JPH0663101U - Liquid phase adsorption filter - Google Patents

Liquid phase adsorption filter

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Publication number
JPH0663101U
JPH0663101U JP905493U JP905493U JPH0663101U JP H0663101 U JPH0663101 U JP H0663101U JP 905493 U JP905493 U JP 905493U JP 905493 U JP905493 U JP 905493U JP H0663101 U JPH0663101 U JP H0663101U
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Japan
Prior art keywords
activated carbon
sheet
filter
adsorption
liquid
Prior art date
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Pending
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JP905493U
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Japanese (ja)
Inventor
智子 米原
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Unitika Ltd
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Unitika Ltd
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Priority to JP905493U priority Critical patent/JPH0663101U/en
Publication of JPH0663101U publication Critical patent/JPH0663101U/en
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  • Treatment Of Liquids With Adsorbents In General (AREA)

Abstract

(57)【要約】 【目的】 繊維状活性炭と粉末あるいは粒状活性炭の各
々の長所を生かすとともに,短所を解消し,広範囲の物
質が吸着可能で,優れた吸着性能と濾過性能とを有する
液相吸着フィルターを提供する。 【構成】 繊維状活性炭を含有するシート1と,粉末あ
るいは粒状活性炭と有機あるいは無機の繊維とバインダ
ーとを混合して抄紙したシート2とを重ねて円筒状に巻
き上げてフィルター本体3を形成し,処理液の出口側と
なる側面を繊維層で構成された補助フィルター4で覆っ
た液相吸着フィルター。
(57) [Summary] [Purpose] A liquid phase that has the advantages of fibrous activated carbon and powdered or granular activated carbon, eliminates the disadvantages, can adsorb a wide range of substances, and has excellent adsorption and filtration performance. Provide an adsorption filter. [Structure] A sheet 1 containing fibrous activated carbon and a sheet 2 made by mixing powdered or granular activated carbon with organic or inorganic fibers and a binder are stacked and rolled up into a cylindrical shape to form a filter body 3, A liquid phase adsorption filter in which the side surface on the outlet side of the treatment liquid is covered with an auxiliary filter 4 composed of a fiber layer.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は,広範囲の物質が吸着可能で,優れた吸着性能と濾過性能を有する液 相吸着フィルターに関するものである。 The present invention relates to a liquid phase adsorption filter capable of adsorbing a wide range of substances and having excellent adsorption performance and filtration performance.

【0002】[0002]

【従来の技術】[Prior art]

活性炭は,粉末,粒状,繊維状等の形態のものが使用されているが,それぞれ に特性を有している。粉末及び粒状活性炭は,その表面の細孔特性により,比較 的高分子量の物質が吸着可能であり,しかも充填密度が高いので,単位容積当た りの吸着量が大きい。しかしながら,定形性がなく,充填密度が高いので,圧力 損失が大きい。また,取扱い性や加工性に劣り,活性炭の一部が流出したり脱落 したりしやすいという欠点がある。 Activated carbon is used in the form of powder, granules, fibres, etc., each with its own characteristics. Powdered and granular activated carbon can adsorb comparatively high molecular weight substances due to the surface pore characteristics, and since the packing density is high, the adsorption amount per unit volume is large. However, there is no fixed form and the packing density is high, so the pressure loss is large. In addition, it has the disadvantages of poor handling and processability, and some of the activated carbon easily flows out or falls off.

【0003】 一方,繊維状活性炭は吸着速度が速く,比較的低分子量の物質に対する吸着性 に優れている。また,取扱い性や加工性がよく,圧力損失もそれほど大きくはな らない。しかしながら,その表面の細孔特性により,分子量の高い化合物の吸着 性が劣る。また,充填密度が低いので,単位容積当たりの吸着量が小さいという 欠点がある。On the other hand, fibrous activated carbon has a fast adsorption rate and is excellent in adsorption to a substance having a relatively low molecular weight. In addition, it is easy to handle and work, and the pressure loss is not so large. However, due to the surface pore characteristics, the adsorption of high molecular weight compounds is poor. In addition, since the packing density is low, there is the drawback that the adsorption amount per unit volume is small.

