JPH08108016A - Filter medium clogging preventive device in vacuum dehydrator for water-containing material - Google Patents

Filter medium clogging preventive device in vacuum dehydrator for water-containing material

Info

Publication number
JPH08108016A
JPH08108016A JP6268005A JP26800594A JPH08108016A JP H08108016 A JPH08108016 A JP H08108016A JP 6268005 A JP6268005 A JP 6268005A JP 26800594 A JP26800594 A JP 26800594A JP H08108016 A JPH08108016 A JP H08108016A
Authority
JP
Japan
Prior art keywords
filter medium
filter
stock solution
small bubbles
immersed
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.)
Granted
Application number
JP6268005A
Other languages
Japanese (ja)
Other versions
JP2701198B2 (en
Inventor
Shigetaka Hosobuchi
慈貴 細渕
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.)
HOSOBUCHII ENG KK
Original Assignee
HOSOBUCHII ENG KK
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 HOSOBUCHII ENG KK filed Critical HOSOBUCHII ENG KK
Priority to JP6268005A priority Critical patent/JP2701198B2/en
Publication of JPH08108016A publication Critical patent/JPH08108016A/en
Application granted granted Critical
Publication of JP2701198B2 publication Critical patent/JP2701198B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE: To prevent the clogging of a filter medium even for a material to be treated having high viscosity or the one containing fine particles by installing a bubble discharging device for feeding many small bubbles onto the outer surface of a filter medium of a filter hollow body immersed in an original liquid in an original tank. CONSTITUTION: Below both the right and left sides viewed from the circular side face of the back surface of a filter cylindrical body 11 immersed in an original liquid 7 in an original liquid tank 6, bubble discharging pipes 11 consisting of porous unglazed pottery are arranged parallel over the total length in the axial direction of the filter cylindrical body 1, and one end of each bubble discharging pipe 1 1 is connected to an air compressor through a pipe. In this way, small bubbles fed from the filter medium 3 side from the bubble discharging pipe 11 form many through holes leading to a filter medium 3 in a filter cake bed. Therefore, filtration is surely continued to adsorb filter cake thick.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本願発明は、汚泥等の含水物の脱
水に使用される真空脱水機の改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of a vacuum dehydrator used for dehydrating water-containing substances such as sludge.

【0002】[0002]

【従来の技術】従来、例えば、円筒体の外周面に濾材を
張り、該濾材の内側に内周面に沿って互に仕切られた多
数の吸引小室を配設してなる濾過ドラムを、その軸を水
平に支持した状態で、ドラム下半部を汚泥が注入される
原液タンクの原液中に浸し、そして上記濾過ドラムの回
転に従い、上記吸引小室が内部を減圧しつつ原液中に導
かれて汚泥を吸引し、汚泥中の水分は濾液として吸入し
つつ固形分は濾滓として濾材外面に捕捉し、順次厚く堆
積させていき、ついで上記吸引小室が引き続き減圧しつ
つ原液中から大気中に出ると、上記堆積濾滓に含まれる
水分を吸引脱水して脱水ケーキをつくり、ついで上記吸
引小室内に圧縮空気を送って上記脱水ケーキを濾材外面
からゆるめ、ついでスクレーパにより上記脱水ケーキを
濾材面から剥離する真空円筒型脱水機が広く知られてい
る。
2. Description of the Related Art Conventionally, for example, a filter drum having a cylindrical body covered with a filter medium and a large number of suction chambers partitioned from each other along the inner peripheral face of the filter medium are provided inside the filter drum. With the shaft supported horizontally, the lower half of the drum is immersed in the stock solution in the stock solution tank where sludge is injected, and the suction chamber is guided into the stock solution while depressurizing the inside according to the rotation of the filtration drum. The sludge is sucked in, while the moisture in the sludge is sucked in as a filtrate, while the solid content is captured as a sludge on the outer surface of the filter medium, and is successively deposited thickly, and then the suction chamber is continuously depressurized and discharged from the stock solution into the atmosphere. And sucking and dehydrating the water contained in the accumulated filter cake to form a dehydrated cake, then sending compressed air into the suction chamber to loosen the dehydrated cake from the outer surface of the filter medium, and then scraping the dehydrated cake from the surface of the filter medium. Peel off Vacuum cylindrical dehydrator are widely known.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記の従来機
では、処理すべき汚泥の粘性が高い場合や汚泥に含まれ
る固形分が微粒子である場合等に、原液中での汚泥濾過
工程において、粘性濾滓が層をなして濾材面にべったり
密着したり、濾滓の微粒子同志が緻密に密着して濾材面
に圧密濾滓層をつくり、それにより濾材の透過孔を閉塞
し、それ以上濾滓を厚く吸着させることができないばか
りでなく次の大気中での脱水工程において脱水不能に至
らしめる不都合があった。
However, in the above conventional machine, when the sludge to be treated has a high viscosity or the solid content in the sludge is fine particles, in the sludge filtration step in the stock solution, The viscous filter cake forms a layer and sticks or adheres to the filter medium surface, and the fine particles of the filter cake closely adhere to each other to form a compacted filter cake layer on the filter medium surface, thereby closing the permeation holes of the filter medium and further filtering. Not only can the slag not be adsorbed thickly, but there is also the inconvenience that it cannot be dehydrated in the subsequent dehydration process in the atmosphere.

