JPH09220415A - Filter - Google Patents
FilterInfo
- Publication number
- JPH09220415A JPH09220415A JP8052506A JP5250696A JPH09220415A JP H09220415 A JPH09220415 A JP H09220415A JP 8052506 A JP8052506 A JP 8052506A JP 5250696 A JP5250696 A JP 5250696A JP H09220415 A JPH09220415 A JP H09220415A
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- JP
- Japan
- Prior art keywords
- filter
- filter element
- weight
- oil
- sheet
- 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.)
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- Filtering Materials (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、フィルタに関
し、特に、使用して汚れた食用油を再生するのに好適な
フィルタに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter, and more particularly to a filter suitable for reclaiming dirty edible oil when used.
【0002】[0002]
【従来の技術】従来、セルロース繊維と活性白土や活性
炭等の吸着材とからなるシート状のフィルタを使用して
汚れた食用油を再生する技術が特開昭56−16682
0号,特開昭57−187012号,特開平3−776
15号公報等によって公知である。食用油は、固形分が
フィルタに捕捉される他に、吸着剤によって脱臭・脱色
される。2. Description of the Related Art Conventionally, there is a technique for regenerating soiled edible oil by using a sheet-shaped filter made of cellulose fibers and an adsorbent such as activated clay or activated carbon.
No. 0, JP-A-57-187012, JP-A-3-776.
It is known from the publication No. 15, etc. The edible oil is deodorized and decolorized by the adsorbent, in addition to the solid content being captured by the filter.
【0003】[0003]
【発明が解決しようとする課題】前記公知のフィルタ
は、フィルタ上に残る固形分で目が詰まり、油のろ過速
度が低下し易い。また、油の脱臭・脱色の程度は、吸着
剤との接触時間によって左右されるから、一枚のシート
状フィルタを透過させるだけで十分に長い接触時間を得
ることは難しい。フィルタを複数枚重ねることで、その
時間を長くすることは可能であるが、最上層のフィルタ
が目詰まりするとろ過速度が低下してしまうから、この
ようなろ過方法は効率的とはいい難い。The known filter is apt to be clogged with the solid content remaining on the filter, and the oil filtration rate is likely to decrease. Further, since the degree of deodorization and decolorization of oil depends on the contact time with the adsorbent, it is difficult to obtain a sufficiently long contact time by only passing through one sheet-shaped filter. Although it is possible to extend the time by stacking a plurality of filters, it is difficult to say that such a filtration method is efficient because the filtration speed decreases when the filter in the uppermost layer is clogged.
【0004】そこでこの発明は、吸着剤との接触時間を
長くすることが容易であって、しかも目詰まりし難いフ
ィルタを得ることを課題にしている。[0004] Therefore, an object of the present invention is to obtain a filter which can easily prolong contact time with an adsorbent and which is less likely to be clogged.
【0005】[0005]
【課題を解決するための手段】前記課題を解決するため
に、この発明に係るフィルタにおいては、20〜80重
量%のセルロース繊維と、20〜80重量%の活性白土
と、0〜4重量%の結合剤と、0〜40重量%の活性炭
とを含み、20〜150g/m2の目付と、シート面に
凹凸とを有するシート状フィルタエレメントが、見掛け
密度0.20〜0.40g/cm3となるように重ね合
わせられ、かつ、重なり合う前記フィルタエレメントの
縁部が切り揃えられて平滑な面を形成していることを特
徴としている。In order to solve the above problems, in the filter according to the present invention, 20 to 80% by weight of cellulose fibers, 20 to 80% by weight of activated clay and 0 to 4% by weight are used. And a binder of 0 to 40% by weight, and a sheet-shaped filter element having a basis weight of 20 to 150 g / m 2 and unevenness on the sheet surface, and an apparent density of 0.20 to 0.40 g / cm 2. It is characterized in that the edges of the filter elements that are overlapped with each other so as to be 3 and are overlapped with each other are cut and aligned to form a smooth surface.
