JPS5955722A - Molding method of diaphragm made of fluorocarbon resin - Google Patents
Molding method of diaphragm made of fluorocarbon resinInfo
- Publication number
- JPS5955722A JPS5955722A JP16916182A JP16916182A JPS5955722A JP S5955722 A JPS5955722 A JP S5955722A JP 16916182 A JP16916182 A JP 16916182A JP 16916182 A JP16916182 A JP 16916182A JP S5955722 A JPS5955722 A JP S5955722A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- diaphragm
- mixed powder
- silicahydrate
- molded
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
との発明は弗素樹脂製隔膜の製造法に関するものであシ
、含水シリカ微粉末を配合することによシミ気抵抗が小
さく、かつ透水量の少い弗素樹脂製隔膜を製造する方法
に関するものである。[Detailed Description of the Invention] The invention relates to a method for producing a fluororesin diaphragm, and the fluororesin diaphragm has low stain resistance and low water permeability by incorporating hydrated silica fine powder. The present invention relates to a method for manufacturing.
従来との種の隔膜を製造する方法としては、弗素樹脂粉
末とシリカ微粉末とを、水或は有機溶剤などの溶媒と活
性剤(分散剤)と共に混合してペースト状とし、これを
フィルム状に押し出した後加熱焼成する湿式法が採用さ
れているが、この製造法では混合に手間がかかると共に
、溶媒や活性剤の除去に手数がかかるという欠点がある
。The conventional method for producing a diaphragm is to mix fluororesin powder and fine silica powder together with a solvent such as water or an organic solvent and an activator (dispersant) to form a paste, and then form this into a film. A wet method is used in which the mixture is extruded and then heated and baked, but this manufacturing method has the disadvantage that mixing is time-consuming and removal of the solvent and activator is time-consuming.
また弗素樹脂粉末と無水のシリカゲル微粉末とを溶媒を
用いずに乾式で混合し、これを成型加工する方法も提案
されているが、混合粉末が無水物であるため混合中に粉
末が帯電し、混合機の壁に付着して塊状に造粒するので
、均一な組成の隔膜を得ることが困難であった。A method has also been proposed in which fluororesin powder and anhydrous fine silica gel powder are dry mixed without using a solvent and then molded, but since the mixed powder is anhydrous, the powder becomes electrically charged during mixing. However, it was difficult to obtain a diaphragm with a uniform composition because it adhered to the wall of the mixer and granulated into lumps.
この発明は従来の欠点を解消し、弗素樹脂粉末とシリカ
微粉末とを乾式で混合した後、この混合粉末を加圧成型
し、脱型後加熱焼成して得た成型体から膜を切削するこ
とによシ、均一な組成の隔膜を容易に製造する方法を提
供するものである。This invention solves the conventional drawbacks by dry mixing fluororesin powder and fine silica powder, molding the mixed powder under pressure, removing the mold, and then heating and baking to cut a film from the molded body. In particular, it provides a method for easily producing membranes of uniform composition.
この発明において、弗素樹脂としては四弗化エチレン樹
脂、六弗化プロピレン樹脂などが用いられ、含水シリカ
微粉末としては湿式法で得られた一次粒子径がlO〜2
0 ミIJミクロン、比表面積(BIT法)が200m
”7g −230mugの高活性シリカが用いられる。In this invention, the fluororesin used is tetrafluoroethylene resin, hexafluoropropylene resin, etc., and the hydrated silica fine powder has a primary particle size of 10 to 2
0 micron IJ micron, specific surface area (BIT method) 200m
7g - 230mg of highly active silica is used.
弗素樹脂粉末の配合量は76− 、!’タ重量メ、含水
シリカ微粉末の配合量は/よ〜、2j重量ズが好ましい
。含水シリカ微粉末の配合量が/j重重量%下(弗素樹
脂粉末の配合量がlr!重量重量上以上は隔膜の電気抵
抗が増大し、含水シリカ微粉末の配合量がコj重量喀以
上(弗素樹脂粉末の配合量が7j重量メ以下)では混合
粉末の成型が困難になシ、また隔膜の強度も低下する。The blended amount of fluororesin powder is 76-,! The amount of the hydrated silica fine powder to be blended is preferably 20 to 20% by weight. If the blended amount of hydrated silica fine powder is below /jwt% (the blended amount of fluororesin powder is lr!), the electrical resistance of the diaphragm will increase, and if the blended amount of hydrated silica fine powder is above cojwt% (If the amount of fluororesin powder is less than 7Jwt), it becomes difficult to mold the mixed powder, and the strength of the diaphragm also decreases.