【0004】また、処理すべき汚泥が砂等の比重の大き
い固形物を含む場合は、そのような重い固形物が原液タ
ンクの底に高く沈積し、この沈積固形物が、濾過ドラム
の回転時に、せっかく濾材外面に厚く吸着させた濾滓を
けずり取ってしまう難点もあった。
Further, when the sludge to be treated contains solids having a large specific gravity such as sand, such heavy solids are highly deposited on the bottom of the stock solution tank, and the deposited solids are generated when the filtration drum rotates. However, there is also a problem that the filter cake thickly adsorbed on the outer surface of the filter material is scraped off.

【0005】本願第1発明は、処理すべき含水物の粘性
が高い場合や微粒子の固形分を含む場合にも濾材の閉塞
を防止することを課題とし、
The first invention of the present application has an object to prevent the clogging of the filter medium even when the water-containing material to be treated has a high viscosity or contains a solid content of fine particles.

【0006】本願第2発明は、上記第1発明の課題に加
え、処理すべき汚泥が比重の大きい固形物を含む場合に
沈積固形物のもたらす障害を解消することを課題とす
る。
In addition to the problems of the first invention, the second invention of the present application has an object of eliminating the obstacle caused by the deposited solid matter when the sludge to be treated contains the solid matter having a large specific gravity.

【0007】[0007]

【課題を解決するための手段】上記課題解決のため、本
願第1発明は、中空体の外面に濾材を位置させ、中空体
内部に上記濾材の内側に位置すべき吸引室を配設してな
る濾過中空体を、上記吸引室が原液タンクの原液中およ
び大気中に交互に導かれるように、回転自在に支持した
真空脱水機において、上記原液タンク内に、上記濾過中
空体の原液中に浸っている濾材外面に多数の小気泡を連
続的に供給すべき気泡放出器を設けた、含水物の真空脱
水機における濾材閉塞防止装置を提案し、
In order to solve the above problems, the first invention of the present application is such that a filter medium is located on the outer surface of a hollow body, and a suction chamber to be located inside the filter medium is provided inside the hollow body. In a vacuum dehydrator rotatably supported, such that the suction chamber is alternately introduced into the stock solution of the stock solution tank and into the atmosphere, in the stock solution tank, in the stock solution of the filtration hollow body. Providing a filter medium blockage prevention device in a vacuum dehydrator for hydrated substances, provided with a bubble discharger for continuously supplying a large number of small bubbles to the outer surface of the immersed filter medium,

