JPH01199618A - Filter for filtration - Google Patents
Filter for filtrationInfo
- Publication number
- JPH01199618A JPH01199618A JP2310488A JP2310488A JPH01199618A JP H01199618 A JPH01199618 A JP H01199618A JP 2310488 A JP2310488 A JP 2310488A JP 2310488 A JP2310488 A JP 2310488A JP H01199618 A JPH01199618 A JP H01199618A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- zinc oxide
- whiskers
- high pressure
- filtration
- 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
- 238000001914 filtration Methods 0.000 title claims abstract description 16
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000011787 zinc oxide Substances 0.000 claims abstract description 15
- 239000011521 glass Substances 0.000 claims abstract description 10
- 238000010304 firing Methods 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 14
- 230000035699 permeability Effects 0.000 abstract description 9
- 238000001354 calcination Methods 0.000 abstract 1
- 230000006866 deterioration Effects 0.000 abstract 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 13
- 238000000034 method Methods 0.000 description 8
- 239000013078 crystal Substances 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 239000011148 porous material Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 229910052725 zinc Inorganic materials 0.000 description 5
- 239000011701 zinc Substances 0.000 description 5
- 239000011230 binding agent Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000012784 inorganic fiber Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000007751 thermal spraying Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Landscapes
- Filtering Materials (AREA)
- Porous Artificial Stone Or Porous Ceramic Products (AREA)
Abstract
Description
【発明の詳細な説明】 産業上の利用分野 本発明は汚れ処理、遣水等の水処理フィルター。[Detailed description of the invention] Industrial applications The present invention is a water treatment filter for dirt treatment, water supply, etc.
空気浄化フィルター、食品工業等の懸濁液処理フィルタ
ー、化学工業等の水、排水プロセス・フィルター等とし
て利用される濾過フィルターに関する。It relates to filtration filters that are used as air purification filters, suspension processing filters in the food industry, etc., water and wastewater process filters in the chemical industry, etc.
従来の技術
従来の濾過フィルターには、■F紙、P布等の有機質a
、誰をからませて連結したもの、不織布のように別種バ
インダーで連結したもの、■金網。Conventional technology Conventional filtration filters include ■organic materials such as F paper and P cloth.
, those that are connected by entangling them, those that are connected using a different type of binder like non-woven fabric, ■ Wire mesh.
ガラスマット、ガラスクロスの如く細線物、無機質繊維
を互に絡せたり、バインダーで連結したもの、@有機シ
ート状物に網孔6微細孔を発現させたもの、cD焼結金
属のように無機非繊維質粒状物を溶着又は別種バインダ
ーで連結したもの等がある。Fine wire materials such as glass mats and glass cloth, inorganic fibers entwined with each other or connected with a binder, organic sheet materials with 6 micropores, and inorganic materials such as cD sintered metals. There are also those in which non-fibrous particulates are welded or connected with a different type of binder.
発明が解決しようとする課題
これらはそれぞれな特長を有するが、濾過効率の点では
、■@は繊維状物の径が小ならば低圧下では拒絶性、透
過性共に良好であるが、高圧下では繊維部分の変形によ
り圧密化して透過性が低下する。@は低圧下でも孔形成
密度に限界があシ透過性が前者より劣る。又高圧下では
圧密化により孔寸法が変化して透過率が下がる。■は低
圧下。Problems to be Solved by the Invention Each of these has its own features, but in terms of filtration efficiency, ■@ has good rejection and permeability under low pressure if the diameter of the fibrous material is small, but it has good rejection and permeability under high pressure. In this case, the fibers become compacted due to deformation and the permeability decreases. @ has a limited pore formation density even under low pressure and is inferior to the former in permeability. Also, under high pressure, the pore size changes due to compaction and the transmittance decreases. ■ is under low pressure.
高圧下で孔寸法は変化しないが、空孔率が充分に上がら
ない。Although the pore size does not change under high pressure, the porosity does not increase sufficiently.
本発明では従来の各種フィルターの問題点である高圧下
での濾過特性の低下を改良して、常圧下。The present invention improves the problem of conventional various filters, which is the decline in filtration characteristics under high pressure, and improves the filtration characteristics under normal pressure.