この発明で用いる含水シリカ微粉末の含水率はj−/J
重重量%好ましく、含水率が!重量メ以下では粉末が混
合中に帯電して均一な混合ができず、13重重量%上で
は成型体を焼成する際成型体の収縮が大きくなシ割れや
すくなる。The moisture content of the hydrated silica fine powder used in this invention is j-/J
% by weight is preferred, and moisture content! If the weight is less than 13% by weight, the powder will be charged during mixing and uniform mixing will not be possible, and if it is more than 13% by weight, the molded product will shrink significantly and tend to crack when fired.
前述した含水シリカ微粉末と弗素樹脂粉末とを溶媒を用
いずに混合機で乾式混合すると、混合中に粉末が帯電せ
ず非常に均一に分散した混合粉末を得ることができる。When the above-mentioned hydrated silica fine powder and fluororesin powder are dry mixed in a mixer without using a solvent, the powder is not charged with electricity during mixing, and a mixed powder can be obtained that is very uniformly dispersed.
この混合粉末を金型内に充填して/、tθ〜300 k
g/l*2の圧力で加圧成型し、脱型後330〜310
℃の温度で加熱焼成して得た成型体から膜を切削するこ
とにより、高品質の隔膜が得られる。Fill this mixed powder into a mold /, tθ ~ 300 k
Pressure molded at a pressure of g/l*2, 330-310 after demolding
A high-quality diaphragm can be obtained by cutting the membrane from a molded body obtained by heating and baking at a temperature of .degree.
次にこの発明を実施例によシ説明する。Next, the present invention will be explained with reference to examples.
実施例1゜
四弗化エチレン樹脂粉末♂j重量メと含水シリカ微粉末
(日本シリカニ業11JiJ II! N1psil
VH2。Example 1゜Tetrafluoroethylene resin powder
VH2.
含水率を重量s’)tsl量算とを混合機で乾式混合し
、この混合粉末を金型に充填して予備成型圧力、200
に4/cI112で加圧成型し、内径7Qm。The moisture content and weight s')tsl were dry mixed in a mixer, and this mixed powder was filled into a mold and the premolding pressure was set to 200.
Pressure molded with 4/cI112, inner diameter 7Qm.
外径2’lOwgの筒状成型体を得た。これを加熱焼成
後、厚さ0..2111N 、θ、、2.1t III
の隔膜を切削した。各隔膜の性能は表−1の通りである
。A cylindrical molded body having an outer diameter of 2'lOwg was obtained. After heating and baking this, the thickness is 0. .. 2111N, θ,, 2.1t III
The septum was cut. The performance of each diaphragm is shown in Table 1.
表−1
実施例2゜
四弗化エチレン樹脂粉末ざ/重量−と含水シリカ微粉末
(日本シリカニ業■製N1psi’l LP 。Table 1 Example 2 Tetrafluoroethylene resin powder/weight - and hydrated silica fine powder (N1psi'l LP manufactured by Nippon Silkani Industry).
含水率73重量S)lり重量メとを混合機で乾式混合し
、この混合粉末を金型に充填して予備成型圧力、zro
kq/ax”で加圧成型し、内径70KM。Moisture content: 73 weight S
Pressure molded with "kq/ax", inner diameter 70KM.
外径、2弘θ顛の筒状成型体を得た。これを加熱焼成後
、厚さ0..211I 、 Q、23m 、 Q、3
mg 、 Q、グーの隔膜を切削した。各隔膜の性能は
表−2の通シである。A cylindrical molded body with an outer diameter of 2 mm and θ was obtained. After heating and baking this, the thickness is 0. .. 211I, Q, 23m, Q, 3
The diaphragms of mg, Q, and Gu were cut. The performance of each diaphragm is shown in Table 2.
表−2
実施例3゜
四弗化エチレン樹脂粉末7!重量メと含水シリカ微粉末
(日本シリカニ業■製N1psil NS 。Table-2 Example 3゜Tetrafluoroethylene resin powder 7! Weight and water-containing silica fine powder (N1psil NS manufactured by Nippon Silikani Co., Ltd.).
含水率j重量%)、2夕重量メとを混合機で乾式混合し
、この混合粉末を金型に充填して予備成型圧力300知
/ax2で加圧成型し、内径70n。Water content (Jwt%) and 200g/ax2 were dry mixed in a mixer, and this mixed powder was filled into a mold and press-molded at a pre-molding pressure of 300mm/ax2 to have an inner diameter of 70n.
外径2’lOWの筒状成型体を得た。これを加熱焼成後
、厚さQ、3gm、θ、り鱈の隔膜を切削した。各隔膜
の性能は表−3の通シである。A cylindrical molded body having an outer diameter of 2'lOW was obtained. After heating and baking this, a cod diaphragm having a thickness Q of 3 gm and θ was cut. The performance of each diaphragm is shown in Table 3.
表−3
隔膜をjNの食塩水溶液に十分平衡にした後、jNの食
塩水溶液中でAO1000Hzで温度コjbにおいて測
定する。Table 3 After fully equilibrating the diaphragm in a saline solution of jN, measurements are taken in a saline solution of jN at an AO of 1000 Hz and at a temperature of 1000 Hz.
