JPH067788Y2 - Membrane separation device - Google Patents
Membrane separation deviceInfo
- Publication number
- JPH067788Y2 JPH067788Y2 JP12678790U JP12678790U JPH067788Y2 JP H067788 Y2 JPH067788 Y2 JP H067788Y2 JP 12678790 U JP12678790 U JP 12678790U JP 12678790 U JP12678790 U JP 12678790U JP H067788 Y2 JPH067788 Y2 JP H067788Y2
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- holder
- cleaning member
- liquid
- membrane separation
- 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
Links
- 239000012528 membrane Substances 0.000 title claims description 104
- 238000000926 separation method Methods 0.000 title claims description 39
- 238000004140 cleaning Methods 0.000 claims description 43
- 239000007788 liquid Substances 0.000 claims description 37
- 230000007246 mechanism Effects 0.000 claims description 3
- 239000012466 permeate Substances 0.000 description 7
- 238000003780 insertion Methods 0.000 description 4
- 230000037431 insertion Effects 0.000 description 4
- 238000007790 scraping Methods 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000007779 soft material Substances 0.000 description 3
- 230000002706 hydrostatic effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000010287 polarization Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 229920005830 Polyurethane Foam Polymers 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000013013 elastic material Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000011496 polyurethane foam Substances 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 239000013585 weight reducing agent Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Description
【考案の詳細な説明】 〈産業上の利用分野〉 本考案は、液体の膜分離に伴い円板膜の膜面上に付着す
る濁質等の堆積物を除去するための洗浄機構を備えた膜
分離装置の改良に関するものである。[Detailed Description of the Invention] <Industrial Application Field> The present invention has a cleaning mechanism for removing deposits such as turbidity adhering to the film surface of a disk film due to liquid film separation. The present invention relates to improvement of a membrane separation device.
〈従来の技術〉 精密濾過膜、限外濾過膜、逆浸透膜などの膜を用いた膜
分離装置としては、従来より中空糸状、管膜状、スパイ
ラル状、平板状などの膜分離手段を用いたものがある
が、近年、特に濁質濃度の高い液体の膜分離に適したも
のとして、回転する円板膜を用いる膜分離装置が提案さ
れている。<Prior art> As a membrane separation device using a membrane such as a microfiltration membrane, an ultrafiltration membrane, or a reverse osmosis membrane, conventionally, a hollow fiber-shaped, tubular membrane-shaped, spiral-shaped, or flat-shaped membrane separation means has been used. However, in recent years, a membrane separation device using a rotating disc membrane has been proposed as a device particularly suitable for membrane separation of a liquid having a high turbidity concentration.
当該膜分離装置は、中空の回転軸の軸方向に、回転軸と
一体に回転する円板膜を所定の間隔をおいて複数枚並列
させてなる膜分離手段を、開放状あるいは密閉状の容器
内に収納した構造のものであり、使用に際しては容器内
に被処理液を流入させて前記膜分離手段を被処理液中に
浸漬して被処理液の膜分離を行い、円板膜の内部に得ら
れる膜透過液を回転軸の中空部に集液して容器外へ流出
させる。そして、前記膜分離手段を開放状の容器内に収
納して使用する場合には、被処理液の静水圧を利用する
か、あるいは膜透過液側、すなわち円板膜の内側を減圧
することによって膜分離を行い、また密閉状の容器内に
収納して使用する場合は被処理液を主に加圧することに
よって膜分離を行う。このような膜分離装置は、円板膜
自体の回転によって膜面の濃度分極を抑制できるので、
容器内の被処理液を他の手段で攪拌あるいは流動させる
必要がなく、低エネルギーで液体分離を行うことができ
るという利点を有する。The membrane separation device is an open or closed container having a membrane separation means in which a plurality of disc membranes that rotate integrally with the rotary shaft are arranged in parallel in the axial direction of the hollow rotary shaft at predetermined intervals. When used, the liquid to be treated is made to flow into the container and the membrane separation means is immersed in the liquid to be treated to perform membrane separation of the liquid to be treated. The membrane-permeated liquid obtained in (1) is collected in the hollow part of the rotating shaft and allowed to flow out of the container. When the membrane separation means is used by being housed in an open container, the hydrostatic pressure of the liquid to be treated is used, or the membrane permeate side, that is, the pressure inside the disc membrane is reduced. Membrane separation is performed, and when the membrane is housed in a closed container for use, the liquid to be treated is mainly pressurized to perform membrane separation. Such a membrane separator can suppress concentration polarization on the membrane surface by rotating the disc membrane itself,
There is no need to stir or flow the liquid to be treated in the container by other means, and the liquid can be separated with low energy.