【0008】本願第2発明は、上記第1発明における気
泡放出器に代え、空気噴射器を、上記原液タンク内底に
沈積する固形物に向けて空気を噴射し且つ噴射により生
成される小気泡を上記原液中に浸っている濾材外面に供
給する位置関係に設けた、含水物の真空脱水機における
濾材閉塞防止装置を提案する。
The second invention of the present application, in place of the bubble ejector of the first invention, injects air toward the solid matter deposited on the inner bottom of the stock solution tank by using an air ejector, and produces small bubbles. The present invention proposes a device for preventing clogging of a filter medium in a vacuum dehydrator for a water-containing substance, which is provided in a positional relationship of supplying the above to the outer surface of the filter medium immersed in the stock solution.

【0009】本願発明における上記「濾過中空体」と
は、外周面に濾材を張設し、内部に内周面に沿って複数
の吸引室を配設した濾過円筒体、内周面に沿って複数の
吸引室を配設した円筒体の外周面に、無端帯状濾材を該
円筒体外周面の約280度範囲に掛け回した濾過円筒
体、複数の中空円盤を同一軸に等間隔をあけて取りつ
け、各中空円盤の両面に濾材をそれぞれ張設すると共に
各円盤内に複数の吸引室を配設した濾過円盤体、その他
種々の構造のものを含む。また、上記「濾材」は、濾
布、多孔板、濾過膜その他種々のものが適宜選択的に使
用される。さらに、上記「気泡放出器」として、多孔素
焼陶器、多孔金属等からなる管状体、筒状体、球状体等
に高圧空気を送りこんで気泡を放出させるものがであ
る。以下図面を参照して本願発明の実施例について説明
する。
The "filtering hollow body" in the present invention means a filter cylinder having an outer peripheral surface provided with a filter material and a plurality of suction chambers provided along the inner peripheral surface, along the inner peripheral surface. On the outer peripheral surface of the cylindrical body in which a plurality of suction chambers are arranged, an endless band-shaped filter medium is wound around the outer peripheral surface of the cylindrical body in a range of about 280 degrees, and a plurality of hollow disks are equidistantly arranged on the same axis. It includes a filter disk body in which a filter medium is attached to both sides of each hollow disk and a plurality of suction chambers are arranged in each disk, and various other structures. Further, as the above-mentioned "filter material", a filter cloth, a perforated plate, a filter membrane and various other materials are appropriately and selectively used. Further, as the above-mentioned "bubble discharger", there is one that sends high pressure air to a tubular body, a tubular body, a spherical body or the like made of porous porcelain ware, porous metal or the like to discharge bubbles. Embodiments of the present invention will be described below with reference to the drawings.

【0010】[0010]

【実施例】図1は真空円筒型脱水機に実施した例で、そ
の濾過円筒体(1)は、中心に軸(2)を縦通固着した
中空円筒体の外周面に濾布からなる濾材(3)を張設
し、中空円筒体内部には、上記濾材(3)の内側に多数
の吸引小室(4)…を内周面に沿って隣接状態で環状に
配設すると共に、各小室(4)…に一端を接続された吸
引管(5)…の各他端を上記軸(2)に被嵌されたスイ
ベル継手を介して真空装置およびコンプレッサに連継し
てあり、この濾過円筒体(1)を、その軸心線を水平に
向け且つ原液タンク(6)内の原液(7)中に約下半部
を浸した状態で、軸(2)を介して回転自在に支持させ
ると共に、該軸(2)にモータの回転をプーリおよびベ
ルトを介して伝達できるようにしてある。(8)は上記
濾過円筒体(1)の一側において濾材(3)の外面に先
端を当接させたスクレーパ、(9)は原液タンク(6)
内への原液供給管、(10)は撹拌機である。
EXAMPLE FIG. 1 shows an example of application to a vacuum cylinder type dehydrator, in which a filtering cylinder (1) is a hollow cylindrical body having a shaft (2) longitudinally secured to the center and a filter material made of a filter cloth on the outer peripheral surface. (3) is stretched, and a large number of suction small chambers (4) are arranged inside the filter medium (3) inside the hollow cylindrical body along the inner peripheral surface in an adjacent state, and each small chamber is arranged. The other end of the suction pipe (5), one end of which is connected to (4), is connected to the vacuum device and the compressor through the swivel joint fitted to the shaft (2). The body (1) is rotatably supported via the shaft (2) with its axis centered horizontally and with its lower half part immersed in the undiluted solution (7) in the undiluted solution tank (6). At the same time, the rotation of the motor can be transmitted to the shaft (2) through a pulley and a belt. (8) is a scraper whose tip is in contact with the outer surface of the filter medium (3) on one side of the filtration cylinder (1), and (9) is a stock solution tank (6)
A stock solution supply pipe into the inside, and (10) is a stirrer.

