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JP3661206B2 - Immersion membrane separator - Google Patents
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JP3661206B2 - Immersion membrane separator - Google Patents

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JP3661206B2
JP3661206B2 JP21679194A JP21679194A JP3661206B2 JP 3661206 B2 JP3661206 B2 JP 3661206B2 JP 21679194 A JP21679194 A JP 21679194A JP 21679194 A JP21679194 A JP 21679194A JP 3661206 B2 JP3661206 B2 JP 3661206B2
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membrane
water tank
unit
membrane unit
tank
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JP21679194A
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JPH0857271A (en
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邦博 岩崎
克己 石黒
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Kurita Water Industries Ltd
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Kurita Water Industries Ltd
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Description

【0001】
【産業上の利用分野】
本発明は、液中に膜を浸漬して膜分離処理を行なう浸漬型膜分離装置に関するもので、特に浮力体を付した浸漬型膜分離装置に関する。
【0002】
【従来の技術】
従来の浸漬型膜分離装置は、一般的には、集水管や支持部材などで膜ユニットを槽内に強固に固定する構造を採る。また、濾過膜取付座の下部に膜ユニットたる円筒状の濾過膜を取り付け、上部には水室を取付ネジ等によって液密に取り付け、その下方に逆凹形の空気室を形成し、かかる濾過膜取付座を濾過槽内に装填して空気室の浮力により浮上させ、水室の上面に設けた加振レバーを電磁石により上下に動かすことにより振動を与える構造を採ったものもある。
【0003】
【発明が解決しようとする課題】
しかし、このように膜ユニットを槽内に強固に固定したり、或は加振レバーで接続した従来の浸漬型膜分離装置では、液面が大きく低下したとき、膜が大気にさらされて膜が乾燥したり、空気を吸い込んだりして膜を駄目にしてしまうことがあった。また、膜ユニットの設置作業には多大な労力と時間を要した。
【0004】
また、膜の取付座を空気室の浮力で浮かす従来の膜分離装置は、液面の上下に応じて取付座が多少上下することはできるが、この取付座は加振レバーで接続しているので液面が大きく上下した場合には追随することができない。また、この膜分離装置は、膜の上部が空気中に露出しているので、膜面積の有効利用が図れていない。
【0005】
さらに、膜ユニットの下方から曝気することにより膜面のケーキ層の形成を抑制する場合に、最もケーキ層の抑制効果の高い液面近傍に膜ユニットを位置させることが望ましいが、前記した従来の膜分離装置は、いずれも液面の上下に追随できないので、曝気による効率の良いケーキ層抑制効果を期待できなかった。
【0006】
そこで、本発明の目的は、膜ユニットが液面の上下動に追随して常時に液面付近に位置すると共に膜上部の空気中への露出がなくなるようにした浸漬型膜分離装置を提供しようとすることにある。
【0007】
【課題を解決するための手段】