しかし、上述の膜分離装置で液体の膜分離を継続して行
うと、円板膜の膜面に被処理液中に含有される濁質が堆
積したり、あるいはゲル層が堆積したりして膜透過流速
が著しく低下する。However, when the membrane separation of the liquid is continuously performed with the above-mentioned membrane separation device, suspended matter contained in the liquid to be treated is deposited on the membrane surface of the disc membrane, or a gel layer is deposited. The membrane permeation flow rate is significantly reduced.
従来、このような堆積物を膜面から除去し、膜透過流速
を回復させるには、円板膜を断続的に高速回転させると
よいといわれているが、この方法は実際にはあまり効果
がない。Conventionally, it has been said that it is good to intermittently rotate the disc membrane at a high speed in order to remove such deposits from the membrane surface and recover the membrane permeation flow velocity, but this method is actually not very effective. Absent.
そこで、この問題を解消するために、円板膜の膜面にス
ポンジなどの柔軟材からなる洗浄部材を接触させて、洗
浄部材によって膜面上に付着する堆積物を擦り取るよう
にした膜分離装置が提案されている。Therefore, in order to solve this problem, a cleaning member made of a soft material such as a sponge is brought into contact with the film surface of the disc film, and the deposit adhered to the film surface is scraped off by the cleaning member. A device has been proposed.
従来の膜分離装置を第5図に基づいて説明すると、横置
きにした円筒形の密閉構造の容器51の中心軸に、中空
の回転軸52が、その両端部を容器51の側壁に貫通さ
せた状態で設置され、回転軸52の軸方向に所定の間隔
をおいて、かつ膜面が回転軸方向52に対して垂直とな
るように円板膜53が複数枚並設されている。円板膜5
3は、例えば円板状の支持枠体の両面に前記したような
分離膜を張設した構造をなしたもので、回転軸52と一
体に回転するように取り付けられており、回転軸52は
その一端側に取り付けられたモータ55によって駆動さ
れ回転する。なお、符号54は回転軸52と円板膜53
とで構成される膜分離手段を示している。A conventional membrane separation device will be described with reference to FIG. 5. A hollow rotating shaft 52 is inserted into a side wall of the container 51 with a hollow rotating shaft 52 extending through a center axis of a horizontally closed cylindrical container 51 having a closed structure. In this state, a plurality of disc films 53 are arranged side by side at a predetermined interval in the axial direction of the rotating shaft 52 and the film surfaces are perpendicular to the rotating shaft direction 52. Disk membrane 5
3 has, for example, a structure in which the above-mentioned separation membrane is stretched on both sides of a disk-shaped support frame, and is attached so as to rotate integrally with the rotary shaft 52. It is driven and rotated by a motor 55 attached to one end thereof. In addition, reference numeral 54 represents the rotating shaft 52 and the disc film 53.
The membrane separation means composed of and is shown.
各円板膜53の膜面には、スポンジなどの柔軟材からな
る洗浄部材56が接触している。洗浄部材56は例えば
接着剤などによって棒状のホールダ57に接着、固定さ
れており、またホールダ57は、その一端部を容器51
内に横設した固定棒58に固定されている。A cleaning member 56 made of a soft material such as sponge is in contact with the film surface of each disk film 53. The cleaning member 56 is adhered and fixed to a rod-shaped holder 57 with, for example, an adhesive agent, and the holder 57 has one end portion thereof attached to the container 51.
It is fixed to a fixed rod 58 provided inside.
