JPH08973Y2 - Membrane-embedded microbial treatment or solid-liquid separation device - Google Patents

Membrane-embedded microbial treatment or solid-liquid separation device

Info

Publication number
JPH08973Y2
JPH08973Y2 JP1990116960U JP11696090U JPH08973Y2 JP H08973 Y2 JPH08973 Y2 JP H08973Y2 JP 1990116960 U JP1990116960 U JP 1990116960U JP 11696090 U JP11696090 U JP 11696090U JP H08973 Y2 JPH08973 Y2 JP H08973Y2
Authority
JP
Japan
Prior art keywords
membrane
solid
liquid separation
guide wall
modules
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP1990116960U
Other languages
Japanese (ja)
Other versions
JPH0474526U (en
Inventor
幹治 徳島
善久 鳴上
恭典 岡本
英助 栢分
昌継 山縣
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP1990116960U priority Critical patent/JPH08973Y2/en
Publication of JPH0474526U publication Critical patent/JPH0474526U/ja
Application granted granted Critical
Publication of JPH08973Y2 publication Critical patent/JPH08973Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は並設した多数のチューブ状ろ過膜を、上部に
前記ろ過膜の出入口を開放状態にして設け、且つ、下部
に曝気装置を設けた生物反応槽の液内に配置してある膜
内蔵型微生物処理用もしくは固液分離用装置に関する。
[Detailed Description of the Invention] [Industrial field of application] The present invention provides a large number of tubular filtration membranes arranged side by side, with the inlet and outlet of the filtration membranes open at the top and an aeration device at the bottom. The present invention relates to a membrane-embedded microbial treatment device or solid-liquid separation device arranged in the liquid of a biological reaction tank.

〔従来の技術〕[Conventional technology]

従来の上記膜内蔵型微生物処理用もしくは固液分離用
装置(以下固液分離用装置と略記)では、前記ろ過膜群
を、全て一つの枠部材に固定すると共に、曝記装置から
の気泡をろ過膜群に案内するガイド壁を生物反応槽に固
定してあった。
In the conventional membrane-embedded microbial treatment or solid-liquid separation device (hereinafter abbreviated as solid-liquid separation device), all the filtration membrane groups are fixed to one frame member, and air bubbles from the exposure device are removed. The guide wall for guiding the filtration membrane group was fixed to the biological reaction tank.

〔考案が解決しようとする課題〕[Problems to be solved by the device]

しかし、生物反応槽の処理容量が大きくなればなるほ
ど、ろ過膜の本数を多くして固液分離処理量を増やさな
ければならず、そのために、大きな生物反応槽では固液
分離装置を大型にせざるを得なく、一つの枠部材に固定
された固液分離装置では、重量がかなり大きくなるため
に、ろ過膜の補修点検や、洗浄の際には、生物反応槽内
の混合溶液を抜いてしまうか、又は、クレーン等で枠部
材と共に、ろ過膜全体を、吊り上げて生物反応槽から取
出さなければならず、前者の場合は、時間が多くかかっ
て作業性が悪く、また、後者の場合は装置の運転を止め
る等の作業が多がかりで手間が多くかかるという欠点が
あり、その上、枠部材及びガイド壁を生物反応槽の容量
に応じて個々に製作しなければならず、製作コストが高
くつく欠点があった。
However, as the processing capacity of the biological reaction tank increases, the number of filtration membranes must be increased to increase the amount of solid-liquid separation processing, and therefore the solid-liquid separation device must be large in a large biological reaction tank. In the solid-liquid separation device fixed to one frame member, the weight is considerably large, so the mixed solution in the biological reaction tank is pulled out during repair inspection and cleaning of the filtration membrane. Or, the whole filtration membrane must be lifted and taken out from the biological reaction tank together with the frame member using a crane, etc. In the former case, it takes much time and the workability is poor, and in the latter case, There is a drawback that it takes a lot of time and labor because of many operations such as stopping the operation of the device, and in addition, the frame member and the guide wall have to be individually manufactured according to the capacity of the biological reaction tank, and the manufacturing cost is high. There was an expensive defect

本考案の目的は、固液分離装置を、生物反応槽の容量
に応じて簡単に形成できると共に、生物反応槽から簡単
に取出して、補修点検や洗浄が出来るようにする点にあ
る。
An object of the present invention is to easily form a solid-liquid separation device according to the capacity of a biological reaction tank and to easily take it out from the biological reaction tank for repair inspection and cleaning.