【0004】 以上のような繊維状活性炭,粉末及び粒状活性炭を各々単独で使用する場合の 欠点を解消するため,実開昭63-94527号公報には,繊維状活性炭シートと,シー ト状支持体に担持された活性炭とが層状に配され, かつ外周が通気性シートで包 被された空気清浄機用吸着フイルターが提案されている。In order to eliminate the above-mentioned drawbacks when using fibrous activated carbon, powder and granular activated carbon alone, Japanese Utility Model Laid-Open No. 63-94527 discloses a fibrous activated carbon sheet and a sheet-like support. An adsorption filter for an air cleaner has been proposed in which activated carbon supported on the body is arranged in layers and the outer periphery is covered with a breathable sheet.

【0005】[0005]

【考案が解決しようとする課題】[Problems to be solved by the device]

上記の実開昭63-94527号公報記載のフイルターは,気相吸着処理には適するも のであったが,液相処理には不適であった。すなわち,シート状支持体に活性炭 を担持する場合, 活性炭はシート状支持体の表面に薄く担持されるだけで,表面 に偏在する。このため,気相に比較して拡散速度の遅い液相吸着では, 液中の分 子を効率よく吸着することは困難であった。 また,シート状支持体に活性炭を担持しただけでは活性炭が脱落し,液中に流 出することが避けられない。一部の活性炭が脱落すれば,活性炭はフイルター中 でさらに偏在することとなり,吸着性能が低下する。 さらに,シート状支持体に活性炭を担持する場合, シート状支持体内において 活性炭量のばらつきが大きく,前述した活性炭の脱落が多いこともあって, 個々 のフイルター間の性能のばらつきが大きいという問題があった。 The filter described in Japanese Utility Model Laid-Open No. 63-94527 was suitable for gas phase adsorption treatment, but was not suitable for liquid phase treatment. In other words, when supporting activated carbon on a sheet-shaped support, activated carbon is only thinly supported on the surface of the sheet-shaped support and is unevenly distributed on the surface. For this reason, it was difficult to efficiently adsorb the molecules in the liquid by liquid-phase adsorption, which has a slower diffusion rate than in the gas phase. In addition, it is inevitable that the activated carbon will fall off and flow out into the liquid simply by supporting the activated carbon on the sheet-shaped support. If some of the activated carbon falls off, the activated carbon will be more unevenly distributed in the filter, and the adsorption performance will decrease. Furthermore, when activated carbon is loaded on the sheet-shaped support, there is a large variation in the amount of activated carbon in the sheet-shaped support, and as a result of the large amount of activated carbon falling off, there is a problem that there is a large variation in the performance between individual filters. there were.

【0006】 本考案は,上記の問題を解決し,繊維状活性炭と粉末あるいは粒状活性炭の各 々の長所を生かすとともに,短所を解消し,広範囲の物質が吸着可能で,優れた 吸着性能と濾過性能とを有する液相吸着フィルターを提供することを技術的な課 題とするものである。The present invention solves the above problems and utilizes the advantages of each of the fibrous activated carbon and the powdered or granular activated carbon, while eliminating the disadvantages, capable of adsorbing a wide range of substances, and having excellent adsorption performance and filtration. The technical problem is to provide a liquid phase adsorption filter having high performance.

【0007】[0007]

【課題を解決するための手段】[Means for Solving the Problems]

本考案者らは,このような課題を解決するために鋭意検討した結果,本考案に 到達した。 すなわち,本考案は,繊維状活性炭を含有するシートと,粉末あるいは粒状活 性炭と有機あるいは無機の繊維とバインダーとを混合して抄紙したシートとを重 ねて円筒状に巻き上げてフィルター本体を形成し,処理液の出口側となる側面を 繊維層で構成された補助フィルターで覆ってなることを特徴とする液相吸着フィ ルターを要旨とするものである。 The present inventors have arrived at the present invention as a result of extensive studies to solve these problems. That is, according to the present invention, a sheet containing fibrous activated carbon and a sheet made by mixing powdered or granular activated carbon with organic or inorganic fibers and a binder are stacked and rolled up in a cylindrical shape to form a filter body. The gist is a liquid-phase adsorption filter, which is formed by covering the side surface on the outlet side of the treatment liquid with an auxiliary filter composed of a fiber layer.

