JPS6356891B2 - - Google Patents
Info
- Publication number
- JPS6356891B2 JPS6356891B2 JP57169161A JP16916182A JPS6356891B2 JP S6356891 B2 JPS6356891 B2 JP S6356891B2 JP 57169161 A JP57169161 A JP 57169161A JP 16916182 A JP16916182 A JP 16916182A JP S6356891 B2 JPS6356891 B2 JP S6356891B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- weight
- diaphragm
- mixed
- fluororesin
- 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.)
- Expired
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
Description
この発明は弗素樹脂製隔膜の製造法に関するも
のであり、含水シリカ微粉末を配合することによ
り電気抵抗が小さく、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。
従来こ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、これをフイ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。
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
ることが困難であつた。
この発明は従来の欠点を解消し、弗素樹粉末75
〜85重量%と混合時の含水率が5〜13重量%であ
り、湿式法によつて得られた比表面積が200m2/
g〜250m2/gの高活性シリカである含水シリカ
微粉末15〜25重量%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150〜300Kg/cm2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により、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。
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10〜20ミリミクロン、比表面積
(BET法)が200m2/g〜250m2/gの高活性シリ
カが用いられる。弗素樹脂粉末の配合量は75〜85
重量%、含水シリカ微粉末の配合量は15〜25重量
%が好ましい。含水シリカ微粉末の配合量が15重
量%以下(弗素樹脂粉末の配合量が85重量%以
上)で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25重量%以上(弗素樹脂粉末の配
合量が75重量%以下)では混合粉末の成型が困難
になり、また隔膜の強度も低下する。
この発明で用いる含水シリカ微粉末の含水率は
5〜13重量%が好ましく、含水率が5重量%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重量%以上では成型体を焼成する際成型体
の収縮が大きくなり割れやすくなる。
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。この混合粉末を金型内に充
填して150〜300Kg/cm2の圧力で加圧成型し、脱型
後330〜380℃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。
次にこの発明を実施例により説明する。
実施例 1
四弗化エチレン樹脂粉末85重量%と含水シリカ
微粉末(日本シリカ工業(株)製Nipsil VN3,含水
率8重量%)15重量%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
Kg/cm2で加圧成型し、内径70mm,外径240mmの筒
状成型体を得た。これを加熱焼成後、厚さ0.2mm,
0.25mmの隔膜を切削した。各隔膜の性能は表―1
の通りである。
The present invention relates to a method for manufacturing a fluororesin diaphragm, and relates to a method for manufacturing a fluororesin diaphragm that has low electrical resistance and low water permeability by blending fine hydrated silica powder. Conventionally, the method for producing this type of diaphragm is to mix fluororesin powder and fine silica powder 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 extrusion is followed by heating and baking, but this production method has the drawbacks that mixing is time-consuming and removal of the solvent and activator is time-consuming. A method has also been proposed in which fluororesin powder and anhydrous fine silica gel powder are mixed dry without using a solvent and then molded, but since the mixed powder is anhydrous, the powder becomes electrically charged during mixing. Since it adheres to the wall of the mixer and granulates into lumps, it is difficult to obtain a diaphragm with a uniform composition. This invention eliminates the conventional drawbacks and makes fluorine powder 75
-85% by weight, the moisture content at the time of mixing is 5-13% by weight, and the specific surface area obtained by the wet method is 200m 2 /
After dry mixing with 15 to 25% by weight of hydrated silica fine powder, which is highly active silica with a weight of ~250 m 2 /g, this mixed powder is filled into a mold and applied at a pressure of 150 to 300 Kg / cm 2 . The present invention provides a method for easily manufacturing a diaphragm having a uniform composition by cutting the membrane from a molded body obtained by pressure molding, demolding, and heating and baking. In this invention, the fluororesin used is tetrafluoroethylene resin, hexafluoropropylene resin, etc., and the hydrated silica fine powder has a primary particle diameter of 10 to 20 millimicrons obtained by a wet method, and a specific surface area (BET Highly active silica having a particle diameter of 200 m 2 /g to 250 m 2 /g is used. The blending amount of fluororesin powder is 75 to 85
The amount by weight of the hydrated silica fine powder is preferably 15 to 25% by weight. When the amount of hydrated silica fine powder is 15% by weight or less (the amount of fluororesin powder is 85% or more), the electrical resistance of the diaphragm increases; If the blending amount is less than 75% by weight), it becomes difficult to mold the mixed powder, and the strength of the diaphragm also decreases. The water content of the hydrated silica fine powder used in this invention is preferably 5 to 13% by weight; if the water content is less than 5% 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 not be able to be mixed uniformly. When firing, the molded product shrinks more and becomes more susceptible to cracking. 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. This mixed powder is filled into a mold, pressure molded at a pressure of 150 to 300 kg/ cm2 , and after demolding, the membrane is cut from the molded body obtained by heating and baking at a temperature of 330 to 380°C. , a high quality diaphragm can be obtained. Next, the present invention will be explained with reference to examples. Example 1 85% by weight of tetrafluoroethylene resin powder and 15% by weight of hydrated silica fine powder (Nipsil VN3 manufactured by Nippon Silica Kogyo Co., Ltd., water content: 8% by weight) were dry mixed in a mixer,
This mixed powder is filled into a mold and the pre-molding pressure is 200.