〔課題を解決するための手段〕[Means for solving the problem]

本考案の膜内蔵型微生物処理用もしくは固液分離用装
置の特徴構成は、ろ過膜群が、架台上で上下に積層した
複数の膜モジュールから成り、曝気装置からの気泡を最
下部の前記膜モジュールに案内するほぼ筒状の第1ガイ
ド壁を、前記架台の周部に設け、上方に隣接する前記膜
モジュールに対して前記気泡を案内するほぼ筒状の第2
ガイド壁を、前記膜モジュールの周部に設けて、前記膜
モジュールを上下に積層した時に隣接するものどうしが
ほぼ連通する上下方向に形成してあることにあり、ま
た、ろ過膜群が、架台上で上下に積層した複数の膜モジ
ュールから成り、曝気装置からの気泡を最下部の前記膜
モジュールに案内し、且つ、上部ほど膜モジュールの中
心寄りに傾斜した斜面を有する第1ガイド壁を、前記架
台のほぼ全周に設け、上方に隣接する前記膜モジュール
に対して前記気泡を案内する第2ガイド壁を、上部ほど
前記膜モジュールの中心寄りに傾斜させて前記膜モジュ
ールの周部に設けてあることにあり、それらの作用効果
は、次の通りである。
The characteristic structure of the membrane-embedded microbial treatment apparatus or solid-liquid separation apparatus of the present invention is that the filtration membrane group is composed of a plurality of membrane modules that are vertically stacked on a pedestal, and bubbles from the aerator are placed at the bottom of the membrane. A substantially tubular first guide wall that guides the module is provided on a peripheral portion of the gantry, and a substantially tubular second guide wall that guides the bubbles to the membrane module adjacent to the upper side.
The guide wall is provided in the peripheral portion of the membrane module, and is formed in the vertical direction in which adjacent ones are almost in communication with each other when the membrane modules are stacked one above the other. A first guide wall, which is composed of a plurality of membrane modules stacked above and below, guides bubbles from the aerator to the membrane module at the bottom, and has a sloped surface inclined toward the center of the membrane module toward the top, A second guide wall, which is provided on substantially the entire circumference of the gantry and guides the bubbles to the membrane module adjacent to the upper side, is provided in the peripheral portion of the membrane module with the upper portion inclined toward the center of the membrane module. The operational effects thereof are as follows.

〔作用〕[Action]

つまり、前記装置は、架台上に複数の膜モジュールを
積層するだけで形成できるばかりか、架台及び膜モジュ
ール夫々に設けた第1、第2ガイド壁によって、曝気装
置からの気泡を案内して、ろ過膜群を気泡が確実に通過
して、各ろ過膜の目詰まりが防止されるために、生物反
応槽にガイド壁を固定する必要がなく、 しかも、ろ過膜の補修点検や洗浄の際には、生物反応
槽内の混合溶液を抜き取ることなく、上下に積層した膜
モジュールを、1つづつ分離させて生物反応槽から取出
すことができる。
That is, the device can be formed not only by stacking a plurality of membrane modules on the pedestal, but also by guiding the bubbles from the aeration device by the first and second guide walls provided on the pedestal and the membrane module, respectively. Since air bubbles reliably pass through the filtration membrane group and clogging of each filtration membrane is prevented, it is not necessary to fix the guide wall to the biological reaction tank, and moreover, when repairing and inspecting or cleaning the filtration membrane. Can separate the upper and lower stacked membrane modules one by one and take them out from the biological reaction tank without extracting the mixed solution in the biological reaction tank.

〔考案の効果〕[Effect of device]

従って、短時間で、且つ、簡単な作業で、固液分離用
装置の組付けやろ過膜のメンテナンス及び洗浄を行うこ
とができ、その結果、施工性を向上させ、ろ過性能の維
持管理を簡単に行わせやすくすることができた。
Therefore, it is possible to assemble the solid-liquid separation device and maintain and clean the filtration membrane in a short time and with a simple operation. As a result, the workability is improved and the maintenance of the filtration performance is easy. Could be made easier.

