JPH0542286B2 - - Google Patents

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Publication number
JPH0542286B2
JPH0542286B2 JP61164709A JP16470986A JPH0542286B2 JP H0542286 B2 JPH0542286 B2 JP H0542286B2 JP 61164709 A JP61164709 A JP 61164709A JP 16470986 A JP16470986 A JP 16470986A JP H0542286 B2 JPH0542286 B2 JP H0542286B2
Authority
JP
Japan
Prior art keywords
ceramic porous
filtrate
filtration device
inner cylinder
flow path
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 - Fee Related
Application number
JP61164709A
Other languages
Japanese (ja)
Other versions
JPS6320011A (en
Inventor
Magoji Okamoto
Akimitsu Hiraki
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP61164709A priority Critical patent/JPS6320011A/en
Priority to US07/069,020 priority patent/US4830749A/en
Priority to EP87306203A priority patent/EP0253620B1/en
Priority to DE8787306203T priority patent/DE3783398T2/en
Publication of JPS6320011A publication Critical patent/JPS6320011A/en
Publication of JPH0542286B2 publication Critical patent/JPH0542286B2/ja
Granted legal-status Critical Current

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  • Filtering Materials (AREA)
  • Filtration Of Liquid (AREA)
  • Porous Artificial Stone Or Porous Ceramic Products (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) 本発明は複数のセラミツク多孔濾過体を用いた
濾過装置、特に原子力発電所より発生する放射能
で汚染された懸濁性物質を含む水の浄化に有用な
濾過装置に関するものである。 (従来の技術) 従来、例えば原子力発電所等より発生する使用
済炉内構造物(チヤンネルボツクス、制御棒等)
は水を充填したプール内に貯蔵されているが、放
射能で汚染された照射金属廃棄物をプール内に沈
める際にはプール水の透明度が作業上必要であ
る。そのため、プール水の一部を常時焼結金属フ
イルタからなる濾過装置で濾過浄化している。 従来使用されている浄化フイルタユニツト51
は、第4図に示すようにユニツト内に筒状の4個
の焼結金属フイルタ52が備えられ、フイルタ缶
体53によりそれらの外部を覆う構造をとつてい
る。プール内に貯蔵されている水はフイルタ缶体
53の上部入口54から供給され、各焼結金属フ
イルタ52の頂部から中心流路55を流れ、焼結
金属フイルタ52中を内部から外部に向つて流れ
ることにより濾過浄化された後出口56から排出
される。 (発明が解決しようとする問題点) しかしながら、上述した焼結金属フイルタより
なる濾過装置は、高価であるとともに寿命が短い
という問題点のほか、濾過面積が小さく、構造も
複雑であると共に重量が重い欠点もあつた。これ
らの問題点のうちいくつかのものを解消する手段
として、例えば特開昭56−148607号公報に記載さ
れたセラミツク多孔体より成る濾過装置の使用も
考えられるが、この場合はセラミツク多孔体が焼
物であるため、小型のものしか製作できず濾過面
積の大きなものは製作できない問題点があつた。 本発明の目的は上述した不具合を解消して、使
用寿命を延長できると共に軽量化を達成できしか
も低コストな濾過装置を提供しようとするもので
ある。 (問題点を解決するための手段) 本発明の濾過装置は、多数の貫通孔を平行に有
するセラミツク多孔体の各貫通孔の前端部又は後
端部を規則的に交互に密封した構造よりなるセラ
ミツク多孔濾過体と、各セラミツク多孔体を収納
する底部に段部を有しかつ段部の一側に濾液排出
口又は原液供給口を有する収納缶と、内筒と外筒
との間を縦方向に2区分して原液流路と濾液流路
を形成するとともに、その内筒中に、複数個の収
納缶を各収納缶の間にパツキングを介して液密に
積重する2重缶体とを具え、隣接する前記セラミ
ツク多孔濾過体の間に原液供給室と濾液排出室と
を交互に設け、原液供給室を前記2重缶体の内筒
と外筒との間を2区分した一方の原液流路に前記
原液供給口及び内筒を通して接続すると共に、濾
液排出室と内筒と外筒との間を2区分した他方の
濾液流路に前記濾液排出口及び内筒を通して接続
したことを特徴とするものである。 (作用) 上述した構成により、濾過されるべき原液は原
液流路から原液供給室に流入した後、多段に積み
重ねたセラミツク多孔濾過体のうち1つの濾過体
を通り抜けることにより濾過浄化され、濾液排出
室を介して2重缶体と原液流路と分離して設けた
濾液流路を通つてあるいは直接濾過装置外部へ排
出される。このとき、2重缶体内の原液流路と濾
液流路は完全に分離されているため、原液と濾液
との混合が全くなく確実に濾過浄化作業を行なう
ことができる。 また、軽量でかつ焼結金属に比べて安価なセラ
ミツク多孔濾過体を使用しているため、濾過装置
も安価でかつ軽量とすることができると共に、こ
のセラミツク多孔濾過体を複数個並列的に積み重
ねて濾過装置を形成しているため、濾過面積を極
めて大きくすることができる。 (実施例) まず、本発明で使用するセラミツク多孔濾過体
について説明する。第1図a,b,cはそれぞれ
本発明で使用するセラミツク多孔濾過体の一例を
模式的に示す入口側の側面図および縦断面図であ
る。第1図において、セラミツク多孔濾過体1は
アルミナ、ムライト、シリカ、コーデイエライト
等よりなり多数の貫通孔2を平行に有している。
各貫通孔2は、その入口側を第1図aに示すよう
に、1つおきの端部を前端又は後端でセラミツク
目封じ材3により密封している。そのため、第1
図bにおいて入口側端部4から矢印で示すように
濾過すべき原液を供給すると、セラミツク多孔質
薄壁5を通つて濾過洗浄化された後濾液は出口側
端部6の開放されている孔より排出される。 第1図cはaとは異なる形状の例を示すもの
で、セラミツク多孔体の1つの貫通孔の前端と該
貫通孔の周囲の貫通孔の後端とを規則的に交互に
密封した構造を示すのもので、その作用は前述と
同じである。 第2図aは本発明の濾過装置25の一実施例を
示す縦断面図、第2図bはそのa−a線に沿つた
断面図である。本実施例では、5個のセラミツク
多孔濾過体1を、内筒13aと外筒13bとの間
を縦方向にほぼ等分に2区分する仕切板13cに
より原液流路11と濾液流路12を形成した好ま
しくは金属よりなる2重缶体13中の内筒13a
中に収納している。収納に際し各セラミツク多孔
濾過体1は、底部に段部Aを有しかつ段部Aの一
側に原液流路11または濾液流路12と連通する
原液供給口14または濾液排出口15を有する収
納筒缶16にシール用パツキング17または保護
