JPS59228917A - Filter medium - Google Patents

Filter medium

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Publication number
JPS59228917A
JPS59228917A JP10166683A JP10166683A JPS59228917A JP S59228917 A JPS59228917 A JP S59228917A JP 10166683 A JP10166683 A JP 10166683A JP 10166683 A JP10166683 A JP 10166683A JP S59228917 A JPS59228917 A JP S59228917A
Authority
JP
Japan
Prior art keywords
mos
filtration
filter
comparative example
liquid
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
Application number
JP10166683A
Other languages
Japanese (ja)
Other versions
JPH0148045B2 (en
Inventor
Takayuki Kimura
隆幸 木村
Yukimasa Ito
伊藤 幸勝
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ube Corp
Original Assignee
Ube Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP10166683A priority Critical patent/JPS59228917A/en
Publication of JPS59228917A publication Critical patent/JPS59228917A/en
Publication of JPH0148045B2 publication Critical patent/JPH0148045B2/ja
Granted legal-status Critical Current

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  • Filtering Materials (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

PURPOSE:To obtain the filtrate with high clarity in a short time by using fibrous magnesium oxysulfate as a filter medium. CONSTITUTION:The fibrous magnesium oxysulfate (MOS) is a synthetic inorganic compd. expressed as MgSO4.5MgO.8H2O or MgSO4.5Mg(OH)2.3H2O. The MOS, having 2.0-2.5 true sp.gr., 5-100mum fiber length, and 0.1-2mum fiber diameter, is a highly voluminous fibrous substance, and assumes the needle crystal structure as the general form. The medium is used solely or in combination with well-known filter mediums or filter aids. In the combined use, >=1wt% is prefferably added. The MOS can be molded with resins, etc. and used.

Description

【発明の詳細な説明】 本発明は液体の濾過材料に関する。さらに詳しくは本発
明は液体の清澄濾過の性能向上と濾過速度の促進を計る
ため、繊維状マグネシウムオキシサルフェート(以下M
O8と略記する。)を含む濾過材料に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to liquid filtration materials. More specifically, the present invention uses fibrous magnesium oxysulfate (hereinafter M
It is abbreviated as O8. ).

従来から化学工業の製造工程において枦剤及び濾過助剤
(併せて濾過材料と言う。)として繊維状あるいは粒状
の無機質天然品である石綿、珪藻土。
Asbestos and diatomaceous earth, which are fibrous or granular inorganic natural products, have traditionally been used as resiliency agents and filter aids (together referred to as filtration materials) in the manufacturing process of the chemical industry.

酸性白土、膠質土、陶土、沸石などが、また有機質天然
品である無煙炭、木炭粉末、パルプなどが。
Acid clay, colloidal clay, china clay, zeolite, etc., as well as organic natural products such as anthracite, charcoal powder, and pulp.

また合成品であるアルミナゲル、珪藻ゲル、金属酸化物
ゲル、ガラス繊維などが用いられている。さらに高い清
澄度が要求される食品、医薬、農薬。
Synthetic products such as alumina gel, diatom gel, metal oxide gel, and glass fiber are also used. Foods, pharmaceuticals, and agricultural chemicals that require even higher levels of clarity.

化粧品分野ではメンブランフィルタ−1金属焼結゛フイ
ルター、セラミックフィルターなどが用いられてきた。
In the cosmetics field, membrane filter-1 metal sintered filters, ceramic filters, etc. have been used.

しかしながら、上述の公知の濾過材料を用いてもなお被
濾過液によっては清澄性能が不充分であったり、目詰シ
を起し、長い濾過時間を要する欠点があった。また濾過
助剤と高性能フィルターとを併用して濾過速度の向上を
計っているが不充分であった。
However, even when the above-mentioned known filtration materials are used, there are still disadvantages in that the clarification performance is insufficient depending on the liquid to be filtered, clogging occurs, and a long filtration time is required. In addition, attempts have been made to improve the filtration rate by using a filter aid and a high-performance filter, but this has not been sufficient.