その上、一種類の膜モジュールを製作して、上下必要
なら横方向にも並列的に積層する数を変えるだけで、生
物反応槽の処理容量に応じた大きさの固液分離装置を、
自在に形成でき、従来のように異なった処理容量の生物
反応槽ごとに、枠部材及び生物反応槽に固定するための
ガイド壁を製作して異なった大きさの固液分離装置を造
るのに比べ、現場製作でなく簡単に工場で製作して現場
据付できるようになり、結局固液分離装置としての製品
コストを低下させることができた。
In addition, by manufacturing one type of membrane module and changing the number of layers stacked in parallel in the horizontal direction if necessary, a solid-liquid separation device of a size corresponding to the processing capacity of the biological reaction tank can be obtained.
It can be freely formed, and it is possible to make solid-liquid separation devices of different sizes by making frame members and guide walls for fixing to biological reaction tanks with different treatment capacities as in the past. Compared with this, it became possible to easily manufacture it in the factory and install it on site, rather than on-site production, and eventually it was possible to reduce the product cost as a solid-liquid separation device.

〔実施例〕〔Example〕

次に、本考案の実施例を、図面に基づいて説明する。 Next, an embodiment of the present invention will be described with reference to the drawings.

第1図に示すように、し尿や下水等の廃水、食品加工
廃水、産業廃水等の原水を、下部に設けた曝気装置
(1)で曝気して活性汚泥により好気性処理する上部開
放型の生物反応槽(2)を設け、チューブ状のろ過膜
(3)を多数本並設した状態で生物反応槽(2)内に浸
漬配置して、生物反応槽(2)内の処理水をろ過膜
(3)を介してろ過水と濃縮汚泥とに分離する固液分離
装置(4)を設けて全体として廃水処理装置を構成して
ある。
As shown in Fig. 1, wastewater such as human waste and sewage, raw water such as food processing wastewater, industrial wastewater, etc. are aerated by an aeration device (1) provided at the bottom and aerobically treated with activated sludge. A biological reaction tank (2) is provided, and a plurality of tubular filtration membranes (3) are arranged side by side in the biological reaction tank (2), and the treated water in the biological reaction tank (2) is filtered. A solid-liquid separation device (4) for separating filtered water and concentrated sludge through the membrane (3) is provided to constitute a wastewater treatment device as a whole.

前記曝気装置(1)は、散気管(1A)は、その散気管
(1A)に空気を送るブロワー(1B)とから成り、散気管
(1A)の上方に固液分離装置(4)を配置して、散気管
(1A)から出る気泡による乱流作用と、エアーリフト作
用に基づく上昇流によってろ過膜(3)への活性汚泥の
付着を抑制できるように構成してある。
The aeration device (1) includes an air diffuser (1A) and a blower (1B) that sends air to the air diffuser (1A), and a solid-liquid separator (4) is arranged above the air diffuser (1A). Then, the turbulent action due to the bubbles coming out of the air diffuser (1A) and the upward flow due to the air lift action can suppress the adhesion of the activated sludge to the filtration membrane (3).

前記固液分離装置(4)は、第2図及び第3図に示す
ように、架台(12)上で上下に膜モジュール(5)を複
数積層したものから成り、複数の膜モジュール(5)に
よってろ過膜(3)群を形成してある。
As shown in FIG. 2 and FIG. 3, the solid-liquid separator (4) comprises a plurality of membrane modules (5) stacked vertically on a pedestal (12), and a plurality of membrane modules (5). To form a filtration membrane (3) group.

前記架台(12)は、内側に散気管(1A)を収容する空
間(S)を形成し、曝気装置(1)からの気泡を最下部
の膜モジュール(5)に案内するほぼ筒状の第1ガイド
壁(13)を、架台(12)の周部に設けてある。
The pedestal (12) forms a space (S) for accommodating the air diffuser (1A) therein, and guides bubbles from the aeration device (1) to the lowermost membrane module (5). The 1 guide wall (13) is provided on the periphery of the gantry (12).

