JPH0245559B2 - - Google Patents

Info

Publication number
JPH0245559B2
JPH0245559B2 JP58237825A JP23782583A JPH0245559B2 JP H0245559 B2 JPH0245559 B2 JP H0245559B2 JP 58237825 A JP58237825 A JP 58237825A JP 23782583 A JP23782583 A JP 23782583A JP H0245559 B2 JPH0245559 B2 JP H0245559B2
Authority
JP
Japan
Prior art keywords
sludge
cloth
endless
pressure
forming machine
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 - Lifetime
Application number
JP58237825A
Other languages
Japanese (ja)
Other versions
JPS60130498A (en
Inventor
Kyoshi Uyama
Yoshio Sugano
Kyoteru Segawa
Yasuhiko Kihara
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.)
JFE Engineering Corp
Original Assignee
Nippon Kokan 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 Nippon Kokan Ltd filed Critical Nippon Kokan Ltd
Priority to JP58237825A priority Critical patent/JPS60130498A/en
Publication of JPS60130498A publication Critical patent/JPS60130498A/en
Publication of JPH0245559B2 publication Critical patent/JPH0245559B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/04Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams
    • B30B9/10Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams without use of a casing
    • B30B9/105Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams without use of a casing using a press ram co-operating with an intermittently moved endless conveyor

Description

【発明の詳細な説明】 この発明は脱水機に関する。[Detailed description of the invention] This invention relates to a dehydrator.

汚水処理設備等で発生した含水汚泥を脱水する
装置として、代表的なものにベルトプレス式のも
のとフイルタープレス式のものが知られている。
As devices for dewatering water-containing sludge generated in sewage treatment facilities, etc., belt press type devices and filter press type devices are known as typical devices.

ベルトプレス式は走行する一対の布に汚泥を
挟みロールに連続的に巻きつけることにより脱水
を行う構成のものである。このベルトプレス式の
場合、連続脱水できるため処理能力が大きいが、
圧搾圧力が小さいため脱水ケーキ含水率が高い欠
点がある。
The belt press type has a structure in which sludge is sandwiched between a pair of running cloths and dewatered by continuously winding the sludge around a roll. This belt press type has a large processing capacity because it can perform continuous dehydration, but
The drawback is that the water content of the dehydrated cake is high because the pressing pressure is low.

一方、フイルタープレス式は加圧室に汚泥を封
入し高圧力をかけて脱水した後、該加圧室を開け
て脱水ケーキを排出する構成のものである。この
構成の場合、圧搾圧力を大きくとることができる
が、脱水を連続的に行うことができずバツチ処理
となるため処理能力が小さい欠点がある。
On the other hand, the filter press type has a structure in which sludge is sealed in a pressurizing chamber, dehydrated by applying high pressure, and then the pressurizing chamber is opened to discharge the dehydrated cake. In the case of this configuration, a large squeezing pressure can be obtained, but dehydration cannot be performed continuously and batch processing is required, so there is a drawback that the processing capacity is low.

