JPS60122020A - Filter and its preparation - Google Patents

Filter and its preparation

Info

Publication number
JPS60122020A
JPS60122020A JP22701783A JP22701783A JPS60122020A JP S60122020 A JPS60122020 A JP S60122020A JP 22701783 A JP22701783 A JP 22701783A JP 22701783 A JP22701783 A JP 22701783A JP S60122020 A JPS60122020 A JP S60122020A
Authority
JP
Japan
Prior art keywords
water
fibers
filter
powder
fiber
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
JP22701783A
Other languages
Japanese (ja)
Other versions
JPH0450846B2 (en
Inventor
Takao Katsuragi
桂木 隆夫
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP22701783A priority Critical patent/JPS60122020A/en
Publication of JPS60122020A publication Critical patent/JPS60122020A/en
Publication of JPH0450846B2 publication Critical patent/JPH0450846B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/16Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • B01D39/1607Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
    • B01D39/1623Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/0208Separation of non-miscible liquids by sedimentation
    • B01D17/0214Separation of non-miscible liquids by sedimentation with removal of one of the phases

Abstract

PURPOSE:To capture oil component dispersed in water effectively by sticking oil adsorptive powder which has been finished previously to have hydrophobic or water repelling property to the surface of fiber for forming felt. CONSTITUTION:The filter consists of a fiber layer constituted of fibers 20 covered on its whole surface with powder 19 of oil adsorptive additive. Large amt. of fine space 21 is formed in the fiber layer. The powder 19 consists of powder of cristobalite, zeolite, or active carbon, which has been previously finished to have hydrophobicity. The fiber 20 consists essentially of vegetable fibers such as linter or wood pulp, etc. and if necessary, of animal fibers or synthetic resin fibers. 2-4 times weight of the hydrophobic adsorbent powder basing on the own weight of the fiber is deposited on the surface of the fiber.

Description

【発明の詳細な説明】 本発明は、主として水中に分散する油性分を有効に除去
するフェノと層状のフィルターとその製造方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a phenol-layered filter that effectively removes oily components mainly dispersed in water, and a method for manufacturing the same.

従来、フェルト状フィルターの毛細管現象を利用して、
水面に層状に浮遊した油稚分を吸引するタイプのフィル
ターが用いられているが、油性分のみを分離吸引させる
ことは出来ず水分の吸引が避けられなかった。また従来
のフィルターでは、水中にエマルジョン化して浮遊する
油性分の除去は不可能であった。
Conventionally, using the capillary action of a felt filter,
A type of filter is used that sucks out the oily particles floating in a layer on the water surface, but it is not possible to separate and suction only the oily particles, and the suction of water is unavoidable. Furthermore, with conventional filters, it has been impossible to remove oily substances that emulsify and float in water.

本発明は、以上の点に鑑みてなしたもので、水中に分散
する油性分でも、水とは分離して有効に捕促し得るフィ
ルターとその製造方法を提供することを目的とするもの
である。
The present invention has been made in view of the above points, and an object of the present invention is to provide a filter that can effectively capture even oily components dispersed in water while separating them from water, and a method for manufacturing the filter. .

すなわち、本発明に係るフィルターは、繊維がフェルト
状に形成されたフィルターにおいて、該フィルターを形
成する繊維の表面には、予じめ疎水若しくは撥水加工が
施こされた油吸着性の粉末が付着されて寿ることを特徴
としている。
That is, the filter according to the present invention is a filter in which fibers are formed in a felt shape, and the surface of the fibers forming the filter is coated with an oil-absorbing powder that has been previously treated with a hydrophobic or water-repellent finish. It is characterized by being attached to it for a long time.

また、本発明に係るフィルターの製造方法は、予じめ疎
水若しくは撥水加工が施こされた油吸着性の粉末が表面
に添着された繊維を水中に懸濁せしめ、該懸濁液中に高
圧の空気飽和水を放出する事によって発生するマイクロ
気泡を前記繊維の周縁に耐着せしめて該繊維を浮上させ
ることにょシ多量の微細空間を含む繊維層を水面上に形
成せしめ、該繊維層を脱水、乾燥ぜしめてなることを特
徴としている。
In addition, the method for producing a filter according to the present invention involves suspending fibers on the surface of which oil-absorbing powder, which has been previously treated with hydrophobic or water-repellent treatment, is suspended in water. Microbubbles generated by releasing high-pressure air-saturated water are made to adhere to the periphery of the fibers, causing the fibers to float, forming a fiber layer containing a large amount of microscopic spaces on the water surface, and forming a fiber layer containing a large amount of microscopic spaces on the water surface. It is characterized by being completely dehydrated and dried.

次に、本発明を図の実施例によって説明する。Next, the present invention will be explained by means of illustrated embodiments.

第1図は、本発明に係るフィルターの製造方法を実施す
る装置の1例を示す系統図であり、これにより製造方法
を説明する。
FIG. 1 is a system diagram showing an example of an apparatus for carrying out the filter manufacturing method according to the present invention, and the manufacturing method will be explained using this diagram.