本発明は高い清澄度を短時間に得るべく9種々検討を加
えた結果、濾過材料としてMOSを用いることによシ、
従来の濾過材料の持つ機能をはるかに超えた濾過機能を
発揮することができることを見出し2本発明を完成する
に至った。
As a result of nine various studies in order to obtain high clarity in a short time, the present invention has been developed by using MOS as a filter material.
The present invention was completed based on the discovery that the present invention can exhibit a filtration function that far exceeds that of conventional filtration materials.

すなわち2本発明は繊維状マグネシウムオキシサルフェ
ートを含むことを特徴とする濾過材料に関するものであ
る。
That is, the present invention relates to a filtration material characterized by containing fibrous magnesium oxysulfate.

本発明で用いる。MOSはMPS04・5M20・8H
20またはMP8045MIF(OH)2・3H20”
?’表わされる合成無機化合物であ−る。このMOSは
例えば酸化マグネシラム、あるいは水酸化マグネシウム
を硫酸マグネシウム水溶液中に分散させて、加熱反応さ
せる方法、または水酸化マグネシウムを硫酸溶液中に分
散させて加熱反応させる方法により、製造することがで
きる(特開昭56−149318号公報参照)。
Used in the present invention. MOS is MPS04/5M20/8H
20 or MP8045MIF(OH)2・3H20”
? It is a synthetic inorganic compound represented by '. This MOS can be produced, for example, by dispersing magnesium oxide or magnesium hydroxide in an aqueous magnesium sulfate solution and subjecting it to a heating reaction, or by dispersing magnesium hydroxide in a sulfuric acid solution and subjecting it to a heating reaction ( (See Japanese Unexamined Patent Publication No. 149318/1983).

MOSの一般的形態は真比重2.0〜2.5長さく繊維
長)5〜100μm、直径(繊維径)0.1〜2μm、
嵩比重0.05〜0.2を有する極めて嵩高い針状結晶
構造の繊維状物質と表現できる。
The general form of MOS is true specific gravity 2.0 to 2.5, fiber length) 5 to 100 μm, diameter (fiber diameter) 0.1 to 2 μm,
It can be described as an extremely bulky fibrous material with an acicular crystal structure having a bulk specific gravity of 0.05 to 0.2.

MOSは単独使用または公知の濾過材料やp過動剤と併
用することが可能である。公知の濾過材料には1重量係
以上、好ましくは30重量係以上。
MOS can be used alone or in combination with known filtration materials and p-transactive agents. Known filtration materials have a weight factor of 1 or more, preferably 30 or more.

さらには50重量係以上併用することもできる。Furthermore, it is also possible to use a weight factor of 50 or more.

また2本発明に用いるMOSまたはMOSを含む濾過材
料は乾燥状であっても液体で濡れた状態であっても良い
が濡れた状態がより好ましい。
Further, the MOS or the filtration material containing MOS used in the present invention may be in a dry state or in a wet state with a liquid, but a wet state is more preferable.

本発明におけるMOSまたはMOSを含む濾過材料の利
用方法はプリコート法、ボディーフィード法いずれでも
良く、さらに両方法の併用によシ濾過機能がさらに向上
する。さらにMOSまたはMOSを含む濾過材料を樹脂
、その他の材料を用い、成形してフィルターを作成し用
いることができる。
The MOS or the filtration material containing MOS in the present invention may be used by either a precoat method or a body feed method, and the filtration function is further improved by a combination of both methods. Furthermore, a filter can be created and used by molding MOS or a filtration material containing MOS using resin or other materials.

次に本発明を実施例により具体的に説明する。Next, the present invention will be specifically explained using examples.

参考例(MOSの製造例) 硫酸マグネシウム・7水和物9 Kgを水120Aに溶
解し、この溶液に水酸化マグネシウム2]25にダ、お
よび種晶となるMOS0.4Kfを分散させた。
Reference Example (Manufacturing Example of MOS) 9 kg of magnesium sulfate heptahydrate was dissolved in 120 A of water, and in this solution were dispersed magnesium hydroxide 2]25 and 0.4 Kf of MOS as a seed crystal.