また、第5図において符号59は被処理液の流入口、6
0は濃縮液の流出口を示している。Further, in FIG. 5, reference numeral 59 is an inlet for the liquid to be treated, 6
0 indicates the outlet of the concentrated liquid.
上述のような膜分離装置を用いて液体の処理を行う場合
は、流入口59から容器51内に被処理液を加圧下に供
給するとともに、モータ55を駆動して円板膜53を回
転させながら膜分離を行うと、容器51内に供給された
被処理液は円板膜53と接触して膜透過液と非透過液と
に分離され、円板膜53を透過して円板膜53の内部に
集められた膜透過液は回転軸52の中空部に集液されて
回転軸52の一端側の開口部61から容器51外へ流出
し、一方非透過液は流出口60から容器51外へ排出さ
れる。When the liquid is processed using the above-described membrane separation device, the liquid to be treated is supplied from the inlet 59 into the container 51 under pressure, and the motor 55 is driven to rotate the disc membrane 53. While performing the membrane separation, the liquid to be treated supplied into the container 51 comes into contact with the disc membrane 53 to be separated into a membrane permeate liquid and a non-permeate liquid, and permeates the disc membrane 53 to form the disc membrane 53. The membrane permeated liquid collected inside is discharged to the outside of the container 51 through the opening 61 at one end of the rotary shaft 52 while the non-permeated liquid is collected from the outlet port 60 through the container 51. It is discharged to the outside.
上記構成の膜分離装置においては、円板膜53の膜面に
当接された洗浄部材56により、被処理液の膜分離に伴
って膜面上に付着する堆積物は常時擦り取られることと
なり、したがって膜面堆積物による透過流速の低下を防
止することが可能である。In the membrane separation device having the above-described configuration, the cleaning member 56 that is in contact with the membrane surface of the disc membrane 53 constantly scrapes off the deposits that adhere to the membrane surface due to the membrane separation of the liquid to be treated. Therefore, it is possible to prevent the permeation velocity from decreasing due to the film surface deposit.
〈考案が解決しようとする問題点〉 従来装置においては洗浄部材が円板膜に常時当接されて
おり、したがって洗浄部材を支持、固定しているホール
ダには、円板膜の回転に伴って円板膜と洗浄部材との摩
擦によるかなり大きな応力がかかることとなる。<Problems to be Solved by the Invention> In the conventional apparatus, the cleaning member is always in contact with the disk membrane, and therefore the holder supporting and fixing the cleaning member is accompanied by the rotation of the disk film. A considerable amount of stress is applied due to the friction between the disc film and the cleaning member.
しかしながら、従来はホールダをその一端部においての
み固定棒に固定した構成を採用しているので、前記の応
力がホールダと固定棒との接合部の一点に集中し、よっ
てホールダと固定棒との接合部の強度をかなり強くしな
いと前記の応力によってホールダが脱落したり、傾いた
りしてしまうという不具合を生じ、一方前記の応力に耐
え得るような支持構造とする場合は、使用する材質も例
えばステンレス鋼などの、強度的に優れた支持構造を採
れる金属製のものに限定されるとともに、多大なコスト
がかかるという問題点があった。However, conventionally, since the structure in which the holder is fixed to the fixed rod only at one end thereof is adopted, the above-mentioned stress concentrates at one point of the joint between the holder and the fixed rod, so that the joint between the holder and the fixed rod is made. If the strength of the part is not made sufficiently strong, the above-mentioned stress causes the holder to fall off or tilt, while in the case of a support structure that can withstand the above-mentioned stress, the material used is also stainless steel, for example. There is a problem in that it is limited to metal such as steel that can have a support structure excellent in strength, and that it costs a lot.