【0008】 以下, 本考案について詳細に説明する。Hereinafter, the present invention will be described in detail.

【0009】 本考案の液相吸着フィルターは,図2のように,繊維状活性炭を含有するシー ト1と,粉末あるいは粒状活性炭と有機あるいは無機の繊維とバインダーとを混 合して抄紙したシート2とを重ねて円筒状に巻き上げてフィルター本体3を形成 し,少なくとも処理液の出口側となる側面を繊維層で構成された補助フィルター 4で覆ったものであり,図1の例は,フィルター本体3の両側を補助フィルター 4で覆った例を示すものである。The liquid phase adsorption filter of the present invention, as shown in FIG. 2, is a sheet made by mixing a sheet 1 containing fibrous activated carbon, powdered or granular activated carbon, organic or inorganic fibers and a binder. 2 is piled up and rolled up into a cylindrical shape to form a filter body 3, and at least the side surface on the outlet side of the processing liquid is covered with an auxiliary filter 4 composed of a fiber layer. The example of FIG. 1 is a filter. This shows an example in which both sides of the main body 3 are covered with auxiliary filters 4.

【0010】 シート1と2を円筒状に巻き上げて成形する場合,シート1,2の位置関係は 特に限定されるものではないが,シート2が被処理液の入口側とすれば,粉末あ るいは粒状活性炭が万一シート2から脱落してもシート1で捕集され,粉末ある いは粒状活性炭が処理液中に流出するのを防止することができる。また,シート 1及び2を各々1枚以上,異なる枚数を重ねて成形してもよい。When the sheets 1 and 2 are rolled up into a cylindrical shape and formed, the positional relationship between the sheets 1 and 2 is not particularly limited, but if the sheet 2 is on the inlet side of the liquid to be treated, it may be powdery. Even if the granular activated carbon falls off from the sheet 2, it can be collected by the sheet 1 and the powder or granular activated carbon can be prevented from flowing out into the treatment liquid. Alternatively, one or more sheets 1 and 2 may be formed by stacking different numbers.

【0011】 本考案では,フィルター本体の,少なくとも処理液の出口側となる側面を繊維 層で構成された補助フィルターで覆う必要があるが,通常は抵抗を少なくするた め外周側から内周側に被処理液を流すことが多いので,内周側に設けるのが一般 的である。In the present invention, it is necessary to cover at least the side surface on the outlet side of the processing liquid of the filter main body with an auxiliary filter composed of a fiber layer, but normally, from the outer peripheral side to the inner peripheral side in order to reduce resistance. Since the liquid to be treated often flows to the inside, it is generally installed on the inner peripheral side.

【0012】 シート1に含まれる繊維状活性炭の原料としては,再生セルロース繊維,アク リル繊維,フェノール繊維,石炭ピッチ等いずれでもよい。また,良好な吸着性 能を付与するためには, 繊維状活性炭の比表面積は 300m2/g以上, 特に 500〜 2500m2 /gが好ましい。The raw material of the fibrous activated carbon contained in the sheet 1 may be regenerated cellulose fiber, acrylic fiber, phenol fiber, coal pitch or the like. Further, in order to impart good adsorption performance, the specific surface area of the fibrous activated carbon is preferably 300 m 2 / g or more, particularly 500 to 2500 m 2 / g.

【0013】 シート2に含まれる粉末あるいは粒状活性炭の原料としては,ヤシ殻,石炭, 木粉等いずれでもよいが,良好な吸着性能を付与するためには比表面積 300m2 /g以上, 特に 500〜1500m2 /gのものが好ましい。また,繊維状活性炭の欠 点である比較的高分子量の物質の吸着能力不足を補うためには,細孔径20Å以上 の細孔容積が全細孔容積の15%以上で, 粒径0.5mm以下のものが90%以上である ものが好ましい。The powder or granular activated carbon contained in the sheet 2 may be coconut shell, coal, wood powder, or the like, but a specific surface area of 300 m 2 / g or more, particularly 500 to give good adsorption performance. It is preferably about 1500 m 2 / g. In order to compensate for the lack of adsorption capacity for relatively high molecular weight substances, which is a deficiency of fibrous activated carbon, the volume of pores with a pore size of 20Å or more is 15% or more of the total pore volume, and the particle size is 0.5 mm. The following are 90% or more and are preferable.

