JPH04892Y2 - - Google Patents

Info

Publication number
JPH04892Y2
JPH04892Y2 JP16731185U JP16731185U JPH04892Y2 JP H04892 Y2 JPH04892 Y2 JP H04892Y2 JP 16731185 U JP16731185 U JP 16731185U JP 16731185 U JP16731185 U JP 16731185U JP H04892 Y2 JPH04892 Y2 JP H04892Y2
Authority
JP
Japan
Prior art keywords
holes
honeycomb structure
partition wall
porous honeycomb
permeate
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.)
Expired
Application number
JP16731185U
Other languages
Japanese (ja)
Other versions
JPS6275803U (en
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 filed Critical
Priority to JP16731185U priority Critical patent/JPH04892Y2/ja
Publication of JPS6275803U publication Critical patent/JPS6275803U/ja
Application granted granted Critical
Publication of JPH04892Y2 publication Critical patent/JPH04892Y2/ja
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は限外濾過、精密濾過によつて流体と流
体中の特定成分とを分離する為に膜分離装置内に
使用されるセラミツクフイルターに関するもので
ある。
[Detailed description of the invention] [Field of industrial application] The present invention relates to a ceramic filter used in a membrane separation device to separate a fluid from a specific component in the fluid by ultrafiltration or precision filtration. It is something.

〔従来技術及びその問題点〕[Prior art and its problems]

従来、セラミツクフイルターはセラミツク製の
管状分離膜群両端をOリングや接着剤を介して固
定用管板に固定することによつて集積化されてい
た。
Conventionally, ceramic filters have been integrated by fixing both ends of a group of ceramic tubular separation membranes to a fixing tube plate via O-rings or adhesives.

ところが、斯る従来例の場合、下記の問題点が
ある。
However, in the case of such a conventional example, there are the following problems.

固定用管板に管状分離膜を嵌合させる嵌合口
若しくは連通口を開口する際、嵌合口や連通口
相互を近接して開口するのが難かしく、その数
には制限がある為、管状分離膜群をコンパクト
に集積できず、膜分離装置内に装備するに際し
て単位容積あたりの膜面積が大きくできず、濾
過効率の向上が望めない。
When opening the fitting ports or communication ports for fitting the tubular separation membrane to the fixing tube plate, it is difficult to open the fitting ports or communication ports close to each other, and there is a limit to the number of ports, so tubular separation Membranes cannot be assembled compactly, and the membrane area per unit volume cannot be increased when installed in a membrane separation device, making it impossible to expect improvement in filtration efficiency.

管状分離膜個々を固定用管板に嵌合固定する
作業や内部流路と連通孔とを合致させる位置合
わせ作業が面倒である。
The work of fitting and fixing each tubular separation membrane to the fixing tube plate and the positioning work of matching the internal channels and the communication holes are troublesome.

そこで、今日、上記する従来例を解決する為に
特開昭56−129020号公報のものが開発された。
Therefore, in order to solve the above-mentioned conventional problem, the one disclosed in Japanese Patent Application Laid-open No. 129020/1983 has been developed.

この改良例は第5図に示すように単位容積あた
りの膜面積が大きく且つモジユール化が容易な多
数の貫通孔101を有する多孔質ハニカム構造体
100内の少なくとも一辺の隔壁101′を共有
する貫通孔101,101相互において一方の貫
通孔101は一端を、他方の貫通孔101は他端
を夫々封止して一方を原液流路102、他方を透
過液流路103としたものである。
As shown in FIG. 5, this improved example is a porous honeycomb structure 100 having a large membrane area per unit volume and a large number of through holes 101 that can be easily modularized. Regarding the holes 101 and 101, one end of one through hole 101 and the other end of the other through hole 101 are sealed, respectively, so that one end becomes a stock solution flow path 102 and the other end becomes a permeate flow path 103.

しかし乍ら、斯る改良例の場合、原液流路10
2は一端、即ち出口端を封止した構造となるか
ら、クロス・フロー濾過方法が採用できず全濾過
方法になるので透過を制限された成分が膜面にゲ
ル化、付着・成長して急速に透過流束が減衰し、
濾過効率の急激な低下を招くばかりでなく、逆流
によつてゲル層の除去を実施する際、原液流路1
02は一端を閉口している為、その封止端近傍の
隔壁面に付着したゲル層の除去が確実ではない問
題点を有する。
However, in the case of such an improved example, the stock solution flow path 10
2 has a structure in which one end, that is, the outlet end, is sealed, so a cross-flow filtration method cannot be adopted and a total filtration method is used. Therefore, components whose permeation is restricted gel, adhere, and grow on the membrane surface and rapidly The permeation flux is attenuated to
Not only will this result in a rapid decrease in filtration efficiency, but also when removing the gel layer by backflow,
Since 02 has one end closed, there is a problem in that the gel layer attached to the partition surface near the sealed end cannot be removed reliably.

「考案が解決しようとする問題点〕 本考案が解決しようとする問題点は多孔質のハ
ニカム構造体でありながら濾過効率が高いクロ
ス・フローの濾過方法を採用でき、しかも逆洗効
率のアツプを期待できるセラミツクフイルターを
供することにある。
``Problems to be solved by this invention'' The problems to be solved by this invention are that it is possible to adopt a cross-flow filtration method with high filtration efficiency even though it is a porous honeycomb structure, and to increase backwashing efficiency. Our goal is to provide ceramic filters that can be expected.

〔問題点を解決する為の手段〕[Means for solving problems]

上記問題点を解決する為に講じた技術的手段
は、多数の貫通孔を有する多孔質ハニカム構造体
内の少なくとも一辺の隔壁を共有して隣接する貫
通孔相互において、一方の貫通孔両端を閉塞する
ことにより貫通孔で構成される原液流路に隣接し
て透過液室を形成し、該透過液室夫々を、共有す
る隔壁を介して多孔質ハニカム構造体の外壁に至
るまで連続状に配置し、その透過液室相互の共有
する隔壁と多孔質ハニカム構造体の外壁に連通孔
を開孔して透過液排出流路を形成したことであ
る。
The technical means taken to solve the above problem is to close both ends of one of the through holes in which adjacent through holes share at least one side partition wall in a porous honeycomb structure having a large number of through holes. By this, a permeated liquid chamber is formed adjacent to the raw liquid flow path constituted by the through hole, and each of the permeated liquid chambers is arranged in a continuous manner up to the outer wall of the porous honeycomb structure via a shared partition wall. , a communication hole is formed in the partition wall shared between the permeate chambers and the outer wall of the porous honeycomb structure to form a permeate discharge flow path.

〔作 用〕[Effect]

本考案の技術的手段による作用は原液を、貫通
孔によつて構成された原液流路内に流通させる一
方、透過液を原液流路の隔壁を介して隣接し且つ
貫通孔両端を閉塞して形成した透過液室内に流入
せしめ、透過液室相互の共有する隔壁に開孔した
連通孔によつて形成された透過液排出流路からハ
ニカム構造体外部へ排出する。
The effect of the technical means of the present invention is to allow the stock solution to flow through the stock solution flow path formed by the through-hole, while the permeate is passed through the stock solution flow path adjacent to the stock solution flow path through the partition wall, and by closing both ends of the through-hole. The permeate flows into the formed permeate chambers and is discharged to the outside of the honeycomb structure from a permeate discharge channel formed by a communication hole opened in a partition wall shared between the permeate chambers.

逆洗時には透過液排出流路から洗浄水を流入さ
せて原液流路を形成する隔壁に付着したゲル層を
剥離せしめ、両開放端から排出する。
During backwashing, washing water is introduced from the permeate discharge channel to peel off the gel layer adhering to the partition wall forming the stock solution channel, and is discharged from both open ends.

〔実施例〕〔Example〕

次に本考案の実施例を図面と共に説明する。 Next, embodiments of the present invention will be described with reference to the drawings.

多孔質ハニカム構造体Aは所望形状の多数の貫
通孔1を有し、隔壁1′を0.01〜10μmの平均気孔
径で10〜60%の気孔率を有するように成形したセ
ラミツク製の多孔質体であり、このハニカム構造
体Aに原液流路2、透過液室3、透過液排出流路
4、を形成する。
The porous honeycomb structure A is a ceramic porous body having a large number of through holes 1 of a desired shape, and having partition walls 1' having an average pore diameter of 0.01 to 10 μm and a porosity of 10 to 60%. In this honeycomb structure A, a raw solution channel 2, a permeate chamber 3, and a permeate discharge channel 4 are formed.

透過液室3は上記ハニカム構造体Aの少なくと
も一辺の隔壁1′を共有した隣接する貫通孔1,
1相互において、一方の貫通孔1両端を封止部材
6で閉塞し、貫通孔1によつて構成された原液流
路2に隣接して形成する。
The permeate chamber 3 includes adjacent through holes 1 that share a partition wall 1' on at least one side of the honeycomb structure A,
1, both ends of one through hole 1 are closed with a sealing member 6, and are formed adjacent to the stock solution flow path 2 constituted by the through hole 1.

また、透過液室3,3は夫々共有する隔壁3′
部分を介して多孔質ハニカム構造体Aの外壁a1
至るまで連続するように配置し、透過液排出流路
4を介して内部の透過液を外部へ排出するように
する。
Further, the permeate chambers 3 and 3 each have a common partition wall 3'.
The porous honeycomb structure A is disposed so as to be continuous up to the outer wall a1 of the porous honeycomb structure A, and the permeate inside is discharged to the outside via the permeate discharge channel 4.

その透過液室3の配置パターンは第1図のL字
模様、第3図の市松模様、第4図の列模様等、共
有する夫々隔壁3′を介して多孔質ハニカム構造
体Aの外壁、a1に至るまで連続するように配置す
るパターンであれば、配置パターンは限定されな
い。
The arrangement pattern of the permeate chamber 3 is the L-shaped pattern shown in FIG. 1, the checkered pattern shown in FIG. 3, the row pattern shown in FIG. The arrangement pattern is not limited as long as it is arranged continuously up to a 1 .

透過液排出流路4は前記パターンに配置された
透過液室3,3相互の共有する隔壁3′と多孔質
ハニカム構造体Aの外壁a1に連通孔5を開孔する
ことによつて形成する。
The permeated liquid discharge channel 4 is formed by opening a communication hole 5 in the partition wall 3' shared by the permeated liquid chambers 3 and 3 arranged in the pattern and the outer wall a1 of the porous honeycomb structure A. do.

透過液室3の両端を封止する封止部材6は多孔
質ハニカム構造体Aと同質のセラミツク材料、ガ
ラス、樹脂等が挙げられる。
The sealing member 6 that seals both ends of the permeated liquid chamber 3 may be made of the same ceramic material as the porous honeycomb structure A, glass, resin, or the like.

尚、図面では貫通孔1形状を四角形としたが、
円形やその他の形状を選定することは任意であ
り、透過液排出流路4の形状個数は隔壁1′(膜)
の透過性能等との関連から設定する。
In addition, in the drawing, the shape of the through hole is square, but
It is optional to select a circular or other shape, and the number of shapes of the permeate discharge channel 4 is determined by the partition wall 1' (membrane).
It is set in relation to the transmission performance, etc.

〔考案の効果〕[Effect of idea]

本考案は以上のように構成したので、単位容積
あたりの膜面積が大きく且つモジユール化が容易
なハニカム構造体を用いながらクロス・フロー濾
過方式を実現して高い膜透過性能を付与できる。
しかも、原液流路は貫通孔で構成されているから
目詰りを起こしても、逆洗等で容易に初期の膜透
過性能に復元できる。
Since the present invention is constructed as described above, it is possible to realize a cross-flow filtration system and provide high membrane permeation performance while using a honeycomb structure that has a large membrane area per unit volume and is easy to modularize.
Moreover, since the stock solution channel is composed of through-holes, even if it becomes clogged, it can be easily restored to its initial membrane permeation performance by backwashing or the like.

依つて、所期の目的を達成できる。 Thus, the intended purpose can be achieved.

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

図面は本考案セラミツクフイルターの実施例を
示し、第1図は正面断面図、第2図は2−2断面
図、第3図、第4図は他の実施例の正面断面図、
第5図は従来例の部分拡大断面図である。 尚、図中、A……多孔質ハニカム構造体、1…
…貫通孔、1′……隔壁、2……原液流路、3…
…透過液室、5……連通孔、4……透過液排出通
路、a1……多孔質ハニカム構造体の外壁、3′…
…透過液室の隔壁、6……封止部材。
The drawings show embodiments of the ceramic filter of the present invention; FIG. 1 is a front sectional view, FIG. 2 is a 2-2 sectional view, and FIGS. 3 and 4 are front sectional views of other embodiments.
FIG. 5 is a partially enlarged sectional view of a conventional example. In the figure, A... porous honeycomb structure, 1...
...through hole, 1'... partition wall, 2... stock solution flow path, 3...
... Permeated liquid chamber, 5... Communication hole, 4... Permeated liquid discharge passage, a 1 ... Outer wall of porous honeycomb structure, 3'...
...Partition wall of permeated liquid chamber, 6...Sealing member.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 多数の貫通孔を有する多孔質ハニカム構造体内
の少なくとも一辺の隔壁を共有して隣接する貫通
孔相互において、一方の貫通孔両端を閉塞するこ
とにより貫通孔で構成される原液流路に隣接して
透過液室を形成し、該透過液室夫々を、共有する
隔壁を介して多孔質ハニカム構造体の外壁に至る
まで連続状に配置し、その透過液室相互の共有す
る隔壁と多孔質ハニカム構造体の外壁に連通孔を
開孔して透過液排出流路を形成してなるセラミツ
クフイルター。
In a porous honeycomb structure having a large number of through holes, adjacent through holes that share a partition wall on at least one side are closed at both ends of one of the through holes, so that the through holes are adjacent to the stock solution flow path formed by the through holes. A permeated liquid chamber is formed, and each of the permeated liquid chambers is arranged in a continuous manner up to the outer wall of the porous honeycomb structure via a shared partition wall, and the permeated liquid chambers are arranged in a continuous manner through a shared partition wall and the porous honeycomb structure. A ceramic filter with communication holes formed in the outer wall of the body to form a permeate discharge channel.
JP16731185U 1985-10-30 1985-10-30 Expired JPH04892Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16731185U JPH04892Y2 (en) 1985-10-30 1985-10-30

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16731185U JPH04892Y2 (en) 1985-10-30 1985-10-30

Publications (2)

Publication Number Publication Date
JPS6275803U JPS6275803U (en) 1987-05-15
JPH04892Y2 true JPH04892Y2 (en) 1992-01-13

Family

ID=31099124

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16731185U Expired JPH04892Y2 (en) 1985-10-30 1985-10-30

Country Status (1)

Country Link
JP (1) JPH04892Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8465648B2 (en) 2009-05-18 2013-06-18 Ngk Insulators, Ltd. Ceramic pervaporation membrane and ceramic vapor-permeable membrane

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4094771B2 (en) * 1999-06-08 2008-06-04 日本碍子株式会社 Ceramic filter substrate and method for producing the same
JP2002166115A (en) * 2000-12-04 2002-06-11 Ngk Insulators Ltd Filter element and method for manufacturing the same
WO2014119742A1 (en) * 2013-02-01 2014-08-07 日本碍子株式会社 Method for using ceramic filter, and filter device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8465648B2 (en) 2009-05-18 2013-06-18 Ngk Insulators, Ltd. Ceramic pervaporation membrane and ceramic vapor-permeable membrane

Also Published As

Publication number Publication date
JPS6275803U (en) 1987-05-15

Similar Documents

Publication Publication Date Title
KR100732436B1 (en) Membrane filter for water treatment
US5009781A (en) Cross-flow filtration device with filtrate network and method of forming same
US4707268A (en) Hollow fiber potted microfilter
US4244820A (en) Fluid purification system
JPH04892Y2 (en)
US4869822A (en) Filter apparatus employing hollow fibers
WO1984001522A1 (en) Filter
JPH0575449B2 (en)
US4919805A (en) Vertical leaf filter flush
JPH04893Y2 (en)
JP4358538B2 (en) Ceramic filter
EP2415514B1 (en) Membrane plates separation device
JPS5982906A (en) Sheetlike separating membrane element and separating membrane module
JP2004524140A (en) Hollow fiber membrane cassette
JP2004081942A (en) Filtering method using ceramic membrane module
JP2004524140A5 (en)
JPH11169681A (en) Monolithic ceramic filter device
US20040045890A1 (en) Hollow fiber membrane cassette
JPS6320003A (en) Precision filter
JP2000079329A (en) Filter membrane module
RU2262978C2 (en) Diaphragm ultra-microfiltration roll material and method of restoration of its serviceability
JP3008945B1 (en) Combined filtration module and filtration method
JP4020510B2 (en) Tank type filtration device
JPS62197108A (en) Hollow yarn membrane
JPH11137974A (en) Spiral membrane element