本発明は上記した従来のベルトプレス式とフイ
ルタープレス式の欠点を解消し、圧搾圧力が大き
くしかも連続的に処理することができ、また全体
の脱水効率も高い脱水機を提供しようとするもの
で、その基本的特徴とするところは、高含水汚泥
を一次的に脱水する重力脱水部と、凹凸歯を持つ
た1対のロールを有し、前記重力脱水部から排出
かれる汚泥を受けこれをウドン状に形成排出すべ
く、重力脱水部汚泥排出側に設けられる形成機
と、該形成機側から排出される汚泥を受ける第1
のエンドレス布及び該第1のエンドレス布と
の間で汚泥を挟む第2のエンドレス布からなる
1対のエンドレス布と、形成機から排出される
汚泥を受け、これを第1のエンドレス布上に落
下供給すべく、形成機と第1のエンドレス布と
の間に、第1のエンドレス布長手方向に対し水
平移動可能に配される移動コンベアと、1対のエ
ンドレス布に挟まれた汚泥を圧力板により高圧
で圧搾脱水する高圧脱水機構と、該高圧脱水機構
による圧搾脱水時には前記布の移動を停止し非
圧搾脱水時には前記布を移動させる駆動機構と
を有することにある。
The present invention aims to eliminate the drawbacks of the conventional belt press type and filter press type described above, and to provide a dewatering machine that has a large squeezing pressure, can process continuously, and has a high overall dewatering efficiency. Its basic features include a gravity dewatering section that primarily dehydrates high water content sludge, and a pair of rolls with uneven teeth, which receive the sludge discharged from the gravity dewatering section and process it into udon. A forming machine is installed on the sludge discharge side of the gravity dewatering section in order to form and discharge the sludge into a shape.
a pair of endless cloths consisting of an endless cloth and a second endless cloth that sandwiches sludge between the first endless cloth, and receives the sludge discharged from the forming machine and transfers it onto the first endless cloth. A moving conveyor is disposed between the forming machine and the first endless cloth so as to be able to move horizontally in the longitudinal direction of the first endless cloth, and the sludge sandwiched between the pair of endless cloths is pressurized. The present invention includes a high-pressure dehydration mechanism that compresses and dehydrates the cloth at high pressure using a plate, and a drive mechanism that stops moving the cloth when the high-pressure dehydrator is compressing and dewatering, and moves the cloth when it is not being compressed and dehydrated.

以下本発明の実施例を図面に基づいて説明す
る。
Embodiments of the present invention will be described below based on the drawings.

第1図において、1は重力脱水部、22は形成
機、2cは移動コンベア、3a,3bはエンドレ
ス布、4は高圧脱水機構である。
In FIG. 1, 1 is a gravity dewatering section, 22 is a forming machine, 2c is a moving conveyor, 3a and 3b are endless cloths, and 4 is a high pressure dewatering mechanism.

前記重力脱水部1は、ロール10,10に巻掛
けられたベルトコンベア状の布11から成り、
その一端に汚泥を載せ、他端に移動する間に重力
により脱水を行うようになつている。本発明は前
記形成機22を設け、これにより汚泥を形成処理
するものであるが、高含水率の汚泥は、多くの場
合そのままでは適切な成形ができず、形成機によ
る汚泥の形成は、この重力脱水部1によりある程
度脱水することにより可能である。
The gravity dewatering section 1 consists of a belt conveyor-like cloth 11 wrapped around rolls 10, 10,
The sludge is placed on one end and dewatered by gravity as it moves to the other end. The present invention is provided with the forming machine 22 to form and process sludge. However, in many cases, sludge with a high water content cannot be formed properly as it is, and the formation of sludge by the forming machine is limited to this process. This is possible by dehydrating to some extent using the gravity dewatering section 1.

前記形成機22は、重力脱水部1の汚泥排出側
に設けられている。この形成機22は、凹凸歯を
持つた1対のロール220を有しており、重力脱
水部1から排出される汚泥を受け、これをウドン
状に形成・排出するよう構成されている。このよ
うに汚泥Xを形成することにより、形成した汚泥
の間に〓間(水みち)が生じ、そこから排水が円
滑に行われる。
The forming machine 22 is provided on the sludge discharge side of the gravity dewatering section 1. This forming machine 22 has a pair of rolls 220 with uneven teeth, and is configured to receive the sludge discharged from the gravity dewatering section 1, form it into a udon shape, and discharge it. By forming the sludge X in this manner, water paths are created between the formed sludge, and drainage is smoothly carried out from there.