〈問題を解決するための手段〉 本考案は、従来装置における上述のような問題点を解決
することを目的とするもので、容器内に取り付けた中空
の固定軸に複数枚の円板膜を間隔を置いて挿着して膜分
離手段を構成するとともに、各円板膜の膜面に接して洗
浄部材を設けて洗浄機構を構成して、円板膜の膜透過液
を固定軸の中空部に集液して容器外へ流出させ、円板膜
の膜面上に付着した堆積物を洗浄部材によって擦り取る
ようにした膜分離装置であって、円板膜群の両端の固定
軸に支持枠体を回転可能に取付けるとともに支持枠体の
間に駆動部材を掛け渡し、さらに洗浄部材のホールダの
一端部に設けた取付口を固定軸に回転可能に取付け、ま
たホールダの他端部を駆動部材に係合し、支持枠体を回
転させて駆動部材によって洗浄部材のホールダを回転さ
せることを特徴とするものである。<Means for Solving the Problem> The present invention is intended to solve the above-mentioned problems in the conventional apparatus, and a plurality of disc membranes are attached to a hollow fixed shaft mounted in a container. A membrane separating means is formed by inserting at intervals, and a cleaning member is provided in contact with the membrane surface of each disc membrane to form a cleaning mechanism, and the membrane permeate of the disc membrane is hollow on the fixed shaft. It is a membrane separation device that collects liquid in a part of the disk and flows it out of the container, and scrapes off the deposit adhered on the film surface of the disk film by a cleaning member. The support frame is rotatably mounted, the drive member is hung between the support frames, and the mounting port provided at one end of the holder of the cleaning member is rotatably attached to the fixed shaft, and the other end of the holder is attached. The cleaning member is engaged by the drive member and the support frame is rotated so that the cleaning member is rotated by the drive member. It is characterized by rotating the ruda.
〈作用〉 以上述べたように、本考案は、支持枠体と駆動部材によ
って洗浄部材のホールダを回転させて円板膜の膜面上に
付着した堆積物を擦り取ることによって、洗浄部材の回
転に伴って円板膜との摩擦によりかかる応力、堆積物の
擦り取り時にかかる応力を、ホールダの取付口と駆動部
材の係合部分との両方に分散させて受け止め、ホールダ
を強固に支持するものである。<Operation> As described above, the present invention rotates the cleaning member by rotating the holder of the cleaning member with the support frame and the driving member to scrape off the deposits adhering to the film surface of the disc film. Along with this, the stress applied by friction with the disc film and the stress applied when scraping off the deposit are dispersed and received by both the holder mounting port and the engaging part of the drive member, and the holder is firmly supported. Is.
〈実施例〉 以下に本考案の実施例を図面に基づいて詳細に説明す
る。<Embodiment> An embodiment of the present invention will be described below in detail with reference to the drawings.
第1図は本考案の一実施例を示す膜分離装置の説明図、
第2図は第1図のA−A線断面図、第3図は第1図に示
した装置の洗浄部材部分の拡大斜視図である。FIG. 1 is an explanatory view of a membrane separation device showing an embodiment of the present invention,
2 is a sectional view taken along the line AA of FIG. 1, and FIG. 3 is an enlarged perspective view of a cleaning member portion of the apparatus shown in FIG.
図面において、1は横置きにした円筒形の密閉構造の容
器、2は容器1の中心軸に設置した中空の固定軸、3は
固定軸2の軸方向に所定の間隔をおいて、かつ膜面が固
定軸2に対して垂直となるように挿着した複数枚(図で
は3枚)の円板膜であり、4は固定軸2と円板膜3とで
構成される膜分離手段を示している。In the drawings, 1 is a horizontal cylindrical container having a closed structure, 2 is a hollow fixed shaft installed at the center axis of the container 1, 3 is a fixed space in the axial direction of the fixed shaft 2, and a membrane. A plurality of (three in the figure) disc membranes are inserted and attached so that their surfaces are perpendicular to the fixed shaft 2, and 4 is a membrane separation means composed of the fixed shaft 2 and the disc membrane 3. Shows.