【0006】[0006]
【実施例】添付の図面を参照して、この発明にかかるフ
ィルタの詳細を説明すると、以下のとおりである。DESCRIPTION OF THE PREFERRED EMBODIMENTS The details of the filter according to the present invention will be described below with reference to the accompanying drawings.
【0007】図1に斜視図で示すフィルタ1は、円筒状
の巻心2にフィルタエレメント(ろ紙)3を巻きつけ、
巻心2の上端にキャップ4を嵌めた円柱状体である。フ
ィルタ1は、上下端面6,7と、周面8とを有し、両端
面6,7は平滑面となるようにフィルタエレメント3の
縁部が切り揃えられている。周面8にはフィルタエレメ
ント3の末端部9があり、該末端部9が必要に応じてそ
の下に位置するフィルタエレメント3に接合されてい
る。巻心2の下端は開放状態にあり、必要ならここにも
キャップ4を嵌めることができる。A filter 1 shown in a perspective view in FIG. 1 has a cylindrical core 2 around which a filter element (filter paper) 3 is wound.
It is a columnar body in which a cap 4 is fitted on the upper end of the winding core 2. The filter 1 has upper and lower end surfaces 6 and 7, and a peripheral surface 8, and the edges of the filter element 3 are cut and aligned so that both end surfaces 6 and 7 are smooth surfaces. On the peripheral surface 8 there is an end 9 of the filter element 3, which is optionally joined to the filter element 3 located below it. The lower end of the winding core 2 is in an open state, and the cap 4 can be fitted here as well if necessary.
【0008】図2は、使用済みの食用油をろ過するため
の容器11に収納されたフィルタ1の部分破断側面図で
ある。フィルタ1は、プラスチック製メッシュ地の袋1
0に入れられたうえで、円筒状のろ過容器11に収納さ
れている。容器11は、本体12と蓋13とからなり、
ろ過作業中には、これら本体12と蓋13とが適宜の手
段(図示せず)により、密閉状態に保たれている。本体
12は、周壁15に食用油の導入口16,底壁17に排
出口18を有し、底壁17は中央部19とそれよりも高
い周縁段差部20とを有する。蓋13の内面には、垂下
部21があって、収納したフィルタ1の上端面6に圧接
可能であり、それによってフィルタ1の下端面7が容器
11の段差部20に密着する。FIG. 2 is a partially cutaway side view of the filter 1 housed in a container 11 for filtering used cooking oil. Filter 1 is a plastic mesh bag 1
After being put in 0, it is stored in the cylindrical filtration container 11. The container 11 includes a main body 12 and a lid 13,
During the filtration work, the main body 12 and the lid 13 are kept in a sealed state by an appropriate means (not shown). The main body 12 has an inlet 16 for cooking oil in the peripheral wall 15 and an outlet 18 in the bottom wall 17, and the bottom wall 17 has a central portion 19 and a peripheral step portion 20 higher than that. The lid 13 has a hanging portion 21 on the inner surface thereof, which can be pressed against the upper end surface 6 of the housed filter 1, whereby the lower end surface 7 of the filter 1 is brought into close contact with the step portion 20 of the container 11.
【0009】ろ過すべき食用油は、導入口16から入
り、矢印A〜Fで示す方向へ流れる。フィルタ1では、
上端面6から下端面7に向かって流れ、ろ過された油が
下端面7から排出口18を経て外に出る。油は、フィル
タ1において、周面からも浸入可能であるが、フィルタ
エレメント3が幾重にも重なり合っているので、その浸
入量は、上端面6からの量に比べると無視できる。The edible oil to be filtered enters through the inlet 16 and flows in the directions indicated by arrows AF. In filter 1,
The filtered oil flows from the upper end surface 6 toward the lower end surface 7, and the filtered oil exits from the lower end surface 7 through the discharge port 18. The oil can enter the filter 1 from the peripheral surface as well, but since the filter elements 3 overlap each other in multiple layers, the amount of oil that can enter the oil is negligible as compared with the amount from the upper end surface 6.