前記一対のエンドレス布のうち、第1のエン
ドレス布3bは、形成機22の下方で水平走行
し、ここで形成機側から供給される汚泥を受ける
ようになつている。このエンドレス布3bはピ
ンチロール30の位置で上側の第2のエンドレス
布3aと合わさり、ここで汚泥Xを挟んで高圧
脱水機構4へと導かれる。脱水機構4を出たエン
ドレス布は再び上下に分かれて、脱水後の汚泥
ケーキYを排出する。この排出部近傍には、上下
のエンドレス布3a,3bに付着した汚泥をか
き落すためのスクレーパ31,31が装着されて
いる。また上下のエンドレス布3a,3bの適
宜位置に布洗浄装置32,32が配設され、エ
ンドレス布3の洗浄を行なうように構成されて
いる。
Of the pair of endless cloths, the first endless cloth 3b runs horizontally below the forming machine 22 and receives the sludge supplied from the forming machine. This endless cloth 3b is combined with the upper second endless cloth 3a at the position of the pinch roll 30, and is led to the high-pressure dewatering mechanism 4 with the sludge X sandwiched therebetween. The endless cloth that has exited the dewatering mechanism 4 is again divided into upper and lower parts, and the sludge cake Y after dewatering is discharged. Scrapers 31, 31 for scraping off sludge adhering to the upper and lower endless cloths 3a, 3b are installed near the discharge section. Further, cloth cleaning devices 32, 32 are disposed at appropriate positions on the upper and lower endless cloths 3a, 3b, and are configured to clean the endless cloth 3.

前記移動コンベア2cは、前記形成機22と第
1のエンドレス布3bとの間の位置に、第1の
エンドレス布長手方向に対し水平移動可能に配
されており、形成機から排出される汚泥を受け、
これを第1のエンドレス布3b上に均一に供給
し得るよう構成されている。
The moving conveyor 2c is disposed between the forming machine 22 and the first endless cloth 3b so as to be movable horizontally with respect to the longitudinal direction of the first endless cloth, and carries the sludge discharged from the forming machine. received,
It is configured to be able to uniformly supply this onto the first endless cloth 3b.

本発明のように圧力板を備えた高圧脱水機構を
有し、且つその前工程に上記のような重力脱水部
1を有する装置では、連続運転される重力脱水部
1に対し、高圧脱水部側のエンドレス布を間歇
的に走行、停止させ、停止中に圧力板による圧搾
脱水が行われる。一方、、エンドレス布と圧力
板とによる高圧圧搾を効果的に行うためには、重
力脱水部側から連続的に排出される汚泥を、間歇
的に走行するエンドレス布上に常に均一に供給
する必要がある。加えて、形成機22によりウド
ン状に形成された汚泥は、これをホツパ等に貯留
することなく直ちに布上に供給しないとその形
が崩れて〓間がなくなり、折角形成した意味がな
くなつてしまう。
In an apparatus having a high-pressure dewatering mechanism equipped with a pressure plate as in the present invention and having the gravity dewatering section 1 as described above in the preceding process, the high-pressure dehydrating section side is The endless cloth is run and stopped intermittently, and dewatering is performed by pressing with a pressure plate while it is stopped. On the other hand, in order to effectively perform high-pressure compression using an endless cloth and a pressure plate, it is necessary to constantly and uniformly supply the sludge discharged continuously from the gravity dewatering section onto the endless cloth that runs intermittently. There is. In addition, if the sludge formed into a udon-like shape by the forming machine 22 is not stored in a hopper or the like and immediately supplied onto the cloth, its shape will collapse and there will be no time left, and there will be no point in forming the sludge. Put it away.

前記移動コンベア2cはこのような観点から設
けられたもので、この移動コンベア2cにより、
形成機22から排出されたウドン状の汚泥を直ち
に布上に落下供給させるようにするとともに、
移動コンベア2cの移動供給により布の間歇的
走行にかかわらず、布上に均一にウドン状の汚
泥を供給できるようにしている。
The moving conveyor 2c was provided from this point of view, and with this moving conveyor 2c,
The udon-like sludge discharged from the forming machine 22 is immediately dropped onto the cloth, and
The moving supply of the moving conveyor 2c makes it possible to uniformly supply udon-like sludge onto the cloth regardless of the intermittent running of the cloth.