パルプ槽1にリンター(綿くず)又は木材・ぐルデの4
%液を作り、薬液槽2にメラミン樹脂の0.1 %液を
作シ、粉末槽3に予め疎水加工をした200メツシユの
クリストバール粉末の4チ液を作り、このろ液を10:
3:10の割合で原料槽4に於て混合して原料液(A液
)を作る。他方連続加圧水母5にはコンプレッサー6に
よって3 kg/ o1以上に加圧された空気飽和水(
B液)を作り、且つ薬液槽7には高分子凝集剤例えばポ
リエチレンオキサイドの10,000倍稀釈液(C液)
を作り、このろ液をA液10.、B液3、c液0.1の
割合で混合浮上槽8の底辺に連続的に放出する。この放
出によってA液中に懸濁浮遊するクリストバール粉末は
C液の媒介によって速かに繊維の表面と添着結合して液
中の浮遊粉末はなくなり、同時にB液が発生する無数の
マイクロ気泡は繊維の周縁に耐着し、その浮力によって
浮上する繊維は大量の気泡を含んだ繊維層9を形成する
4 of linter (cotton waste) or wood/gurude in pulp tank 1
Prepare a 0.1% solution of melamine resin in chemical solution tank 2, make a 4% solution of 200 mesh Cristobal powder that has been hydrophobically treated in advance in powder tank 3, and add this filtrate to 10% solution.
A raw material liquid (liquid A) is prepared by mixing in a raw material tank 4 at a ratio of 3:10. On the other hand, the continuous pressurized water tank 5 contains air-saturated water (pressured to 3 kg/o1 or more by a compressor 6).
A 10,000-fold diluted solution of a polymer flocculant such as polyethylene oxide (solution C) is prepared in the chemical tank 7.
Make this filtrate and make 10. solution A. , B liquid is 3, and C liquid is 0.1 at a ratio of 0.1 to 1. As a result of this release, the Cristobal powder suspended in liquid A quickly attaches to the surface of the fibers through the medium of liquid C, and the suspended powder in the liquid disappears, and at the same time, the countless microbubbles generated in liquid B disappear. The fibers that adhere to the periphery of the fibers and float due to their buoyancy form a fiber layer 9 containing a large amount of air bubbles.

水面に形成された繊維層9は次々に下方が浮上してくる
繊維の圧力をうけて混合槽8の出口1゜から溢流して、
運動する網状のコンベヤー11の上に移動し、移動しな
がらサクションボックス12によって真空脱水された後
乾燥機13で乾燥されて製品フィルター14となる。
The fiber layer 9 formed on the water surface is overflowed from the outlet 1° of the mixing tank 8 under the pressure of the fibers that are rising one after another.
The filter is moved onto a moving mesh conveyor 11, vacuum-dehydrated in a suction box 12 while moving, and then dried in a drier 13 to become a product filter 14.

浮上槽8内で浮上する繊維は斜面板15及びそれに対向
する内壁に沿って上昇し、凝集する繊維を分離した残余
の、水は斜面板15の間隙を通って斜下方に移動し、遂
次槽内底辺の排出口16から流出してクッションタンク
17に一旦貯溜される。
The fibers floating in the flotation tank 8 rise along the slope plate 15 and the inner wall facing it, and the remaining water after separating the coagulated fibers passes through the gap in the slope plate 15 and moves obliquely downward, and then It flows out from the outlet 16 at the bottom of the tank and is temporarily stored in the cushion tank 17.

又サクションボックス12によって脱水された水も集水
槽18に集めた後クッションタンク17に流入する。こ
のクッションタンク17に回収すれた水は再び、A液、
B液、C成用の水とじて再使用する事が可能である。
Further, water dehydrated by the suction box 12 is also collected in a water collecting tank 18 and then flows into a cushion tank 17. The water collected in this cushion tank 17 is again used as liquid A,
It is possible to reuse the water for B and C compositions.

上記の方法においては、製造されるフィルターの主体と
なるフェルト繊維に添着せしめる活性炭、クリスバール
等の添着物に予め疎水性加工を施し、それによって、そ
れらが水を吸着する事なく、専ら選択的に例へば油エマ
ルジヨン中の油成分のみを吸着する様な性質を附与する
ようにしている。
In the above method, the impregnants, such as activated carbon and Crisbar, which are impregnated with the felt fibers that form the main body of the filter to be manufactured, are subjected to hydrophobic treatment in advance, so that they do not adsorb water and only selectively absorb water. For example, it is imparted with the property of adsorbing only the oil component in the oil emulsion.

この様な疎水加工の方法は種々あるが、例えば一般的な
ものは、上記の添着物に疎水性シリコーン樹脂の1チ溶
液の等量を噴霧又は漬浸によって添加せしめた後、乾燥
し粉砕する方法である。
There are various methods for such hydrophobic finishing, but a common one is to add an equal amount of a 1-ti solution of hydrophobic silicone resin to the above impregnated material by spraying or dipping, then drying and pulverizing. It's a method.

第2図は、本発明に係るフィルターの拡大断面図である
FIG. 2 is an enlarged sectional view of a filter according to the present invention.