また、固定軸2にはスペースリング5を介して洗浄部材
6を取り付けたホールダ7を回転可能に設けるが、この
ホールダ7は、第3図に示すように、例えば発泡ポリウ
レタン性スポンジ、ゴムなどの柔軟材あるいは弾性材な
どの洗浄部材6を接着などの手段によって張り付けると
ともに、その一端部に取付口8を設けたもので、この取
付口8を固定軸2に挿着したスペースリング5の溝に遊
びを持たせてはめ込めばよく、その他これに限らずホー
ルダ7を固定軸2に回転可能に取付けられれば、どのよ
うな手段でもよい。Further, a holder 7 having a cleaning member 6 attached thereto is rotatably provided on the fixed shaft 2 via a space ring 5. As shown in FIG. 3, the holder 7 is made of, for example, polyurethane foam sponge or rubber. A cleaning member 6 such as a soft material or an elastic material is attached by means such as adhesion, and a mounting port 8 is provided at one end thereof. The groove of the space ring 5 in which the mounting port 8 is inserted into the fixed shaft 2 is attached. Any means may be used as long as the holder 7 is rotatably attached to the fixed shaft 2 without being limited thereto.
なお、ホールダ7の洗浄部材6は各円板膜3の膜面、す
なわち円板膜3の両面に接触するようにする必要があ
る。The cleaning member 6 of the holder 7 needs to contact the film surface of each disk film 3, that is, both surfaces of the disk film 3.
また、ホールダ7はその一端部に取付口8を設けずに、
第4図に示すように、ホールダ7の一端部に、取付口8
を有する環状の端部材9を突設したものであってもよ
い。Further, the holder 7 does not have the mounting opening 8 at one end thereof,
As shown in FIG. 4, one end of the holder 7 has a mounting opening 8
The annular end member 9 may be provided so as to project.
洗浄部材6のホールダ7は平板状、棒状などいずれでも
よく、また洗浄部材6をホールダ7の周囲に巻付けた構
造としてもよい。The holder 7 of the cleaning member 6 may have a flat plate shape, a rod shape, or the like, and may have a structure in which the cleaning member 6 is wound around the holder 7.
また固定軸2に挿着するスペースリング5は、各円板膜
3の間に介在させることによって複数枚の円板膜3を所
定の間隔に保持して膜分離手段を効果的に機能させる役
目も持っている。Further, the space ring 5 inserted into the fixed shaft 2 serves to hold the plurality of disc membranes 3 at a predetermined interval by interposing them between the disc membranes 3 so that the membrane separating means can effectively function. I also have
さらに、円板膜3群の両端の固定軸2には支持枠体10
を回転可能に取付けるが、取付方法としては、支持枠体
10の中央部に設けた挿入穴11を固定軸2に遊びを持
たせて挿入すればよい。Further, the support frames 10 are provided on the fixed shafts 2 at both ends of the disk membrane group 3.
Is rotatably mounted. As a mounting method, the insertion hole 11 provided in the central portion of the support frame 10 may be inserted into the fixed shaft 2 with play.
支持枠体10の間に洗浄部材6の駆動部材12を掛け渡
し、支持枠体10を回転させて駆動部材12によって洗
浄部材6のホールダ7を回転させるためにホールダ7の
他端部を駆動部材12に係合させる。The drive member 12 of the cleaning member 6 is spanned between the support frames 10, and the support frame 10 is rotated to rotate the holder 7 of the cleaning member 6 by the drive member 12. 12 is engaged.
駆動部材12の形状としては、棒状、長手平板状のもの
などを用いることができるが、軽量化をはかり、かつ強
度をもたせるために樋状の部材を用いてもよい。The driving member 12 may have a rod shape, a long flat plate shape, or the like, but a gutter-shaped member may be used for weight reduction and strength.
なお、支持枠体10を回転させる手段の一つとしては、
第1図に示すように、固定軸2の一端部の外周に回転軸
13を設け、回転軸13に付設した回転基板14の接続
棒15を支持枠体10の挿入穴16に嵌め込んでもよ
く、これ以外にも回転基板14と支持枠体10とをボル
ト(図示してない)で固定するなど支持枠体10を回転
軸13によって回転させる手段であればどのようなもの
でもよい。In addition, as one of means for rotating the support frame 10,
As shown in FIG. 1, a rotary shaft 13 may be provided on the outer periphery of one end of the fixed shaft 2, and a connecting rod 15 of a rotary substrate 14 attached to the rotary shaft 13 may be fitted into an insertion hole 16 of the support frame 10. Other than this, any means may be used as long as it rotates the support frame 10 by the rotating shaft 13, such as fixing the rotary substrate 14 and the support frame 10 with bolts (not shown).