パツキング18を介して設けられ、この収納筒缶
16を保護パツキング18またはシール用パツキ
ング17を介して複数個積み重ねている。収納筒
缶16は金属により、またシール用パツキング1
7および保護パツキング18はゴム等の弾性体に
より作製されることが好ましい。上述したように
して各セラミツク多孔濾過体1を積み重ねて、各
セラミツク濾過体1の間に原液供給口14と連通
した原液供給室19および濾液排出口15とを連
通した濾液排出室20を交互に設ける。なお、最
下部の収納筒缶16だけは、濾液排出口を介さず
直接濾液を外部に排出している。また、積み重ね
るときに収納筒缶16に底部にOリング21を設
け、2重缶体13の内筒と収納筒缶16との間を
シールする構造となつている。2重缶体13の下
部外周にはネジ22を設け、中央部に濾液排出用
の孔23を有するフイルタ押え蓋24と係合させ
て5個のセラミツク多孔濾過体1を固定して、本
発明の濾過装置25を構成している。 上述した本発明の濾過装置25では、濾過すべ
き原液は第2図矢印で示す流路に従つて流れる。
すなわち、原液の一部は頂部より最上段のセラミ
ツク多孔体1に供給されると共に、原液流路11
と各原液供給口14を介して各原液供給室19に
供給される。そして各セラミツク多孔濾過体1で
濾過された濾液は濾液排出室20へ供給され、さ
らに濾液排出口15および濾液流路12を介して
濾過装置25の外部へ排出される。なお、最下部
のセラミツク多孔濾過体1を通つた濾液は直接孔
23を通して濾過装置25の外部へ排出される。 第3図は本発明の濾過装置25を使用した実際
のフイルタユニツト30の一実施例を示す線図で
ある。第3図に示すように、4個の濾過装置25
のそれぞれをユニツト押えバネ31によりユニツ
ト蓋32に取り付けると共に、フイルタ缶体33
によりそれらの外部を覆つてフイルタユニツト3
0を形成している。このフイルタユニツト30の
入口34からの原液を供給すると、出口35から
濾過された濾液が排出される。 上述した本発明の濾過装置のうちセラミツク多
孔濾過体が第2図に図示する5段のものと、比較
のため第4図に示す従来の焼結金属によるフイル
タを使用したフイルタユニツトをそれぞれ作製し
て種々の性能を比較測定した。結果を第1表に示
す。
(Industrial Application Field) The present invention relates to a filtration device using a plurality of ceramic porous filters, and particularly to a filtration device useful for purifying water containing suspended matter contaminated with radioactivity generated from nuclear power plants. It is something. (Conventional technology) Conventionally, spent reactor internals (channel boxes, control rods, etc.) generated from nuclear power plants, etc.
is stored in a pool filled with water, but when irradiated metal waste contaminated with radioactivity is submerged in the pool, transparency of the pool water is necessary for work. Therefore, a portion of the pool water is constantly filtered and purified using a filtration device consisting of a sintered metal filter. Conventionally used purification filter unit 51
As shown in FIG. 4, four cylindrical sintered metal filters 52 are provided in the unit, and the outside of the filter is covered with a filter can 53. Water stored in the pool is supplied from the upper inlet 54 of the filter body 53, flows from the top of each sintered metal filter 52 through the central channel 55, and flows through the sintered metal filter 52 from the inside to the outside. After being filtered and purified by flowing, it is discharged from the outlet 56. (Problems to be Solved by the Invention) However, the above-mentioned filtration device made of a sintered metal filter has problems that it is expensive and has a short lifespan, as well as a small filtration area, a complicated structure, and a high weight. There were also serious drawbacks. As a means to solve some of these problems, it is possible to use a filtration device made of a ceramic porous body, as described in Japanese Patent Application Laid-open No. 56-148607, but in this case, the ceramic porous body is Since it is a pottery product, there was a problem that only small-sized products could be manufactured, and it was not possible to manufacture products with a large filtration area. SUMMARY OF THE INVENTION An object of the present invention is to eliminate the above-mentioned problems and to provide a filtration device that can extend its service life, reduce its weight, and be inexpensive. (Means for Solving the Problems) The filtration device of the present invention has a structure in which the front end or the rear end of each through hole of a ceramic porous body having a large number of parallel through holes is regularly and alternately sealed. A ceramic porous filter body, a