高圧下共に高拒絶率、高透過性を達成する濾過フィルタ
ーを提供しようとするものである。The purpose of this invention is to provide a filter that achieves high rejection rate and high permeability under high pressure.
課題を解決するための手段
本発明は2方向以上に分岐した構造を有する酸化亜鉛ウ
ィスカーにガラスフリットを添加し焼成してなるもので
ある。Means for Solving the Problems The present invention is made by adding glass frit to zinc oxide whiskers having a structure branched in two or more directions and firing the resulting whiskers.
作用
上記ウィスカーの針状部は互に絡プ、細孔で且つ空孔率
の高い極めて秀れたF材構造が達成される。孔径寸法は
成型時のプレス圧により縮シ、針状部の交点は添加した
ガラスフリットの溶融により連結される。又、上記ウィ
スカーは水、溶媒等のぬれ特性が良好であシ、単結晶で
内部格子欠かんの無い完全結晶強度に近似した強度を有
する素材であり高圧下でも全く変化なく、濾過特性を発
揮するものである。Function: The acicular portions of the whiskers are intertwined with each other, achieving an extremely excellent F material structure with fine pores and high porosity. The pore size is reduced by the press pressure during molding, and the intersections of the needle-shaped parts are connected by melting the added glass frit. In addition, the above whiskers have good wetting properties with water, solvents, etc., and are a single crystal material with a strength close to that of a perfect crystal with no internal lattice defects, and exhibit filtration properties without changing at all even under high pressure. It is something to do.
実施例 以下1本発明の実施列について説明する。Example One embodiment of the present invention will be described below.
まず、金属亜鉛を酸化して製造された酸化亜鉛ウィスカ
ーを準備する。具体的に説明すると、この酸化亜鉛ウィ
スカーは、従来の酸化亜鉛の製造方法や酸化亜鉛ウィス
カーの製造方法と異なり。First, zinc oxide whiskers produced by oxidizing metallic zinc are prepared. Specifically, this zinc oxide whisker is different from conventional zinc oxide manufacturing methods and zinc oxide whisker manufacturing methods.
金属亜鉛粉末を使用することによって得られる。Obtained by using metallic zinc powder.
それらの粒子径は0.1〜500μmが使用可能であり
、なかでも10〜300μmのものが最良の結果となる
。又これらの金属亜鉛粉末は亜鉛線や亜鉛粉末をアーク
式の溶射装置で空気中に溶射することによシ得た粉末が
好ましいが、他の粉砕法。Particle diameters of 0.1 to 500 μm can be used, and among them, those of 10 to 300 μm give the best results. Preferably, these metallic zinc powders are powders obtained by spraying zinc wire or zinc powder into the air using an arc-type thermal spraying device, but other pulverization methods may also be used.
噴霧法、スタンプミル法、ボールミル法より得られる上
記範囲の亜鉛粉末を用いることもできる。Zinc powder within the above range obtained by a spray method, a stamp mill method, or a ball mill method can also be used.
上記の亜鉛粉末の表面に酸化皮膜を形成する方法として
は、以下の方法が好ましい。まず、水共存下での機械的
処理として、乳鉢式薄情機、ロール等で処理を行い1粒
子に機械的に圧力を加える。As a method for forming an oxide film on the surface of the above zinc powder, the following method is preferable. First, mechanical treatment in the coexistence of water is performed using a mortar-type thinning machine, a roll, etc., and mechanical pressure is applied to each particle.
更にこれを水中に24時間以上、なかでも76時間なら
ば如何なる大きさの粒子の粒子径でも完全なる結果を与
える。又放置温度は20℃以上に保つことが好ましい。Furthermore, if it is left in water for 24 hours or more, especially 76 hours, it will give perfect results regardless of the particle size. Further, it is preferable to keep the temperature at which the product is left standing at 20° C. or higher.