この分散液を内容積1707のオートクレーブに入れ、
170°Cで3時間反応させた。生成した沈澱を取り出
し、水洗を行った後に160’cで乾燥させてMOEI
を得た。このようにして得られたMOSを用いて以下の
実験を行った。
This dispersion was put into an autoclave with an internal volume of 1707,
The reaction was carried out at 170°C for 3 hours. The generated precipitate was taken out, washed with water, dried at 160'C, and MOEI
I got it. The following experiment was conducted using the MOS thus obtained.

なお、濾過方法は次のようである。The filtration method is as follows.

プリコート法;あらかじめ濾過材料を被濾過液に用いら
れている分散媒などにょシ分散させ、P布やガラス多孔
板などのF床に固着させた後、濾過を行う方法。
Pre-coating method: A method in which the filtration material is dispersed in advance in a dispersion medium used for the liquid to be filtered, and is fixed on a F bed such as P cloth or a perforated glass plate, followed by filtration.

ボディーフィード法;濾過材料を被濾過液中に適量分散
させた分散液を、P布やガラス多孔板などのP床に供給
して濾過する方法。
Body feed method: A method in which a dispersion liquid in which an appropriate amount of filtration material is dispersed in a liquid to be filtered is supplied to a P bed such as P cloth or a glass porous plate for filtration.

実施例1 前述の方法で製造したMOS2.Ofをトルエン200
m/中で超音波分散させた。このMO8分散液を直径3
0解のガラスフィルター(Gi ・孔径100〜150
μm)に注ぎ、減圧下トルエンを除去しあらかじめトル
エンを含浸させたMO8P’床を形成した。
Example 1 MOS2 manufactured by the method described above. Of toluene 200
Ultrasonic dispersion was carried out in m/m. This MO8 dispersion was
0 solution glass filter (Gi, pore size 100-150
The toluene was removed under reduced pressure to form a MO8P' bed previously impregnated with toluene.

清澄用試料として粒径0.025〜0.o4μmジオキ
サジン顔料商標名:(sumitone East V
ioletRLi住友化学■製) 0.59をトルエン
100罰中で超音波分散させた。この0,5 wt% 
ジオキサジン分散トルエンを用いてプリコートしたMO
Sの濾過性能の試験を行った。濾過は真空ポンプを用い
て12mHf一定の減圧下で行い、濾過時間およびF液
の吸光度(最大吸収波長、600■で測定)を純トルエ
ンを対称にして測定した。結果を第1表に示した。
As a sample for clarification, the particle size is 0.025-0. o4μm dioxazine pigment Trade name: (sumitone East V
ioletRLi (manufactured by Sumitomo Chemical ■) 0.59 was ultrasonically dispersed in toluene 100%. This 0,5 wt%
MO precoated with dioxazine dispersed toluene
A test was conducted on the filtration performance of S. Filtration was carried out under a constant reduced pressure of 12 mHf using a vacuum pump, and the filtration time and the absorbance (measured at maximum absorption wavelength, 600 cm) of liquid F were measured using pure toluene as a symmetry. The results are shown in Table 1.

実施例2 実施例1と同様の方法でプリコートし、  MOSのF
床を形成し+  0.5wt%ジオキサジン分散液を調
整した。さらにこの分散液にMOS0.59を加えて実
施例1と同様に濾過を行い、濾過に要する時間とP液の
透過率を測定した。結果を第1表に示した。
Example 2 Pre-coated in the same manner as in Example 1, and
A bed was formed and a +0.5 wt% dioxazine dispersion was prepared. Further, MOS 0.59 was added to this dispersion liquid, and filtration was performed in the same manner as in Example 1, and the time required for filtration and the transmittance of the P liquid were measured. The results are shown in Table 1.