storage can having a step at the bottom for storing each ceramic porous body and having a filtrate discharge port or stock solution supply port on one side of the step, and a vertical pipe between the inner cylinder and the outer cylinder. A double can body that is divided into two in the direction to form a raw solution flow path and a filtrate flow path, and in which a plurality of storage cans are stacked liquid-tightly with packing between each storage can. A stock solution supply chamber and a filtrate discharge chamber are provided alternately between the adjacent ceramic porous filter bodies, and the stock solution supply chamber is one of two sections divided between the inner cylinder and the outer cylinder of the double can body. It is connected to the stock solution flow path through the stock solution supply port and the inner cylinder, and is connected to the other filtrate flow path that is divided into two parts between the filtrate discharge chamber, the inner cylinder, and the outer cylinder through the filtrate discharge port and the inner cylinder. This is a characteristic feature. (Function) With the above-described configuration, the stock solution to be filtered flows into the stock solution supply chamber from the stock solution flow path, and then is filtered and purified by passing through one of the ceramic porous filters stacked in multiple stages, and the filtrate is discharged. The filtrate is directly discharged to the outside of the filtration device through a filtrate flow path that is separated from the double can body and the stock solution flow path via a chamber. At this time, since the stock solution channel and the filtrate channel in the double can are completely separated, there is no mixing of the stock solution and the filtrate, and the filtration and purification work can be performed reliably. In addition, since we use ceramic porous filters that are lightweight and cheaper than sintered metals, the filtration device can be made inexpensive and lightweight, and multiple ceramic porous filters can be stacked in parallel. Since the filtration device is formed by using multiple filters, the filtration area can be made extremely large. (Example) First, the ceramic porous filter used in the present invention will be explained. FIGS. 1a, 1b, and 1c are a side view and a vertical cross-sectional view, respectively, of the inlet side schematically showing an example of a ceramic porous filter used in the present invention. In FIG. 1, a ceramic porous filter body 1 is made of alumina, mullite, silica, cordierite, etc. and has a large number of through holes 2 arranged in parallel.
As shown in FIG. 1a, the entrance side of each through hole 2 is sealed at every other end with a ceramic sealing material 3 at the front end or the rear end. Therefore, the first
When the stock solution to be filtered is supplied from the inlet end 4 as shown by the arrow in FIG. more excreted. Fig. 1c shows an example of a shape different from that shown in a, which has a structure in which the front end of one through hole of the ceramic porous body and the rear end of the surrounding through holes are regularly and alternately sealed. The operation is the same as described above. FIG. 2a is a longitudinal cross-sectional view showing one embodiment of the filtering device 25 of the present invention, and FIG. 2b is a cross-sectional view taken along line a-a. In this embodiment, the five ceramic porous filters 1 are divided into the stock solution flow path 11 and the filtrate flow path 12 by a partition plate 13c that divides the inner cylinder 13a and the outer cylinder 13b into two almost equal parts in the vertical direction. Inner cylinder 13a in the formed double can body 13 preferably made of metal