上述した方法及び装置によって製造されるこのフィルタ
ー14は、フィルターの本体は上記油吸着性添加物の粉
末19によって表面全体が被覆された繊維20によって
構成される繊維層であシ、且つその繊維層内に多量の微
細空間21が形成されている。しかして、上記の粉末1
9は、予じめ疎水処理を施しだクリスバール、ゼオライ
ト、活性炭等の粉末によって形成されている。また繊維
20は、主としてリンター又は木材パルプ等の植物性繊
維で構成され必要に応じて、動物性又は合成樹脂性の繊
維が用いられ、又は添加されている。
This filter 14 manufactured by the method and apparatus described above has a main body composed of a fibrous layer composed of fibers 20 whose entire surface is covered with the powder 19 of the oil-absorbing additive, and the fibrous layer A large amount of microscopic spaces 21 are formed inside. However, the above powder 1
9 is made of powder of Crisbar, zeolite, activated carbon, etc., which has been subjected to hydrophobic treatment in advance. The fibers 20 are mainly composed of vegetable fibers such as linter or wood pulp, and animal or synthetic resin fibers are used or added as necessary.

・この様にして作られたフィルターの繊維は自重の2〜
4倍の疎水性吸着剤の粉末をその表面に添着する事が出
来る。この事はフィルターの全重量の65〜80チが微
粉末の吸着剤の繊維状のからみ合いによって構成される
小を意味する事であり、これによって一方では良好な通
水性を持ち、一方では極めて高い油エマルジヨンの吸着
性能をもつフィルターを作る事を可能にしたものである
・The fibers of the filter made in this way weigh 2~
Four times more hydrophobic adsorbent powder can be attached to its surface. This means that 65 to 80 inches of the total weight of the filter is composed of a fibrous intertwining of finely powdered adsorbent, which on the one hand has good water permeability and on the other hand is extremely This made it possible to create a filter with high oil emulsion adsorption performance.

次に、上記フィルターの特長を説明する。Next, the features of the above filter will be explained.

良好な透水(湧水)性能を有すること。Must have good water permeability (spring water) performance.

すなわち、本フィルターの主要構造は見せかけ比重0.
08程度の繊維層である。この繊維層は内部に極めて多
量の微細空間を形成しながら各繊維が緊密に接合し合っ
ているフェルト状の繊維層であって、その最も基本的な
性質は1.内部の空間が、植物繊維特有の枝状分岐のか
らみ合いによって複雑且つ緻密な構造をもっているにも
かかわらず、極めてすぐれた通気性と吸水性及通水性を
有する事である。即ち、吸水、保水性は自重の約15倍
の能力を有し、その通水性は厚さ20crn面積10c
rl水圧300kg/m”の場合1分間1500CC程
度である。この通水性は繊維がそれと同量の添加物を添
着している場合に於てもなお1分間700CC程度の通
水性能を示す。
In other words, the main structure of this filter has an apparent specific gravity of 0.
It is a fiber layer of about 08. This fiber layer is a felt-like fiber layer in which each fiber is closely joined to each other while forming an extremely large amount of microscopic spaces inside, and its most basic properties are 1. Although the internal space has a complex and dense structure due to the intertwining of branches peculiar to plant fibers, it has extremely excellent air permeability, water absorption and water permeability. In other words, it has the ability to absorb and retain water about 15 times its own weight, and its water permeability is 20 crn in thickness and 10 cm in area.
When the rl water pressure is 300 kg/m'', the water permeability is about 1500 cc per minute. Even when the fiber is impregnated with the same amount of additives, it still shows a water permeability of about 700 cc per minute.

油のエマルジョン吸着性が良好であること。一般に吸着
剤の性能は第1次的にはその個有の性質と内包する空間
の表面積の大きさに由来するものであるが、第2次的に
は実際に通過する空気又は水の流れと直接に接触してい
るその表面積の大きさによって大きく影響されるもので
ある。
Good emulsion adsorption of oil. In general, the performance of an adsorbent primarily comes from its unique properties and the surface area of the space it contains, but secondarily it depends on the flow of air or water that actually passes through it. It is greatly influenced by the size of the surface area with which it is in direct contact.

従ってこれらの吸着剤を極力小さな粒度で使用する事は
その吸着性能を充分発揮せしむる上から最も望ましい事
であるにもかかわらず、多くの場合粗い粒度で使用する
事をよぎなくされているのは、微粉末にした場合にはそ
の通気性及通水性が著しく悪くなり、殊にクリスバール
の如く水中に於て粘土化するものは僅か数量の厚さでも
通水杜絶となる欠点がある為であった。
Therefore, although it is most desirable to use these adsorbents with a particle size as small as possible in order to fully demonstrate their adsorption performance, in many cases it is unavoidable to use them with a coarse particle size. The reason is that when it is made into a fine powder, its air permeability and water permeability become extremely poor, and especially those that turn into clay in water, such as Crisbar, have the disadvantage that even a small amount of thickness prevents water permeation. It was for a certain reason.

この為一般に添加物の粒度の細かさと良好な通水性とは
基本的に相反する性質であるとするのが従来の常識とな
っているのである。
For this reason, it has generally been conventional wisdom that the fine particle size of additives and good water permeability are fundamentally contradictory properties.

本フィルターの特長は、この常識に反し、添加物の粒度
は小さければ小さい程その通気性と通水性を良くする構
造上の特徴(第2図参照)を有し、従って、それによっ
て添加物の粒度を極限まで微細化する事によって、その
吸着能力を最高限度まで発揮せしむることを実際上可能
にした点にある。
Contrary to this common sense, the feature of this filter is that the smaller the particle size of the additive, the better its air permeability and water permeability (see Figure 2). By making the particle size as fine as possible, it is practically possible to maximize its adsorption capacity.