【0011】上記のよう脱水機において、原液タンク
(6)内における原液(7)に浸っている濾過円筒体
(1)下面の円形側面からみて左右両側下位に、多孔素
焼陶器からなる気泡放出管(11)、(11)を円筒体
(1)の軸方向全長にわたって円筒体軸心線と平行に配
設し、各気泡放出管(11)、(11)の一端を管を介
してエアコンプレッサ(図示略)に接続してある。
In the dehydrator as described above, a bubble discharge tube made of porous porcelain is provided on the lower left and right sides when viewed from the circular side surface of the lower surface of the filtration cylinder (1) immersed in the undiluted solution (7) in the undiluted solution tank (6). (11), (11) are arranged in parallel with the axis of the cylindrical body over the entire length of the cylindrical body (1) in the axial direction, and one end of each bubble discharge pipe (11), (11) is connected to the air compressor via the pipe. (Not shown).

【0012】上例の作用を次に説明する。一例として土
質、繊維質等その他種々の有機質微粒子を含む汚泥を原
液供給管(9)から原液タンク(6)内に連続的に供給
する。濾過円筒体(1)を回転させると共に真空装置の
駆動により各吸引小室(4)…内を減圧し、それと共に
気泡放出管(11)、(11)に空気を圧送して小気泡
を放出させると、原液(7)中を移動する濾過工程にお
いて、濾材(3)に汚泥を吸引し、それに含まれる微粒
固形物を濾材(3)外面に濾滓として吸着し、水分は濾
材(3)を通して濾液として小室(4)…内に吸入し、
これを継続して濾材(3)外面に濾滓層(m)を堆積さ
せていく。一方、気泡放出管(11)、(11)から放
出される小気泡は上昇して原液中の濾材(3)面ほぼ全
面に分散しつつ濾材(3)に吸引され、この吸引力によ
り該小気泡が濾滓層(m)に穿孔して濾材(3)に達す
る多数の通孔を形成しつつ吸入されていき、その際、上
記小気泡が濾滓内の大小固形物の間を曲りくねって穿孔
流通することにより、図2のように不規則に分岐した曲
折通孔(12)…を形成する。一旦穿孔された通孔(1
2)…には、その後供給される小気泡を流通させて通孔
(12)…を開口状態に維持すると共に、該通孔(1
2)…を通じて新たな汚泥を吸引して濾滓堆積を増大さ
せていき、以後これを継続していく。
The operation of the above example will now be described. As an example, sludge containing various organic fine particles such as soil and fiber is continuously supplied into the stock solution tank (6) from the stock solution supply pipe (9). The inside of each suction small chamber (4) is decompressed by rotating the filtration cylinder (1) and driving a vacuum device, and at the same time, air is pumped to the bubble discharge pipes (11) and (11) to discharge small bubbles. In the filtration step of moving in the undiluted solution (7), the sludge is sucked into the filter medium (3), the fine solid particles contained therein are adsorbed on the outer surface of the filter medium (3) as a filter residue, and water is passed through the filter medium (3). As a filtrate, inhale into the small chamber (4) ...
By continuing this, the filter cake layer (m) is deposited on the outer surface of the filter medium (3). On the other hand, the small bubbles discharged from the bubble discharge pipes (11) and (11) rise and are dispersed on almost the entire surface of the filter medium (3) in the undiluted solution and are sucked by the filter medium (3). Air bubbles are sucked while perforating the filter residue layer (m) to form a large number of through holes reaching the filter medium (3), and the small bubbles meander between the large and small solid matters in the filter residue. As shown in FIG. 2, the bent through holes (12) ... Once a through hole (1
2) ... Allows the small bubbles to be supplied thereafter to flow to maintain the through holes (12) ...
2) ... to suck new sludge to increase the buildup of slag, and continue this process.