前記高圧脱水機構4は複数の圧力板40と複数
のリターンロール41とから構成され、リターン
ロール41により、エンドレス布3を蛇行さ
せ、その間に圧力板による圧搾を行うようにして
いる。圧力板40には油圧機構等が設けられてお
り、エンドレス布3を左右から挟んで高圧で圧
搾するように構成されており、これは従来のフイ
ルタープレス式におけるものと同一の構成で良
い。
The high-pressure dewatering mechanism 4 is composed of a plurality of pressure plates 40 and a plurality of return rolls 41, and the endless cloth 3 is meandered by the return rolls 41, during which compression is performed by the pressure plates. The pressure plate 40 is provided with a hydraulic mechanism, etc., and is configured to pinch the endless cloth 3 from the left and right sides and compress it under high pressure, and this may be the same configuration as that in the conventional filter press type.

リターンロール41の適宜の一部又は全部には
駆動機構(図示せず)が設けられており、圧力板
40によりエンドレス布3を圧搾している間は
エンドレス布3の走行を停止し、非圧搾時には
エンドレス布3を移動するようにしている。
A drive mechanism (not shown) is provided in a suitable part or all of the return roll 41, and while the endless cloth 3 is being compressed by the pressure plate 40, the running of the endless cloth 3 is stopped, and the endless cloth 3 is not compressed. Sometimes the endless cloth 3 is moved.

なお、上記脱水機構4においては、通常、5
Kg/cm2の圧力が60sec以上の時間かけられる。
In addition, in the dehydration mechanism 4, normally 5
A pressure of Kg/cm 2 is applied for a period of 60 seconds or more.

次に動作を説明する。 Next, the operation will be explained.

重力脱水部1で連続的に脱水された汚泥Xは形
成機22のホツパに受け入れられ、この形成機の
凹凸歯を有する1対のロール220によりウドン
状に形成され、下方の移動コンベア2c上に排出
される。移動コンベア2cは図中左から右へ移動
しつつ落下点を変えながら汚泥Xをエンドレス
布3b上の所定の範囲(長さ)に均一に供給す
る。この間、高圧脱水機構4では汚泥を挟んだエ
ンドレス布3a,3bを圧搾し脱水を行う。高
圧脱水機構における加圧が終つたら、高圧脱水機
構4の加圧を解いて、駆動機構によりエンドレス
布3を移動コンベアのほぼ移動距離分だけ移動
走行させる。この時、汚泥ケーキYが排出され
る。また移動コンベア2cも元の位置に戻す。そ
して再び高圧脱水機構4によりエンドレス布3
を圧搾脱水する一方、移動コンベア2cからエン
ドレス布3b上に汚泥を供給し、以下同様な動
作を繰返す。
Slud It is discharged. The moving conveyor 2c moves from left to right in the figure and uniformly supplies the sludge X to a predetermined range (length) on the endless cloth 3b while changing the falling point. During this time, the high-pressure dewatering mechanism 4 squeezes the endless cloths 3a and 3b sandwiching the sludge to dewater. When the pressurization in the high-pressure dehydration mechanism is finished, the pressurization in the high-pressure dehydration mechanism 4 is released, and the endless cloth 3 is caused to travel by approximately the travel distance of the moving conveyor by the drive mechanism. At this time, sludge cake Y is discharged. The moving conveyor 2c is also returned to its original position. Then, the endless cloth 3 is again processed by the high-pressure dehydration mechanism 4.
While compressing and dewatering the sludge, sludge is supplied from the moving conveyor 2c onto the endless cloth 3b, and the same operation is repeated thereafter.

この場合、エンドレス布3は高圧脱水機構4
内を少しずつ移動し、複数の圧力板40により順
次脱水をうけることになるため、布3の位置に
よる脱水の不均一は生せず、均一の脱水が行われ
る。
In this case, the endless cloth 3 has a high-pressure dewatering mechanism 4
Since the fabric 3 moves little by little and is sequentially dehydrated by the plurality of pressure plates 40, there is no uneven dehydration depending on the position of the cloth 3, and uniform dehydration is performed.