次に実施例を示す。Next, examples will be shown.

直径3crn長さ50>のカラムの下部2oL:1nに
クリスバール添着フィルター(リンター1に対し200
メツシユのクリスバール2の比率で添着せしめたもの)
25fを挿入し、カラムの上方から1.000 ppm
のA重油エマルヅヨンを入れて濾過した場合、濾過速度
毎分50CCに於て濾液の濃度15 ppm以下である
At the bottom of a column with a diameter of 3 crn and a length of 50 mm, a Crisbar filter (200 m
Attached at the ratio of Metsuyu's Crisbar 2)
Insert 25f and add 1.000 ppm from the top of the column.
When filtered with A heavy oil emulsion, the concentration of the filtrate is 15 ppm or less at a filtration rate of 50 CC/min.

以上説明したように、本発明に係るフィルターによれば
、水面あるいは水中の油性分を、水とは分離して捕捉さ
せることが出来、特に水中にエマルジョン比して分散さ
れる油性分の捕捉が可能となる。
As explained above, according to the filter of the present invention, oily components on the water surface or in water can be captured separately from water, and in particular, oily components dispersed in water can be captured more easily than in emulsions. It becomes possible.

また本発明の方法によれば、上記のようなフィルターを
効率良く製造することが出来る効果がある。
Further, according to the method of the present invention, there is an effect that the above-mentioned filter can be efficiently manufactured.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、本発明に係る方法の実施に使用する装置の系
統図、第2図は、本発明に係るフィルターの拡大断面図
である。 1・・・パルプ伯、2・・・薬液イー!h’ N 3・
・・粉末槽、4・・・原料槽(A液槽)、5・・・連続
加圧水母(B液槽)、7・・・薬液檜(C液槽)、8・
・・混合浮上槽、9・・・繊維R11,0・・・浮上槽
出口、11・・・ベルトコンベヤー、12・・・ザクジ
ョンボックス、13・・・乾燥袋R114・・・フィル
ター、15・・・斜面板、16・・・排出口、17・・
・クッションタンク、18川集中槽、A・・・原料液、
B・・・加圧飽和水、C・・・添加液、19・・・粉末
、20・・・繊維、21・・・繊維間空間。 特許出願人 桂 木 隆 夫 板 谷 康 男 代理人・弁理士 西 村 教 光 手 続 補 正 書 特許庁長官 志 賀 学 殿 1.1バ件の表示 昭和58年 特 許 願 第227017号2、発明の
名称 フィルターとその製造方法3、補正をする者 !バ件との関係 特許出願人 7、補正の対象 明細書 8、補正の内容 明 細 書 ■1発明の名称 フィルターとその製造方法 2、特許請求の範囲 (1)繊維がフェルト状に形成されたフィルターにおい
て、該フィルターを形成するmisの表面には、予じめ
疎水若しくは 水加工が施こされた油吸着性の粉末が附
着されてなることを特徴とするフィルター。 (2)予じめ疎水若しくは 水加工が施こされた油吸着
性の粉末を水中に懸濁する繊維の表面に吸着せしめ、該
懸濁液中に高圧の空気飽和水を放出する事によって発生
するマイクロ気泡を前記繊維の周縁に附着せしめで該繊
維を浮」ニさせることにより多量の微細空間を含む繊維
層を水面上に形成せしめ、該Ia維層を脱水、乾燥せし
めてなることを特徴とするフィルターの製造方法。 効に除去するフェルト状のフィルターとその製造方法に
関するものである。 従来のフィルターでは、水中にエマルジョン化して浮遊
する油性分の除去は不可能であった。 本発明は、以1−の点に鑑みてなしたもので、水中にエ
マルジョンとなって分散する油成分でも、水とは分離し
て有効に捕捉し得るフィルターとその製造方法を提供す
ることを目的とするものである。 すなわち、本発明に係るフィルターは、繊維がフェルト
状に形成されたフィルターにおいて、該フィルターを形
成する繊維の表面には、予じめ疎水若しくは撥水加工が
施こされた油吸着性の粉末が伺着されてなることを特徴
としている。 また、本発明に係るフィルターの製造方法は、rじめ疎
水若しくは撥水加工が施こされた油吸着性の粉末を水中
に懸濁する繊維の表面に添着せしめ、該懸濁液中に高圧
の空気飽和水を放出する事によって発生するマイクロ気
泡を前記繊維の周縁に防着゛せしめて該繊維を浮上させ
ることにより多量の微細空間を含む繊維層を水面上に形
成せしめ、該繊維層を脱水、乾燥せしめてなることを特
徴としている。 次に、本発明を図の実施例によって説明する。 第1図は1本発明に係るフィルターの製造方法を実施す
る装置の1例を示す系統図であり、これにより製造方法
を説明する。 パルプ槽1にリンター(綿くず)又は木材パルプの4%
液を作り、薬液槽2にメラミン樹脂の0.1%液を作り
、粉末槽3に予め疎水加工をした200メツシユのクリ
ストバール粉末の4%液を作り、この3液を10二3:
10の割合で原料槽4に於て混合して原料液(A液)を
作る。他方連続加圧水母5にはコンプレッサー6によっ
て3k g / c m’以上に加圧された空気飽和水
(B液)を作り、且つ薬液槽7には高分子凝集剤例えば
ポリエチレンオキサイドの10.000倍稀釈液(C液
)を作り、このろ液をA液1O1B液3、C液0.1 
(7)割合で混合浮上槽8の底辺に連続的に放出する。 この放出によってA液中に懸濁浮遊するグリストパール
粉末はC液の媒介によって速かに繊維の表面と添着結合
して液中の浮遊粉末はなくなり、同時にB液が発生する
無数のマイクロ気泡は繊維の周縁に耐着し、その浮力に
よって浮上する繊維は大隣の気泡を含んだm離層9を形
成する。 水面に形成された繊維層9は次々に下方が浮上してくる
繊維の圧力をうけて混合槽8の出口10から溢流して、
運動する網状のコンベヤー11のにに移動し、移動しな
がらサクションボックスL24こよって真空脱水された
後乾燥fi13で乾燥されて製品フィルター14となる
。 浮1―槽8内で浮」ニする繊維は斜面板15及びそれに
対向する内壁に沿ってLJ7L、凝集する繊維11した
残余の水は斜面板15の間隔を通って肩ド方に移動し、
逐次槽内底辺の排出口16から流出してクッションタン
ク17に一旦貯溜される。又サクションホックス12に
よって脱水された水も集水槽18に集めた後クッション
タンク17に流入する。このクッションタンク17に回
収された水はilfび、A液、B液、C法用の水として
再使用する事が可能である。 上記の方法においては、製造されるフィルターの主体と
なるフェルト繊維に添着せしめる活性炭、クリスバール
等の添着物に予め疎水性加工を施し、それによって、そ
れらが水を吸着する事なく、専ら選択的に例へば油エマ
ルジヨン中の油成分のみを吸着する様な性質を照写する
ようにしている。 この様な疎水加工の方法は種々あるが、例えば一般的な
ものは、上記の添着物に疎水性シリコーン樹脂の1%溶
液の等量を噴霧又は漬浸によって添加せしめた後、乾燥
し粉砕する方法である。 第2図は、本発明に係るフィルターの拡大断面図である
。 」二連した方法及び装置によって製造されるこのフィル
ター14は、フィルターの本体は」−配油吸着性添加物
の粉末19によって表面全体が被覆された繊維20によ
って構成される繊維層であり、且つその繊m層内に多量
の微細空間21が形成されている。しかして、上記の粉
末19は、予しめ疎水処理を施したクリスバール、ゼオ
ライト、活性炭等の粉末によって形成されている。また
繊維20は、主としてリンター又は木材パルプ等の植物
性繊維で構成され必要に応じて、動物性又は合成樹脂性
の繊維が用いられ、又は添加されて、いる。この様にし
て作られたフィルターの繊維は自車の2〜4倍の疎水性
吸着剤の粉末をその表面に添着する事が出来る。この事
はフィルターの全型;11の65〜80%が微粉末の吸
着剤の繊維状のからみ合いによって構成される事を意味
する車であり、これによって一方では良好な通水性を持
ち、一方では極めて高い油エマルジョンの吸着性能をも
つフィルターを作る水を可能にしたものである。 次に、1−記フイルターの特長を説明する。 良iifな透水(通水)性能を有すること。 すなわち、本フィルターの主要構造は見せかけ比重0.
08程度の繊維層である。この繊維層は内部に極めて多
を葭の微細空間を形成しながら各繊維が緊畜に接合し合
っているフェルト状の繊維層であって、その最も基本的
な性質は、内部の空間が。 植物繊維特有の枝状分岐のからみ合いによって複雑且つ
緻密な構造をもっているにもかかわらず、極めてすぐれ
た通気性と吸水性及通水性を有する市である。即ち、吸
水、保水性は自重の約15倍の能力を有し、その通水性
は厚さ20cm面積10cm’水圧300kg/m’の
場合1分間15QOcc程度である。この通水性はm維
がそれと同量の添加物を添着している場合に於てもなお
1分間700CC程度の通水性能を示す。 油のエマルジョン吸着性が良好であること。一般に吸着
剤の性能は第1次的にはそ−の個有の性質と内包する空
間の表面積の大きさに由来するものであるが、第2次的
には実際に通過する空気又は水の流れと直接に接触して
いるその表面積の大きさによって大きく影響されるもの
である。 従ってこれらの吸着剤を極力小さな粒度で使用する事は
その吸着性能を充分発揮せしむる上から最も望ましい事
であるにもかかわらず、多くの場合粗い粒度で使用する
事をよぎなくされているのは、微粉末にした場合にはそ
の通気性及通水性が勇しく悪くなり、殊にクリスバール
の如く水中に於て粘土化するものは僅か数ll1ffl
の厚さでも通水壮絶となる欠点がある為であった。 この為一般に添加物の粒度の細かさと良好な通水性とは
基本的に相反する性質であるとするのが従来の常識とな
っているのである。 本フィルターの特長は、この常識に反し、添加物の粒度
は小さければ小さい程その通気性と通水に1を良くする
構造−にの特徴(第2図参照)を有し、従って、それに
よって添加物の粒度を極限まで微細化する・ISによっ
て、その吸着能力を最高限度まで発揮せしむることを実
際上n1能にした点にある。 次に実施例を示す。 1白f’f:3cm長さ50cI11のカラムの下部2
0cmにクリスバール添r1フィルター(リンターlに
対し200メンシユのクリスバール2の比率でg着−t
tしめたもの)25gを挿入し、カラ11の上方から1
.000 ppmのA 重油エマルジョンを入れて一過
した場合、龜過速度毎分50ccに於て濾液の濃度15
ppm以下である。 以上説明したように、本発明に係るフィルターによれば
、特に水中にエマルジョン化しテ分netされる油性分
の捕捉が可能となる。 また本発明の方法によれば、」二記のようなフィルター
を効率良く製造することが出来る効果がある。 4、図面の簡単な説明 第1図は、本発明に係る方法の実施に使用する装置の系
統図、第2図は、本発明に係るフィルターの拡大断面図
である。 ■・・・パルプ槽、2・・・薬液槽、3・・・粉末槽、
4・・・原料槽(A液槽)、5・・・i!I!続加圧水
缶(水母槽)、7・・・薬液槽(C液槽)、8・・・混
合浮上槽、9・・・繊帷槽、lO・・・浮J二’rfl
 出D、11・・・ヘルI・コンベヤー、12・・・サ
クションボックス、13・・・乾燥装置、14・・・フ
ィルター、15・・・斜面板、16・・・排出口、17
・・・クッションタンク、18・・・集中槽、A・・・
原料液、B・・・加圧飽和水、C・・・添加液、l9・
・・粉末、20・・・繊維、21・・・繊維間空間。 特許出願人 桂木隆 夫 板 谷 康 男 代理人・弁理士 西 村 教 光
FIG. 1 is a system diagram of an apparatus used to carry out the method according to the invention, and FIG. 2 is an enlarged sectional view of a filter according to the invention. 1...Pulp Haku, 2...Medicine E! h' N 3・