次に放置後乾燥する。この乾燥は粉末表面の水切りが達
成されればよく1次の焼成工程の高温中へ移行した当初
の俗書が防がれるように、即ちるつぼ1割れ、粉のとび
散りがなくなる程度に乾燥すれば良好である。このため
風乾から亜鉛粉末の溶融しない温度範囲まで行うことが
できる。次に乾した粉末は1耐熱容器通窩はアルミナ等
のるつぼに入れ、酸素を含む雰囲気中でgoo〜150
0℃、なかでも900〜11oO℃で加熱するのがいか
なる粒子径でも良好な結果を与える。Then leave it to dry. This drying should be done as long as the water on the powder surface is drained, and the drying should be done to the extent that the crucible does not crack and the powder does not scatter, so as to prevent the initial slang caused by the transition to the high temperature of the first firing process. If it is good. Therefore, drying can be carried out from air drying to a temperature range where the zinc powder does not melt. Next, the dried powder is placed in a crucible made of alumina, etc., and heated to a temperature of 150°C in an atmosphere containing oxygen.
Heating at 0°C, particularly 900-110°C, gives good results for any particle size.
前記の加熱焼成は1通常空気中で行えばよいが、窒素と
酸素の混合ガス中で行ってもよい。The heating and firing described above may normally be carried out in air, but may also be carried out in a mixed gas of nitrogen and oxygen.
金属亜鉛粉末を、前記のように、水共存下で薄情やロー
ル等で機成的圧力を付与することによシ表面に酸化皮膜
が形成されるが、後の水中での放置によシこの皮膜が成
長する。これはX線回折法により確認された。又このよ
うにして形成した酸化皮膜は、特別な効果を与える。す
なわち乾燥雰囲気中で通常亜鉛表面に形成される薄い不
動態的皮膜を有するものでは、焼成時に不均一焼成とな
り、団塊状酸化亜鉛と金属亜鉛が共存するものとなる。As mentioned above, an oxide film is formed on the surface of metallic zinc powder when mechanical pressure is applied to it in the presence of water, such as by rolling or rolling, but this film is formed when left in water afterwards. A film grows. This was confirmed by X-ray diffraction. The oxide film thus formed also provides special effects. That is, in the case of a product having a thin passive film that is normally formed on the surface of zinc in a dry atmosphere, the firing process will be uneven, resulting in the coexistence of nodular zinc oxide and metallic zinc.
一方、上記の成長した酸化皮膜を有する亜鉛粉末では、
高温焼成が均一かつ完全に進行して。On the other hand, in the zinc powder with the above-mentioned grown oxide film,
High temperature firing progresses uniformly and completely.
金属亜鉛は完全に酸化されて、高率に酸化亜鉛ウィスカ
ーに成長する。また、高温暁成時、容器内部に設置した
原斜は容器内部で反応が終結する。Metallic zinc is completely oxidized and grows into zinc oxide whiskers at a high rate. In addition, during high-temperature formation, the reaction of the original slope installed inside the vessel ends inside the vessel.
また、こと【生成するウィスカーは、従来の酸化亜鉛ウ
ィスカーにみられる単純な?!1&維状単結晶体ではな
く、核部から4輪に成長した針状結晶構造を有するテト
ラボッド状構造を有する。Also, is it possible that [the whiskers produced are simple compared to those seen in conventional zinc oxide whiskers?] ! It has a tetrabod-like structure with a needle-like crystal structure that has grown into four rings from the core, rather than a fibrous single crystal.
この酸化亜鉛ウィスカーは、テトラボッド状1J造が基
本形状であるが、3軸に成長した針状結晶構造を有する
ものが多い。これを二次加工1例えばボールミルで24
時間粉砕処理して結晶成長軸のつけ根部分より切断し、
棒状の針状酸化亜鉛とすることは勿論可能である。The basic shape of the zinc oxide whiskers is a tetrabod-like 1J structure, but many have a triaxially grown needle-like crystal structure. This is subjected to secondary processing 1, for example, using a ball mill.
After time crushing, cut from the base of the crystal growth axis,
Of course, it is possible to use rod-shaped needle-shaped zinc oxide.