回転軸13はモータ20などの回転手段に接続するが、
場合によっては、モータ20の駆動力をプーリ、ベルト
などを介して回転軸13に伝えてもよい。なお、固定軸
2の回転基板14に接続する一端部は閉塞させ、また他
端部は開口させて透過液の流出口17とする。The rotating shaft 13 is connected to rotating means such as the motor 20,
In some cases, the driving force of the motor 20 may be transmitted to the rotary shaft 13 via a pulley, a belt or the like. It should be noted that one end of the fixed shaft 2 connected to the rotary substrate 14 is closed, and the other end is opened to serve as a permeate outlet 17.
また、ホールダ7の他端部と駆動部材12の係合部分
は、ホールダ7の他端部を駆動部材12に掛けた構造と
してあるが、本構造に限定されず、ホールダ7の他端部
に設けた挿入穴(図示せず)に駆動部材12を遊びを持
たせて挿入するなど、駆動部材12を駆動させることに
よりホールダ7の取付口8を中心としてホールダ7が回
転する構造であれば、どのようなものでもよい。Also, the other end of the holder 7 and the engaging portion of the driving member 12 have a structure in which the other end of the holder 7 is hung on the driving member 12, but the structure is not limited to this structure, and the other end of the holder 7 is If the structure is such that the drive member 12 is inserted into the provided insertion hole (not shown) with play, and the drive member 12 is driven to rotate the holder 7 around the mounting port 8 of the holder 7, It can be anything.
容器1には被処理液の流入管18と濃縮液の流出管19
を接続する。The container 1 has an inflow pipe 18 for the liquid to be treated and an outflow pipe 19 for the concentrated liquid.
Connect.
上記構成の本考案装置を用いて液体の膜分離を行う場合
は、前記従来装置の場合と同様に被処理液を流入口18
から容器1内に加圧下に供給するとともに、モータ20
を駆動して回転軸13、回転基板14、支持枠体10を
回転させて駆動部材12によって洗浄部材6のホールダ
7を回転させて、液体の膜分離処理を行うと、円板膜3
の膜透過液は固定軸2の中空部に集液して容器1外へ流
出して行き、円板膜3を透過しなかった非透過液は流出
管19から容器1外へ流出して行くが、膜分離処理に伴
い円板膜3の膜面上に付着した堆積物を洗浄部材6によ
って擦り取りながら膜分離処理を継続する。When performing the membrane separation of the liquid using the device of the present invention having the above-mentioned configuration, the liquid to be treated is introduced into the inlet 18 as in the case of the conventional device.
Is supplied to the container 1 under pressure from the motor 20
Is driven to rotate the rotary shaft 13, the rotary substrate 14, and the support frame 10, and the drive member 12 rotates the holder 7 of the cleaning member 6 to perform the liquid membrane separation process.
The membrane permeated liquid of (3) is collected in the hollow portion of the fixed shaft 2 and flows out of the container 1, and the non-permeated liquid that has not permeated the disc membrane 3 flows out of the container 1 through the outflow pipe 19. However, the membrane separation process is continued while scraping off the deposit adhered on the film surface of the disc membrane 3 by the cleaning member 6 with the membrane separation process.
このような膜分離処理を行っている間、円板膜3の膜面
は膜面に接触している洗浄部材6によって常時洗浄され
るが、洗浄部材6を取り付けたホールダ7を、支持枠体
10と駆動部材12によって回転させることによって、
堆積物の擦り取り時にかかる摩擦によるホールダ7に対
する応力を、ホールダ7の取付口8と駆動部材12の係
合部との両方に分散して受け止め、従来装置のように洗
浄部材を取り付けたホールダ7の一端部のみで支持して
いた場合に比べてより強固にホールダ7を支持すること
が可能である。While such a membrane separation process is being performed, the membrane surface of the disc membrane 3 is always cleaned by the cleaning member 6 in contact with the membrane surface. By rotating with 10 and the drive member 12,
The stress applied to the holder 7 due to the friction applied at the time of scraping off the deposits is dispersedly received by both the mounting port 8 of the holder 7 and the engaging portion of the driving member 12, and the holder 7 having the cleaning member attached thereto as in the conventional device is received. It is possible to more firmly support the holder 7 as compared with the case where the holder 7 is supported only at one end.