... Powder tank, 4... Raw material tank (A liquid tank), 5... Continuously pressurized water mother (B liquid tank), 7... Chemical solution cypress (C liquid tank), 8.
...Mixing flotation tank, 9...Fiber R11,0...Flotation tank outlet, 11...Belt conveyor, 12...Zakujo box, 13...Drying bag R114...Filter, 15. ...Slope plate, 16...Discharge port, 17...
・Cushion tank, 18 river concentration tank, A...raw material liquid,
B... Pressurized saturated water, C... Additive liquid, 19... Powder, 20... Fiber, 21... Interfiber space. Patent Applicant Takashi Katsuragi Yasushi Ita Yasushi Tani Agent/Patent Attorney Norihiro Nishimura Procedural Amendments Director General of the Patent Office Manabu Shiga 1.1 Indication of Patent Application No. 227017 1982 2. Title of the invention Filter and its manufacturing method 3, person who corrects it! Relationship with the case Patent applicant 7, Specification subject to amendment 8, Specification of contents of amendment ■1 Name of the invention Filter and its manufacturing method 2, Claims (1) Fibers are formed into a felt shape A filter characterized in that an oil-absorbing powder that has been previously subjected to hydrophobic or water treatment is attached to the surface of the mis that forms the filter. (2) Generated by adsorbing oil-absorbing powder that has been previously hydrophobically or water-treated onto the surface of fibers suspended in water, and releasing high-pressure air-saturated water into the suspension. A fiber layer containing a large amount of microscopic spaces is formed on the water surface by attaching microbubbles to the periphery of the fibers to make the fibers float, and the Ia fiber layer is dehydrated and dried. A method for manufacturing a filter. The present invention relates to a felt-like filter that effectively removes water and a method for manufacturing the same. Conventional filters have been unable to remove oily substances that emulsify and float in water. The present invention has been made in view of the above point 1-, and it is an object of the present invention to provide a filter that can effectively capture oil components that are dispersed as an emulsion in water, separated from water, and a method for producing the same. This is the purpose. That is, the filter according to the present invention is a filter in which fibers are formed in a felt shape, and the surface of the fibers forming the filter is coated with an oil-absorbing powder that has been previously treated with a hydrophobic or water-repellent finish. It is characterized by being visited. In addition, the method for producing a filter according to the present invention involves applying oil-absorbing powder that has been subjected to hydrophobic or water-repellent finishing to the surface of fibers suspended in water, and applying high pressure to the suspension. By discharging air-saturated water, the microbubbles generated are prevented from adhering to the periphery of the fibers, causing the fibers to float, thereby forming a fiber layer containing a large amount of microscopic spaces on the water surface. It is characterized by being dehydrated and dried. Next, the present invention will be explained by means of illustrated embodiments. FIG. 1 is a system diagram showing an example of an apparatus for carrying out the filter manufacturing method according to the present invention, and the manufacturing method will be explained using this diagram. 4% of linter (cotton waste) or wood pulp in pulp tank 1
Make a 0.1% solution of melamine resin in chemical tank 2, make a 4% solution of 200 mesh Cristobal powder that has been hydrophobically treated in advance in powder tank 3, and mix these three solutions into 1023:
A raw material liquid (liquid A) is prepared by mixing in a raw material tank 4 at a ratio of 10 parts. On the other hand, air-saturated water (liquid B) pressurized to 3 kg/cm' or more is prepared by a compressor 6 in the continuous pressurized water tank 5, and a polymer flocculant, for example, 10.000 times as much as polyethylene oxide, is added to the chemical tank 7. Make a diluted solution (solution C) and add this filtrate to 100% of solution A, 3% solution of B, and 0.1% of solution C.
(7) Continuously discharge to the bottom of the mixed flotation tank 8 at the ratio. As a result of this release, the grist pearl powder suspended in liquid A quickly adheres to the surface of the fibers through the medium of liquid C, and the suspended powder in the liquid disappears, and at the same time, the countless microbubbles generated in liquid B disappear. The fibers that adhere to the periphery of the fibers and float due to their buoyancy form a delamination layer 9 containing adjacent air bubbles. The fiber layer 9 formed on the water surface is overflowed from the outlet 10 of the mixing tank 8 under the pressure of the fibers that are rising one after another from below.
It moves to the moving net-like conveyor 11, and while moving, it is vacuum dehydrated in the suction box L24 and then dried in the drying filter 13 to become the product filter 14. The fibers floating in the floating tank 8 move along the slope plate 15 and the inner wall facing it LJ7L, and the remaining water that forms the aggregated fibers 11 passes through the gap between the slope plates 15 and moves toward the shoulder.