前記膜モジュール(5)は、並設した多数本のチュー
ブ状ろ過膜(3)と、それらの両端を夫々各別に固定す
る一対の保持部(5A),(5B)と、膜モジュール(5)
どうしを上下に積層した時に隣接するものどうしが連通
する上下長さで、且つ、両保持部(5A),(5B)にわた
って設けた左右両側壁部(5C),(5C)とから成り、両
保持部(5A),(5B)と両側壁部(5C),(5C)とか
ら、上方に隣接する膜モジュール(5)に対して曝気装
置(1)からの気泡を案内するほぼ筒状の第2ガイド壁
(14)を形成してある。第1図中(9)は、各ろ過膜
(3)と吸引ポンプ(P)を連通接続するろ過水吸引管
で、各膜モジュール(9)の保持部(5A)に連結してあ
る。
The membrane module (5) comprises a large number of tubular filtration membranes (3) arranged side by side, a pair of holding portions (5A), (5B) for individually fixing both ends thereof, and the membrane module (5).
It is composed of the left and right side wall parts (5C) and (5C), which are the vertical length that allows adjacent parts to communicate with each other when they are stacked on top of each other, and is provided over both holding parts (5A) and (5B). From the holding parts (5A), (5B) and the side wall parts (5C), (5C), a substantially cylindrical shape for guiding the bubbles from the aeration device (1) to the membrane module (5) adjacent to the upper side. A second guide wall (14) is formed. In FIG. 1, (9) is a filtered water suction pipe which connects each filtration membrane (3) and a suction pump (P) for communication, and is connected to a holding portion (5A) of each membrane module (9).

〔別実施例〕[Another embodiment]

第4図に示すように、前記第1ガイド壁(13)を、上
部ほど中心寄りに傾斜した斜面を有して、架台(12)の
全周又はほぼ全周に設けてあり、前記第2ガイド壁(1
4)に、上部ほど膜モジュール(5)の中心寄りに傾斜
させた側壁部(5C)を設けて、下方から上昇してくる気
泡を、膜モジュール(5)の外方に逃がさずに、周囲の
処理水と共に上方の膜モジュール(5)に案内するよう
に形成してあっても良い。第6図、第7図は前述の第3
図もしくは第4図に示されている単位膜モジュール
(5)を2ユニット並置させた場合の第1および第2ガ
イド壁(13),(14)を取り付け状況の1例を示してい
る。この時、単位膜モジュール(5)間の隣接点(Q)
での膜チューブ間のピッチ(Ps)は各単位膜モジュール
(5)内の膜チューブ間のピッチ(P)と等しくなるよ
うに各膜モジュール(5)は配置されている。
As shown in FIG. 4, the first guide wall (13) is provided on the entire circumference or substantially the entire circumference of the gantry (12) with a slope inclined toward the center toward the top. Guide wall (1
4) A side wall portion (5C) inclined toward the center of the membrane module (5) is provided in the upper part so that bubbles rising from below do not escape to the outside of the membrane module (5), It may be formed so as to guide it to the upper membrane module (5) together with the treated water. 6 and 7 show the above-mentioned third part.
An example of the attachment state of the first and second guide walls (13) and (14) when two unit membrane modules (5) shown in the figure or FIG. 4 are arranged side by side is shown. At this time, the adjacent points (Q) between the unit membrane modules (5)
The membrane modules (5) are arranged such that the pitch (Ps) between the membrane tubes in (1) is equal to the pitch (P) between the membrane tubes in each unit membrane module (5).

尚、実用新案登録請求の範囲の項に図面との対照を便
利にする為に符号を記すが、該記入により本考案は添付
図面の構造に限定されるものではない。
It should be noted that reference numerals are added to the claims of the utility model for convenience of comparison with the drawings, but the present invention is not limited to the structure of the accompanying drawings by the entry.

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

図面は本考案に係る膜内蔵型微生物処理用もしくは固液
分離用装置の実施例を示し、第1図は一部切欠いた全体
側面図、第2図は要部分解斜視図、第3図は固液分離用
装置の縦断面図、第4図は別実施例を示す縦断面図、第
5図及び第6図は、膜モジュールユニットを2個並列に
配置した場合の別実施例を示す縦断面図である。 (1)……曝気装置、(2)……生物反応槽、(3)…
…ろ過膜、(5)……膜モジュール、(10)……出入
口、(12)……架台、(13)……第1ガイド壁、(14)
……第2ガイド壁。
FIG. 1 shows an embodiment of the apparatus for microbial treatment or solid-liquid separation according to the present invention. FIG. 1 is an overall side view with a part cut away, FIG. 2 is an exploded perspective view of essential parts, and FIG. FIG. 4 is a vertical cross-sectional view of the solid-liquid separation device, FIG. 4 is a vertical cross-sectional view showing another embodiment, and FIGS. 5 and 6 are vertical cross-sections showing another embodiment when two membrane module units are arranged in parallel. It is a side view. (1) ... Aeration device, (2) ... Bioreaction tank, (3) ...
… Filtration membrane, (5) …… membrane module, (10) …… doorway, (12) …… frame, (13) …… first guide wall, (14)
The second guide wall.

───────────────────────────────────────────────────── フロントページの続き (72)考案者 栢分 英助 大阪府大阪市浪速区敷津東1丁目2番47号 株式会社クボタ大阪本社内 (72)考案者 山縣 昌継 大阪府大阪市浪速区敷津東1丁目2番47号 株式会社クボタ大阪本社内 (56)参考文献 特開 平2−86893(JP,A) 特開 平1−168304(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Eisuke Kasubu 1-247 Shishizu East, Naniwa-ku, Osaka City, Osaka Prefecture Kubota Osaka Head Office (72) Inventor Masatsugu Yamagata, Naniwa-ku, Osaka City, Osaka Prefecture Tsuto 1-24-27 Kubota Osaka Head Office (56) Reference JP-A-2-86893 (JP, A) JP-A-1-168304 (JP, A)

Claims (5)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】並設した多数のチューブ状ろ過膜(3)
を、上部に前記ろ過膜(3)の出入口(10)を開放状態
にして設け、且つ、下部に曝気装置(1)を設けた生物
反応槽(2)の液内に配置してある膜内蔵型微生物処理
用もしくは固液分離用装置であって、前記ろ過膜(3)
群が、架台(12)上で上下に積層した複数の膜モジュー
ル(5)から成り、前記曝気装置(1)からの気泡を最
下部の前記膜モジュール(5)に案内するほぼ筒状の第
1ガイド壁(13)を、前記架台(12)の周部に設け、上
方に隣接する前記膜モジュール(5)に対して前記気泡
を案内するほぼ筒状の第2ガイド壁(14)を、前記膜モ
ジュール(5)の周部に設けて、前記膜モジュール
(5)を上下に積層した時に隣接するものどうしがほぼ
連通する上下長さに形成してある膜内蔵型微生物処理用
もしくは固液分離用装置。
1. A number of tubular filtration membranes (3) arranged in parallel.
With a built-in membrane, which is provided in the upper part of the biological reaction tank (2) with the inlet / outlet (10) of the filtration membrane (3) opened and the aeration device (1) provided in the lower part Type microbiological treatment or solid-liquid separation device, said filtration membrane (3)
The group is composed of a plurality of membrane modules (5) stacked vertically on a pedestal (12), and has a substantially cylindrical shape that guides bubbles from the aeration device (1) to the membrane module (5) at the bottom. 1 guide wall (13) is provided on the periphery of the gantry (12), and a substantially cylindrical second guide wall (14) for guiding the bubbles to the membrane module (5) adjacent to the upper side is provided. A membrane-embedded microbial treatment or solid liquid provided on the periphery of the membrane module (5) and formed in a vertical length such that adjacent ones of the membrane modules (5) are almost in communication with each other when the membrane modules (5) are vertically stacked. Separation device.
【請求項2】並設した多数のチューブ状ろ過膜(3)
を、上部に前記ろ過膜(3)の出入口(10)を設け、且
つ、下部に曝気装置(1)を設けた生物反応槽(2)の
液内に浸漬配置してある膜内蔵型微生物処理用もしくは
固液分離用装置であって、前記ろ過膜(3)群が、架台
(12)上で上下に積層した複数の膜モジュール(5)か
ら成り、前記曝気装置(1)からの気泡を最下部の前記
膜モジュール(5)に案内し、且つ、上部ほど前記膜モ
ジュール(5)の中心寄りに傾斜した斜面を有する第1
ガイド壁(13)を、前記架台(12)のほぼ全周に設け、
上方に隣接する前記膜モジュール(5)に対して前記気
泡を案内する第2ガイド壁(14)を、上部ほど前記膜モ
ジュール(5)の中心寄りに傾斜させて前記膜モジュー
ル(5)の周部に設けてある膜内蔵型微生物処理用もし
くは固液分離用装置。
2. A plurality of tubular filtration membranes (3) arranged in parallel.
Is a membrane-incorporated microbial treatment in which the inlet / outlet (10) of the filtration membrane (3) is provided in the upper portion and the aeration device (1) is provided in the lower portion to be immersed in the liquid in the biological reaction tank (2). Or an apparatus for solid-liquid separation, wherein the group of filtration membranes (3) is composed of a plurality of membrane modules (5) stacked vertically on a pedestal (12) to remove air bubbles from the aeration apparatus (1). A first slanted surface that guides to the membrane module (5) at the bottom, and slopes toward the center of the membrane module (5) toward the top
A guide wall (13) is provided almost all around the frame (12),
The second guide wall (14) for guiding the air bubbles to the membrane module (5) adjacent to the upper side is inclined toward the center of the membrane module (5) toward the upper part, and the circumference of the membrane module (5) is increased. A device for microbial treatment or solid-liquid separation with a built-in membrane provided in the section.
【請求項3】多数の前記膜モジュール(5)を前記生物
反応槽(2)の液内に浸漬した状態において、前記積層
した膜モジュール(5)を横方向に並列に配置する請求
項1又は2記載の膜内蔵型微生物処理用もしくは固液分
離用装置。
3. The stacked membrane modules (5) are arranged in parallel laterally in a state where a large number of the membrane modules (5) are immersed in the liquid of the biological reaction tank (2). 2. The membrane-embedded microbial treatment or solid-liquid separation device according to 2.
【請求項4】前記積層した膜モジュール(5)を多数並
列に配置した状態で、前記第2ガイド壁(14)を、互に
横に隣接する前記膜モジュール(5),(5)間には設
けないことを特徴とする請求項1又は2記載の膜内蔵型
微生物処理用もしくは固液分離用装置。
4. The second guide wall (14) is provided between the membrane modules (5), (5) laterally adjacent to each other in a state where a large number of the laminated membrane modules (5) are arranged in parallel. 3. The membrane-embedded microbial treatment apparatus or solid-liquid separation apparatus according to claim 1, wherein is not provided.
【請求項5】前記第2ガイド壁(14)を互に隣接する前
記膜モジュール(5),(5)間には設けない状態で、
前記チューブ状ろ過膜(3)のピッチ(膜間隔)は、横
方向に隣接する前記膜モジュール(5),(5)間のろ
過膜ピッチを含め同一間隔とした請求項4記載の膜内蔵
型微生物処理用もしくは固液分離用装置。
5. In a state where the second guide wall (14) is not provided between the membrane modules (5), (5) adjacent to each other,
The membrane-embedded type according to claim 4, wherein the tubular filtration membranes (3) have the same pitch (membrane spacing) including the filtration membrane pitch between the membrane modules (5) (5) that are laterally adjacent to each other. Equipment for microbial treatment or solid-liquid separation.
JP1990116960U 1990-11-06 1990-11-06 Membrane-embedded microbial treatment or solid-liquid separation device Expired - Lifetime JPH08973Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1990116960U JPH08973Y2 (en) 1990-11-06 1990-11-06 Membrane-embedded microbial treatment or solid-liquid separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1990116960U JPH08973Y2 (en) 1990-11-06 1990-11-06 Membrane-embedded microbial treatment or solid-liquid separation device

Publications (2)

Publication Number Publication Date
JPH0474526U JPH0474526U (en) 1992-06-30
JPH08973Y2 true JPH08973Y2 (en) 1996-01-17

Family

ID=31864822

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1990116960U Expired - Lifetime JPH08973Y2 (en) 1990-11-06 1990-11-06 Membrane-embedded microbial treatment or solid-liquid separation device

Country Status (1)

Country Link
JP (1) JPH08973Y2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2661848B2 (en) * 1992-09-22 1997-10-08 工業技術院長 Culture method and culture device
JP4614188B2 (en) * 2007-05-15 2011-01-19 株式会社日立プラントテクノロジー Immersion flat membrane filtration device
JP5425394B2 (en) * 2007-12-27 2014-02-26 月島機械株式会社 Filtration module, filtration module laminate, and filtration device
WO2011052525A1 (en) * 2009-10-26 2011-05-05 株式会社明電舎 Membrane module, membrane unit, and membrane separation device

Also Published As

Publication number Publication date
JPH0474526U (en) 1992-06-30

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