本発明は上記目的を達成するために提案されたものであり、請求項1記載の発明は、浸漬槽と、該浸漬槽内に浸漬された膜ユニットと、該膜ユニットを液中で浮かせる浮力体と、該浮力体を固定する取付べースと、該取付べース上に搭載された吸引ポンプと、該膜ユニットと吸引ポン吸引側とを接続する配管と、吸引ポンプ吐出側に設けた排水管とを含む浸漬膜分離装置である。また、請求項2記載の発明は、膜ユニットの下部に錘を取り付けた請求項1記載の浸漬膜分離装置である。また、請求項3記載の発明は、浸漬槽は円筒形水槽の中央部に別途円筒が立設されて該円筒内が透過水槽、円筒の外側が環状水槽部として区画され、前記環状水槽部内に仕切板が設けられて洗浄部となり、洗浄部内の水の排出用配管と、洗浄部への薬液供給管が設けられてなり、前記膜ユニットを浸漬させた請求項1又は2記載の浸漬膜分離装置である。また、請求項4記載の発明は、環状水槽部の上面開口部に半径の異なる円弧状の途切れた案内レールを水平方向に設け、該案内レールに取付ベースを摺動案内するように構成した請求項3に記載の浸漬膜分離装置である。また、請求項5記載の発明は、吸引ポンプの吐出側に設けた排水管を円筒内の透過水槽に通した請求項3,4のいずれか1項に記載の浸漬膜分離装置である。
【0008】
【作用】
膜ユニットの自重を含む保持手段により、膜ユニットの全域が液面下に浸漬状態で保持され、結果的に膜ユニット全体が水面下となるように浮力体に取り付けられる。これにより、膜ユニットの下方からの散気によるエアーリフト循環流が生じ、膜間の閉塞が防止でき、バブリングによる洗浄効果が向上する。また、膜ユニットが槽に固定されていないので、この膜ユニットが液面の上下に追随し、膜が空気中に露出することがなく、疎水化しない。また液面に連動して垂直に移動できるばかりでなく、水平方向にも自由に動くことが可能となる。
【0009】
【実施例】
以下、本発明の実施例を図面に基づいて説明する。
図1に示す浸漬型膜分離装置1は、本発明の基本的な実施例であり、浸漬槽2内に膜ユニット3が浮力体4の浮力によって浮遊した状態で浸漬されている。膜ユニット3は、例えば浸漬型の平膜、中空糸膜、あるいはそれらのユニットであって、上部に2つの浮力体4を有し、これにより常に液面付近に浮上され、液面レベルの変動に応じてその位置を変え得るように構成されている。
【0010】
浮力体4は球体、多面体など適宜な形状であるが、内部を中空にしたり、或は発泡スチロール等を充填するなどして、自重に比して大きな容積を有する。なお、この浮力体4は、膜ユニット3に十分な浮力を与えることができれば、どのような形状、構造であってもよく、また、取り付ける数も限定されない。
【0011】
5は膜ユニット3と浮力体4とを結ぶ連結部材であり、この連結部材5には帯状物のような柔軟性のあるもの、あるいは剛体構造により膜ユニット3と一体になったものなどを適宜に選択して用いてもよい。また、浮力体4と膜ユニット3の膜上端との距離は自由に設定でき、膜の上端が液面から空気中に突出しなければ良い。
【0012】
膜ユニット3の上部に設けた2つの浮力体4は板状の取付ベース6に固定されており、この取付ベース6上には、吸引ポンプ7を搭載し、該吸引ポンプ7の吸引側の配管8を集水管として膜ユニット3に接続し、吐出側には途中にフレキシブルチューブを介在した排水管9を接続し、膜ユニット3の水深差と吸引ポンプ7の吸引力を利用して吸引濾過し、膜ユニット3の膜を透過した透過水を配管8で集水して排水管9から排水するようにしてある。
【0013】
また、膜ユニット3の下部には、膜ユニット3の膜面をその全域に亘って液面下に浸漬させる保持手段の一構成要素として、錘10が垂下されている。これは膜ユニット3の自重が容積の割りに軽い、即ち比重が軽い場合であり、浮力体4を付した膜ユニット3の下に錘10を取り付けて、膜面が大気中に浮いてこないようにしているのである。したがって、錘10を付けない場合でも、膜ユニット3自体の重さが上記保持手段として働くことになる。
【0014】
この様な構成により液面下に浮いた膜ユニット3は、図2に示すように、浸漬槽2内の液面レベルの上下動に連動して垂直方向に移動したり、容易に水平方向に移動したりすることができる。なお、膜ユニット3の下方には曝気装置の一部を構成する散気管11を配設してあるので、ブロワー12から送られてくる空気を散気管11から液中に送出し、この気泡により膜ユニット3の膜面に成長するケーキ層を剥離できる。また、膜ユニット3が液面のレベルに応じて鉛直方向、或は水平方向に移動しても、排水管9の途中にフレキシブルチューブを介在させ、また、十分にたわませて配管してあるので、膜ユニット3からの透過水を排水するに当っての支障はない。