It sequentially flows out from the outlet 16 at the bottom of the tank and is temporarily stored in the cushion tank 17. Further, water dehydrated by the suction hox 12 is also collected in a water collecting tank 18 and then flows into a cushion tank 17. The water collected in the cushion tank 17 can be recycled and reused as water for the A liquid, B liquid, and C method. In the above method, the impregnants, such as activated carbon and Crisbar, which are impregnated with the felt fibers that form the main body of the filter to be manufactured, are subjected to hydrophobic treatment in advance, so that they do not adsorb water and only selectively absorb water. For example, the property of adsorbing only the oil component in an oil emulsion is shown. There are various methods for such hydrophobic finishing, but a common one is to add an equal amount of a 1% solution of a hydrophobic silicone resin to the above impregnated material by spraying or dipping, then drying and pulverizing. It's a method. FIG. 2 is an enlarged sectional view of a filter according to the present invention. ``This filter 14, which is manufactured by a dual method and apparatus, is characterized in that the body of the filter is ``a fibrous layer constituted by fibers 20 whose entire surface is coated with a powder 19 of an oleosorbent additive, and A large amount of microscopic spaces 21 are formed within the fiber layer. The above-mentioned powder 19 is made of powder of Crisbar, zeolite, activated carbon, etc., which has been subjected to hydrophobic treatment in advance. The fibers 20 are mainly composed of vegetable fibers such as linter or wood pulp, and animal or synthetic resin fibers may be used or added as necessary. The fibers of the filter made in this way can have 2 to 4 times more hydrophobic adsorbent powder attached to the surface of the fiber than the own vehicle. This means that 65-80% of the entire filter type is composed of a fibrous intertwining of finely powdered adsorbent, which on the one hand has good water permeability and on the other hand. This made it possible to create a water filter with extremely high oil emulsion adsorption performance. Next, the features of the filter described in 1- will be explained. Must have good water permeability (water passing) performance. In other words, the main structure of this filter has an apparent specific gravity of 0.
It is a fiber layer of about 08. This fiber layer is a felt-like fiber layer in which each fiber is tightly bonded to each other while forming an extremely large number of minute spaces inside, and its most basic property is the inner space. Although it has a complex and dense structure due to the intertwining of branches peculiar to plant fibers, it has extremely excellent breathability, water absorption, and water permeability. That is, the water absorption and water retention ability is about 15 times that of its own weight, and its water permeability is about 15 QOcc per minute when the thickness is 20 cm, the area is 10 cm, and the water pressure is 300 kg/m. This water permeability shows a water permeability of about 700 cc per minute even when the same amount of additives are attached to the m fibers. Good emulsion adsorption of oil. In general, the performance of an adsorbent is primarily derived from its unique properties and the surface area of the space it contains, but secondarily it is derived from the amount of air or water that actually passes through it. It is strongly influenced by the amount of surface area in direct contact with the flow. Therefore, although it is most desirable to use these adsorbents with a particle size as small as possible in order to fully demonstrate their adsorption performance, in many cases it is unavoidable to use them with a coarse particle size. The reason for this is that when it is made into a fine powder, its air permeability and water permeability deteriorate significantly, especially when it turns into clay in water, such as Crisbar, only a few liters of water permeate.
This was because it had the disadvantage that even with its thickness, water flow was extremely difficult. For this reason, it has generally been conventional wisdom that the fine particle size of additives and good water permeability are fundamentally contradictory properties. Contrary to this common sense, the feature of this filter is that the smaller the particle size of the additive, the better its air permeability and water permeability (see Figure 2). By making the particle size of the additive as fine as possible by IS, we have practically achieved the n1 ability to demonstrate its adsorption ability to the maximum limit. Next, examples will be shown. 1 white f'f: 3cm length 50c I11 column bottom 2
0cm with Crisbar added R1 filter (g-t at a ratio of 200 mm of Crisbar 2 to linter l)
Insert 25g of
.. When a heavy oil emulsion of 000 ppm is added, the concentration of the filtrate is 15 at an overspeed of 50 cc per minute.
ppm or less. As explained above, according to the filter according to the present invention, it is possible to capture especially oily substances that are emulsified in water and become netted. Further, according to the method of the present invention, there is an effect that the filter as described in "2" can be efficiently manufactured. 4. Brief Description of the Drawings FIG. 1 is a system diagram of the apparatus used to carry out the method according to the present invention, and FIG. 2 is an enlarged sectional view of the filter according to the present invention. ■... Pulp tank, 2... Chemical solution tank, 3... Powder tank,
4... Raw material tank (A liquid tank), 5... i! I! Continuously pressurized water can (water mother tank), 7... Chemical liquid tank (C liquid tank), 8... Mixed flotation tank, 9... Fiber tank, lO... Float J2'rfl
Output D, 11...Hell I conveyor, 12...Suction box, 13...Drying device, 14...Filter, 15...Slope plate, 16...Discharge port, 17
...Cushion tank, 18...Concentration tank, A...
Raw material liquid, B...pressurized saturated water, C...additive liquid, l9.
... Powder, 20... Fiber, 21... Interfiber space. Patent applicant: Takashi Katsuragi, Yasushi Ita, male agent/patent attorney: Norimitsu Nishimura

