特に引張伸度が低くなり舎浸性も悪くなる。If the amount of pulp-like material is more than 9% by weight, the mechanical properties, especially the tensile elongation, will be low and the soakability will be poor.
逆にパルプ状物質の量が1の重量%より少し、とシート
の機械的性質、絶縁破壊電圧が低下する。パルプ状物質
とポリプロピレン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、最網式或いは円絹式の製紙
機を用いて湿式法により抄紙するのが良い、この時必要
に応じて界面活性剤、ポリェーテル、トロロアオイの根
汁等の分散剤、増粘剤を加えても良い。ポリプロピレン
短繊維は一般に市販されているものが充分使用できる。Conversely, if the amount of pulp-like material is less than 1% by weight, the mechanical properties and dielectric breakdown voltage of the sheet will decrease. It is best to make paper from pulp-like substances and short polypropylene fibers using a wet process using a remeshing or circular-type papermaking machine, as in the case of papermaking from conventional natural pulp. A surfactant, a polyether, a dispersant such as root juice of A. japonica, and a thickener may also be added. Generally commercially available short polypropylene fibers can be used.
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って、
すぐれた性能を発現する。After the sheet obtained as described above is dried, it is heated under pressure using a heat press or a heat roll.
Demonstrates excellent performance.
加圧する時の温度は、シート中のパルプ状物質の量等に
よって多少異なるが70〜18000が適当である。The temperature at the time of pressurization varies somewhat depending on the amount of pulp-like material in the sheet, etc., but an appropriate temperature is 70 to 18,000.
圧力は温度と同様に、シート中のパルプ状物質の量等に
よって異なるが400k9/仇以下が望ましい。The pressure, like the temperature, varies depending on the amount of pulp-like material in the sheet, etc., but is preferably 400 k9/min or less.
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。The method for measuring the main measured values in the present invention will be explained below.
引張強度;JISP8118の方法に準じて実施しkg
/側2で表わした。Tensile strength: kg according to JISP8118 method
/ side 2.
引張伸度;JISP8132の方法により測定し%で表
わした。Tensile elongation: Measured according to the method of JISP8132 and expressed in %.
絶縁破壊電圧;JISC2111の方法により交流電圧
で測定した。Dielectric breakdown voltage: Measured using AC voltage according to the method of JISC2111.
誘電率、誘電正接;JISC2111の方法により20
℃6に/Sで測定した。Dielectric constant, dielectric loss tangent: 20 according to JISC2111 method
Measured at 6°C/S.
含浸性;直径1物舷の円板状に切断した試料をJISI
号絶縁油の表面に浮べて、全面に絶縁油が浸透してくる
までの所要時間を測定
し、試料の厚さで割ってSec/肌で表わした。Impregnating property: A sample cut into a disk shape with a diameter of 1 shipboard was measured according to JISI
The sample was floated on the surface of No. 1 insulating oil, and the time required for the insulating oil to penetrate the entire surface was measured, and the time was divided by the thickness of the sample and expressed as Sec/skin.
実施例 1
重合体溶液の作成
ポリ−4・4−ジオキシジフエニル−2・2−プロパン
カーボネートの粉末1箱重量部を水分含有量0.2重量
%のNMP80重量部に燭拝しながら投入した後、60
ooまで加溢して、重合体を完全に溶解した。Example 1 Preparation of polymer solution One box part by weight of poly-4,4-dioxydiphenyl-2,2-propane carbonate powder was poured into 80 parts by weight of NMP with a moisture content of 0.2% by weight. After that, 60
The polymer was completely dissolved by flooding to 0.0°C.
次いで、溶液の温度を30qoにまで冷却し、パルプ状
物質製造用の溶液とした。沈澱剤の作凶
NMP6り重量部と水33重量部とを混合し沈澱剤とし
た。Next, the temperature of the solution was cooled to 30 qo to prepare a solution for producing a pulp-like material. 6 parts by weight of NMP and 33 parts by weight of water were mixed to prepare a precipitant.