比較例1〜5 実施例1におけるMOSの替りに珪藻±(比較例1)、
活性アルミナ(比較例2)、粉砕パルプ(比較例6)、
活性炭(比較例4)をプリコートしたもの、また、グリ
コーートシたMOSの替りに孔径0.1岡のメンブラン
フィルタ−(比較例5)を用いた。他の条件は実施例1
と全く同様にして減圧沖過を行い、濾過速度、およびF
液の透過率(600■)を測定した。結果を第1表に示
した。
Comparative Examples 1 to 5 Diatom ± (Comparative Example 1) instead of MOS in Example 1,
Activated alumina (Comparative Example 2), crushed pulp (Comparative Example 6),
A membrane filter pre-coated with activated carbon (Comparative Example 4) and a membrane filter with a pore size of 0.1 mm (Comparative Example 5) were used in place of the glycated MOS. Other conditions are Example 1
Perform vacuum filtration in exactly the same manner as above to determine the filtration rate and F
The transmittance (600 .mu.) of the liquid was measured. The results are shown in Table 1.

比較例6 実施例1におけるプリコートしたMOSの濾過床の替り
に孔径0.1μmのメンブランフィルタ−を用い、実施
例1と同様に0.5 wtチジオキサジン分散トルエン
を調製した。さらに濾過助剤として珪藻±0.5 fを
0.5 wt%ジオキサジン分散トルエンに加えた後、
減圧濾過を行って濾過時間および涙液の透過率(600
m)を測定した。結果を第1表に示した。
Comparative Example 6 0.5 wt thidioxazine-dispersed toluene was prepared in the same manner as in Example 1, using a membrane filter with a pore size of 0.1 μm instead of the precoated MOS filter bed in Example 1. Furthermore, after adding diatom ±0.5 f as a filter aid to 0.5 wt% dioxazine-dispersed toluene,
Perform vacuum filtration to determine filtration time and tear fluid permeability (600
m) was measured. The results are shown in Table 1.

比較例7 実施例1におけるプリコートしたMOSの濾過床の替シ
に活性炭をプリコートし、実施例1と同様K O,5w
t%ジオキサジン分散トルエンを調製し。
Comparative Example 7 A replacement for the pre-coated MOS filter bed in Example 1 was pre-coated with activated carbon, and the same K O,5w as in Example 1 was applied.
Prepare t% dioxazine-dispersed toluene.

さらにこの分散液に活性炭0.52を加えて分散させ、
減圧濾過を行って濾過速度およびテ液の透過率(600
mm)を測定した。結果を第1表に示した。
Furthermore, 0.52% of activated carbon was added to this dispersion and dispersed.
Perform vacuum filtration to determine the filtration rate and permeability of the solution (600
mm) was measured. The results are shown in Table 1.

以上の実験結果から、  MOSは他の公知の濾過材料
であるメンブランフィルタ−(多孔質フィルム)。
From the above experimental results, MOS is a membrane filter (porous film) that is another known filtration material.

珪藻土、アルミナゲル、パルプに比べて濾過効率(濾過
速度)および清澄度(透過率)ともに非常に優れている
ことが明らかである。また、ボディーフィード法を′併
せて利用することにより濾過機能がさらに向上する。
It is clear that both filtration efficiency (filtration rate) and clarity (transmittance) are very superior compared to diatomaceous earth, alumina gel, and pulp. In addition, the filtration function can be further improved by using the body feed method in combination.

実施例6 実施例1における0、5 wt%ジオキサジン顔料分散
トルエンの替りに平均粒径7mμmアエロジル〔≠38
02日本アエロジル■製〕を用い、その他の条件は実施
例1と全く同様に行った。濾過時間、およびF液の清澄
度(白色光による透過度)を測定した。結果を第2表に
示した。
Example 6 In place of the 0.5 wt% dioxazine pigment-dispersed toluene in Example 1, Aerosil with an average particle size of 7 mμm [≠38
02 (manufactured by Nippon Aerosil ■)], and the other conditions were exactly the same as in Example 1. The filtration time and the clarity (transmittance by white light) of the F solution were measured. The results are shown in Table 2.

