JPS62101B2 - - Google Patents
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- Publication number
- JPS62101B2 JPS62101B2 JP57103058A JP10305882A JPS62101B2 JP S62101 B2 JPS62101 B2 JP S62101B2 JP 57103058 A JP57103058 A JP 57103058A JP 10305882 A JP10305882 A JP 10305882A JP S62101 B2 JPS62101 B2 JP S62101B2
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- Prior art keywords
- inorganic
- fibers
- pulp
- sheet
- weight
- 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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Description
本発明は焼結性を有する無機質物シートに関す
るものである。従来セラミツクスの製造方法とし
ては、原料(粉末)→成形→焼結を一つの操作で
行なうホツトプレス法、溶融鋳造法、ガスクラツ
キング法、鍛造法等の直接法と、乾式プレス、押
し出し、鋳込み、射出成形、ドクターブレード、
ラバープレス等の間接法とが行われていた。工業
的には間接法が主流であるが、なかでもドクター
ブレード法は厚み精度が高く、しかも薄いシート
が得られることから好んで用いられている。これ
ら成形シート(グリーンテープ)に要求される特
徴としては
(1) テープの厚みが均一であること
(2) 均一な組成であること
(3) 寸法安定性が良いこと
(4) 適当な柔軟性と耐張力を持つこと
(5) 熱分解しやすく灰分を残さないこと
等がある。これらの要求特性を満たすために、こ
れまで種々の溶媒、結合剤、可塑剤、解膠剤、湿
潤剤等が検討されてきた。しかしこの方法は結合
剤にポリビニルブチラール等の高価な材料が必要
であり、また溶剤を使用することによる操業上の
種々の困難性が伴なうため、従来より有機溶剤等
を使用しない水系の方法が求められている。この
ような観点からいくつかの方法が提案されてお
り、その一つにセルローズパルプを置換度0.02〜
0.04にカチオン変性した後水度200〜100mlCSF
に叩解したパルプと無機物質粉末を通常の抄紙法
で抄造する方法(特開昭56−63099)、あらかじめ
凝集剤を含浸させたパルプを使用する方法(特開
昭56−167407)等がある。前者は予めパルプをカ
チオン化する工程が必要であり、またパルプの
水度が100〜200c.c.(JIS法)の叩解度では多量の
無機物質粉末を含むシートの製造が困難であるこ
とから高品質のセラミツクの製造ができない欠点
があつた。本発明者等は有機繊維の物理的形態お
よび無機物質の占積率の観点から鋭意研究を重ね
た結果、シート中の全無機物質の占積率が25%以
上で繊維懸濁液の水度が濃度0.03重量%におい
て100〜400c.c./0.3gの有機繊維3〜20重量%か
ら成る無機質物シートが極めて良好なセラミツク
が得られることを見出し本発明を完成するに至つ
た。
一般に無機質物シートが均質な焼結性を有する
ためには焼成前の無機材料の占積率が重要であ
る。構成材料の占積率は焼成前のシートの密度お
よび各成分の密度から下記の式に基づいて計算す
ることが出来る。
無機材料の占積率Vi=P/Pixw
有機材料の占積率Vo=P−PiVi/Po
空隙分の占積率 Va=1−(Vi+Vo)
但し
P:成型生シートの密度
Vi:無機分占積率
Vo:有機分 〃
Va:空隙分 〃
Pi:無機分理想焼結後密度
Po:有機分平均密度
xw:無機分重量比率
こゝで有機分平均密度(Po)とはパルプ成分
とバインダー樹脂との平均密度を意味しており、
下記の式により計算される。
Po=P1P2(x1+x2)/P1x2+P2x1
但し
P1:パルプ繊維密度
P2:バインダー樹脂密度
x1:パルプ分重量密度
x2:バインダー樹脂重量比率
無機質物シートを焼結してセラミツクを製造す
るにあたつて無機占積率が低い場合は均一な焼結
体が得られず焼結状態が低密度であつたり、歪み
を生じたりあるいは極端な場合には一体に焼成せ
ずに分断状態になつてしまうこともある。したが
つて無機分占積率は高い程望ましい。第1図はア
ルミナについての通常の焼結を示す焼成温度と生
シートの無機分占積率との関係を示す。斜線部は
焼結可能な領域であるが、寸法精度および経済性
からは生シートの無機分占積率としては25%以上
必要であり好ましくは40%以上であることが望ま
しい。
他の焼結性材料についても、良好な焼結体を得
るために必要な生シートの無機分占積率はアルミ
ナと同程度であることを確認した。上記無機体積
比率を達成するために必要な無機物質粉末の重量
比率は、その真比重により若干異るが、およそ70
%以上であることが種々の実験結果から判明し
た。
特に比重の高い無機質物を高密度で焼結させよ
うとする場合は90重量%以上好ましくは95重量%
以上の高い無機質分比率を必要とすることもわか
つた。
通常の木材パルプ原料(600〜100c.c.CSF)を
用いてこのように高い無機質分比率を有するシー
トを製造することは極めて困難であるばかりでな
く、仮りに可能であつたとしても、焼結後のパル
プ消失跡が10μ径のパイプ状となつて残るため平
滑性等の面から好ましくない。本発明者等はかゝ
る現状を充分把握し、鋭意研究を重ねた結果、無
機物質粉末が充分定着し、一般抄紙機で抄造可能
で且つ焼成後に良好な焼結性を有する無機質物シ
ートを得るに至つた。
本発明において用いられる有機繊維としては、
広葉樹パルプ、針葉樹パルプ、コツトンリンター
等の植物繊維、アクリル繊維、ポリエステル繊
維、ポリプロピレン繊維、レーヨン繊維等の合成
繊維が挙げられるが、これらの中でも本発明では
微細フイブリル化可能な繊維が適しており、この
点で植物繊維のほか合成繊維の中でもアクリル繊
維、レーヨン繊維が特に好適である。またこれら
の繊維の一部を無機繊維に置き替えることもでき
る。
濾水度の測定法としては、一般にJISP8121に
定められたカナダ標準濾水度が知られているが、
本発明において使用される微細フイブリル化可能
な有機繊維では濾水度の値が極めて小さくなり、
濾水度の表示が適切にできないので、下記に示す
ような濾水度測定法(以下濾水度H法又は単にH
法と呼ぶ)を採用した。
濾水度H法
JISP8121に定められたカナダ標準形濾水度試
験器を用いて、濾水筒の底の黄銅製のふるい板を
50メツシユ金網に変え、離解したパルプの濃度
0.3%を0.03%に変える以外には、JIS法と全く同
様な手順で濾水度測定操作を行ない、測定値をH
法濾水度とした。このH法は微細フイブリル化の