【0014】 巻き上げ時の加工性がよく,また,優れた濾過性能を有し, 圧力損失が小さい 液相吸着フィルターとするには,シート1,2の目付は20〜 800g/m2 が好ま しく,また,嵩密度はシート1が0.01〜0.2g/cm3 ,シート2が0.02〜0.5g /cm3 が好ましい。 シート1,2における繊維状活性炭又は粉末あるいは粒状活性炭の含有量は, 優れた吸着能力を付与するために各々5重量%以上であることが好ましい。[0014] In order to obtain a liquid phase adsorption filter which has good workability at the time of winding and has excellent filtration performance and a small pressure loss, it is preferable that the basis weight of the sheets 1 and 2 is 20 to 800 g / m 2. The sheet 1 preferably has a bulk density of 0.01 to 0.2 g / cm 3 , and the sheet 2 preferably has a bulk density of 0.02 to 0.5 g / cm 3 . The content of the fibrous activated carbon or the powdered or granular activated carbon in the sheets 1 and 2 is preferably 5% by weight or more in order to impart excellent adsorption ability.

【0015】 シート1に含有される他の材料としては,天然繊維,合成繊維,パルプ,ガラ ス繊維,セラミック繊維等の有機及び無機物質があり,これらの1種あるいは複 数種を同時に用いてもよい。成形性をよくするためには, 特に熱融着可能な材料 ,例えば合成繊維を配合することが好ましく,合成繊維としては,ポリエステル ,共重合ポリエステル,ポリオレフィン,ポリアミド等が好ましく使用される。 また,シート2には,粉末あるいは粒状活性炭と,有機あるいは無機の繊維及 びバインダー以外にパルプ等の他の材料を含有させてもよい。Other materials contained in the sheet 1 include organic and inorganic substances such as natural fibers, synthetic fibers, pulp, glass fibers, ceramic fibers, etc., and one or more of them may be used at the same time. Good. In order to improve the moldability, it is particularly preferable to blend a heat-fusible material such as synthetic fiber, and as the synthetic fiber, polyester, copolyester, polyolefin, polyamide, etc. are preferably used. Further, the sheet 2 may contain powder or granular activated carbon and other materials such as pulp in addition to organic or inorganic fibers and binder.

【0016】 シート1の製造方法としては,カード機に繊維状活性炭と他の材料を供給し, 開繊と混合を行ってウエッブを形成する方法,あるいは繊維状活性炭と他の材料 を混合し,湿式抄造する方法等がある。The sheet 1 is manufactured by a method of supplying fibrous activated carbon and other materials to a card machine and performing opening and mixing to form a web, or by mixing fibrous activated carbon and other materials, There are methods such as wet papermaking.

【0017】 また,シート2は,粉末あるいは粒状活性炭と有機あるいは無機の繊維とポリ ビニルアルコール等のバインダーとを混合し,このスラリーを抄紙して得るが, バインダーの配合量はシート2の10重量%以下が好ましい。なお,有機繊維と無 機繊維の両方を混合してシート2を形成してもよい。The sheet 2 is obtained by mixing powdered or granular activated carbon, organic or inorganic fibers and a binder such as polyvinyl alcohol, and making a paper from this slurry. The amount of the binder blended is 10% by weight of the sheet 2. % Or less is preferable. The sheet 2 may be formed by mixing both organic fibers and inorganic fibers.

【0018】 フィルター本体3の,少なくとも処理液の出口側となる側面を覆う補助フィル ター4の素材は特に限定されるものではないが,加工性のよい熱融着性を有する 織物あるいは不織布が好ましい。また,補助フィルター4は濾過性能に優れたも ので,かつある程度の通気性のあるものがよく,目付は10〜 100g/m2 が好ま しい。The material of the auxiliary filter 4 that covers at least the side surface of the filter body 3 that is the outlet side of the treatment liquid is not particularly limited, but a woven or non-woven fabric having good workability and heat-sealing property is preferable. . Further, the auxiliary filter 4 has excellent filtering performance and is preferably breathable to some extent, and the basis weight is preferably 10 to 100 g / m 2 .

【0019】 本考案の液相吸着フィルターは,繊維状活性炭を含有するシートと,粉末ある いは粒状活性炭と有機あるいは無機の繊維とバインダーとを混合して抄紙したシ ートとを重ねるだけで, 繊維状活性炭と粉末あるいは粒状活性炭を組み合わせる ことができるので,他の方法に比較して製造の手間もコストもかからず,また, 非常にコンパクトなものとなる。The liquid phase adsorption filter of the present invention can be obtained by simply stacking a sheet containing fibrous activated carbon and a sheet made by mixing powdered or granular activated carbon with organic or inorganic fibers and a binder. Since fibrous activated carbon can be combined with powdered or granular activated carbon, it requires less labor and cost compared to other methods, and is extremely compact.

【0020】 また,繊維状活性炭を含有するシートと,粉末あるいは粒状活性炭と有機ある いは無機の繊維とバインダーとを混合して抄紙したシートを各々何種類か用意す れば,各種の組み合わせのフィルターを簡単に作ることができる。さらに,重ね る枚数を調整することにより,繊維状活性炭と,粉末あるいは粒状活性炭の割合 を簡単に変えることが可能である。In addition, if a sheet containing fibrous activated carbon and several types of sheets made by mixing powdered or granular activated carbon with organic or inorganic fibers and a binder are prepared, various combinations can be prepared. You can easily make a filter. Furthermore, the ratio of fibrous activated carbon and powdered or granular activated carbon can be easily changed by adjusting the number of layers.

【0021】[0021]

【作用】[Action]

本考案の液相吸着フィルターは,粉末あるいは粒状活性炭を,有機あるいは無 機の繊維とバインダーと混合し,抄紙されたシートにして円筒状に成形している ので,粉末あるいは粒状活性炭をシート全体に均一に分散させ,固定させること ができる。しかも,粉末あるいは粒状活性炭は,有機あるいは無機の繊維が重な り合い,絡み合った内部の隙間に存在し,有機あるいは無機の繊維で移動するの が抑えられるので,脱落して液中に流出し難い。さらに,繊維状活性炭を含有す るシートと,粉末あるいは粒状活性炭と有機あるいは無機の繊維とバインダーと を混合して抄紙したシートを何層も重ねて成形すれば,濾過容積の大きなフィル ターとなるが,処理液の出口側となる側面に設けた補助フィルターで濾過性能を 一段と強化するとともに,たとえ粉末あるいは粒状活性炭がフィルター本体から 脱落しても,液中に流出するのを防止することができる。 In the liquid phase adsorption filter of the present invention, powder or granular activated carbon is mixed with organic or organic fiber and binder to form a paper-made sheet into a cylindrical shape. It can be evenly dispersed and fixed. In addition, the powdered or granular activated carbon is present in the interstices inside the organic or inorganic fibers that are overlapped and entangled with each other, and the movement of the organic or inorganic fibers is suppressed, so they fall off and flow into the liquid. hard. Furthermore, if a sheet containing fibrous activated carbon is mixed with powdered or granular activated carbon, organic or inorganic fibers and a binder and formed into multiple layers to form a sheet, a filter with a large filtration volume is obtained. However, it is possible to further enhance the filtration performance with an auxiliary filter provided on the side that is the outlet side of the treatment liquid, and to prevent the powder or granular activated carbon from flowing out into the liquid even if it falls off from the filter body. .

【0022】 また,吸着特性の異なる繊維状活性炭と粉末あるいは粒状活性炭によって,低 分子量から高分子量の広範囲に及ぶ物質を吸着することができる。この場合,吸 着速度の速い繊維状活性炭の効率のよい吸着能力と充填密度の高い粉末あるいは 粒状活性炭によって単位容積当たりの吸着量を補うことにより,定められた容積 内で十分な吸着能力を発揮することができる。しかも,圧力損失は大きくならず ,活性炭の一部の流出,脱落がない。Further, the fibrous activated carbon and powder or granular activated carbon having different adsorption properties can adsorb a wide range of substances from low molecular weight to high molecular weight. In this case, the efficient adsorption capacity of the fibrous activated carbon with a high adsorption rate and the powder or granular activated carbon with a high packing density are used to supplement the adsorption amount per unit volume, thereby exhibiting a sufficient adsorption capacity within the specified volume. can do. Moreover, the pressure loss does not increase, and part of activated carbon does not flow out or fall off.

【0023】[0023]

【実施例】【Example】

次に,本考案を実施例により具体的に説明する。 Next, the present invention will be specifically described with reference to examples.

【0024】 実施例1 繊維状活性炭として,石炭ピッチを原料とし,5mmにカットしたものを準備し た。この繊維状活性炭の比表面積をカンタクロム社製「オートソーブ6」自動ガ ス吸着測定装置により低温窒素吸着法で測定したところ,1000m2/gであり,ま た, 同様の方法で細孔容積を調べたところ,全細孔容積は0.52cm3/g,そのうち 細孔径20Å以上のものが2%であった。Example 1 As fibrous activated carbon, a material prepared from coal pitch and cut into 5 mm was prepared. The specific surface area of this fibrous activated carbon was measured by the low temperature nitrogen adsorption method using the "Autosorb 6" automatic gas adsorption measuring device manufactured by Kantachrome Co., and was 1000 m 2 / g. Also, the pore volume was examined by the same method. As a result, the total pore volume was 0.52 cm 3 / g, of which 2% had a pore size of 20 Å or more.

【0025】 上記の繊維状活性炭70重量%,平均繊維長1.3mmのポリエチレン合成パルプ30 重量%の割合で混合したスラリーを用いて湿式法で抄造してシート1を得た。得 られたシート1の目付は80g/m2 ,嵩密度は0.11g/cm3 であった。Sheet 1 was obtained by a wet method using a slurry obtained by mixing 70% by weight of the above fibrous activated carbon and 30% by weight of a polyethylene synthetic pulp having an average fiber length of 1.3 mm. The obtained sheet 1 had a basis weight of 80 g / m 2 and a bulk density of 0.11 g / cm 3 .

【0026】 また,粉末活性炭として, ヤシ殻を原料としたもので,100メッシュパス, すな わち粒径0.149mm 以下のものが94.5%のものを準備した。繊維状活性炭と同じ方 法で測定したこの粉末活性炭の比表面積は 912m2/g, 全細孔容積は0.66cm3/g ,そのうち細孔径20Å以上のものが42%であった。Further, as powdered activated carbon, coconut shell was used as a raw material, and 100% mesh pass, that is, particle size of 0.149 mm or less was prepared at 94.5%. The specific surface area of this powdered activated carbon measured by the same method as the fibrous activated carbon was 912 m 2 / g, the total pore volume was 0.66 cm 3 / g, and 42% of them had a pore diameter of 20 Å or more.

【0027】 上記の粉末活性炭62重量%,麻30%及びポリビニルアルコール7重量%の割合 で混合したスラリーを用いて湿式法で抄造してシート2を得た。得られたシート 2の目付は60g/m2 ,嵩密度は0.3g/cm3 であった。Sheet 2 was obtained by a wet method using a slurry prepared by mixing 62% by weight of the above powdered activated carbon, 30% of hemp and 7% by weight of polyvinyl alcohol. The sheet 2 thus obtained had a basis weight of 60 g / m 2 and a bulk density of 0.3 g / cm 3 .

【0028】 上記で得られたシート1とシート2とをシート2が外側になるように重ね,あ らかじめ不織布を巻いた鉄芯に巻いて円筒状物を作り,その上からさらに不織布 を巻いた後,熱処理して円筒状に成形した。得られた液相吸着フィルターは, 円 筒状をしたフィルター本体の内外層が不織布からなる補助フィルターで覆われて おり,外径60mm,内径30mmのものであった。 なお,上記で使用した不織布は,ポリエチレンテレフタレートを芯とし,ポリ エチレンを鞘とした複合繊維からなり,目付30g/m2 のものであった。 得られた長さ 250mmの液相吸着フィルターを用いて行った吸着試験結果を表1 に示す。The sheet 1 and the sheet 2 obtained above are stacked so that the sheet 2 is on the outside, and the sheet is preliminarily wound around an iron core wrapped with a non-woven fabric to form a cylindrical object, and the non-woven fabric is further formed on the cylindrical product. After winding, it was heat treated to form a cylindrical shape. The obtained liquid-phase adsorption filter had an outer diameter of 60 mm and an inner diameter of 30 mm, with the inner and outer layers of the cylindrical filter body covered with an auxiliary filter made of non-woven fabric. The non-woven fabric used above was composed of a composite fiber having polyethylene terephthalate as a core and polyethylene as a sheath, and had a basis weight of 30 g / m 2 . Table 1 shows the results of adsorption tests conducted using the obtained liquid phase adsorption filter having a length of 250 mm.

【0029】 また,比較例1として,フィルター本体を上記で得たシート1のみで形成した 以外は実施例1と同様にしてフィルターを製造した。さらに,比較例2として比 表面積1000m2 /g,30〜60メッシュのヤシ殻系粒状活性炭を実施例1のフィル ターと同じ大きさになるように充填し,その外側と内側を不織布で覆った。 比較例1及び2で得られたフィルターを用いて行った吸着試験結果を表1に示 す。Further, as Comparative Example 1, a filter was manufactured in the same manner as in Example 1 except that the filter body was formed only from the sheet 1 obtained above. Further, as Comparative Example 2, coconut shell-based granular activated carbon having a specific surface area of 1000 m 2 / g and 30 to 60 mesh was filled so as to have the same size as that of the filter of Example 1, and the outside and the inside were covered with a nonwoven fabric. . Table 1 shows the results of the adsorption test conducted using the filters obtained in Comparative Examples 1 and 2.

【0030】[0030]

【表1】 [Table 1]

【0031】 表1において,活性炭充填量とは,繊維状活性炭と粉末もしくは活性炭の含有 量の合計を示す。また,圧損は,5リットル/min で10分間通水した後の圧力損 失を示す。次に,吸着試験は,分子量 400のFast Red A及び分子量1357のビタミ ンB12をイオン交換水にて100mg/リットルに調整した液を各々1リットル/min で通液し,10分間通水した後に出口にて着色が認められないものを○,認められ るものを×として評価した。さらに,活性炭の流出については,5リットル/min で通水した直後に,出口でサンプリングした水を孔径0.45μmのメンブランフィ ルターで濾過して確認した。 なお,上記の各試験は,すべて被処理水をフィルターの外周側から内周側に通 過させて行った。In Table 1, the activated carbon filling amount indicates the total content of fibrous activated carbon and powder or activated carbon. In addition, the pressure loss indicates the pressure loss after passing water at 5 liter / min for 10 minutes. Next, in the adsorption test, Fast Red A having a molecular weight of 400 and Vitamin B 12 having a molecular weight of 1357 were adjusted to 100 mg / liter with ion-exchanged water and passed at 1 liter / min for 10 minutes. After that, those with no coloration at the outlet were evaluated as ◯, and those with coloration were evaluated as x. Furthermore, the outflow of activated carbon was confirmed by filtering the water sampled at the outlet with a membrane filter with a pore size of 0.45 μm immediately after passing water at 5 liters / min. All of the above tests were carried out by passing the water to be treated from the outer peripheral side to the inner peripheral side of the filter.

【0032】 表1から明らかなように,実施例1で得られたフィルターの場合,活性炭の流 出がなく,Fast Red AもビタミンB12もよく吸着することができた。また,活性 炭充填量も比較例1より多くすることができた。 さらに,濾過性能を調べるために,10ppm水酸化鉄水溶液を流量4リットル/min で流し,濾過前後の液の粒子数をコールターカウンターで測定したところ,2.52 μm以上の粒子は90%除去されていた。As is clear from Table 1, in the case of the filter obtained in Example 1, activated carbon did not flow out, and both Fast Red A and vitamin B 12 could be adsorbed well. Also, the activated carbon filling amount could be increased as compared with Comparative Example 1. Furthermore, in order to examine the filtration performance, a 10 ppm iron hydroxide aqueous solution was flown at a flow rate of 4 liters / min, and the number of particles in the solution before and after filtration was measured by a Coulter counter. .

【0033】 一方,比較例1では,圧損,Fast Red Aの吸着及び活性炭の流出については問 題はないが,分子量の大きいビタミンB12を吸着する能力が劣っており,活性炭 の充填量も少なかった。比較例2では,活性炭充填量は多いが,活性炭の流出が 認められ,さらに,粒状活性炭であるため,吸着速度が遅く,上記の通液条件で は吸着能を十分に発揮することができなかった。On the other hand, in Comparative Example 1, there is no problem with pressure loss, adsorption of Fast Red A, and outflow of activated carbon, but the ability to adsorb vitamin B 12 having a large molecular weight is inferior and the amount of activated carbon packed is small. It was In Comparative Example 2, although the activated carbon filling amount was large, the activated carbon was observed to flow out, and since it was granular activated carbon, the adsorption rate was slow, and the adsorption capacity could not be fully exhibited under the above liquid passing conditions. It was

【0034】[0034]

【考案の効果】[Effect of device]

本考案によれば,広範囲の物質が吸着可能で,繊維状活性炭と粉末あるいは粒 状活性炭の各々の長所を生かすとともに,短所を解消し,広範囲の物質が吸着可 能で,優れた吸着性能と濾過性能とを有し,浄水処理,メッキ浴の浄化,醸造酒 の精製等,種々多様な分野における液相処理用に好適な液相吸着フィルターを提 供することが可能となる。 According to the present invention, a wide range of substances can be adsorbed, the advantages of each of fibrous activated carbon and powdered or granular activated carbon can be utilized, the disadvantages can be eliminated, and a wide range of substances can be adsorbed, resulting in excellent adsorption performance. It is possible to provide a liquid-phase adsorption filter that has filtration performance and is suitable for liquid-phase treatment in various fields such as water purification, plating bath purification, and brewing liquor purification.

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

【図1】本考案の液相吸着フィルターの一実施態様を示
す斜視図である。
FIG. 1 is a perspective view showing an embodiment of a liquid phase adsorption filter of the present invention.

【図2】シート1と2を重ねて円筒状に巻き上げる状態
を示す斜視図である。
FIG. 2 is a perspective view showing a state in which sheets 1 and 2 are stacked and rolled up into a cylindrical shape.

【符号の説明】[Explanation of symbols]

1 シート1 2 シート2 3 フィルター本体 4 補助フィルター 1 sheet 1 2 sheet 2 3 filter body 4 auxiliary filter

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 繊維状活性炭を含有するシートと,粉末
あるいは粒状活性炭と有機あるいは無機の繊維とバイン
ダーとを混合して抄紙したシートとを重ねて円筒状に巻
き上げてフィルター本体を形成し,処理液の出口側とな
る側面を繊維層で構成された補助フィルターで覆ってな
ることを特徴とする液相吸着フィルター。
1. A filter main body is formed by stacking a sheet containing fibrous activated carbon and a sheet made by mixing powdered or granular activated carbon, organic or inorganic fibers and a binder and making a paper, to form a filter body. A liquid-phase adsorption filter characterized in that the side surface on the outlet side of the liquid is covered with an auxiliary filter composed of a fiber layer.
JP905493U 1993-02-08 1993-02-08 Liquid phase adsorption filter Pending JPH0663101U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP905493U JPH0663101U (en) 1993-02-08 1993-02-08 Liquid phase adsorption filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP905493U JPH0663101U (en) 1993-02-08 1993-02-08 Liquid phase adsorption filter

Publications (1)

Publication Number Publication Date
JPH0663101U true JPH0663101U (en) 1994-09-06

Family

ID=11709924

Family Applications (1)

Application Number Title Priority Date Filing Date
JP905493U Pending JPH0663101U (en) 1993-02-08 1993-02-08 Liquid phase adsorption filter

Country Status (1)

Country Link
JP (1) JPH0663101U (en)

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