なお、上記動作中、スクレーパ31と布洗浄
装置32により布3は加圧中であつても洗浄さ
れている。
Note that during the above operation, the cloth 3 is cleaned by the scraper 31 and the cloth cleaning device 32 even while pressurized.

以上述べた本発明によれば、重力脱水機構と1
対のエンドレス布及び圧力板を用いた高圧圧搾
脱水機構とを組み合せることにより、ベルトプレ
ス式と同様の連続処理でありながら、フイルター
プレス並みの脱水性能を得ることができる。
According to the present invention described above, the gravity dehydration mechanism and the
By combining a high-pressure dehydration mechanism using a pair of endless cloths and a pressure plate, it is possible to obtain dehydration performance comparable to that of a filter press, although it is a continuous process similar to that of a belt press type.

さらに本発明では、汚泥はまず重力脱水部で軽
度に脱水された後、形成機でウドン状に形成さ
れ、しかる後直ちに移動コンベアで第1のエンド
レス布上に落下供給されるため、汚泥が連続的
な片面状態ではなく言わば小間切れ状態で布上
に供給されることにより、布上の汚泥には〓間
が無数に生じることになり、これが水みちとなつ
てそこから汚泥内の水分が極めて円滑に排出され
ることになる。加えて、汚泥中には繊維等の夾雑
物が比較的多く含まれ、この夾雑物の存在も汚泥
含有水の排出を妨げる大きな原因となつている
が、本発明では形成機による汚泥処理がこのよう
な繊維等の夾雑物をときほぐすように作用し、こ
れによつても汚泥含有水の排出が円滑に促進され
ることになる。
Furthermore, in the present invention, the sludge is first lightly dehydrated in the gravity dewatering section, then formed into a udon-like shape in the forming machine, and then immediately dropped and supplied onto the first endless cloth by the moving conveyor, so that the sludge is continuously Because the sludge is supplied onto the cloth in small pieces rather than on one side, countless gaps are created in the sludge on the cloth, which become water channels from which water in the sludge drains extremely smoothly. will be discharged. In addition, sludge contains a relatively large amount of impurities such as fibers, and the presence of these impurities is a major cause of hindering the discharge of sludge-containing water, but in the present invention, sludge treatment using a forming machine This acts to loosen impurities such as fibers, and this also facilitates the smooth discharge of sludge-containing water.

エンドレス布を用いた高圧脱水では、布上
に供給された汚泥は、圧搾脱水までの間に効果的
に重力脱水されることが望ましく、これが実現す
ると全体的な脱水効率を大きく上げることができ
る。この点本発明では、上述したように凹凸歯を
持つ1対のローラを有する形成機による汚泥の処
理により、水みちとなるべき汚泥内の〓間の形成
と、排水を阻害する夾雑物の処理とを同時に行
い、布上での汚泥中水分の排出を非常に円滑化
し、汚泥の脱水効率を効果的に向上させることが
できる。
In high-pressure dewatering using an endless cloth, it is desirable that the sludge supplied onto the cloth be effectively dehydrated by gravity before being compressed and dewatered, and if this is achieved, the overall dewatering efficiency can be greatly increased. In this regard, in the present invention, as described above, by processing the sludge using a forming machine having a pair of rollers with concave and convex teeth, the formation of gaps in the sludge that should become water channels, and the treatment of impurities that obstruct drainage. At the same time, the water in the sludge can be discharged very smoothly on the cloth, and the dewatering efficiency of the sludge can be effectively improved.

加えて、本発明では移動コンベアの移動供給に
より布の間歇的走行にかかわらず、布上に均
一のウドン状の汚泥を供給でき、これによつて圧
力板による高圧圧搾を適切に行わしめることがで
きる。
In addition, in the present invention, a uniform udon-like sludge can be supplied onto the cloth regardless of the intermittent running of the cloth due to the moving supply of the moving conveyor, thereby making it possible to appropriately perform high-pressure squeezing by the pressure plate. can.