【0013】次に、原液(7)中から大気中に露出して
スクレーパ(8)の適宜手前まで移動する脱水工程にお
いて、上記濾滓層(m)に含まれる水分を上記通孔(1
2)…を通じて大気とともに吸入し、脱水濾滓層
(m’)とする。
Next, in a dehydration step in which the raw solution (7) is exposed to the atmosphere and moved to a position immediately before the scraper (8), the water contained in the filter cake layer (m) is passed through the through hole (1).
2) Inhale with the atmosphere through ... to form a dehydrated filter residue layer (m ').

【0014】次に剥離工程において、小室(4)内に圧
縮空気を送り、該空気を濾材(3)を通じて外方へ噴出
させ、それにより濾材(3)外面と濾滓層(m’)の付
着をゆるめ、ついでスクレーパ(8)により濾滓をケー
キとして剥離する。
Next, in the peeling step, compressed air is sent into the small chamber (4) to blow the air outward through the filter medium (3), whereby the outer surface of the filter medium (3) and the filter cake layer (m ') are discharged. The adhesion is loosened, and then the filter cake is peeled off as a cake with a scraper (8).

【0015】図3の真空円筒脱水機は、図1の脱水機に
おける気泡放出管(11)、(11)に代え、空気噴射
器として多数の空気噴射ノズル(13a)…を有する空
気噴射管(11a)、(11a)を、上記気泡放出管
(11)、(11)とほぼ同じ位置で、各噴射ノズル
(13a)…、(13a)…を原液タンク(6a)の谷
形底面のほぼ最深底部へ向けた状態に配設すると共に、
撹拌機を除き、他の構造は図1と実質的に同一である。
本機において、一例として有機質微粒子のほか細砂等の
比重の大きい固形物を含む汚泥を原液供給管(9a)を
介して原液タンク(6a)内に連続的に供給する。供給
される汚泥中の細砂等の比重の大きい固形物はタンク
(6a)の底部に沈澱して次第に厚く堆積していく。濾
過円筒体(1a)を回転させると共に図1の場合と同様
に吸引小室(4a)…を減圧し、それと共に空気噴射ノ
ズル(13a)…から空気を噴射すると、濾材(3a)
からの濾過を行い、濾材(3a)外面に固形物を吸着さ
せていき、一方上記ノズルから噴射される空気は気泡化
しつつ底部に沈澱する細砂等を拡散して上記濾材(3
a)面への吸着を促すと共に、上記細砂等に衝突して小
気泡に細分されつつ原液中の濾材(3a)全面に分散し
て吸引され、それにより図1、2の場合と同様に濾滓層
(ma)に濾材(3a)に通じる多数の通孔を形成して
濾材の閉塞を防止し、濾滓を厚く堆積させていく。
The vacuum cylindrical dehydrator of FIG. 3 is replaced with the bubble discharge pipes (11) and (11) in the dehydrator of FIG. 1 and has an air injection pipe (a plurality of air injection nozzles (13a) ... 11a) and (11a) at substantially the same positions as the bubble discharge pipes (11) and (11), and the injection nozzles (13a) ... (13a) ... to the substantially deepest bottom of the valley bottom of the stock solution tank (6a). While arranging in the state facing the bottom,
Except for the stirrer, the other structure is substantially the same as in FIG.
In this machine, as an example, sludge containing solid particles having a large specific gravity such as fine sand in addition to organic fine particles is continuously supplied into the stock solution tank (6a) through the stock solution supply pipe (9a). The solid matter having a large specific gravity such as fine sand in the supplied sludge is settled on the bottom of the tank (6a) and gradually thickened. When the filtering cylinder (1a) is rotated and the suction chambers (4a) are decompressed in the same manner as in FIG. 1 and air is jetted from the air jet nozzles (13a) ... at the same time, the filter medium (3a)
The solids are adsorbed on the outer surface of the filter medium (3a), while the air jetted from the nozzle diffuses the fine sand or the like that settles at the bottom while forming air bubbles.
a) The adsorption to the surface is promoted, and the particles are collided with the fine sand or the like to be subdivided into small bubbles and are dispersed and sucked over the entire surface of the filter medium (3a) in the undiluted solution, whereby as in the case of FIGS. A large number of holes communicating with the filter material (3a) are formed in the filter residue layer (ma) to prevent the filter material from being blocked, and the filter residue is deposited thickly.