【0010】このように構成されるフィルタ1のフィル
タエレメント3は、20〜80重量%のセルロース繊維
と、20〜80重量%の活性白土と、これら繊維と活性
白土とを結合させるための0〜4重量%の樹脂結合剤
と、さらに必要に応じて添加される0〜40重量%の活
性炭とを含むもので、20〜150g/m2の目付を有
し、クレープ加工およびエンボス加工のいずれかが施さ
れている。そのクレープまたはエンボス加工は、その付
与率を5〜20%にすることが好ましい。フィルタエレ
メント3を巻心2に巻きとるときには、互いに重なり合
うフィルタエレメント3の見掛けの密度が0.20〜
0.40g/cm3となるように巻き取り条件を調整す
る。巻心2には、慣用の紙管やプラスチックパイプ等の
心材が使用され、キャップ4には、プラスチックや金属
などの加工品が使用される。The filter element 3 of the filter 1 thus constructed has 20 to 80% by weight of cellulose fibers, 20 to 80% by weight of activated clay, and 0 to 0% for binding these fibers and activated clay. It contains 4% by weight of a resin binder and 0-40% by weight of activated carbon which is further added as required, has a basis weight of 20-150 g / m 2 , and is either creped or embossed. Has been applied. As for the crepe or embossing, the application rate is preferably 5 to 20%. When the filter element 3 is wound around the winding core 2, the apparent density of the filter elements 3 overlapping each other is 0.20 to 20.
The winding condition is adjusted so as to be 0.40 g / cm 3 . A core material such as a conventional paper tube or a plastic pipe is used for the winding core 2, and a processed product such as plastic or metal is used for the cap 4.
【0011】このフィルタ1で油がろ過される機構は、
次のように考えられる。フィルタエレメント3は、クレ
ープ加工およびエンボス加工のいずれかによってシート
面に凹凸を有するから、巻きとられて重なり合うフィル
タエレメント3どうしの間には、互いに接触する部位と
離間する部位とが生じる。そのときに、フィルタエレメ
ント3の目付と見掛けの密度とが前記条件であると、前
記接触する部位が間欠的に存在し、前記離間する部位が
適度の離間距離を有し、フィルタ1の上下端面6,7間
で複雑に屈曲する油の通路が形成される。図3は、かか
る通路100の模式図である。通路100は、重なり合
うフィルタエレメント3Aと3Bとによって画成され、
多数の屈曲部位101や直状部位102を有する。汚れ
た油がフィルタ1の上端面6から通路100に浸入する
際に、油中の固形分105は、その上端面6で捕捉され
る他に、通路100の屈曲部位101や直状部位102
に付着することによって捕捉される。屈曲部位101で
は、通路100の傾斜が緩やかで、油の流れが遅くなる
から、そこでの捕捉量は特に多くなる。The mechanism by which oil is filtered by this filter 1 is
It is considered as follows. Since the filter element 3 has unevenness on the sheet surface by either crepe processing or embossing processing, a portion contacting with each other and a portion separating from each other occur between the filter elements 3 that are wound and overlap each other. At that time, when the basis weight and the apparent density of the filter element 3 are the above-mentioned conditions, the contacting portions are intermittently present, and the separating portions have an appropriate separation distance, and the upper and lower end surfaces of the filter 1 are provided. A complicatedly curved oil passage is formed between 6 and 7. FIG. 3 is a schematic view of the passage 100. The passage 100 is defined by overlapping filter elements 3A and 3B,
It has a large number of bent portions 101 and straight portions 102. When the dirty oil enters the passage 100 from the upper end surface 6 of the filter 1, the solid content 105 in the oil is captured by the upper end surface 6 of the filter 1, and the bent portion 101 and the straight portion 102 of the passage 100.
Are captured by attaching to. In the bent portion 101, the inclination of the passage 100 is gentle and the oil flow is slow, so that the trapped amount is particularly large.