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

第1図は本発明の一実施例を示す正面図であ
る。 図中、1……重力脱水部、2c……移動コンベ
ア、3a,3b……エンドレス布、4……高圧
脱水機構、22……形成機、220……ロール。
FIG. 1 is a front view showing an embodiment of the present invention. In the figure, 1...Gravity dewatering section, 2c...Moving conveyor, 3a, 3b...Endless cloth, 4...High pressure dewatering mechanism, 22...Forming machine, 220...Roll.

Claims (1)

【特許請求の範囲】[Claims] 1 高含水汚泥を一次的に脱水する重力脱水部
と、凹凸歯を持つた1対のロールを有し、前記重
力脱水部から排出される汚泥を受けこれをウドン
状に形成排出すべく、重力脱水部汚泥排出側に設
けられる形成機と、該形成機側から排出される汚
泥を受ける第1のエンドレス布及び該第1のエ
ンドレス布との間で汚泥を挟む第2のエンドレ
ス布からなる1対のエンドレス布と、形成機
から排出される汚泥を受け、これを第1のエンド
レス布上に落下供給すべく、形成機と第1のエ
ンドレス布との間に、第1のエンドレス布長
手方向に対し水平移動可能に配される移動コンベ
アと、1対のエンドレス布に挟まれた汚泥を圧
力板により高圧で圧搾脱水する高圧脱水機構と、
該高圧脱水機構による圧搾脱水時には前記布の
移動を停止し非圧搾脱水時には前記布を移動さ
せる駆動機構とを有することを特徴とする脱水
機。
1. It has a gravity dewatering section that primarily dewaters high water content sludge, and a pair of rolls with uneven teeth, which receives the sludge discharged from the gravity dewatering section and forms it into a udon shape and discharges it. A forming machine provided on the sludge discharge side of the dewatering section, a first endless cloth that receives the sludge discharged from the forming machine, and a second endless cloth that sandwiches the sludge between the first endless cloth. In order to receive the sludge discharged from the pair of endless cloths and the forming machine and to drop and supply the sludge onto the first endless cloth, a first endless cloth is provided between the forming machine and the first endless cloth in the longitudinal direction. a moving conveyor that can be moved horizontally, and a high-pressure dewatering mechanism that compresses and dewaters the sludge sandwiched between a pair of endless cloths under high pressure using a pressure plate.
A dewatering machine characterized by having a drive mechanism that stops moving the cloth during press dehydration by the high-pressure dehydration mechanism and moves the cloth during non-press dehydration.
JP58237825A 1983-12-19 1983-12-19 Dehydrator Granted JPS60130498A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58237825A JPS60130498A (en) 1983-12-19 1983-12-19 Dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58237825A JPS60130498A (en) 1983-12-19 1983-12-19 Dehydrator

Publications (2)

Publication Number Publication Date
JPS60130498A JPS60130498A (en) 1985-07-11
JPH0245559B2 true JPH0245559B2 (en) 1990-10-09

Family

ID=17020956

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58237825A Granted JPS60130498A (en) 1983-12-19 1983-12-19 Dehydrator

Country Status (1)

Country Link
JP (1) JPS60130498A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2568139B1 (en) * 1984-07-25 1989-06-16 Degremont APPARATUS FOR SEPARATING THE LIQUID PHASE OF A SOLID-LIQUID SUSPENSION
JPS62189896U (en) * 1986-05-22 1987-12-03
FR3066925B1 (en) * 2017-05-30 2021-09-17 Ste De Fabrication Et Ateliers Lucien Choquenet INSTALLATION AND METHOD OF FILTRATION OF A LIQUID / SOLID MIXTURE

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5318869A (en) * 1976-08-05 1978-02-21 Baehr Albert Extractor for sludge or the like
JPS57177899A (en) * 1981-04-13 1982-11-01 Ginaaru Do Separashion Soc Filter device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5318869A (en) * 1976-08-05 1978-02-21 Baehr Albert Extractor for sludge or the like
JPS57177899A (en) * 1981-04-13 1982-11-01 Ginaaru Do Separashion Soc Filter device

Also Published As

Publication number Publication date
JPS60130498A (en) 1985-07-11

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