パルプ状物目の重り造
バッファのついてるステーターとタービン翼型ローター
との組み合せからなり、かつ沈澱剤、溶液の供給口およ
び沈澱後のパルプ状物質スラリ−の排出口を備えた管路
燈洋式連続沈澱機に、溶液0.5k9/min、沈澱剤
5k9/minの流量で同時に供給し、パルプ状物質ス
ラリーを排出口からとり出した。A conduit-type continuous sedimentation machine consisting of a combination of a stator with a weighted buffer of pulp-like material and a turbine blade-shaped rotor, and equipped with an inlet for a precipitant, a solution, and an outlet for a slurry of pulp-like material after precipitation. The solution was simultaneously fed into the machine at a flow rate of 0.5 k9/min and the precipitant was fed at a flow rate of 5 k9/min, and the pulp-like material slurry was taken out from the outlet.
この際、沈澱剤の温度は370、溶液は30ooに調節
した。At this time, the temperature of the precipitant was adjusted to 370°C, and the temperature of the solution was adjusted to 30°C.
又、ローターの回転は7,10仇.r.m.とした。得
られたパルプ状物質スラリーを200メッシュのステン
レス製金網を備えたヌッチェ型減圧櫨過機に入れ、大部
分の沈澱剤を漏液として分離した。Also, the rotation of the rotor is 7.10 times. r. m. And so. The resulting pulpy material slurry was placed in a Nutsche type vacuum sieve equipped with a 200-mesh stainless wire mesh to separate most of the precipitant as leakage.
次いで、渡過機からパルプ状物質をとり出すことなくパ
ルプ状物質(間型分)の3ぴ音量のイオン交換水を供給
し、減圧にして洗浄した。Next, without taking out the pulp-like material from the transfer machine, ion-exchanged water was supplied in an amount equal to three times the amount of the pulp-like material (between molds), and the material was washed under reduced pressure.
かくして得られたパルプ状物質にはパルプ状物質(固型
分)の約4倍量の水が付着していた。Approximately four times the amount of water as the pulp-like material (solid content) was attached to the pulp-like material thus obtained.
この付着水中のNMP濃度をガスクロマトグラフ法で測
定したところ、o.ol重量%でり、実用上何ら差支え
ない程度にまで充分洗浄できていた。製紙前記によって
得られたパルプ状物質1.2夕(固型分)と単糸織度2
デニール、繊維長さ6側のポリプロピレン短繊維(三菱
レーヨン製、商品名パイレン)0.8夕を含む水分散液
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いシートを得た。When the NMP concentration in this adhered water was measured by gas chromatography, it was found that o. % by weight, and the cleaning was sufficient to the extent that there was no practical problem. The pulp-like material obtained by the papermaking method described above has a solid content of 1.2 mm (solid content) and a single yarn weave of 2
When paper was made from an aqueous dispersion containing polypropylene short fibers (manufactured by Mitsubishi Rayon, trade name: Pyren) with a denier of 6 and a fiber length of 0.8 mm using a Tatsupi standard sheet machine, the paper-making properties were good and the texture was good. Got a sheet.
このシートを乾燥後、70℃、300kg/地の条件で
1段目の熱プレスをし、次いで15ぴ0200k9/の
の条件で2段目の熱プレスをして、厚さ約145側の紙
を得た。この紙の引張強度は4.7k9/柵2 、仲度
は14.0%、誘電率2.7、誘電正援0.05%であ
った又、絶緑破壊強度は12.靴V肋、含浸性は190
船ec/側であった。After drying this sheet, it was heat pressed in the first stage at 70℃ and 300 kg/base, then in the second stage under the conditions of 15 mm, 0,200 kg/base, and the thickness of the paper was approximately 145 mm. I got it. The tensile strength of this paper was 4.7k9/fence 2, the density was 14.0%, the dielectric constant was 2.7, and the dielectric support was 0.05%.Also, the breaking strength was 12. Shoe V rib, impregnability is 190
It was on the ship ec/side.
実施例 2
実施例1において、重合体溶液中の重合度濃度を9重量
%に、又沈澱剤中のNMP濃度を4の重量%とする以外
は実施例1と全く同様にしてパルプ状物質を得た。Example 2 A pulp-like material was prepared in exactly the same manner as in Example 1, except that the polymerization degree concentration in the polymer solution was 9% by weight, and the NMP concentration in the precipitant was 4% by weight. Obtained.