透水量の測定方法
水柱/、Omの圧力下で、20α2の膜から透水してく
る蒸留水の量を測定する。Method for Measuring Water Permeation Amount The amount of distilled water permeating through a 20α2 membrane is measured under a pressure of water column/Om.
以上に述べたようにこの発明によれば、弗素樹脂粉末と
含水シリカ微粉末とを乾式混合するので、混合中に粉末
が帯電するとと々く、均一に分散混合した粉末を簡単な
工程で得ることができる。またこの混合粉末を加圧成型
した後加熱焼成した成型体から隔膜を切削するので、隔
膜の量産が容易であわ、得られた隔膜は含水シリカ微粉
末が均一に分散しているので、電気抵抗が小さく、かつ
透水量が少いと共に、含水シリカ微粉末が弗素樹脂に融
着しているので、使用中に脱落すること力く長期間安定
した性能が維持されるなどの利点を有する。As described above, according to the present invention, since the fluororesin powder and the hydrated silica fine powder are dry-mixed, as soon as the powder is charged during mixing, uniformly dispersed and mixed powder can be obtained in a simple process. be able to. In addition, since the diaphragm is cut from the molded body after press-molding this mixed powder and then heating and firing, mass production of the diaphragm is easy.The obtained diaphragm has hydrated silica fine powder evenly dispersed, so it has a high electrical resistance. It has the advantage of having a small amount of water permeation, and since the hydrated silica fine powder is fused to the fluororesin, it does not fall off during use and maintains stable performance over a long period of time.
特許出願人 ニチアス株式会社 7 − 137−Patent applicant: NICHIAS Co., Ltd. 7 - 137-
Claims (2)
カ微粉末/J′〜、2!重量メとを乾式で混合した後、
この混合粉末を金型内に充填してito〜300kg/
cx2の圧力で加圧成型し、これを脱型後加熱焼成して
得た成型体から膜を切削することを特徴とする弗素樹脂
製隔膜の製造法。(1) Fluororesin powder 7! ~trr weight and hydrated silica fine powder/J'~, 2! After dry mixing with the weight method,
This mixed powder is filled into a mold and weighs up to 300 kg/
A method for producing a fluororesin diaphragm, which comprises press molding at a pressure of cx2, demolding the mold, and then cutting the membrane from the resulting molded body.
/3重量メであ)、湿式法によって得られた比表面積が
200m”7g−2J′Om”7gの高活性シリカであ
ることを特徴とする特許請求の範囲第1項記載の弗素樹
脂製隔膜の製造法。(2) The hydrated silica fine powder has a moisture content of j-
The fluororesin diaphragm according to claim 1, which is made of highly active silica having a specific surface area of 200m"7g-2J'Om"7g obtained by a wet method. manufacturing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16916182A JPS5955722A (en) | 1982-09-27 | 1982-09-27 | Molding method of diaphragm made of fluorocarbon resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16916182A JPS5955722A (en) | 1982-09-27 | 1982-09-27 | Molding method of diaphragm made of fluorocarbon resin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5955722A true JPS5955722A (en) | 1984-03-30 |
JPS6356891B2 JPS6356891B2 (en) | 1988-11-09 |
Family
ID=15881399
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16916182A Granted JPS5955722A (en) | 1982-09-27 | 1982-09-27 | Molding method of diaphragm made of fluorocarbon resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5955722A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60153903A (en) * | 1984-01-23 | 1985-08-13 | Nok Corp | Ultrafiltration membrane and its preparation |
JPS6140811A (en) * | 1984-07-31 | 1986-02-27 | Nippon Chem Ind Co Ltd:The | Hydrated silica for melting and manufacture of melted silica by using it |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0424231U (en) * | 1990-06-19 | 1992-02-27 |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5741554A (en) * | 1980-08-21 | 1982-03-08 | Mitsubishi Electric Corp | Refrigerating plant |
-
1982
- 1982-09-27 JP JP16916182A patent/JPS5955722A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5741554A (en) * | 1980-08-21 | 1982-03-08 | Mitsubishi Electric Corp | Refrigerating plant |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60153903A (en) * | 1984-01-23 | 1985-08-13 | Nok Corp | Ultrafiltration membrane and its preparation |
JPH042291B2 (en) * | 1984-01-23 | 1992-01-17 | ||
JPS6140811A (en) * | 1984-07-31 | 1986-02-27 | Nippon Chem Ind Co Ltd:The | Hydrated silica for melting and manufacture of melted silica by using it |
JPH0127003B2 (en) * | 1984-07-31 | 1989-05-26 | Nippon Chemical Ind |
Also Published As
Publication number | Publication date |
---|---|
JPS6356891B2 (en) | 1988-11-09 |
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