It is stored inside. When stored, each ceramic porous filter 1 has a step A at the bottom and a stock solution supply port 14 or filtrate discharge port 15 on one side of the step A that communicates with the stock solution flow path 11 or the filtrate flow path 12. It is provided on the cylindrical can 16 via a sealing packing 17 or a protective packing 18, and a plurality of storage cylindrical cans 16 are stacked with the protective packing 18 or sealing packing 17 interposed therebetween. The storage cylinder can 16 is made of metal and has a sealing packing 1.
7 and the protective packing 18 are preferably made of an elastic body such as rubber. As described above, the ceramic porous filter bodies 1 are stacked, and between each ceramic filter body 1, a stock solution supply chamber 19 that communicates with the stock solution supply port 14 and a filtrate discharge chamber 20 that communicates with the filtrate discharge port 15 are arranged alternately. establish. Note that only the lowermost storage cylinder can 16 directly discharges the filtrate to the outside without going through the filtrate discharge port. Further, when stacking the storage cylinder cans 16, an O-ring 21 is provided at the bottom of the storage cylinder cans 16 to seal between the inner cylinder of the double can body 13 and the storage cylinder cans 16. A screw 22 is provided on the outer periphery of the lower part of the double can body 13, and is engaged with a filter holding lid 24 having a hole 23 for discharging filtrate in the center to fix the five ceramic porous filter bodies 1. The filtration device 25 is configured as follows. In the above-described filtering device 25 of the present invention, the stock solution to be filtered flows along the flow path indicated by the arrow in FIG.
That is, a part of the stock solution is supplied from the top to the uppermost ceramic porous body 1, and a part of the stock solution is supplied from the top to the top ceramic porous body 1, and the stock solution flow path 11
and are supplied to each stock solution supply chamber 19 via each stock solution supply port 14. The filtrate filtered through each ceramic porous filter body 1 is supplied to the filtrate discharge chamber 20, and is further discharged to the outside of the filtration device 25 through the filtrate discharge port 15 and the filtrate channel 12. The filtrate that has passed through the lowest ceramic porous filter 1 is directly discharged to the outside of the filtration device 25 through the holes 23. FIG. 3 is a diagram showing one embodiment of an actual filter unit 30 using the filtration device 25 of the present invention. As shown in FIG.
are attached to the unit lid 32 by the unit presser spring 31, and the filter can body 33
cover the outside of the filter unit 3.
0 is formed. When the stock solution is supplied from the inlet 34 of the filter unit 30, the filtered filtrate is discharged from the outlet 35. Among the filtration devices of the present invention described above, a five-stage ceramic porous filter shown in FIG. 2 and a filter unit using a conventional sintered metal filter shown in FIG. 4 for comparison were fabricated. We compared and measured various performances. The results are shown in Table 1.

【表】【table】

【表】 第1表から明らかなように、従来の焼結金属を
フイルタエレメントとするものと比較して本発明
のセラミツク多孔濾過体は、エレメントの比濾過
面積が大きく、またそれぞれ4個の濾過装置とし
て構成したフイルタユニツトの重量が軽く総濾過
面積も大きく、フイルタユニツトとしての性能が
格段に上昇していることがわかる。また、濾過停
止差圧3.5Kg/cm2になるまでの寿命も延長できる
ことがわかつた。 本発明は上述した実施例にのみ限定されるもの
ではなく、幾多の変形、変更が可能である。例え
ばセラミツク多孔体の前端部又は後端部を第1図
aおよびc以外の異なる形状に規則的に交互に密
封閉鎖することもできる。 (発明の効果) 以上詳細に説明したところから明らかなよう
に、本発明の濾過装置によれば、濾過体として複
数個のセラミツク多孔濾過体を多段にして使用し
ているため、従来の焼結金属のフイルタと比較し
て濾過面積が大きく、軽量であり、かつコストも
安価で寿命の延長が可能な濾過装置を得ることが
できる。そのため、この濾過装置を使用したフイ
ルタユニツトも軽量で安価なものとなり、特に原
子力発電所の放射能で汚染された水の浄化装置と
して有用である。
[Table] As is clear from Table 1, compared to conventional filter elements made of sintered metal, the ceramic porous filter of the present invention has a larger specific filtration area of the elements, and each element has four filter elements. It can be seen that the weight of the filter unit constructed as an apparatus is light and the total filtration area is large, and the performance as a filter unit is significantly improved. It was also found that the service life until the filtration stop differential pressure reached 3.5 Kg/cm 2 could be extended. The present invention is not limited only to the embodiments described above, and numerous modifications and changes are possible. For example, the front end or the rear end of the ceramic porous body can be regularly and alternately hermetically sealed in different shapes other than those in FIGS. 1a and 1c. (Effects of the Invention) As is clear from the detailed explanation above, according to the filtration device of the present invention, a plurality of ceramic porous filter bodies are used in multiple stages as the filter body, so that the conventional sintering It is possible to obtain a filtration device that has a larger filtration area than a metal filter, is lightweight, is inexpensive, and has an extended lifespan. Therefore, a filter unit using this filtration device is also lightweight and inexpensive, and is particularly useful as a purification device for water contaminated with radioactivity in nuclear power plants.

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

第1図a,b,cはセラミツク多孔濾過体を模
式的に示す入口側の側面図および縦断面図、第2
図は本発明の濾過装置の一実施例を示す縦断面
図、第3図は本発明の濾過装置を使用した実際の
フイルタユニツトの一実施例を示す線図、第4図
は従来のフイルタユニツトの一実施例を示す線図
である。 1……セラミツク多孔濾過体、2……貫通孔、
3……セラミツク目封じ材、4……入口側端部、
5……多孔質薄壁、6……出口側端部、11……
原液流路、12……濾液流路、13……2重缶
体、14……原液供給口、15……濾液排出口、
16……収納筒缶、17……シール用パツキン
グ、18……保護パツキング、19……原液供給
室、20……濾液排出室、21……Oリング、2
2……ネジ、23……孔、24……フイルタ押え
蓋、25……濾過装置、30……フイルタユニツ
ト、31……ユニツト押えバネ、32……ユニツ
ト蓋、33……フイルタ缶体、34……入口、3
5……出口。
Figures 1 a, b, and c schematically show a side view and longitudinal sectional view of the inlet side of a ceramic porous filter;
The figure is a longitudinal sectional view showing one embodiment of the filtration device of the present invention, FIG. 3 is a line diagram showing one embodiment of an actual filter unit using the filtration device of the present invention, and FIG. 4 is a diagram of a conventional filter unit. It is a line diagram showing one example of. 1... Ceramic porous filter body, 2... Through holes,
3... Ceramic sealing material, 4... Inlet side end,
5... Porous thin wall, 6... Outlet side end, 11...
Raw solution flow path, 12... Filtrate flow path, 13... Double can body, 14... Raw solution supply port, 15... Filtrate discharge port,
16... Storage cylinder can, 17... Seal packing, 18... Protection packing, 19... Raw solution supply chamber, 20... Filtrate discharge chamber, 21... O ring, 2
2... Screw, 23... Hole, 24... Filter holding lid, 25... Filtration device, 30... Filter unit, 31... Unit holding spring, 32... Unit lid, 33... Filter can body, 34 ...Entrance, 3
5...Exit.