Claims (1)

【特許請求の範囲】 11) 繊維がフェルト状に形成されたフィルターにお
いて、該フィルターを形成する繊維の表−而には、予じ
め疎水若しくは撥水加工が施こされた油吸着性の粉末が
付着されてなることを特徴とするフィルター。 (2)予じめ疎水若しくは撥水加工が施こされた油吸着
性の粉末が表面に添着された繊維を水中に懸濁せしめ、
該懸濁液中に高圧の空気飽和水を放出する事によって発
生するマイクロ気泡を前記繊維の周縁に耐着せしめて該
繊維を浮上させることにより多量の微細空間を含む繊維
層を水面上に形成せしめ、該繊維層を脱水、乾燥せしめ
てなることを特徴とするフィルターの製造方法。
[Scope of Claims] 11) In a filter in which fibers are formed in the shape of felt, the surface of the fibers forming the filter includes an oil-absorbing powder that has been previously treated with a hydrophobic or water-repellent finish. A filter characterized by being attached with. (2) Suspending fibers with oil-absorbing powder attached to the surface that has been previously treated with hydrophobic or water-repellent treatment in water;
Microbubbles generated by releasing high-pressure air-saturated water into the suspension are made to adhere to the periphery of the fibers, causing the fibers to float, thereby forming a fiber layer containing a large amount of microscopic spaces on the water surface. 1. A method for producing a filter, comprising: dehydrating and drying the fiber layer.
JP22701783A 1983-12-02 1983-12-02 Filter and its preparation Granted JPS60122020A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22701783A JPS60122020A (en) 1983-12-02 1983-12-02 Filter and its preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22701783A JPS60122020A (en) 1983-12-02 1983-12-02 Filter and its preparation