さて、この酸化亜鉛ウィスカーにガラスフリットを添加
し、このガラスフリットの融点以上の温度で焼成するこ
とによυ濾過フィルターを得だ。Now, by adding glass frit to this zinc oxide whisker and firing it at a temperature above the melting point of this glass frit, a υ filtration filter was obtained.
なお、酸化亜鉛ウィスカーの特性と量、ガラスフリット
の添加量と融点、焼成温度は以下の第1表の通りとした
。The characteristics and amount of zinc oxide whiskers, the amount of glass frit added, the melting point, and the firing temperature were as shown in Table 1 below.
(以下余白)
尚、実施例(1)、(2)、(3)共に成型時バインダ
ーと −してポリビニールアルコールを使用しプ
レス圧は200’C9/cITlとした。(The following is a blank space) In Examples (1), (2), and (3), polyvinyl alcohol was used as a binder during molding, and the press pressure was 200'C9/cITl.
以下の第2表は実施列(1)、 (2)、 (3)と従
来例(褐。Table 2 below shows the implementation columns (1), (2), (3) and the conventional example (brown).
(6) 、(6)を一定条件で濾過実検を行い、フィル
ター特性を検討した結果である。(6) This is the result of conducting actual filtration tests under certain conditions and examining the filter characteristics.
(4)、(5)、(6)はそれぞれ濾紙、メンブランフ
ィルタ−、ニッケル焼結金属フィルターである。尚。(4), (5), and (6) are filter paper, membrane filter, and nickel sintered metal filter, respectively. still.
フィルター特性評価は純水に平均粒子径3μmのポリス
チレンゲルを分散させて用いた。For filter characteristic evaluation, polystyrene gel having an average particle size of 3 μm was dispersed in pure water.
米1 F紙の場合を1とした。The case of US 1F paper was set as 1.
以上の様に実施例は低圧下の透水性が大で、高圧下では
更に大きく変化して秀れたフィルター特性2示す。尚、
この時、各フィルター共にポリスチレンゲルの拒絶率は
100%であった。As described above, the examples have high water permeability under low pressure and change even more significantly under high pressure, exhibiting excellent filter properties 2. still,
At this time, the rejection rate of polystyrene gel was 100% for each filter.
発明の効果
以上のよって本発明の濾過フィルターは高圧下でも極め
て安定で高透水性を示し濾過効率の著しい高いものであ
)、その産業性は大である。As a result of the effects of the invention, the filtration filter of the present invention is extremely stable even under high pressure, exhibits high water permeability, and has extremely high filtration efficiency), and has great industrial potential.
Claims (1)
にガラスフリットを添加して焼成してなることを特徴と
するろ過フィルター。A filtration filter characterized by being made by adding glass frit to zinc oxide whiskers having a structure branched in two or more directions and firing the mixture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2310488A JPH07110326B2 (en) | 1988-02-02 | 1988-02-02 | ▲ Ro ▼ over filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2310488A JPH07110326B2 (en) | 1988-02-02 | 1988-02-02 | ▲ Ro ▼ over filter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01199618A true JPH01199618A (en) | 1989-08-11 |
JPH07110326B2 JPH07110326B2 (en) | 1995-11-29 |
Family
ID=12101155
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2310488A Expired - Lifetime JPH07110326B2 (en) | 1988-02-02 | 1988-02-02 | ▲ Ro ▼ over filter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07110326B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1318125A3 (en) * | 2001-12-07 | 2003-10-01 | Ngk Insulators, Ltd. | Ceramic porous body and method of manufacturing glass usable as binder therefor |
-
1988
- 1988-02-02 JP JP2310488A patent/JPH07110326B2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1318125A3 (en) * | 2001-12-07 | 2003-10-01 | Ngk Insulators, Ltd. | Ceramic porous body and method of manufacturing glass usable as binder therefor |
US7053016B2 (en) | 2001-12-07 | 2006-05-30 | Ngk Insulators, Ltd. | Ceramic porous body and method of manufacturing glass usable as binder therefor |
Also Published As
Publication number | Publication date |
---|---|
JPH07110326B2 (en) | 1995-11-29 |
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