Claims (1)

【特許請求の範囲】 1 多数の貫通孔を平行に有するセラミツク多孔
体の各貫通孔の前端部又は後端部を規則的に交互
に密封した構造よりなるセミツク多孔濾過体と、
各セラミツク多孔体を収納する底部に段部を有し
かつ段部の一側に濾液排出口又は原液供給口を有
する収納缶と、内筒と外筒との間を縦方向に2区
分して原液流路と濾液流路を形成するとともに、
その内筒中に、複数個の収納缶を各収納缶の間に
パツキングを介して液密に積重する2重缶体とを
具え、隣接する前記セラミツク多孔濾過体の間に
原液供給室と濾液排出室とを交互に設け、原液供
給室を前記2重缶体の内筒と外筒との間を2区分
した一方の原液流路に前記原液供給口及び内筒を
通して接続すると共に、濾液排出室を内筒と外筒
との間を2区分した他方の濾液流路に前記濾液排
出口及び内筒を通して接続したことを特徴とする
濾過装置。 2 セラミツク多孔濾過体が、セラミツク多孔体
の各貫通孔のうち1つおきの貫通孔の端部を前端
又は後端で交互に密封した構造よりなる特許請求
の範囲第1項記載の濾過装置。 3 セラミツク多孔濾過体が、セラミツク多孔体
の1つの貫通孔の前端と、該貫通孔の周囲の貫通
孔の後端とを交互に密封した構造よりなる特許請
求の範囲第1項記載の濾過装置。 4 前記パツキングがゴム等の弾性体よりなる特
許請求の範囲第1項記載の濾過装置。 5 前記原液流路と濾液流路とが前記セラミツク
多孔濾過体を包む形態に内筒と外筒との間に対向
するよう2区分されている特許請求の範囲第1項
記載の濾過装置。
[Scope of Claims] 1. A ceramic porous filter body having a structure in which the front end or rear end of each through hole of a ceramic porous body having a large number of parallel through holes is regularly and alternately sealed;
A storage can having a step at the bottom for storing each ceramic porous body and a filtrate discharge port or stock solution supply port on one side of the step, and an inner cylinder and an outer cylinder are divided into two in the vertical direction. In addition to forming the stock solution flow path and the filtrate flow path,
The inner cylinder is provided with a double can body in which a plurality of storage cans are liquid-tightly stacked with packing between each storage can, and a stock solution supply chamber and a filtrate supply chamber are provided between the adjacent ceramic porous filter bodies. Discharge chambers are provided alternately, and the concentrate supply chamber is connected through the concentrate supply port and the inner cylinder to one of the concentrate flow paths divided into two between the inner cylinder and the outer cylinder of the double can body, and the filtrate is discharged. A filtration device characterized in that the chamber is connected to the other filtrate flow path which is divided into two parts between the inner cylinder and the outer cylinder through the filtrate outlet and the inner cylinder. 2. The filtration device according to claim 1, wherein the ceramic porous filter body has a structure in which the ends of every other through hole among the through holes of the ceramic porous body are alternately sealed at the front end or the rear end. 3. The filtration device according to claim 1, wherein the ceramic porous filter body has a structure in which the front end of one through-hole of the ceramic porous body and the rear end of the through-holes surrounding the through-hole are alternately sealed. . 4. The filtration device according to claim 1, wherein the packing is made of an elastic body such as rubber. 5. The filtration device according to claim 1, wherein the raw solution flow path and the filtrate flow path are divided into two sections facing each other between an inner cylinder and an outer cylinder so as to surround the ceramic porous filter body.
JP61164709A 1986-07-15 1986-07-15 Filter device Granted JPS6320011A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP61164709A JPS6320011A (en) 1986-07-15 1986-07-15 Filter device
US07/069,020 US4830749A (en) 1986-07-15 1987-07-01 Liquid waste filtering apparatus
EP87306203A EP0253620B1 (en) 1986-07-15 1987-07-14 Filter apparatus
DE8787306203T DE3783398T2 (en) 1986-07-15 1987-07-14 FILTER SYSTEM.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61164709A JPS6320011A (en) 1986-07-15 1986-07-15 Filter device

Publications (2)

Publication Number Publication Date
JPS6320011A JPS6320011A (en) 1988-01-27
JPH0542286B2 true JPH0542286B2 (en) 1993-06-28

Family

ID=15798391

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61164709A Granted JPS6320011A (en) 1986-07-15 1986-07-15 Filter device

Country Status (1)

Country Link
JP (1) JPS6320011A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100967169B1 (en) 2010-02-25 2010-07-05 주식회사성우 Filter apparatus for water-treatment system

Also Published As

Publication number Publication date
JPS6320011A (en) 1988-01-27

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