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JPH08155279A - Filter plate for rotary membrane separator - Google Patents

Filter plate for rotary membrane separator

Info

Publication number
JPH08155279A
JPH08155279A JP32382194A JP32382194A JPH08155279A JP H08155279 A JPH08155279 A JP H08155279A JP 32382194 A JP32382194 A JP 32382194A JP 32382194 A JP32382194 A JP 32382194A JP H08155279 A JPH08155279 A JP H08155279A
Authority
JP
Japan
Prior art keywords
filter plate
rotary membrane
membrane separator
filtered
liquid
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
JP32382194A
Other languages
Japanese (ja)
Other versions
JP3353511B2 (en
Inventor
Yukio Fukushima
幸生 福島
Masamitsu Ito
真実 伊藤
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.)
Hitachi Ltd
Original Assignee
Hitachi Plant Engineering and Construction Co 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 Hitachi Plant Engineering and Construction Co Ltd filed Critical Hitachi Plant Engineering and Construction Co Ltd
Priority to JP32382194A priority Critical patent/JP3353511B2/en
Publication of JPH08155279A publication Critical patent/JPH08155279A/en
Application granted granted Critical
Publication of JP3353511B2 publication Critical patent/JP3353511B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D33/00Filters with filtering elements which move during the filtering operation
    • B01D33/15Filters with filtering elements which move during the filtering operation with rotary plane filtering surfaces
    • B01D33/21Filters with filtering elements which move during the filtering operation with rotary plane filtering surfaces with hollow filtering discs transversely mounted on a hollow rotary shaft

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE: To provide a thin and lightweight filter plate for a rotary membrane separator. CONSTITUTION: This filter plate 20 is formed by superposing a pair of disc- shaped metal flat membranes 30, 30 one upon another to integrally weld the outer peripheral parts 30A, 30A thereof and providing a metal net between the flat membranes 30, 30. When the filter plate 20 is rotated in a liquid to be filtered, the filter plate 20 receives the pressure difference due to the flow of the liquid to be filtered received by both surfaces of the filter plate to be bent but, since the flat membranes 30, 30 on both surfaces of the filter plate 20 and the metal net are formed from a metal being a ductile material, the filter plate 20 is deformed so that the forces received by both surfaces thereof become equal. Therefore, the stress generated in the filter plate 20 is caused only by centrifugal force and the filter plate 20 can be used even if it is thin. By making the filter plate 20 thin, the wt. reduction of the filter plate 20 is achieved.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、回転型膜分離装置用濾
過板に係り、特に医薬品や食品等の製造工程における溶
液の濾過や濃縮に用いられる回転型膜分離装置用濾過板
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter for a rotary membrane separator, and more particularly to a filter for a rotary membrane separator used for filtering and concentrating a solution in the manufacturing process of medicines, foods and the like.

【0002】[0002]

【従来の技術】濾過等に使用される膜分離装置として、
水平に設置した回転自在な支持軸上に濾過板を垂直に設
置し、濾過板を回転させることにより起こる乱流効果で
濾過板表面への汚れの蓄積を防止し、濾過量が低下する
のを制御しながら濾過する装置が考案されている。
2. Description of the Related Art As a membrane separator used for filtration,
A filter plate is installed vertically on a horizontally supported rotatable shaft, and the turbulent flow effect caused by rotating the filter plate prevents dirt from accumulating on the filter plate surface and reduces the filtration amount. Controlled filtration devices have been devised.

【0003】この種の膜分離装置に用いられる濾過板と
しては、耐蝕性、耐熱性に優れた無機材料を用いたもの
が考案されており、例えば、特開平4─358528号
公報に開示されているもののように、セラミック多孔質
材からなる支持体の表面に緻密なセラミック多孔質濾過
膜を被覆した濾過板がある。しかし、このような濾過板
を工業的に利用する場合には、広い膜面積が必要になる
ため、濾過板の外径は500〜1000mmと比較的大き
な部材になる。また、通常、濾過板は1つの支持軸上に
数十枚並設されており、装置の容積効率を高くするため
に濾過板の間隔を狭くしているが、このとき、濾過板間
の被濾過液は濾過板と共回りする。その結果、濾過板表
面の剪断力が小さくなり、濾過板表面に汚れが蓄積して
濾過量が低下する。
As a filter plate used in this type of membrane separator, a filter plate made of an inorganic material having excellent corrosion resistance and heat resistance has been devised. For example, it is disclosed in Japanese Patent Laid-Open No. 4-358528. There is a filter plate in which the surface of a support made of a ceramic porous material is covered with a dense ceramic porous filtration membrane. However, when such a filter plate is industrially used, a wide membrane area is required, and therefore the filter plate has a relatively large outer diameter of 500 to 1000 mm. Usually, dozens of filter plates are arranged side by side on a single support shaft, and the intervals between the filter plates are narrowed in order to increase the volumetric efficiency of the device. The filtrate co-rotates with the filter plate. As a result, the shearing force on the surface of the filter plate is reduced, and dirt is accumulated on the surface of the filter plate, and the filtration amount is reduced.

【0004】ところで、簡易に被濾過液の共回りによる
濾過量の減少を防止する方法としては、実開平3─70
729号公報に開示されたものがある。これは濾過板間
にバッフルプレートを挿入するものであり、このバッフ
ルプレートを挿入することによって、被濾過液が共回り
をしていても、濾過板(回転板)とバッフルプレート
(固定板)の間に速度勾配が生じるので、濾過板表面に
剪断力を与えることができ、汚れを剥離させることがで
きる。
By the way, as a method for simply preventing the decrease of the filtration amount due to the co-rotation of the liquid to be filtered, the actual Kaihei 3-70 is used.
There is one disclosed in Japanese Patent No. 729. This is to insert a baffle plate between the filter plates. By inserting this baffle plate, even if the liquid to be filtered is co-rotating, the filter plate (rotating plate) and the baffle plate (fixed plate) Since a velocity gradient is generated between them, a shearing force can be applied to the surface of the filter plate and dirt can be peeled off.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、工業用
の装置では、濾過板間の真の中心に濾過板と完全に平行
にバッフルプレートを据え付けることは極めて困難であ
り、このため、バッフルプレートの表面と裏面で被濾過
液の流速が異なり、圧力が異なるので、濾過液に曲げ応
力を生じさせることになる。本出願人の実測によれば、
被濾過液中で濾過液を回転させた場合、空気中に比べて
約3倍の負荷応力が生じている。この結果、被濾過液中
で濾過板を回転させる場合には、濾過板の厚さを増して
強度を増す必要がある。(通常、無機多孔質支持体で
は、10mm以上の厚さが必要である)しかしながら、濾
過板の厚みを増すと、容積比率が悪化するだけでなく、
濾過板重量が増すため、支持軸の軸径を大きくする必要
があるとともに、取り扱いが困難になる等の欠点があ
る。
However, in the industrial apparatus, it is extremely difficult to install the baffle plate in the true center between the filter plates and completely parallel to the filter plates. Therefore, the surface of the baffle plate is difficult to install. Since the flow velocity of the liquid to be filtered is different and the pressure is different between the back surface and the back surface, bending stress is generated in the filtered liquid. According to the measurement by the applicant,
When the filtrate is rotated in the liquid-to-be-filtrated, about three times as much load stress is generated as in the air. As a result, when the filter plate is rotated in the liquid to be filtered, it is necessary to increase the thickness of the filter plate to increase its strength. (Usually, an inorganic porous support requires a thickness of 10 mm or more.) However, increasing the thickness of the filter plate not only deteriorates the volume ratio,
Since the weight of the filter plate increases, it is necessary to increase the shaft diameter of the support shaft, and there are drawbacks such that handling becomes difficult.

【0006】本発明はこのような事情を鑑みてなされた
もので、薄くかつ軽量な回転型膜分離装置用濾過板を提
供することを目的とする。
The present invention has been made in view of the above circumstances, and an object thereof is to provide a thin and lightweight filter plate for a rotary membrane separator.

【0007】[0007]

【課題を解決する為の手段】本発明は、前記目的を達成
するために、軸方向に所定の間隔をもって連通口が穿設
された中空の駆動軸を、円筒状のケーシングに回転自在
に配設するとともに該駆動軸にカラーを介して円板状の
複数の濾過板を前記連通口に臨んで固定し、前記ケーシ
ング内に供給される被濾過液を前記濾過板を介して濾過
し、その濾過液を前記駆動軸の内部を通して排出する回
転型膜分離装置において、前記濾過板は、一対の円板状
の金属製平膜の外周を接合して一体形成するとともに該
平膜間にスペーサを設けて形成されることを特徴とす
る。
In order to achieve the above-mentioned object, the present invention rotatably arranges a hollow drive shaft, in which a communication port is bored at a predetermined interval in the axial direction, in a cylindrical casing. A plurality of disk-shaped filter plates are fixed to the drive shaft through a collar while facing the communication port, and the liquid to be filtered supplied into the casing is filtered through the filter plate, In the rotary membrane separator that discharges the filtrate through the inside of the drive shaft, the filtration plate is formed by joining a pair of disc-shaped flat metal membranes integrally with each other and forming a spacer between the flat membranes. It is provided and formed.

【0008】[0008]

【作用】本発明によれば、被濾過液中で濾過板を回転さ
せると、濾過板の両面に受ける被濾過液の流動による圧
力差により濾過板が撓むが、濾過板の両面の平膜は延性
材料である金属で形成されているため、両面に受ける力
が等しくなるように変形する。従って、濾過板に生じる
応力は遠心力によるものだけになり、濾過板が薄くても
使用することができる。
According to the present invention, when the filter plate is rotated in the liquid to be filtered, the filter plate is bent due to the pressure difference due to the flow of the liquid to be filtered which is received on both surfaces of the filter plate. Since is made of a ductile metal, it deforms so that the forces on both sides are equal. Therefore, the stress generated in the filter plate is only due to the centrifugal force, and the filter plate can be used even if it is thin.

【0009】[0009]

【実施例】以下添付図面に従って本発明に係る回転型膜
分離装置用濾過板の好ましい実施例について詳説する。
図1は、本発明に係る濾過板が適用される回転型膜分離
装置の断面図である。同図に示すように、回転型膜分離
装置10は、円筒状に形成された密閉容器12の中心部
に駆動軸14が設置される。この駆動軸14は、内部に
空洞部16が形成されるとともに、外周部14Aに軸の
長手方向に沿って前記空洞部16に通じる連通口18、
18、…が所定間隔で穿設されている。そして、この駆
動軸14には、中空円板状の濾過板20、20、…が前
記連通口18、18、…に連通するようにカラー22、
22、…を介して装着されている。また、前記濾過板2
0、20、…間には、バッフルプレート24、24、…
が配設されており、バッフルプレート24、24、…は
密閉容器12内の壁面12Aに設けられた支持棒26に
支持されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT A preferred embodiment of the filter plate for a rotary membrane separator according to the present invention will be described in detail below with reference to the accompanying drawings.
FIG. 1 is a cross-sectional view of a rotary membrane separation device to which a filter plate according to the present invention is applied. As shown in the figure, in the rotary membrane separation device 10, a drive shaft 14 is installed at the center of a closed container 12 formed in a cylindrical shape. The drive shaft 14 has a hollow portion 16 formed therein, and a communication port 18 communicating with the hollow portion 16 along the longitudinal direction of the shaft in the outer peripheral portion 14A.
18 are formed at predetermined intervals. The drive shaft 14 is provided with a collar 22, so that the hollow disk-shaped filter plates 20, 20, ... Can communicate with the communication ports 18, 18 ,.
It is attached through 22, .... In addition, the filter plate 2
Baffle plates 24, 24, ... Between 0, 20 ,.
Are provided, and the baffle plates 24, 24, ... Are supported by a support rod 26 provided on a wall surface 12A in the closed container 12.

【0010】前記の如く構成される回転型膜分離装置1
0は、密閉容器12内に被濾過液を導入して駆動軸14
を回転させると、被濾過液中に含まれている懸濁物質な
どは、濾過板20、20、…で濾過され、濾過液は駆動
軸14の空洞部16から取り出される。図2は本発明に
係る濾過板の第1実施例の平面図であり、図3は図2に
おける側面図である。図2及び図3に示すように、濾過
板20は、金属製のスペーサ例えばSUS304の金網
28の両面に円板状の金属製平膜30、30を重ね合わ
せ、その外周部30A、30Aを溶接して一体形成した
ものである。この前記金属製平膜30、30は、例え
ば、圧延した金網上に金属微粉末を焼結したものを用
い、厚さは約1mmである。従って、濾過板20の厚さは
約3mmとなる。また、この濾過板20の中心部には、前
記駆動軸14に装着するための装着穴32が形成されて
いる。
The rotary type membrane separation device 1 constructed as described above.
0 is the drive shaft 14 by introducing the liquid to be filtered into the closed container 12.
When is rotated, suspended substances and the like contained in the liquid to be filtered are filtered by the filtration plates 20, 20, ... And the filtered liquid is taken out from the hollow portion 16 of the drive shaft 14. 2 is a plan view of the first embodiment of the filter plate according to the present invention, and FIG. 3 is a side view of FIG. As shown in FIGS. 2 and 3, in the filter plate 20, disc-shaped metal flat films 30, 30 are superposed on both surfaces of a metal spacer, for example, a metal net 28 of SUS304, and outer peripheral portions 30A, 30A thereof are welded. And are integrally formed. The flat metal films 30 and 30 are, for example, those obtained by sintering fine metal powder on a rolled wire mesh and have a thickness of about 1 mm. Therefore, the thickness of the filter plate 20 is about 3 mm. Further, a mounting hole 32 for mounting on the drive shaft 14 is formed at the center of the filter plate 20.

【0011】前記如く構成される第1実施例の濾過板2
0の作用は次のようになる。濾過板20を前記回転型膜
分離装置10にセットして、密閉容器12内に被濾過液
を導入し、その被濾過液中で濾過板20を回転させる
と、被濾過液は金属製平膜30、30を透過し、平膜3
0、30間を金網28に沿って流れ、連通口18を通っ
て駆動軸14の空洞部16に達する。
The filter plate 2 of the first embodiment constructed as described above.
The action of 0 is as follows. When the filtration plate 20 is set in the rotary membrane separator 10 and the liquid to be filtered is introduced into the closed container 12 and the filtration plate 20 is rotated in the liquid to be filtered, the liquid to be filtered is a flat metal film. Permeate through 30, 30, flat membrane 3
It flows along the wire net 28 between 0 and 30 and reaches the cavity 16 of the drive shaft 14 through the communication port 18.

【0012】一方、濾過板20を被濾過液中で回転させ
ると、濾過板20の両面に受ける被濾過液の流動による
圧力差により濾過板20は撓むが、濾過板20の両面の
平膜30、30及び金網28は延性材料である金属で形
成されているため、両面に受ける力が等しくなるように
変形する。従って、濾過板20が受ける応力は遠心力に
よるもののみとなり、濾過板20が薄い場合でも使用が
可能になる。
On the other hand, when the filter plate 20 is rotated in the liquid to be filtered, the filter plate 20 bends due to the pressure difference due to the flow of the liquid to be filtered received on both sides of the filter plate 20, but the flat membranes on both sides of the filter plate 20. Since the wires 30, 30 and the wire netting 28 are made of metal which is a ductile material, they are deformed so that the forces applied to both surfaces are equal. Therefore, the stress applied to the filter plate 20 is only due to the centrifugal force, and it can be used even when the filter plate 20 is thin.

【0013】図4は本発明に係る濾過板の第2実施例の
平面図である。同図に示すように、本第2実施例の濾過
板20は、前記第1実施例で説明した濾過板20の平膜
30、30の外周部30A、30Aの4か所に90度間
隔で切欠部30B、30Bが形成され、その切欠部30
B、30Bにバランスウェイト34、34、…が設けら
れている。このバランスウェイト34、34、…を濾過
板20に設けることにより、濾過板20の回転バランス
調整が可能になり、その調整方法は次のように行う。濾
過板20の回転バランスをバランス測定器で検出し、そ
の結果に基づいて前記バランスウェイト34、34、…
に穴36、36、…を開ける。
FIG. 4 is a plan view of a second embodiment of the filter plate according to the present invention. As shown in the figure, the filter plate 20 of the second embodiment has four flat membranes 30, 30 of the filter plate 20 described in the first embodiment, which are arranged at 90 ° intervals at four positions of the outer peripheral portions 30A, 30A. The cutouts 30B and 30B are formed, and the cutouts 30 are formed.
B and 30B are provided with balance weights 34, 34, .... By providing the balance weights 34, 34, ... On the filter plate 20, it is possible to adjust the rotational balance of the filter plate 20, and the adjustment method is as follows. A balance measuring device detects the rotational balance of the filter plate 20, and based on the result, the balance weights 34, ...
Make holes 36, 36 ...

【0014】このように、本第2実施例の濾過板20に
よれば、簡便に濾過板20のバランス調整をすることが
できる。また、これにより、濾過板20の回転が安定
し、高速回転時の使用にも適用することができる。図5
は本発明に係る濾過板の第3実施例の平面図であり、図
6は図5における側面図である。図5及び図6に示すよ
うに、本第3実施例の濾過板20は、前記第1実施例で
説明した濾過板20の平膜30、30の外周部30A、
30Aの溶接に、リング38を介して行ったものであ
る。
As described above, according to the filter plate 20 of the second embodiment, the balance of the filter plate 20 can be easily adjusted. Further, this stabilizes the rotation of the filter plate 20 and can be applied to the use during high-speed rotation. Figure 5
FIG. 6 is a plan view of a third embodiment of the filter plate according to the present invention, and FIG. 6 is a side view of FIG. As shown in FIGS. 5 and 6, the filter plate 20 according to the third embodiment is the outer peripheral portion 30A of the flat membranes 30, 30 of the filter plate 20 described in the first embodiment.
The welding of 30A was performed via the ring 38.

【0015】これにより、濾過板20が薄い場合であっ
ても、濾過板20はリング38により支持されるので、
持ち運び時に撓まなくなり、取り扱いが容易になる。ま
た、図7及び図8に示すように、濾過板20の中心部
(装着穴32)にリング40を設け、そのリング40よ
り放射状に棒状の補強部材42、42、…を配設してよ
い。この場合、濾過板20は補強部材42、42、…に
より支持される。
As a result, even if the filter plate 20 is thin, the filter plate 20 is supported by the ring 38,
It will not bend when carried and will be easier to handle. Further, as shown in FIGS. 7 and 8, a ring 40 may be provided in the central portion (mounting hole 32) of the filter plate 20, and rod-shaped reinforcing members 42, 42, ... May be arranged radially from the ring 40. . In this case, the filter plate 20 is supported by the reinforcing members 42, 42, ....

【0016】図9は本発明に係る濾過板の第4実施例の
平面図であり、図10は図9における側面図である。図
9及び図10に示すように、本第4実施例の濾過板20
は、前記第1実施例で説明した濾過板20を金属製のカ
ラー18に一体形成したものである。前記カラー18
は、外周面の中心部に連通口18Aが形成されており、
前記濾過板20は、中心部に形成された装着穴32が前
記連通口18Aに連通するように取り付けられて溶接さ
れる。
FIG. 9 is a plan view of a fourth embodiment of the filter plate according to the present invention, and FIG. 10 is a side view of FIG. As shown in FIGS. 9 and 10, the filter plate 20 according to the fourth embodiment.
The filter plate 20 described in the first embodiment is integrally formed with the metal collar 18. The color 18
Has a communication port 18A formed at the center of the outer peripheral surface,
The filter plate 20 is attached and welded so that the mounting hole 32 formed at the center communicates with the communication port 18A.

【0017】これにより、濾過板20を駆動軸14に装
着する際に、別途カラー18を用いることなく装着でき
るため、部品点数を削減することができる。また、図1
1に示すように、カラー18を濾過板20の側面部に溶
接して一体形成してもよい。
As a result, when the filter plate 20 is mounted on the drive shaft 14, the filter plate 20 can be mounted without using a separate collar 18, and the number of parts can be reduced. Also, FIG.
As shown in FIG. 1, the collar 18 may be integrally formed by welding to the side surface portion of the filter plate 20.

【0018】[0018]

【発明の効果】以上説明したように、本発明の回転型膜
分離装置用濾過板によれば、被濾過液中で濾過板を回転
させると、濾過板の両面に受ける被濾過液の流動による
圧力差により濾過板が撓むが、濾過板の両面の平膜は延
性材料である金属で形成されているため、両面に受ける
力が等しくなるように変形する。従って、濾過板に生じ
る応力は遠心力によるものだけになり、濾過板が薄くて
も使用することができる。
As described above, according to the filter plate for a rotary membrane separator of the present invention, when the filter plate is rotated in the liquid to be filtered, the liquid to be filtered receives on both sides of the filter plate. The filter plate bends due to the pressure difference, but since the flat membranes on both sides of the filter plate are made of metal, which is a ductile material, they deform so that the forces applied to both sides are equal. Therefore, the stress generated in the filter plate is only due to the centrifugal force, and the filter plate can be used even if it is thin.

【0019】また、濾過板を薄くすることにより軽量化
も図れ、回転型膜分離装置の駆動軸等の強度を増す必要
がなくなるので、装置制作費を大幅に削減することがで
きる。
Further, by thinning the filter plate, the weight can be reduced, and it is not necessary to increase the strength of the drive shaft of the rotary membrane separation device, so that the production cost of the device can be greatly reduced.

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

【図1】本発明に係る濾過板が適用される回転型膜分離
装置の断面図
FIG. 1 is a cross-sectional view of a rotary membrane separator to which a filter plate according to the present invention is applied.

【図2】本発明に係る濾過板の第1実施例の平面図FIG. 2 is a plan view of a first embodiment of a filter plate according to the present invention.

【図3】図2における側面図FIG. 3 is a side view of FIG.

【図4】本発明に係る濾過板の第2実施例の平面図FIG. 4 is a plan view of a second embodiment of the filter plate according to the present invention.

【図5】本発明に係る濾過板の第3実施例の平面図FIG. 5 is a plan view of a third embodiment of the filter plate according to the present invention.

【図6】図6における側面図6 is a side view of FIG.

【図7】本発明に係る濾過板の第3実施例の変形例を示
す平面図
FIG. 7 is a plan view showing a modification of the third embodiment of the filter plate according to the present invention.

【図8】図7における側面図8 is a side view of FIG.

【図9】本発明に係る濾過板の第4実施例の平面図FIG. 9 is a plan view of a fourth embodiment of the filter plate according to the present invention.

【図10】図9における側面図FIG. 10 is a side view of FIG.

【図11】本発明に係る濾過板の第4実施例の変形例を
示す断面図
FIG. 11 is a sectional view showing a modification of the fourth embodiment of the filter plate according to the present invention.

【符号の説明】[Explanation of symbols]

10…回転型膜分離装置 12…密閉容器 14…駆動軸 16…空洞部 18…連通口 20…濾過板 22…カラー 24…バッフルプレート 28…金網 30…平膜 34…バランスウェイト 38、40…リング 42…補強部材 DESCRIPTION OF SYMBOLS 10 ... Rotation type | formula membrane separator 12 ... Airtight container 14 ... Drive shaft 16 ... Cavity 18 ... Communication port 20 ... Filtration plate 22 ... Collar 24 ... Baffle plate 28 ... Wire mesh 30 ... Flat membrane 34 ... Balance weight 38, 40 ... Ring 42 ... Reinforcing member

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】軸方向に所定の間隔をもって連通口が穿設
された中空の駆動軸を、円筒状のケーシングに回転自在
に配設するとともに該駆動軸にカラーを介して円板状の
複数の濾過板を前記連通口に臨んで固定し、前記ケーシ
ング内に供給される被濾過液を前記濾過板を介して濾過
し、その濾過液を前記駆動軸の内部を通して排出する回
転型膜分離装置において、 前記濾過板は、一対の円板状の金属製平膜の外周を接合
して一体形成するとともに該平膜間にスペーサを設けて
形成されることを特徴とする回転型膜分離装置用濾過
板。
1. A hollow drive shaft having communication holes formed at predetermined intervals in the axial direction is rotatably disposed in a cylindrical casing, and a plurality of disc-shaped drive shafts are provided on the drive shaft via a collar. A rotary membrane separation device that fixes the filter plate facing the communication port, filters the liquid to be filtered supplied into the casing through the filter plate, and discharges the filtered liquid through the inside of the drive shaft. In the rotary membrane separation device, the filter plate is formed by joining the outer circumferences of a pair of disc-shaped metal flat membranes integrally with each other and providing a spacer between the flat membranes. Filter plate.
【請求項2】前記スペーサは、金網であることを特徴と
する請求項1記載の回転式膜分離装置用濾過板。
2. The filter plate for a rotary membrane separator according to claim 1, wherein the spacer is a wire mesh.
【請求項3】前記濾過板は、外周部にバランスウェイト
が設けられていることを特徴とする請求項1記載の回転
式膜分離装置用濾過板。
3. The filter plate for a rotary membrane separator according to claim 1, wherein the filter plate is provided with a balance weight on an outer peripheral portion thereof.
【請求項4】前記濾過板の平膜の外周は、リングを介し
て溶接されていることを特徴とする請求項1記載の回転
型膜分離用濾過板。
4. The rotary membrane separation filter plate according to claim 1, wherein an outer periphery of the flat plate membrane of the filter plate is welded through a ring.
【請求項5】前記濾過板は、前記平膜間に補強部材が放
射状に配設されていることを特徴とする請求項1記載の
回転型膜分離装置用濾過板。
5. The filter plate for a rotary membrane separator according to claim 1, wherein the filter plate has reinforcing members arranged radially between the flat membranes.
【請求項6】前記濾過板は、前記カラーと一体成形され
ていることを特徴とする請求項1記載の回転型膜分離装
置用濾過板。
6. The filter plate for a rotary membrane separator according to claim 1, wherein the filter plate is integrally formed with the collar.
JP32382194A 1994-11-30 1994-11-30 Filter plate for rotary membrane separator Expired - Fee Related JP3353511B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32382194A JP3353511B2 (en) 1994-11-30 1994-11-30 Filter plate for rotary membrane separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32382194A JP3353511B2 (en) 1994-11-30 1994-11-30 Filter plate for rotary membrane separator

Publications (2)

Publication Number Publication Date
JPH08155279A true JPH08155279A (en) 1996-06-18
JP3353511B2 JP3353511B2 (en) 2002-12-03

Family

ID=18158983

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32382194A Expired - Fee Related JP3353511B2 (en) 1994-11-30 1994-11-30 Filter plate for rotary membrane separator

Country Status (1)

Country Link
JP (1) JP3353511B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1236500A1 (en) * 2001-02-26 2002-09-04 Hitachi Plant Engineering & Construction Co., Ltd. Flat membrane disk
US6627080B2 (en) 1999-12-28 2003-09-30 Hitachi Plant Engineering & Construction Co., Ltd. Flat membrane disk
CN1323955C (en) * 2005-09-23 2007-07-04 浙江大学 Rotary disk type membrane bioreactor and its water treatment method
WO2011112872A3 (en) * 2010-03-12 2012-01-12 Levitt David J Fluid filtration and particle concentration device and methods
CN104258624A (en) * 2014-10-03 2015-01-07 安平县中旺矿筛丝网有限公司 Pressure filter stainless steel net bush and manufacturing method thereof
US10286338B2 (en) 2014-01-13 2019-05-14 Spiral Water Technologies, Inc. Flow control features for fluid filtration device and methods
JP2020032316A (en) * 2018-08-27 2020-03-05 国立大学法人高知大学 Wastewater treatment device and wastewater treatment method
JP2020032315A (en) * 2018-08-27 2020-03-05 国立大学法人高知大学 Wastewater treatment equipment

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6627080B2 (en) 1999-12-28 2003-09-30 Hitachi Plant Engineering & Construction Co., Ltd. Flat membrane disk
EP1236500A1 (en) * 2001-02-26 2002-09-04 Hitachi Plant Engineering & Construction Co., Ltd. Flat membrane disk
CN1323955C (en) * 2005-09-23 2007-07-04 浙江大学 Rotary disk type membrane bioreactor and its water treatment method
WO2011112872A3 (en) * 2010-03-12 2012-01-12 Levitt David J Fluid filtration and particle concentration device and methods
AU2011224246B2 (en) * 2010-03-12 2014-03-27 Spiral Water Technologies, Inc. Fluid filtration and particle concentration device and methods
US9409106B2 (en) 2010-03-12 2016-08-09 Spiral Water Technologies, Inc. Fluid filtration and particle concentration device and methods
US9895635B2 (en) 2010-03-12 2018-02-20 Spiral Water Technologies, Inc. Fluid filtration and particle concentration device and methods
US10286338B2 (en) 2014-01-13 2019-05-14 Spiral Water Technologies, Inc. Flow control features for fluid filtration device and methods
CN104258624A (en) * 2014-10-03 2015-01-07 安平县中旺矿筛丝网有限公司 Pressure filter stainless steel net bush and manufacturing method thereof
JP2020032316A (en) * 2018-08-27 2020-03-05 国立大学法人高知大学 Wastewater treatment device and wastewater treatment method
JP2020032315A (en) * 2018-08-27 2020-03-05 国立大学法人高知大学 Wastewater treatment equipment

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