【0016】[0016]

【発明の効果】本願第1発明の含水物の真空脱水機にお
ける濾材閉塞防止装置によれば、処理すべき含水物が粘
性の高いものである場合や微粒子の固形物を含む場合等
であっても、原液中の濾過において、気泡放出器から濾
材がわに供給される小気泡が濾滓層に濾材へ通じる多数
の通孔を形成することができ、それにより濾過を確実に
継続して濾滓を厚く吸着することでができ、また大気中
の脱水においても、上記濾滓層の通孔から十分な脱水を
行うことができるのである。
EFFECTS OF THE INVENTION According to the device for preventing clogging of the filter medium in the vacuum dehydrator for hydrated matter of the first aspect of the present invention, the hydrated matter to be treated has a high viscosity or contains solid matter of fine particles. Also, in the filtration in the undiluted solution, the small bubbles supplied from the bubble ejector to the filter medium can form a large number of through holes in the filter layer, which lead to the filter medium, thereby ensuring the continuous filtration. This can be achieved by thickly adsorbing the slag, and also in the dehydration in the atmosphere, sufficient dehydration can be performed from the through holes of the filter residue layer.

【0017】本願第2発明の含水物の真空脱水機におけ
る濾材閉塞防止装置によれば、処理すべき含水物が比重
の高い固形物を含み、それら固形物が原液タンクの底に
高く沈積する場合に、空気噴射器から噴射される空気が
上記沈積固形物を拡散させて濾材への吸着を促すことが
できると共に、噴射空気が固形物に衝突して小気泡に細
分されて濾材がわに供給されることにより上記第1発明
と同一の効果を奏することができるのである。
According to the device for preventing clogging of the filter medium in the vacuum dehydrator for hydrates of the second aspect of the present invention, the hydrates to be treated include solids having a high specific gravity, and these solids are highly deposited at the bottom of the stock solution tank. In addition, the air ejected from the air ejector can diffuse the deposited solid matter and promote adsorption to the filter medium, and the jetted air collides with the solid matter and is subdivided into small bubbles to supply the filter medium to the crucible. By doing so, the same effect as the first aspect of the invention can be obtained.

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

【図1】濾過円筒体の一部を切欠した真空円筒脱水機の
縦断側面図である。
FIG. 1 is a vertical sectional side view of a vacuum cylinder dehydrator in which a part of a filtration cylinder is cut away.

【図2】濾滓層の一部の拡大断面図である。FIG. 2 is an enlarged cross-sectional view of a part of a filter cake layer.

【図3】濾過円筒の一部を切欠した他の真空円筒脱水機
の縦断側面図である。
FIG. 3 is a vertical sectional side view of another vacuum cylinder dehydrator in which a part of a filtration cylinder is cut away.

【符号の説明】[Explanation of symbols]

1、1a 濾過円筒体 3、3a 濾材 4、4a 吸引室 6、6a 原液タンク 7、7a 汚泥 11 気泡放出管 11a 空気噴射管 13a 空気噴射ノズル 1, 1a Filter cylinder 3, 3a Filter medium 4, 4a Suction chamber 6, 6a Stock solution tank 7, 7a Sludge 11 Bubble discharge pipe 11a Air injection pipe 13a Air injection nozzle

フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 33/58 C02F 11/12 D Continuation of front page (51) Int.Cl. 6 Identification code Office reference number FI Technical display location B01D 33/58 C02F 11/12 D

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 中空体の外面に濾材を位置させ、中空体
内部に上記濾材の内側に位置すべき吸引室を配設してな
る濾過中空体を、上記吸引室が原液タンクの原液中およ
び大気中に交互に導かれるように、回転自在に支持した
真空脱水機において、 上記原液タンク内に、上記濾過中空体の原液中に浸って
いる濾材外面に多数の小気泡を連続的に供給すべき気泡
放出器を設けた、含水物の真空脱水機における濾材閉塞
防止装置。
1. A filtration hollow body comprising a hollow body and a suction medium to be located inside the filter medium, wherein the suction medium is located in the stock solution of a stock solution tank. In a vacuum dehydrator rotatably supported so as to be alternately guided to the atmosphere, a large number of small bubbles are continuously supplied to the outer surface of the filter medium immersed in the undiluted solution of the filtration hollow body in the undiluted solution tank. An apparatus for preventing blockage of a filter medium in a vacuum dehydrator for hydrated materials, which is provided with a power bubble discharger.
【請求項2】 上記気泡放出器に代え、空気噴射器を、
上記原液タンク内底に沈積する固形物に向けて空気を噴
射し且つ噴射により生成される小気泡を上記原液中に浸
っている濾材外面に供給する位置関係に設けた、請求項
1に記載の含水物の真空脱水機における濾材閉塞防止装
置。
2. An air ejector in place of the bubble ejector,
2. The position relationship is provided in which the air is jetted toward the solid matter deposited on the inner bottom of the stock solution tank and the small bubbles generated by the jet are supplied to the outer surface of the filter medium immersed in the stock solution. A filter material blockage prevention device in a vacuum dehydrator for hydrated materials.
JP6268005A 1994-10-07 1994-10-07 Filter media blockage prevention device for vacuum dehydrator of hydrate Expired - Lifetime JP2701198B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6268005A JP2701198B2 (en) 1994-10-07 1994-10-07 Filter media blockage prevention device for vacuum dehydrator of hydrate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6268005A JP2701198B2 (en) 1994-10-07 1994-10-07 Filter media blockage prevention device for vacuum dehydrator of hydrate

Publications (2)

Publication Number Publication Date
JPH08108016A true JPH08108016A (en) 1996-04-30
JP2701198B2 JP2701198B2 (en) 1998-01-21

Family

ID=17452591

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6268005A Expired - Lifetime JP2701198B2 (en) 1994-10-07 1994-10-07 Filter media blockage prevention device for vacuum dehydrator of hydrate

Country Status (1)

Country Link
JP (1) JP2701198B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020010289A (en) * 2000-07-29 2002-02-04 권경남 A vacuum adhesion drying dehydrate
JP2007203184A (en) * 2006-02-01 2007-08-16 Mitsubishi Chemicals Corp Slurry handling method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020010289A (en) * 2000-07-29 2002-02-04 권경남 A vacuum adhesion drying dehydrate
JP2007203184A (en) * 2006-02-01 2007-08-16 Mitsubishi Chemicals Corp Slurry handling method

Also Published As

Publication number Publication date
JP2701198B2 (en) 1998-01-21

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