次いで、実施例1と同様に実施した得た紙の性能は、実
施例1で得た紙とほとんど同じで良好であった。又、こ
の紙の含浸性を測定したところ200$ec/側で良好
であった。実施例 3実施例1において、製紙の際のポ
リカーボネートパルプ状物質とポリプロピレン短繊維の
量を種々変えて実施し、シート中のポリカーボネートパ
ルプ状物質とポリプロピレン短繊維の割合が種々に異な
るシートを得た。Next, the performance of the obtained paper, which was carried out in the same manner as in Example 1, was almost the same as that of the paper obtained in Example 1 and was good. Further, the impregnation property of this paper was measured and was found to be good at 200 $ec/side. Example 3 In Example 1, the amounts of polycarbonate pulp-like material and polypropylene short fibers during paper manufacturing were varied to obtain sheets with various proportions of polycarbonate pulp-like material and polypropylene short fibers in the sheets. .
これらのシートについての測定結果を第1表に示す。第
1表
第1表において、M.1,2,6,7は、シト中のポリ
カーボネートパルプ状物質とポリプロピレン繊維の割合
が本発明の範囲外である場合の例であり、恥.1,2,
6の誘電的性質は優れたものであったが引張強伸度が不
十分であった。Table 1 shows the measurement results for these sheets. Table 1 In Table 1, M. Nos. 1, 2, 6, and 7 are examples in which the ratio of polycarbonate pulp-like material to polypropylene fiber in the sheet is outside the scope of the present invention. 1, 2,
Although the dielectric properties of No. 6 were excellent, the tensile strength and elongation were insufficient.
又、肺.7の場合、抄紙金網から湿紙をとり出すことが
できずシートが得られなかった。Also, lungs. In case No. 7, the wet paper could not be taken out from the paper-making wire mesh, and no sheet could be obtained.
一方、舷.3,4,5は本発明の方法によるものであり
、引張強伸度、誘電的性質ともに満足できる水準のもの
であった。実施例 4
ポリカーポネートとして、ビス(4−ヒドロキシフェニ
ル)−プロパン9刃重量と2−2ービス(4ーヒドロキ
シー3.5−ジブロムーフエニル)プロパン7重量とか
らホスゲン法によって得られたポリカーボネート共重合
物を使用する以外は、実施例1と同機に実施してパルプ
状物質を得た。On the other hand, the gunwale. Samples Nos. 3, 4, and 5 were obtained by the method of the present invention, and had satisfactory levels of both tensile strength and elongation and dielectric properties. Example 4 As a polycarbonate, a polycarbonate obtained by the phosgene method from 9 blade weights of bis(4-hydroxyphenyl)-propane and 7 weights of 2-2-bis(4-hydroxy-3.5-dibromoophenyl)propane was used. A pulp-like material was obtained by carrying out the same procedure as in Example 1 except that a polymer was used.
Claims (1)
び(b) ポリカーボネートをN−メチル−2−ピロリ
ドンに溶解した溶液をN−メチル−2−ピロリドンと水
からある沈澱剤中に撹拌しながら導入することによつて
得たパルプ状物質90〜10重量%とを混合抄紙し、乾
燥し加圧加熱してなるシート。1. A solution of (a) 10 to 90% by weight of short polypropylene fibers and (b) polycarbonate in N-methyl-2-pyrrolidone is introduced with stirring into a precipitant consisting of N-methyl-2-pyrrolidone and water. A sheet made by mixing 90 to 10% by weight of a pulp-like material obtained by the above method, drying, and heating under pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51034166A JPS6024878B2 (en) | 1976-03-30 | 1976-03-30 | sheet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51034166A JPS6024878B2 (en) | 1976-03-30 | 1976-03-30 | sheet |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS52118007A JPS52118007A (en) | 1977-10-04 |
| JPS6024878B2 true JPS6024878B2 (en) | 1985-06-14 |
Family
ID=12406614
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51034166A Expired JPS6024878B2 (en) | 1976-03-30 | 1976-03-30 | sheet |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6024878B2 (en) |
-
1976
- 1976-03-30 JP JP51034166A patent/JPS6024878B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS52118007A (en) | 1977-10-04 |
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