Pressure molding was performed at Kg/cm 2 to obtain a cylindrical molded body with an inner diameter of 70 mm and an outer diameter of 240 mm. After heating and baking this, the thickness is 0.2mm,
A diaphragm of 0.25 mm was cut. Table 1 shows the performance of each diaphragm.
It is as follows.
【表】
実施例 2
四弗化エチレン樹脂粉末81重量%と含水シリカ
微粉末(日本シリカ工業(株)製Nipsil LP,含水率
13重量%)19重量%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250Kg/
cm2で加圧成型し、内径70mm、外径240mmの筒状成
型体を得た。これを加熱焼成後、厚さ0.2mm,
0.25mm,0.3mm,0.4mmの隔膜を切削した。各隔膜
の性能は表―2の通りである。[Table] Example 2 Tetrafluoroethylene resin powder 81% by weight and hydrated silica fine powder (Nipsil LP manufactured by Nippon Silica Kogyo Co., Ltd., water content)
13% by weight) and 19% by weight are dry mixed in a mixer, this mixed powder is filled into a mold, and the pre-molding pressure is 250Kg/
A cylindrical molded body with an inner diameter of 70 mm and an outer diameter of 240 mm was obtained by pressure molding at cm 2 . After heating and baking this, the thickness is 0.2mm,
Diaphragms of 0.25mm, 0.3mm, and 0.4mm were cut. The performance of each membrane is shown in Table 2.
【表】
実施例 3
四弗化エチレン樹脂粉末75重量%と含水シリカ
微粉末(日本シリカ工業(株)製Nipsil NS,含水率
5重量%)25重量%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
Kg/cm2で加圧成型し、内径70mm,外径240mmの筒
状成型体を得た。これを加熱焼成後、厚さ0.3mm,
0.4mmの隔膜を切削した。各隔膜の性能は表―3
の通りである。[Table] Example 3 75% by weight of tetrafluoroethylene resin powder and 25% by weight of hydrated silica fine powder (Nipsil NS manufactured by Nippon Silica Kogyo Co., Ltd., water content: 5% by weight) were dry mixed in a mixer. Fill the mixed powder into the mold and pre-molding pressure 300
Pressure molding was performed at Kg/cm 2 to obtain a cylindrical molded body with an inner diameter of 70 mm and an outer diameter of 240 mm. After heating and baking this, the thickness is 0.3mm,
A 0.4 mm diaphragm was cut. Table 3 shows the performance of each diaphragm.
It is as follows.
【表】
電気抵抗値の測定方法
隔膜を3Nの食塩水溶液に十分平衡にした後、
5Nの食塩水溶液中でAC1000Hzで温度25℃におい
て測定する。
透水量の測定方法
水柱1.0mの圧力下で20cm2の膜から透水してく
る蒸留水の量を測定する。
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ことなく、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
が容易であり、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
とな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。[Table] Method for measuring electrical resistance value After fully equilibrating the diaphragm with a 3N saline solution,
Measured in a 5N saline solution at 1000Hz AC at a temperature of 25℃. Method for measuring water permeation: Measure the amount of distilled water that permeates through a 20 cm 2 membrane under the pressure of 1.0 m of water column. As described above, according to the present invention, since the fluororesin powder and the hydrated silica fine powder are dry mixed, the powder is not charged during mixing, and uniformly dispersed mixed powder can be obtained in a simple process. Can be done. In addition, since the diaphragm is cut from the molded body that is heated and fired after pressure-molding this mixed powder, it is easy to mass-produce the diaphragm.The resulting diaphragm has hydrated silica fine powder evenly dispersed, so it has a high electrical resistance. is small,
In addition, the amount of water permeation is small, and since the hydrated silica fine powder is fused to the fluororesin, it has the advantage that stable performance is maintained for a long period of time without falling off during use.
Claims (1)
が5〜13重量%であり、湿式法によつて得られた
比表面積が200m2/g〜250m2/gの高活性シリカ
である含水シリカ微粉末15〜25重量%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
150〜300Kg/cm2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 Highly active silica with a water content of 5 to 13% by weight when mixed with fluororesin powder of 75 to 85% by weight, and a specific surface area of 200m 2 /g to 250m 2 /g obtained by a wet method. After dry mixing 15 to 25% by weight of hydrated silica fine powder, this mixed powder is filled into a mold.
A method for producing a fluororesin diaphragm, which is characterized in that the membrane is cut from a molded body obtained by pressure molding at a pressure of 150 to 300 Kg/cm 2 , demolding the mold, and then heating and baking the molded body.
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 JPS5955722A (en) | 1984-03-30 |
| JPS6356891B2 true 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 (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0424231U (en) * | 1990-06-19 | 1992-02-27 |
Families Citing this family (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 |
Family Cites Families (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
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0424231U (en) * | 1990-06-19 | 1992-02-27 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5955722A (en) | 1984-03-30 |
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