比較例8〜11 実施例乙におけるプリコートしたMOI9の替りに珪藻
土(比較例8)、活性アルミナ(比較例9)、粉砕パル
プ(比較例1o)をプリコートしたもの、および孔径0
.1μmのメンブランフィルタ−(比較例11)を用い
た。他の条件は実施例1と全く同様にして減圧濾過を行
い、濾過速度およびE液の透過度(白色光)を測定した
Comparative Examples 8 to 11 Pre-coated with diatomaceous earth (Comparative Example 8), activated alumina (Comparative Example 9), and crushed pulp (Comparative Example 1o) instead of pre-coated MOI 9 in Example B, and pore size 0
.. A 1 μm membrane filter (Comparative Example 11) was used. Vacuum filtration was performed under exactly the same conditions as in Example 1, and the filtration rate and the transmittance of liquid E (white light) were measured.

結果を第2表に示した。The results are shown in Table 2.

実施例4 実施例1における0、5wt%ンオキサジン顔料分散ト
ルエンの替りに0.5wt96キナクリドン顔料(0,
1〜0.6μ展分散水を用い、実施例1と同様にプリコ
ートしたMO8F床を用いて濾過試験を行った。濾過速
度およびF液の透過度(白色光)を測定して濾過機能の
評価を行った。結果を第2表に示した。
Example 4 0.5wt96 quinacridone pigment (0.5wt%) instead of toluene dispersed with 0.5wt%
A filtration test was conducted using a MO8F bed precoated in the same manner as in Example 1 using 1 to 0.6 μm of dispersion water. The filtration rate and the permeability (white light) of liquid F were measured to evaluate the filtration function. The results are shown in Table 2.

比較例12〜14 実施例4におけるMOSの替シに珪藻土(比較例12)
、活性アルミナ(比較例13)、粉砕パルプ(比較例1
4)をプリコートして0.5 wt%キナクリドン顔料
分散水を用いた。実施例1と全く同様に減圧沖過し、濾
過速度、およびp液の透過度を測定した。結果を第2表
に示した。
Comparative Examples 12 to 14 Diatomaceous earth was used to replace the MOS in Example 4 (Comparative Example 12)
, activated alumina (Comparative Example 13), crushed pulp (Comparative Example 1)
4) was precoated and 0.5 wt% quinacridone pigment dispersion water was used. It was filtered under reduced pressure in exactly the same manner as in Example 1, and the filtration rate and p-liquid permeability were measured. The results are shown in Table 2.

以上の結果から明らかなどと(、MOSは液体の清澄濾
過用の濾過材料として従来の濾過材料の持つ性能をはる
かに超えた濾過機能を発揮する。
It is clear from the above results that MOS exhibits a filtration function that far exceeds that of conventional filtration materials as a filtration material for clarifying and filtrating liquids.

Claims (1)

【特許請求の範囲】[Claims] 繊維状マグネシウムオキシサルフェートを含むことを特
徴とする濾過材料。
A filtration material comprising fibrous magnesium oxysulfate.
JP10166683A 1983-06-09 1983-06-09 Filter medium Granted JPS59228917A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10166683A JPS59228917A (en) 1983-06-09 1983-06-09 Filter medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10166683A JPS59228917A (en) 1983-06-09 1983-06-09 Filter medium

Publications (2)

Publication Number Publication Date
JPS59228917A true JPS59228917A (en) 1984-12-22
JPH0148045B2 JPH0148045B2 (en) 1989-10-17

Family

ID=14306691

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10166683A Granted JPS59228917A (en) 1983-06-09 1983-06-09 Filter medium

Country Status (1)

Country Link
JP (1) JPS59228917A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2219801B (en) * 1988-06-03 1992-01-02 Ube Industries "antiblocking transparent plastics film"

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2437044C3 (en) * 1974-08-01 1983-04-14 Chemische Werke Hüls AG, 4370 Marl Process for the preparation of polymers and copolymers of vinyl chloride by suspension polymerization

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2219801B (en) * 1988-06-03 1992-01-02 Ube Industries "antiblocking transparent plastics film"

Also Published As

Publication number Publication date
JPH0148045B2 (en) 1989-10-17

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