なお、上述の実施例では膜分離手段を密閉構造の容器内
に収納し、被処理液を加圧下に膜分離する装置例につい
て説明したが、本考案装置はこれに限らず、膜分離手段
を開放状の容器内に収納し、被処理液の静水圧を利用し
て、あるいは膜透過液側を減圧することによって膜分離
を行う構造としてもよい。In the above-described embodiment, the membrane separation means is housed in a container having a closed structure, and the example of the apparatus for membrane separation of the liquid to be treated under pressure has been described, but the device of the present invention is not limited to this, and the membrane separation means is not limited to this. The membrane may be housed in an open container, and the membrane may be separated by utilizing the hydrostatic pressure of the liquid to be treated or by reducing the pressure on the membrane permeate side.
また、上述の実施例では膜分離手段を、その固定軸が水
平となるように容器内に横型に設けたが、膜分離手段
を、その固定軸が垂直となるように竪型に設けてもよ
い。Further, in the above-mentioned embodiment, the membrane separating means is provided horizontally in the container so that its fixed axis is horizontal, but the membrane separating means may be provided vertically so that its fixed axis is vertical. Good.
〈効果〉 本考案によると、洗浄部材を取り付けたホールダを、支
持枠体と駆動部材によって回転させるので、洗浄部材と
円板膜との摩擦によりかかる応力、堆積物の擦り取り時
にかかる応力を、ホールダの取付口と駆動部分12の係
合部との両方で分散させて受け止め、ホールダをより強
固に支持する結果、ホールダの脱落、変形などはなくな
り、従来装置において一端部のみで支持していた場合の
問題点を解決できた。<Effect> According to the present invention, since the holder to which the cleaning member is attached is rotated by the support frame and the driving member, the stress applied by the friction between the cleaning member and the disc film and the stress applied when scraping the deposit are The holder is more firmly supported by being dispersed and received by both the mounting port of the holder and the engaging portion of the driving portion 12, and as a result, the holder does not drop out or be deformed, and only the one end is supported in the conventional device. I was able to solve the problem.
さらに、洗浄部材を回転させることによる攪拌効果によ
って、円板膜面の濃度分極の低減がはかれるというメリ
ットもある。Further, there is also an advantage that the concentration polarization of the disk film surface can be reduced by the stirring effect of rotating the cleaning member.
また、本考案においては、比較的重量の軽いホールダと
洗浄部材を回転させる構成であるので、これらよりはる
かに重い円板膜自体を回転させる従来装置に比べて、回
転トルクの低減という効果も達成できる。Further, in the present invention, since the holder and the cleaning member, which are relatively light in weight, are rotated, the effect of reducing the rotating torque is also achieved as compared with the conventional device that rotates the disc membrane itself, which is much heavier than these. it can.
なお、ホールダの材質としても、従来のように強度のあ
る金属製のものを使用する必要はなく、コスト的に安価
なもの、例えば硬質塩化ビニールなどのプラスチック製
のものを使用することが可能となり、コストの低減をも
はかれる。As for the material of the holder, it is not necessary to use a strong metal one as in the past, and it is possible to use a cheap one, for example, a plastic one such as hard vinyl chloride. The cost can be reduced.