【0012】このように屈曲する通路100は、円柱状
のフィルタ1の丈に比べ、距離が非常に長くなり得る。
それゆえ、この通路100を流れる汚れた油は、フィル
タエレメント3に含まれる吸着剤である活性白土や活性
炭に長時間接触することが可能になり、その時間に応じ
て脱臭・脱色の程度が進むことになる。The passage 100 thus bent can have a very long distance as compared with the length of the cylindrical filter 1.
Therefore, the dirty oil flowing through the passage 100 can come into contact with activated clay or activated carbon, which is an adsorbent contained in the filter element 3, for a long time, and the degree of deodorization / decolorization progresses depending on the time. It will be.
【0013】図2において、使用済みのフィルタ1は、
袋10の頂部10Aを摘持して容器11から簡単に取り
出すことができる。In FIG. 2, the used filter 1 is
The top 10A of the bag 10 can be grasped and easily taken out from the container 11.
【0014】図4は、この発明の一実施態様を示す図で
ある。図の(A)に示すように、フィルタエレメント3
は、一枚一枚がドーナツ状であって、それが多数積み重
ねられて柱状体となり、周面30が画成されるとともに
中央へ上下方向に延びる管路31が画成される。(B)
に示すように、柱状体は、頂部固定板32と、底部固定
板33と、これら両板32,33を連結する棒状または
帯状の固定具34とによって、見掛け密度が0.20〜
0.40g/cm3となるように挟持されている。
(B)のC−C線断面図である(C)に示すように、底
部固定板33の中央には、管路31とほぼ同径の排出口
35がある。このフィルタ1を図2と同様な容器11に
収納して使用すると、油は、フィルタ1の周面8にのぞ
むフィルタエレメント3の縁部からフィルタエレメント
3どうしの間に浸入し、図3と同様な機構によってろ過
されて管路31へと進み、排出口35を経て容器11の
外に出る。このフィルタ1では、フィルタエレメント3
の形状をドーナツ型の他に、長方形や正方形など、適宜
の形状にすることができる。FIG. 4 is a diagram showing an embodiment of the present invention. As shown in FIG.
Each has a donut shape, and a large number of the donuts are stacked to form a columnar body. The peripheral surface 30 is defined, and a duct 31 extending vertically to the center is defined. (B)
As shown in FIG. 5, the columnar body has an apparent density of 0.20 to 20 due to the top fixing plate 32, the bottom fixing plate 33, and the rod-shaped or band-shaped fixing member 34 connecting these plates 32, 33.
It is sandwiched so as to be 0.40 g / cm 3 .
As shown in (C) which is a cross-sectional view taken along the line CC of (B), a discharge port 35 having substantially the same diameter as the duct 31 is provided at the center of the bottom fixing plate 33. When this filter 1 is used by being housed in a container 11 similar to that shown in FIG. 2, oil permeates between the filter elements 3 from the edge of the filter element 3 looking into the peripheral surface 8 of the filter 1, and the same as in FIG. After being filtered by such a mechanism, it advances to the pipe line 31 and goes out of the container 11 through the discharge port 35. In this filter 1, the filter element 3
In addition to the donut shape, the shape can be an appropriate shape such as a rectangle or a square.
【0015】この発明にかかるフィルタ1において、重
なり合うフィルタエレメント3は、見掛け密度が0.2
0g/cm3より小さいと、フィルタエレメント3どう
しの離間寸法が大きくなりすぎて、フィルタ1保存中の
湿度変化に伴う伸縮が生じ易くなったり、油の圧力によ
るフィルタエレメント3の変形が生じ易くなったりす
る。そのために、フィルタ1は所要の形状を保つことが
難しくなる。また、見掛け密度が0.40g/cm3よ
り大きいと、フィルタエレメント3どうしの離間寸法が
小さくなりすぎる。それにより、図1のフィルタ1であ
れば、油中の固形分の多くが上端面6で捕捉されて該上
端面6を塞ぎ、ろ過速度が低下し易くなる。また、油は
高圧をかけて流さねばならないから、その圧力によって
フィルタエレメント3を損傷することが多くなる。In the filter 1 according to the present invention, the overlapping filter elements 3 have an apparent density of 0.2.
If it is less than 0 g / cm 3 , the separation dimension between the filter elements 3 becomes too large, and expansion and contraction due to humidity change during storage of the filter 1 are likely to occur, or deformation of the filter element 3 due to oil pressure is likely to occur. Or Therefore, it becomes difficult for the filter 1 to maintain a desired shape. If the apparent density is greater than 0.40 g / cm 3 , the spacing between the filter elements 3 will be too small. As a result, in the case of the filter 1 of FIG. 1, most of the solid content in the oil is captured by the upper end surface 6 and the upper end surface 6 is blocked, and the filtration speed is likely to decrease. Further, since the oil has to flow under a high pressure, the pressure often damages the filter element 3.
【0016】フィルタエレメント3に使用するセルロー
ス繊維は、木材パルプが好ましい。また、この繊維を補
強するために、フィルタエレメント3の10重量%を限
度として、合成繊維を混合することもできる。The cellulose fibers used in the filter element 3 are preferably wood pulp. In order to reinforce this fiber, it is also possible to mix synthetic fibers up to 10% by weight of the filter element 3.
【0017】フィルタエレメント3の活性白土の量が2
0重量%より少ないと、油と活性白土との十分な接触時
間を確保するために、例えば図1のフィルタ1であれ
ば、その丈を長くしなければならないことがある。それ
により、フィルタ容器11が徒に大きなものとなる。ま
た、活性白土の量が80重量%より多くなると、フィル
タエレメント3の強度が著しく低下し、紙としての形態
を維持することが難しくなる。活性白土および活性炭
は、200メッシュ通過のものが85%以上となる粒径
であることが好ましく、それによってフィルタエレメン
ト3の抄紙が容易となり、また、吸着剤の使用量と対比
したときの吸着効率が高くなる。The amount of activated clay of the filter element 3 is 2
If it is less than 0% by weight, in order to secure a sufficient contact time between the oil and the activated clay, for example, in the case of the filter 1 of FIG. 1, its length may have to be lengthened. Thereby, the filter container 11 becomes unnecessarily large. On the other hand, if the amount of activated clay is more than 80% by weight, the strength of the filter element 3 is significantly reduced, and it becomes difficult to maintain the form of paper. The activated clay and activated carbon preferably have a particle size of 85% or more when passing through 200 mesh, which facilitates paper making of the filter element 3 and also the adsorption efficiency when compared with the amount of the adsorbent used. Becomes higher.
【0018】フィルタエレメント3の目付が20g/m
2より小さいと、フィルタエレメント3は薄すぎてシー
トとしての強度を保つことができない。また、目付が1
50g/m2よりも大きいと、フィルタエレメント3は
厚くなり過ぎて、シートの中心部に吸着力があるにもか
かわらず、シートの表面部の吸着量が飽和に達してしま
い、フィルタ1の交換が必要になるという場合が生じ
る。The basis weight of the filter element 3 is 20 g / m
If it is less than 2 , the filter element 3 is too thin to maintain the strength as a sheet. Also, the basis weight is 1
If it is larger than 50 g / m 2 , the filter element 3 becomes too thick, and the adsorption amount on the surface portion of the sheet reaches saturation even though there is an adsorption force in the central portion of the sheet, and the filter 1 is replaced. Occasionally, it will be necessary.
【0019】樹脂結合剤は、活性白土や活性炭をセルロ
ース繊維に結合し、所要量の吸着剤を含有するフィルタ
エレメント3の抄造を容易にするとともに、これら吸着
剤がフィルタエレメント3から脱落するのを防止するた
めのもので、それにはカチオン型やアニオン型の高分子
凝集剤を使用することができる。The resin binder binds activated clay or activated carbon to the cellulose fibers to facilitate the papermaking of the filter element 3 containing a required amount of the adsorbent and prevent the adsorbent from falling off from the filter element 3. In order to prevent this, a cationic or anionic polymer flocculant can be used.
【0020】フィルタ1をメッシュ地の袋10に入れる
ときには、袋10の頂点に長さ20mm以上の摘持部1
0Aがあると、フィルタ1を容器11に出し入れするこ
とが容易になる。また、メッシュ地としてプラスチック
製ネットを使用すると、伸縮性があって、フィルタ1周
面にフィットし易い袋10を得ることができる。When the filter 1 is put into the mesh bag 10, the gripping portion 1 having a length of 20 mm or more is provided at the top of the bag 10.
With 0A, it becomes easy to put the filter 1 in and out of the container 11. Further, when a plastic net is used as the mesh material, it is possible to obtain the bag 10 which has elasticity and is easy to fit on the peripheral surface of the filter 1.
【0021】このように構成されるフィルタ1は、食用
油の他に、工業油やその他の液体のろ過に使用すること
ができる。The filter 1 thus constructed can be used for filtering industrial oil and other liquids in addition to edible oil.
【0022】フィルタエレメント3とフィルタ1とを製
造するための具体的な一例は次のとおりである。パルプ
100重量部と、粉末状活性白土(日本活性白土株式会
社製活性白土SA−35)200重量部との混合物を、
約2重量%の濃度となるように水に分散させた後、カチ
オン型凝集剤として「ファイレックスRC−104(明
成化学工業株式会社製)」2重量部と、アニオン型凝集
剤として「ファイレックスM(同社製)」1.7重量部
とを順次添加して撹拌する。この混合液を大量の水で希
釈し、慣用の抄紙機で抄紙してクレープ加工を施し、ク
レープ率15%,目付50g/m2,厚さ0.27mm
のフィルタエレメントを得た。このフィルタエレメント
の強熱減量法による活性白土含有量は、63.4重量%
であった。A specific example for manufacturing the filter element 3 and the filter 1 is as follows. A mixture of 100 parts by weight of pulp and 200 parts by weight of powdered activated clay (activated clay SA-35 manufactured by Japan Activated Soil Co., Ltd.),
After dispersing in water to a concentration of about 2% by weight, 2 parts by weight of "Pyrex RC-104 (manufactured by Meisei Chemical Industry Co., Ltd.)" as a cationic coagulant and "Pyrex as anionic coagulant" are used. 1.7 parts by weight of M (manufactured by the same company) are sequentially added and stirred. This mixed solution is diluted with a large amount of water, paper is made with a conventional paper machine and creped, and the crepe ratio is 15%, the basis weight is 50 g / m 2 , and the thickness is 0.27 mm.
To obtain a filter element of. The activated clay content of this filter element measured by the ignition loss method is 63.4% by weight.
Met.
【0023】次に、このフィルタエレメントを幅160
mm,長さ56mの寸法で直径44mmの紙管に一様な
力で巻きとり、直径115mm,重量505g(紙管重
量90gを含む)のロールとし、紙管の一端にナイロン
樹脂製キャップを嵌めてフィルタ1を得た。このフィル
タ1を市販のプラスチック製ネットでできた長さ370
mmのみかん袋10に入れ、フィルタ1の頂部の上方に
長さ約55mmの摘持部10Aを形成した。Next, the filter element is made to have a width of 160.
mm, length 56m, roll 44mm diameter paper tube with uniform force to make roll with 115mm diameter and weight 505g (including paper weight 90g), and fit a nylon resin cap on one end of the paper tube. To obtain Filter 1. This filter 1 has a length 370 made of a commercially available plastic net.
Then, the holding portion 10A having a length of about 55 mm was formed above the top of the filter 1 by placing it in the mandarin orange bag 10 mm.
【0024】[0024]
【発明の効果】この発明にかかるフィルタは、セルロー
ス繊維と吸着剤とを含み、クレープ加工やエンボス加工
による凹凸をシート面に有するフィルタエレメントが重
ね合わせてあるから、全体が比較的小さくても大きなろ
過面積を得ることができる。それにより、このフィルタ
は、容易に目詰まりすることがなく、しかも汚れた食用
油の固形分を効果的に捕捉することができる。また、こ
のフィルタでは、その油が長い時間にわたって吸着剤と
接触可能であるから、脱臭・脱色が確実になる。The filter according to the present invention comprises a cellulose fiber and an adsorbent, and since the filter elements having unevenness on the sheet surface due to crepe processing or embossing are superposed on each other, even if the whole is relatively small, it is large. The filtration area can be obtained. As a result, this filter does not easily become clogged, and moreover, the solid content of soiled edible oil can be effectively captured. Further, in this filter, the oil can contact the adsorbent for a long time, so that deodorization and decolorization are surely performed.
【図1】フィルタの斜視図。FIG. 1 is a perspective view of a filter.
【図2】容器に収納したフィルタの部分破断側面図。FIG. 2 is a partially cutaway side view of a filter housed in a container.
【図3】フィルタの模式的な部分拡大断面図。FIG. 3 is a schematic partially enlarged cross-sectional view of a filter.
【図4】フィルタの一実施態様を示す図面であって、
(A)はフィルタエレメントを重ねた状態の斜視図、
(B)はフィルタの斜視図、(C)は(B)のC−C線
断面図。FIG. 4 is a view showing an embodiment of a filter,
(A) is a perspective view showing a state in which filter elements are stacked,
(B) is a perspective view of the filter, (C) is a sectional view taken along the line CC of (B).
1 フィルタ 2 心材(巻心) 3 シート状フィルタエレメント 6 縁部(上端面) 7 縁部(下端面) 30 縁部(周面) DESCRIPTION OF SYMBOLS 1 Filter 2 Core material (core) 3 Sheet-shaped filter element 6 Edge (upper end surface) 7 Edge (lower end surface) 30 Edge (peripheral surface)
───────────────────────────────────────────────────── フロントページの続き (72)発明者 鈴木 徹臣 東京都品川区大井4丁目13番17号 伊原高 圧継手工業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tetsuomi Suzuki 4-13-17 Oi, Shinagawa-ku, Tokyo Ihara High Pressure Fitting Industry Co., Ltd.
Claims (6)
0〜80重量%の活性白土と、0〜4重量%の結合剤
と、0〜40重量%の活性炭とを含み、20〜150g
/m2の目付と、シート面に凹凸とを有するシート状フ
ィルタエレメントが、見掛け密度0.20〜0.40g
/cm3となるように重ね合わせられ、かつ、重なり合
う前記フィルタエレメントの縁部が切り揃えられて平滑
な面を形成していることを特徴とするフィルタ。1. Cellulose fibers of 20 to 80% by weight and 2
20 to 150 g, containing 0 to 80% by weight of activated clay, 0 to 4% by weight of binder, and 0 to 40% by weight of activated carbon
A sheet-shaped filter element having a fabric weight of / m 2 and unevenness on the sheet surface has an apparent density of 0.20 to 0.40 g.
/ Cm 3 and brought manner overlaid made, and filter, characterized in that it is trimmed is the edge of overlapping the filter element to form a smooth surface.
る凹凸が、クレープおよびエンボスのいずれかである請
求項1に記載のフィルタ。2. The filter according to claim 1, wherein the unevenness on the sheet surface of the filter element is one of a crepe and an emboss.
が心材に巻かれて円柱状を呈し、両端が平滑に切り揃え
られている請求項1記載のフィルタ。3. The filter according to claim 1, wherein the filter element has a cylindrical shape in which the filter element is wound around a core material, and both ends thereof are smoothly cut and aligned.
面板との間に前記フィルタエレメントが多数枚重ねられ
るとともに、それらの板を介して上下方向から加圧保持
された柱状体であって、該柱状体の周面を形成する前記
フィルタエレメントの縁部が平滑に切り揃えられてお
り、かつ、該柱状体の中心部に前記重ねられたフィルタ
エレメントと前記頂面板と底面板のいずれか一方とを貫
通する管路が形成されている請求項1記載のフィルタ。4. The filter is a columnar body in which a large number of the filter elements are stacked between a top plate and a bottom plate which are parallel to each other, and which are pressed and held from above and below through the plates. An edge portion of the filter element forming the peripheral surface of the columnar body is smoothly cut and aligned, and any one of the filter element, the top face plate and the bottom face plate that are stacked on the center portion of the columnar body. The filter according to claim 1, wherein a pipe line is formed so as to pass through one of them.
納められ、該袋が前記フィルタの頂部よりも上に長さ2
0mm以上の摘持可能な部位を有している請求項1〜4
のいずれかに記載のフィルタ。5. The filter is contained in a liquid permeable mesh bag having a length 2 above the top of the filter.
5. A gripping part having a size of 0 mm or more is included.
The filter according to any one of the above.
率またはエンボス率が5〜20%である請求項1〜5の
いずれかに記載のフィルタ。6. The filter according to claim 1, wherein the crepe rate or emboss rate of the filter element is 5 to 20%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP05250696A JP3300597B2 (en) | 1996-02-15 | 1996-02-15 | Liquid filter and filtration device using the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP05250696A JP3300597B2 (en) | 1996-02-15 | 1996-02-15 | Liquid filter and filtration device using the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09220415A true JPH09220415A (en) | 1997-08-26 |
JP3300597B2 JP3300597B2 (en) | 2002-07-08 |
Family
ID=12916626
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP05250696A Expired - Fee Related JP3300597B2 (en) | 1996-02-15 | 1996-02-15 | Liquid filter and filtration device using the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3300597B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001212413A (en) * | 1999-11-22 | 2001-08-07 | Tasuku Corporation:Kk | Filter medium, filtration device, edible oil circulating device and method for utilizing used filter medium |
DK200200907A (en) * | 2002-06-14 | 2002-08-20 | Oilcare Aps | Mineral oil purification involves pre-filtration with oil and passing through filtering unit in which filtering medium comprises organic fibers and carbon particles |
WO2003106603A1 (en) * | 2002-06-14 | 2003-12-24 | Oilcare Aps | A process and an apparatus for purification of waste oil or re-refined oil from mineral or synthetic oil |
JP2006334221A (en) * | 2005-06-03 | 2006-12-14 | Matsushita Electric Ind Co Ltd | Regeneration filter for used edible oil, and regeneration apparatus using the same |
JP2007330290A (en) * | 2006-06-12 | 2007-12-27 | Toray Ind Inc | Carrier module |
US7380676B2 (en) | 2000-10-18 | 2008-06-03 | Winchester Global Pty Ltd | Filtering device |
CN105148830A (en) * | 2015-06-18 | 2015-12-16 | 深圳清华大学研究院 | Decoloring clay adsorbent and preparation method thereof |
-
1996
- 1996-02-15 JP JP05250696A patent/JP3300597B2/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001212413A (en) * | 1999-11-22 | 2001-08-07 | Tasuku Corporation:Kk | Filter medium, filtration device, edible oil circulating device and method for utilizing used filter medium |
US7380676B2 (en) | 2000-10-18 | 2008-06-03 | Winchester Global Pty Ltd | Filtering device |
DK200200907A (en) * | 2002-06-14 | 2002-08-20 | Oilcare Aps | Mineral oil purification involves pre-filtration with oil and passing through filtering unit in which filtering medium comprises organic fibers and carbon particles |
WO2003106603A1 (en) * | 2002-06-14 | 2003-12-24 | Oilcare Aps | A process and an apparatus for purification of waste oil or re-refined oil from mineral or synthetic oil |
JP2006334221A (en) * | 2005-06-03 | 2006-12-14 | Matsushita Electric Ind Co Ltd | Regeneration filter for used edible oil, and regeneration apparatus using the same |
JP2007330290A (en) * | 2006-06-12 | 2007-12-27 | Toray Ind Inc | Carrier module |
CN105148830A (en) * | 2015-06-18 | 2015-12-16 | 深圳清华大学研究院 | Decoloring clay adsorbent and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
JP3300597B2 (en) | 2002-07-08 |
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