状況をよく反映しており本発明に必要な繊維のフ
イブリル化の程度を表示する上において好適な方
法と云える。この方法を用いて各種繊維材料の
水度と無機物質粉末の定着性との関係を調べたと
ころ定着に好適な水度はおよそH法で400c.c.以
下にあることを見出したものである。
無機物質粉末が強誘電体である場合は定着助剤
を用いなくても材料自身の持つ高い極性のため良
好な定着性を示すが、一般の常誘電体の場合は定
着剤を必要とする。この場合の定着剤はノニオン
系高分子定着剤、カチオン性高分子定着剤あるい
は両者の併用により高い定着性が得られる。
上記叩解微細繊維はそれ単独では水性が低く
抄紙困難であるが、無機物質粉末定着後は微小フ
ロツクを形成するために水性が大巾に向上し、
抄紙可能となることは全く予想外の結果であり抄
造上の経済的効果も大きい。またツインワイヤー
からの剥離性と湿紙強度を改善するために焼成後
の平滑性に支障のない範囲で叩解度の比較的粗い
繊維を極く少量添加して更に抄紙性を向上させて
もさしつかえない。これらの比較的粗い繊維原料
は無機物質粉末粒子が定着した微細繊維の支持体
として働くことから、0.5重量%以下ではその効
果は現われにくいが、一方10重量%以上では抄紙
性は良好になるが、焼成時の焼結性が悪くなる傾
向がある。しかし粗い繊維原料が繊維状無機材料
である場合は良好な抄紙性と共に高い無機分占積
率が得られる。
以上の構成原料を主材料とし、必要に応じてバ
インダー樹脂を加えて抄紙工程を経てシート化し
た後通常のドライヤー工程により乾燥処理される
が、更に熱圧ロールによつてカレンダー処理する
ことにより無機質物の体積比率を30%以上にする
ことが可能となる。この場合、熱圧ロールの圧力
は20〜100Kg/cm、該ロールの温度はバインダー
樹脂が使われる場合は少なくとも該バインダーの
軟化温度以上で行なうのが好ましい。
以下実施例により詳細に説明する。
実施例 1
無機粉末としてはアルミナ粉末(例えば真比重
3.93、平均粒子径0.83μmのαアルミナ粉末)を
用い、有機繊維としては、各種叩解度(水度試
験H法により200〜400c.c.)の針葉樹未晒パルプを
用いてシートを作成し、アルミナ粉末の定着性、
焼結性等を確認した。バインダーとしてエマルジ
ヨン型アクリル樹脂を添加した。これらの原料を
第1表に示す配合比率で調合した後原料スラリー
(4%濃度)に定着剤としてノニオン系高分子定
着剤を原料比0.1重量%添加して、アルミナ粉末
およびバインダー樹脂をパルプ繊維表面に定着さ
せ、これを通常の湿式円網ヤンキー抄紙機により
抄速3m/分で抄紙した。抄紙乾燥シートはスー
パーカレンダにより線圧30Kg/cm、温度120℃の
条件で高密度、高平滑化した。
得られた無機質物生シートを焼成温度1600℃で
電気炉中で焼結させ、焼成後のシートの均一性、
表面平滑性を調べ、焼結性を評価した。
第2表に各種叩解度のパルプを用いたシートの
特性を示した。なお無機分定着率は添加重量と焼
成後重量とを測定し求めた。
The present invention relates to an inorganic material sheet having sinterability. Conventional methods for manufacturing ceramics include direct methods such as hot pressing, melt casting, gas cracking, and forging, in which raw materials (powder) → molding → sintering are performed in one operation, and dry pressing, extrusion, and casting. , injection molding, doctor blade,
Indirect methods such as rubber presses were used. Industrially, indirect methods are the mainstream, but the doctor blade method is particularly preferred because it has high thickness accuracy and can yield thin sheets. The characteristics required of these molded sheets (green tapes) are (1) uniform tape thickness (2) uniform composition (3) good dimensional stability (4) appropriate flexibility (5) It is easily thermally decomposed and leaves no ash. In order to satisfy these required properties, various solvents, binders, plasticizers, peptizers, wetting agents, etc. have been studied. However, this method requires expensive materials such as polyvinyl butyral as a binder, and the use of solvents poses various operational difficulties. is required. Several methods have been proposed from this point of view, one of which is to replace cellulose pulp with a degree of substitution of 0.02~
Water content 200-100ml CSF after cationic denaturation to 0.04
There are two methods, such as a method of making paper using a conventional paper-making method using beaten pulp and inorganic powder (Japanese Patent Application Laid-Open No. 56-63099), and a method of using pulp pre-impregnated with a flocculant (Japanese Patent Application Laid-Open No. 56-167407). The former requires a process of cationizing the pulp in advance, and it is difficult to manufacture sheets containing a large amount of inorganic powder when the water content of the pulp is 100 to 200 c.c. (JIS method). The drawback was that high-quality ceramics could not be manufactured. As a result of intensive research from the viewpoint of the physical form of organic fibers and the space factor of inorganic substances, the present inventors found that if the space factor of all inorganic substances in the sheet is 25% or more, the water content of the fiber suspension is It was discovered that an extremely good ceramic can be obtained from an inorganic material sheet consisting of 3 to 20% by weight of organic fibers of 100 to 400 c.c./0.3g at a concentration of 0.03% by weight, leading to the completion of the present invention. Generally, in order for an inorganic material sheet to have homogeneous sinterability, the space factor of the inorganic material before firing is important. The space factor of the constituent material can be calculated based on the following formula from the density of the sheet before firing and the density of each component. Space factor of inorganic material Vi=P/Pixw Space factor of organic material Vo=P-PiVi/Po Space factor of voids Va=1-(Vi+Vo) However, P: Density of raw molded sheet Vi: Inorganic space factor Productivity Vo: Organic content 〃 Va: Voids 〃 Pi: Inorganic content ideal density after sintering Po: Organic content average density xw: Inorganic content weight ratio Here, the organic content average density (Po) is the pulp component and binder resin. It means the average density of
Calculated using the formula below. Po=P 1 P 2 (x 1 + x 2 )/P 1 x 2 + P 2 x 1 P 1 : Pulp fiber density P 2 : Binder resin density x 1 : Pulp weight density x 2 : Binder resin weight ratio Inorganic matter When manufacturing ceramics by sintering a sheet, if the inorganic space factor is low, a uniform sintered body cannot be obtained and the sintered state may be low density, distorted, or in extreme cases. Sometimes they are not fired as a whole and end up in pieces. Therefore, the higher the inorganic space fraction, the more desirable. FIG. 1 shows the relationship between the sintering temperature and the inorganic space factor of the green sheet during normal sintering of alumina. The shaded area is a region that can be sintered, but from the viewpoint of dimensional accuracy and economical efficiency, the inorganic space factor of the green sheet must be 25% or more, preferably 40% or more. It was confirmed that for other sinterable materials, the inorganic space factor of the raw sheet required to obtain a good sintered body is about the same as that of alumina. The weight ratio of the inorganic material powder required to achieve the above inorganic volume ratio varies slightly depending on its true specific gravity, but is approximately 70
% or more from various experimental results. Particularly when attempting to sinter high-density inorganic materials with high specific gravity, 90% by weight or more, preferably 95% by weight.
It was also found that a higher inorganic content ratio is required. It is not only extremely difficult to produce sheets with such a high mineral content using ordinary wood pulp raw materials (600 to 100 c.c. CSF), but even if it were possible, This is undesirable from the viewpoint of smoothness because the pulp disappears after consolidating and remains in the form of a pipe with a diameter of 10 μm. The inventors of the present invention have fully grasped the current situation and have conducted intensive research to create an inorganic material sheet in which the inorganic material powder is sufficiently fixed, which can be made using a general paper machine, and which has good sinterability after firing. I ended up getting it. The organic fibers used in the present invention include:
Examples include vegetable fibers such as hardwood pulp, softwood pulp, and cotton linters, and synthetic fibers such as acrylic fibers, polyester fibers, polypropylene fibers, and rayon fibers. Among these, fibers that can be made into fine fibrils are suitable for the present invention. In this respect, acrylic fibers and rayon fibers are particularly suitable among synthetic fibers in addition to vegetable fibers. Moreover, some of these fibers can also be replaced with inorganic fibers. As a method of measuring freeness, the Canadian standard freeness defined in JISP8121 is generally known.
The fine fibrillable organic fibers used in the present invention have extremely low freeness values;
Since freeness cannot be displayed properly, the freeness measurement method shown below (hereinafter referred to as freeness H method or simply H) is used.
law) was adopted. Freeness H method Using a Canadian standard freeness tester specified in JISP8121, test the brass sieve plate at the bottom of the filter tube.
Concentration of disintegrated pulp after changing to 50 mesh wire mesh
Except for changing 0.3% to 0.03%, the freeness measurement procedure is exactly the same as the JIS method, and the measured value is converted to H
It was defined as legal freeness. This H method reflects the state of fine fibrillation well and can be said to be a suitable method for indicating the degree of fibrillation of fibers necessary for the present invention. Using this method, we investigated the relationship between the water content of various fiber materials and the fixing properties of inorganic powders, and found that the water content suitable for fixing is approximately 400 c.c. or less using the H method. . When the inorganic substance powder is a ferroelectric substance, it exhibits good fixing properties even without the use of a fixing aid due to the high polarity of the material itself, but in the case of a general paraelectric substance, a fixing agent is required. In this case, high fixing properties can be obtained by using a nonionic polymeric fixing agent, a cationic polymeric fixing agent, or a combination of both. The above-mentioned beaten fine fibers alone have low aqueous properties and are difficult to make into paper, but after fixing the inorganic substance powder, the aqueous properties greatly improve as they form micro flocs.
The ability to make paper is a completely unexpected result, and the economic effect on papermaking is also great. In addition, in order to improve the peelability from the twin wire and the strength of the wet paper, it is possible to add a very small amount of relatively coarsely beaten fibers within a range that does not affect the smoothness after firing to further improve the papermaking properties. do not have. These relatively coarse fiber raw materials act as a support for fine fibers on which inorganic powder particles are fixed, so if it is less than 0.5% by weight, the effect is difficult to appear, but if it is more than 10% by weight, papermaking properties are good, but , sinterability during firing tends to deteriorate. However, when the coarse fiber raw material is a fibrous inorganic material, good papermaking properties and a high inorganic fraction can be obtained. The above-mentioned constituent raw materials are used as the main materials, binder resin is added as needed, and after the sheet is formed through the papermaking process, it is dried using a normal dryer process. It becomes possible to increase the volume ratio of objects to 30% or more. In this case, the pressure of the hot pressure roll is preferably 20 to 100 kg/cm, and if a binder resin is used, the temperature of the roll is preferably at least the softening temperature of the binder. This will be explained in detail below using examples. Example 1 The inorganic powder is alumina powder (for example, true specific gravity
3.93, α-alumina powder with an average particle diameter of 0.83 μm), and unbleached softwood pulp of various degrees of beating (200 to 400 c.c. according to the water test H method) as the organic fiber to create sheets. Fixability of alumina powder,
Sinterability etc. were confirmed. An emulsion type acrylic resin was added as a binder. After mixing these raw materials in the proportions shown in Table 1, 0.1% by weight of a nonionic polymer fixing agent was added to the raw material slurry (4% concentration) as a fixing agent, and the alumina powder and binder resin were mixed into pulp fibers. This was fixed on the surface and paper was made using a conventional wet cylinder Yankee paper machine at a speed of 3 m/min. The paper drying sheet was made highly dense and highly smooth using a super calender at a linear pressure of 30 kg/cm and a temperature of 120°C. The obtained inorganic material sheet was sintered in an electric furnace at a firing temperature of 1600°C, and the uniformity of the sheet after firing was evaluated.
The surface smoothness was examined and the sinterability was evaluated. Table 2 shows the properties of sheets using pulps with various degrees of beating. Incidentally, the inorganic content fixing rate was determined by measuring the added weight and the weight after firing.
【表】【table】
【表】【table】
【表】
実施例 2
有機繊維としてはH法による水度で200c.c.に
叩解した未晒針葉樹パルプを用い、無機粉末とし
ては、実施例1と同種のα−アルミナ粉末を用い
て、各種無機比率のシートを作成した。
定着方法及び抄紙方法は全て実施例1と同様に
して行なつた。各種配合比率の原料配合比とその
特性を第3表に示す。[Table] Example 2 As the organic fiber, unbleached softwood pulp beaten to 200 c.c. by H method was used, and as the inorganic powder, α-alumina powder of the same type as in Example 1 was used. A sheet with an inorganic ratio was created. The fixing method and paper making method were all the same as in Example 1. Table 3 shows the raw material blending ratios of various blending ratios and their characteristics.
【表】
実施例 3
実験No.1として実施例1と同様のα−アルミナ
粉末を用い、有機繊維としてH法200c.c.のアクリ
ル繊維・叩解カシミロン繊維、JIS法300c.c.の低叩
解度パルプ等をブレンドして抄紙し、シートを作
成した。
実験No.2は有機繊維としてH法200c.c.のアクリ
ル繊維・叩解カシミロン繊維を、実験No.3はH法
200c.c.の叩解レーヨン繊維をそれぞれ用いて実施
例1と同様にしてシートを作成した。
また実験No.4はアルミナ粉末の一部をアルミナ
繊維に代替する以外は実施例1と全く同様にして
抄紙し、シートを作成した。
以下第4表に配合比率およびシートの特性を示
す。
第4表に示す通り、実験No.1〜No.4のシートは
いずれも焼結性が良好であつた。[Table] Example 3 As Experiment No. 1, the same α-alumina powder as in Example 1 was used, and the organic fibers were acrylic fibers and beaten cashmilon fibers of H method 200 c.c., and low beaten cashmilon fibers of JIS method 300 c.c. Paper was made by blending pulp and other materials to create sheets. Experiment No. 2 used H method 200c.c. acrylic fiber/beaten cashmilon fiber as the organic fiber, and Experiment No. 3 used H method.
Sheets were prepared in the same manner as in Example 1 using 200 c.c. of beaten rayon fibers. In Experiment No. 4, paper was made and sheets were made in exactly the same manner as in Example 1, except that a part of the alumina powder was replaced with alumina fiber. Table 4 below shows the blending ratio and sheet properties. As shown in Table 4, the sheets of Experiments No. 1 to No. 4 all had good sinterability.
【表】【table】
【表】
実施例 4
有機繊維としては水度試験H法で200c.c.に叩
解した未晒針葉樹パルプを用い、無機粉末として
は、平均粒子径2μmのチタン酸バリウム粉末を
使用した。
以下、第5表に配合例および焼結性を示す。抄
紙方法は実施例1と同条件にて作製した。[Table] Example 4 As the organic fiber, unbleached softwood pulp beaten to 200 c.c. by water test method H was used, and as the inorganic powder, barium titanate powder with an average particle size of 2 μm was used. Table 5 below shows blending examples and sinterability. The paper was made under the same conditions as in Example 1.
【表】【table】
第1図はアルミナについての通常の焼結を示す
焼成温度と生シートの無機分占積率との関係を示
す。斜線部は焼成可能な領域である。
FIG. 1 shows the relationship between the sintering temperature and the inorganic space factor of the green sheet during normal sintering of alumina. The shaded area is the area that can be fired.
Claims (1)
抄紙法により製造される無機質物シートにおい
て、 (1) 有機繊維として微細フイブリル化可能な植物
繊維及び/又は合成繊維を用い (2) 該シート中の全無機物質粒子の占積率が25%
以上好ましくは40%以上であり、 (3) 前記有機繊維の瀘水度が0.03重量%濃度の測
定において100〜400c.c.である有機繊維を3〜20
重量%含有する ことを特徴とする無機質物シート。[Scope of Claims] 1. An inorganic material sheet produced by a wet papermaking method using inorganic particles and organic fibers as main raw materials, (1) using plant fibers and/or synthetic fibers capable of forming fine fibrils as the organic fibers ( 2) The space factor of all inorganic particles in the sheet is 25%
The above is preferably 40% or more, and (3) the organic fiber has a water filtration degree of 100 to 400 c.c. when measured at a concentration of 0.03% by weight.
An inorganic material sheet characterized by containing % by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10305882A JPS58223657A (en) | 1982-06-17 | 1982-06-17 | Inorganic sheet |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10305882A JPS58223657A (en) | 1982-06-17 | 1982-06-17 | Inorganic sheet |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58223657A JPS58223657A (en) | 1983-12-26 |
| JPS62101B2 true JPS62101B2 (en) | 1987-01-06 |
Family
ID=14344070
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10305882A Granted JPS58223657A (en) | 1982-06-17 | 1982-06-17 | Inorganic sheet |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58223657A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59169970A (en) * | 1983-03-17 | 1984-09-26 | 明成化学工業株式会社 | Manufacture of fine ceramic sheet |
| JPS638246A (en) * | 1986-06-25 | 1988-01-14 | 株式会社クボタ | Paper-making method for fiber-reinforced inorganic board |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5036248A (en) * | 1973-08-06 | 1975-04-05 | ||
| AU533396B2 (en) * | 1979-10-19 | 1983-11-24 | Turner & Newall Limited | Non-asbestos paper |
| JPS593247B2 (en) * | 1980-03-18 | 1984-01-23 | 日鉄鉱業株式会社 | Manufacturing method of ceramic structure |
-
1982
- 1982-06-17 JP JP10305882A patent/JPS58223657A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58223657A (en) | 1983-12-26 |
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