第1図〜第4図はいずれも本考案の実施例を示す図面で
あり、第1図は本考案装置の説明図、第2図は第1図の
A−A線断面図、第3図は第1図に示した装置の洗浄部
材部分の拡大斜視図、第4図は洗浄部材部分の他の実施
例を示す拡大斜視図である。また第5図は従来装置の一
例を示す断面図である。 1……容器、2……固定軸 3……円板膜、4……膜分離手段 5……スペースリング、6……洗浄部材 7……ホールダ、8……取付口 9……端部材、10……支持枠体 11……挿入穴、12……駆動部材 13……回転軸1 to 4 are drawings showing an embodiment of the present invention, FIG. 1 is an explanatory view of the device of the present invention, FIG. 2 is a sectional view taken along the line AA of FIG. 1, and FIG. FIG. 4 is an enlarged perspective view of a cleaning member portion of the apparatus shown in FIG. 1, and FIG. 4 is an enlarged perspective view showing another embodiment of the cleaning member portion. FIG. 5 is a sectional view showing an example of a conventional device. 1 ... Container, 2 ... Fixed shaft 3 ... Disc membrane, 4 ... Membrane separating means 5 ... Space ring, 6 ... Cleaning member 7 ... Holder, 8 ... Mounting port 9 ... End member, 10 ... Support frame 11 ... Insertion hole, 12 ... Driving member 13 ... Rotating shaft
Claims (2)
取付けた中空の固定軸に、複数枚の円板膜を所定の間隔
を置いて挿着して膜分離手段を構成するとともに、各円
板膜の膜面に洗浄部材が接触するように洗浄部材のホー
ルダを設けて洗浄機構を構成し、液体の膜分離処理を行
うことによって、円板膜の膜透過液を固定軸の中空部に
集液して容器外へ流出させ、膜分離処理に伴い円板膜の
膜面上に付着した堆積物を前記の洗浄部材によって擦り
取るようにした膜分離装置であって、円板膜群の両端の
固定軸に支持枠体を回転可能に取付けるとともに支持枠
体の間に駆動部材を掛け渡し、さらに洗浄部材のホール
ダの一端部に設けた取付口を固定軸に回転可能に取付け
るとともに、ホールダの他端部を駆動部材に係合し、支
持枠体を回転させて駆動部材によって洗浄部材のホール
ダを回転させることを特徴とした膜分離装置。1. A membrane separating means is constructed by inserting a plurality of disc membranes at predetermined intervals on a hollow fixed shaft mounted in a container having a liquid inlet and a liquid outlet. , A cleaning member holder is provided so that the cleaning member comes into contact with the membrane surface of each disk membrane, and a cleaning mechanism is configured, and the membrane permeation liquid of the disk membrane is fixed by performing the membrane separation process of the liquid. A membrane separation device in which liquid is collected in the hollow portion and discharged to the outside of the container, and the deposit adhered to the membrane surface of the disc membrane due to the membrane separation treatment is scraped off by the cleaning member. A support frame is rotatably attached to the fixed shafts at both ends of the membrane group, a drive member is hung between the support frames, and a mounting port provided at one end of the cleaning member holder is rotatably attached to the fixed shaft. At the same time, engage the other end of the holder with the drive member to rotate the support frame. Membrane separation apparatus characterized by rotating the holder of the cleaning member by the drive member.
スリングを介して所定の間隔を置いて挿着し、さらに洗
浄部材のホールダの一端部に設けた取付口をスペースリ
ングに回転可能に取付けた請求項1に記載した膜分離装
置。2. A plurality of disc membranes are inserted and attached at predetermined intervals via a space ring having a fixed shaft inserted therein, and a mounting port provided at one end of a holder of a cleaning member is rotated to the space ring. The membrane separation apparatus according to claim 1, which is mounted so as to be possible.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12678790U JPH067788Y2 (en) | 1990-11-30 | 1990-11-30 | Membrane separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12678790U JPH067788Y2 (en) | 1990-11-30 | 1990-11-30 | Membrane separation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0487730U JPH0487730U (en) | 1992-07-30 |
| JPH067788Y2 true JPH067788Y2 (en) | 1994-03-02 |
Family
ID=31874325
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12678790U Expired - Lifetime JPH067788Y2 (en) | 1990-11-30 | 1990-11-30 | Membrane separation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH067788Y2 (en) |
-
1990
- 1990-11-30 JP JP12678790U patent/JPH067788Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0487730U (en) | 1992-07-30 |
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| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |