JPS63252519A - Rotary disc type separation device - Google Patents

Rotary disc type separation device

Info

Publication number
JPS63252519A
JPS63252519A JP8563587A JP8563587A JPS63252519A JP S63252519 A JPS63252519 A JP S63252519A JP 8563587 A JP8563587 A JP 8563587A JP 8563587 A JP8563587 A JP 8563587A JP S63252519 A JPS63252519 A JP S63252519A
Authority
JP
Japan
Prior art keywords
rotating shaft
rotary disc
separation device
rotating disk
rotating
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.)
Pending
Application number
JP8563587A
Other languages
Japanese (ja)
Inventor
Hiroyuki Horikita
堀北 弘之
Yahei Takagi
高木 弥平
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 JP8563587A priority Critical patent/JPS63252519A/en
Publication of JPS63252519A publication Critical patent/JPS63252519A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To make the structure of a whole device compact, reduce the investment cost and retain a high filtering efficiency by providing a liquid feed means on a rotary disc or a rotating shaft inside the caseing of the device. CONSTITUTION:A liquid feed means of provided on a rotary disc or a rotating shaft inside the casing of a device. For example, a plurality of rotating discs 1 mounted on a rotating shaft 2 are constituted respectively of rotary disc- shaped filter elements, and infiltrate permeating the filtering section is discharged as shown by an arrow mark (a) through the hollow section inside the rotating shaft 2. Further, a plurality of chambers 7 are divided with partition walls 6 inside casing 5, while an impeller 4 as a liquid feed means is mounted on the rotating shaft section located in a flow channel 9 narrowed by the partition wall 6. As a result, the structure of the whole device is made compact to reduce the investment cost, and a high filtering efficiency can be retained.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、回転円板型分離装置に関するものである。[Detailed description of the invention] (Industrial application field) The present invention relates to a rotating disk type separation device.

(従来の技術) 近年、被処理液を濾材面に対して平行に流し、濾材面と
被処理液との間に剪断力を生ぜしめて、濾過することに
より被処理液を濃縮する固液分離方法が、例えばrDe
salination、 35 (1980)第115
〜128頁」 (オランダ、 Elsevier Sc
ientificPublishing Co、出版)
に記載されているように提案されている。
(Prior art) In recent years, a solid-liquid separation method has been developed in which the liquid to be treated is passed parallel to the surface of the filter medium, a shearing force is generated between the surface of the filter medium and the liquid to be treated, and the liquid to be treated is concentrated by filtration. For example, rDe
salination, 35 (1980) No. 115
~128 pages” (Netherlands, Elsevier Sc.
ientific Publishing Co.)
proposed as described in .

このように濾過面と被処理液との間の剪断力を利用する
分離装置として従来種々の回転円板型分離装置が既知で
あり、例えば円板状濾過エレメントを被処理液中で回転
することにより濾材面と被処理液間に剪断力を生せしめ
る形式のもの(特開昭61−25607号、特開昭61
−138505号、特開昭61−181503号)、濾
過エレメントと円板とを交互に設置してその一方を固定
し、他方を回転することによって被処理液の乱流と濾過
エレメントとの間に剪断力を生ぜしめる形式のもの(「
ダイナミックフィルター現状と課題」化学装置、198
5年6月号、第72〜77頁;実開昭61−15900
3号)等が知られている。
Various types of rotating disk type separation devices have been known as separation devices that utilize shearing force between the filtration surface and the liquid to be treated. (Japanese Patent Application Laid-open No. 61-25607,
-138505, Japanese Patent Application Laid-Open No. 61-181503), the filtration element and the disc are installed alternately, one of them is fixed, and the other is rotated, thereby creating a gap between the turbulent flow of the liquid to be treated and the filtration element. Types that generate shearing force (``
Current status and issues of dynamic filters,” Chemical Equipment, 198
June 5th issue, pp. 72-77; Jitsukai Sho 61-15900
No. 3) etc. are known.

(発明が解決しようとする問題点) しかしながら、従来の回転円板型分離装置は被処理液を
装置外から装置内に昇圧して送入するための送液手段と
してポンプを装置外部に設置している。分離装置に大量
の被処理液を昇圧送入する場合、ポンプが大型となり、
また、ポンプと分離装置との間の配管も大径管を使用す
ることになるため、分離装置内部空間を含めて被処理液
の充填容積が大となる問題や設備費が大となる問題があ
るばかりでなく、多数の円板を具える分離装置内で分離
濃縮により高粘性となる被処理液をポンプによって送入
する結果として分離装置内に圧力分布が生じ、最適圧力
を維持することができず、この結果として濾過効率が低
下するという問題がある。
(Problems to be Solved by the Invention) However, in the conventional rotating disk type separator, a pump is installed outside the device as a liquid feeding means to pressurize and feed the liquid to be treated from outside the device into the device. ing. When pumping a large amount of liquid to the separation device under increased pressure, the pump becomes large and
Additionally, since large-diameter pipes are used for the piping between the pump and the separator, there are problems with the large filling volume of the liquid to be treated, including the internal space of the separator, and the problem of high equipment costs. Not only that, but the liquid to be processed, which becomes highly viscous due to separation and concentration, is pumped into the separator equipped with a large number of discs, resulting in a pressure distribution within the separator, making it difficult to maintain the optimum pressure. As a result, there is a problem that the filtration efficiency decreases.

(問題点を解決するための手段) 本発明によれば、第1図に示すように、回転円板1が取
付けられた回転軸2がモータ3によって駆動される回転
円板型分離装置において、送液手段4が回転円板1およ
び/または回転軸2上に設置されて装置外匣5の内部に
設けられていることを特徴とする。
(Means for Solving the Problems) According to the present invention, as shown in FIG. It is characterized in that the liquid feeding means 4 is installed on the rotating disk 1 and/or the rotating shaft 2 and is provided inside the device outer casing 5.

本発明によれば、複数の回転円板間および/または各回
転円板上にそれぞれ送液手段を設けるのが良い。
According to the present invention, it is preferable to provide liquid feeding means between the plurality of rotating disks and/or on each rotating disk.

送液手段として、回転軸上にインペラ、スクリュー等の
既知の適当な手段を設けることができ、また、回転円板
の表面または外周面に送り羽根を設けることができる。
As the liquid feeding means, a known suitable means such as an impeller or a screw can be provided on the rotating shaft, and feeding blades can be provided on the surface or outer peripheral surface of the rotating disk.

(作 用) 本発明によれば、送液手段4を回転円板1または回転軸
2上に設置して、分離装置内に設けることによって回転
軸2の回転により被処理液が分離装置内に引き入れられ
る。これにより装置外部にポンプ等の送液手段を設ける
必要がなくなり、被処理液の充填容積を減少できる。ま
た、各回転円板l上または各回転円板1間の回転軸2上
に送液手段4をそれぞれ設けることによって、回転円板
1の数が増大しても、分離装置内の圧力分布がなくなり
、最適圧力に維持でき、高い濾過効率を維持できる。
(Function) According to the present invention, by installing the liquid feeding means 4 on the rotating disk 1 or the rotating shaft 2 and providing it in the separation device, the liquid to be treated is transferred into the separating device by the rotation of the rotating shaft 2. be drawn in. This eliminates the need to provide a liquid feeding means such as a pump outside the apparatus, and the filling volume of the liquid to be treated can be reduced. Furthermore, by providing the liquid feeding means 4 on each rotating disk 1 or on the rotating shaft 2 between each rotating disk 1, even if the number of rotating disks 1 increases, the pressure distribution within the separation device can be maintained. The optimum pressure can be maintained and high filtration efficiency can be maintained.

(実施例) 第1図は本発明の第1実施例を示す。この第1図に示す
回転円板型分離装置では、回転軸2上に取付けられる複
数個の回転円板1が円板状フィルターエレメントでそれ
ぞれ構成されている。各円板状フィルターエレメントは
回転軸2と一体に回転するとともにそのフィルタ一部を
透過した濾過液が回転軸2の中空内部を経て矢aで示す
ように排出されるよう中空の回転軸1に連結固定されて
いる。
(Embodiment) FIG. 1 shows a first embodiment of the present invention. In the rotating disk type separator shown in FIG. 1, a plurality of rotating disks 1 mounted on a rotating shaft 2 are each composed of a disk-shaped filter element. Each disc-shaped filter element rotates together with the rotating shaft 2, and the hollow rotating shaft 1 is arranged so that the filtrate that has passed through a part of the filter is discharged as shown by arrow a through the hollow interior of the rotating shaft 2. Connection is fixed.

分離装置の竪型円筒形外匣5の内部には仕切壁6によっ
て複数の室7が区画して設けられている。
A plurality of chambers 7 are provided inside the vertical cylindrical outer box 5 of the separation device, separated by a partition wall 6 .

この外匣5内に回転軸2が垂直方向に延長され、その両
端部が外匣端壁5aにそれぞれ貫通され、適当なシール
および軸受8によって外匣端部5aに液密に回転自在に
支承され、回転軸2の上端にモータ3が駆動するよう連
結されている。
A rotating shaft 2 extends vertically inside the outer casing 5, and its both ends are penetrated through the outer casing end wall 5a, and are rotatably supported in the outer casing end 5a by suitable seals and bearings 8 in a fluid-tight manner. A motor 3 is connected to the upper end of the rotating shaft 2 so as to drive it.

回転軸2上に連結固定された円板状フィルターエレメン
トにより構成された回転円板1は各室7内に回転される
よう位置決めされ、仕切壁6によって狭められた流通路
9内に位置する回転軸部分に送液手段としてインペラ4
が取付けられ、これにより回転軸2が回転することによ
って外匣5の入口10から被処理液が矢すで示すように
送入され、矢Cで示すように円板状フィルターエレメン
トの濾材面11に対して実質的に平行に流れ、濾液を分
離されて濃縮された濃縮液が矢dで示すように出口12
から送出される。
A rotating disk 1 constituted by a disk-shaped filter element connected and fixed on a rotating shaft 2 is positioned to be rotated in each chamber 7, and a rotating disk 1 is positioned in a flow path 9 narrowed by a partition wall 6. An impeller 4 is installed on the shaft as a liquid feeding means.
is attached, and as the rotating shaft 2 rotates, the liquid to be treated is fed from the inlet 10 of the outer casing 5 as shown by the arrow C, and the filter medium surface 11 of the disc-shaped filter element is rotated as shown by the arrow C. The filtrate is separated and the concentrated concentrate flows through the outlet 12 as shown by arrow d.
Sent from

第2図は本発明の他の実施例を示し、第2図において第
1図に示したと同様部分に同じ符号を付して示す。
FIG. 2 shows another embodiment of the present invention, in which the same parts as shown in FIG. 1 are denoted by the same reference numerals.

第2図に示す例においては、複数の環状のフィルターエ
レメント15が外匣5の二重壁16の内周壁16aに垂
直方向に離間した位置で取付けられ、各環状フィルター
エレメント15はそのフィルタ一部を透過した濾過液が
2重壁16の内部を経て矢aで示すように排出されるよ
う2重壁16の内周面16aに連結固定されている。
In the example shown in FIG. 2, a plurality of annular filter elements 15 are attached to the inner circumferential wall 16a of the double wall 16 of the outer casing 5 at vertically spaced positions, and each annular filter element 15 is attached to a portion of its filter. It is connected and fixed to the inner circumferential surface 16a of the double wall 16 so that the filtrate that has passed through the double wall 16 is discharged as shown by arrow a through the inside of the double wall 16.

第3図は送液手段として螺旋羽根21が回転軸2の外周
に取付けられてフィードスクリューを形成している例を
示す。
FIG. 3 shows an example in which a spiral blade 21 is attached to the outer periphery of the rotating shaft 2 as a liquid feeding means to form a feed screw.

第4図は送液手段として傾斜羽根22が回転円板1の外
周面1aに取付けられている例を示す。
FIG. 4 shows an example in which inclined blades 22 are attached to the outer circumferential surface 1a of the rotating disk 1 as liquid feeding means.

第5図は送液手段としてインペラ23を回転円板10表
面上に設けた例を示す。
FIG. 5 shows an example in which an impeller 23 is provided on the surface of the rotating disk 10 as a liquid feeding means.

(発明の効果) 本発明によれば分離装置外匣の外部にホンブ等の送液昇
圧手段を設ける必要がなくなり、装置全体としての構造
がコンパクトになり、設備費を低減し得るととも被処理
充填容積が減少し、装置内の圧力分布の発生をなくし、
最適圧力に維持することができ、高い濾過効率を維持す
ることができる。
(Effects of the Invention) According to the present invention, there is no need to provide a liquid feeding pressure boosting means such as a horn on the outside of the outer case of the separation device, the structure of the entire device becomes compact, equipment costs can be reduced, and the The filling volume is reduced, eliminating the occurrence of pressure distribution within the device,
It is possible to maintain the optimum pressure and maintain high filtration efficiency.

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

第1図は本発明による回転円板型分離装置の1実施例を
示す概略線図、 第2図は本発明の他の実施例を示す概略線図、第3〜5
図は送液手段の種々の実施例を示す概略線図である。 1・・・回転円板    2・・・回転軸3・・・モー
タ     4.21.22.23・・・送液手段5・
・・外匣      6・・・仕切壁7・・・室 第1図
Fig. 1 is a schematic diagram showing one embodiment of a rotating disk type separation device according to the present invention, Fig. 2 is a schematic diagram showing another embodiment of the invention, and Figs.
The figures are schematic diagrams showing various embodiments of the liquid feeding means. 1... Rotating disk 2... Rotating shaft 3... Motor 4.21.22.23... Liquid feeding means 5.
...Outer box 6...Partition wall 7...Room diagram 1

Claims (1)

【特許請求の範囲】[Claims] 1、円板状フィルターエレメントまたは固定フィルター
エレメント間に配設された円板によって構成される回転
円板が取付けられた回転軸がモータによって駆動される
回転円板型分離装置において、送液手段が前記回転円板
および/または回転軸2上に設置されて装置外匣内部に
設けられていることを特徴とする回転円板型分離装置。
1. In a rotating disk type separation device in which a rotating shaft to which a rotating disk configured by a disk-shaped filter element or a disk arranged between fixed filter elements is attached is driven by a motor, the liquid feeding means is A rotating disk type separation device, characterized in that it is installed on the rotating disk and/or the rotating shaft 2 and provided inside a device outer casing.
JP8563587A 1987-04-09 1987-04-09 Rotary disc type separation device Pending JPS63252519A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8563587A JPS63252519A (en) 1987-04-09 1987-04-09 Rotary disc type separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8563587A JPS63252519A (en) 1987-04-09 1987-04-09 Rotary disc type separation device

Publications (1)

Publication Number Publication Date
JPS63252519A true JPS63252519A (en) 1988-10-19

Family

ID=13864291

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8563587A Pending JPS63252519A (en) 1987-04-09 1987-04-09 Rotary disc type separation device

Country Status (1)

Country Link
JP (1) JPS63252519A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5228066A (en) * 1975-07-17 1977-03-02 Artisan Ind System for stabilizing disc element of rotary concentrating systems for solid matter containing fluid
JPS5412661A (en) * 1977-06-30 1979-01-30 Toshiba Corp Elastic surface wave element

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5228066A (en) * 1975-07-17 1977-03-02 Artisan Ind System for stabilizing disc element of rotary concentrating systems for solid matter containing fluid
JPS5412661A (en) * 1977-06-30 1979-01-30 Toshiba Corp Elastic surface wave element

Similar Documents

Publication Publication Date Title
JP4686657B2 (en) Rotor for generating eddy current and filtration device using the same
US4886597A (en) Centrifugal reverse-osmosis desalination unit
US6165365A (en) Shear localized filtration system
US6132613A (en) Centrifugal reverse-osmosis desalination unit incorporating an annular membrane cartridge
US6416666B1 (en) Simplified filtration system
JP3034606U (en) Reduced size centrifuge equipment
US3957650A (en) Acoustic centrifuge
US2485390A (en) Centrifugal fluid purifier
US4376049A (en) Dynamic filter system
EP0304833B1 (en) Cross-flow type filter system
US3817446A (en) Pitot pump with centrifugal separator
JPS63252519A (en) Rotary disc type separation device
AU2015345193A1 (en) Active rotating separator
US20050218062A1 (en) Apparatus and method for separating impurities from a stream
GB1509755A (en) Rotary filtration apparatus
US1042295A (en) Filtering apparatus.
GB1334881A (en) Method of separating particles form a fluid laden therewith and a dynamic separator for performing this method
GB1488500A (en) Centrifugal filter
JPS58114707A (en) Flat membrane type separation apparatus
JPH06121919A (en) Rotary membrane eparator
SU1622017A1 (en) Planetary centrifuge
US4251184A (en) Centrifugal pump
JPS63252518A (en) Rotary disc type separator
US674832A (en) Blower.
US3463318A (en) Centrifuging device for separating a mixture into solids and liquid