Publications (2)

Publication Number Publication Date
JPS60122020A true JPS60122020A (en) 1985-06-29
JPH0450846B2 JPH0450846B2 (en) 1992-08-17

Family

ID=16854207

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22701783A Granted JPS60122020A (en) 1983-12-02 1983-12-02 Filter and its preparation

Country Status (1)

Country Link
JP (1) JPS60122020A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0190425A2 (en) * 1985-01-08 1986-08-13 Rhodia Ag Filter for the separation of materials with lipophilic and/or oleophilic and/or nonpolar properties from different liquids, gases or vapors
JPH01199615A (en) * 1988-01-30 1989-08-11 Tsuchiya Mfg Co Ltd Production of filter medium
EP0573666A1 (en) * 1991-12-24 1993-12-15 Kato Research Institute Inc. Filter medium and filter which use animal fibers

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS536611A (en) * 1976-07-08 1978-01-21 Porisuterepu Ag Production of absorbed substance containing paper
JPS5361581A (en) * 1976-11-15 1978-06-02 Sanyo Electric Co Ltd Paper sheet containing activated carbon and production thereof
JPS5853292U (en) * 1981-10-06 1983-04-11 小林 千明 Oil adsorption filter media

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5853292B2 (en) * 1977-11-15 1983-11-28 三菱電機株式会社 Gas flow measuring device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS536611A (en) * 1976-07-08 1978-01-21 Porisuterepu Ag Production of absorbed substance containing paper
JPS5361581A (en) * 1976-11-15 1978-06-02 Sanyo Electric Co Ltd Paper sheet containing activated carbon and production thereof
JPS5853292U (en) * 1981-10-06 1983-04-11 小林 千明 Oil adsorption filter media

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0190425A2 (en) * 1985-01-08 1986-08-13 Rhodia Ag Filter for the separation of materials with lipophilic and/or oleophilic and/or nonpolar properties from different liquids, gases or vapors
JPH01199615A (en) * 1988-01-30 1989-08-11 Tsuchiya Mfg Co Ltd Production of filter medium
EP0573666A1 (en) * 1991-12-24 1993-12-15 Kato Research Institute Inc. Filter medium and filter which use animal fibers
EP0573666A4 (en) * 1991-12-24 1994-06-15 Kato Research Inst Inc Filter medium and filter which use animal fibers

Also Published As

Publication number Publication date
JPH0450846B2 (en) 1992-08-17

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