【0015】
また、本実施例によれば槽2に対する固定部材を特に設ける必要がないし、浸漬槽2内に埋没している構成物がないので、保守管理が容易である。そして、浮力体4を取り付けたことにより、液面レベルの変動がある条件の中でも一定の水位下に膜ユニット3を位置させることができる。
【0016】
膜ユニット3の下方の散気管11から曝気することにより、気泡上昇気流の中で膜濾過するのが膜面のケーキの形成を抑制できて最も効率がよく、水位が変動する水槽内に膜ユニット3を埋没させ固定した条件では水位により膜ユニット3の相対位置が異なるが、本実施例のように浮力体の浮力によって膜ユニット3を、最もケーキ層の抑制効果の高い水面近傍に設置してやれば、常に気泡の破壊やそれに伴なう水の振動がある条件に膜ユニット3を位置させることができる。したがって、膜面にケーキ層が成長し難く、吸引膜濾過に好適である。また、このような効果があるために昼間の期間のみに排出されるような使用条件で24時間かけて膜濾過する使用条件に好適である。
【0017】
さらにまた、浮力体4の取付ベース上に吸引ポンプ7を設けた構成としているので、吸引ポンプ7を陸上に固定して遠く離れた膜ユニット3に配管して吸引濾過する従来の膜分離装置に比較して効率を高めることができる。即ち、吸引配管が長くなるほど管路抵抗が増え、膜ユニット3での真の吸引濾過圧を減じるが、本実施例の様に、膜ユニット3の上部に吸引ポンプ7を配置すると、常に吸引配管の管路抵抗を小さく保つことができる。したがって、効率良く膜濾過することが可能となる。
【0018】
また、湖沼等から膜濾過して濁質のない浄水を得る場合には水面近傍の濁質濃度の低い水だけを対象にして分離できるので好適である。すなわち、膜濾過の障害となる粗大粒子を自然沈降において沈澱させて、最も濁質の希薄な対象水だけを常に濾過対象とする利点を有するからである。
【0019】
前記したように、一定水位以上の条件において膜ユニット3の水平移動が可能であり、これを利用して膜モジュールの移動洗浄ができ、また、水平方向と垂直方向の移動を組み合わせて洗浄水槽への移動が自動化できる。以下、その実施例を説明する。
【0020】
図3〜図11は、上記した基本構成を備えた浸漬型膜分離装置1を複数基設けた実施例であり、各浸漬型膜分離装置1a〜1fは垂直方向の移動のみならず水平方向の移動ができ、円筒形水槽13内の一箇所に形成された洗浄水槽14へ手動、又は自動で移動する構成になっている。
【0021】
図3は円筒形水槽13の平面図、図4は水槽13のA−A断面図である。この円筒形水槽13は、中央部に別途円筒を立設することにより該円筒内を透過水槽15とし、また円筒の外側を環状水槽部16として区画し、且つ透過水槽15の周囲の環状水槽部16内には、2枚の仕切板17を、図のように周方向に所定間隔だけ隔てて配置し、水槽13の底部から下半分の高さまで延在させることにより、一つの浸漬型膜分離装置1を収納可能な洗浄水槽14を区画形成してある。そして、この環状水槽部16内には、複数個、本実施例では6基の浸漬型膜分離装置1を円周方向に等間隔に配置してある。
【0022】
図5及び図6は高水位運転時における各浸漬型膜分離装置1の位置関係を示したもので、6基の浸漬型膜分離装置1a〜1fは仕切板17の上方の水槽内に円周方向に等間隔離れて浮いており、吸引ポンプ7からのフレキシブルチューブから成る排水管9aは、中央部の透過水槽15に通してある。したがって、各浸漬型膜分離装置1a〜1fの膜ユニット3により濾過した透過水は、そのすべてが一旦排水管9aを介して透過水槽15内に集水され、この透過水槽15から別途配管を介して排水される。なお、図5中、仕切板17を点線で表わしたのは、仕切板17が水面下に在ることを示している。
【0023】
また、図7及び図8に示すように、環状水槽部16の上面開口部に半径の異なる円弧状の途切れた案内レール18を水平方向に設け、該案内レール18に各浸漬型膜分離装置1の取付ベース6を摺動案内するように構成してある。なお、6基の浸漬型膜分離装置1を環状水槽部16内で水平方向に移動する手段としては、手動でもよいが、各浸漬型膜分離装置1の取付ベースを押圧する回動腕(図示せず)を環状水槽部16の半径方向に設けるなどして機械的に移動できるように構成することが望ましい。
【0024】
次に、上記した構成からなる装置における洗浄自動化の工程を説明する。
【0025】
図6に示すように、高水位の状態で各浸漬型膜分離装置1を運転すると、膜濾過した透過水量の分だけ水位が低下し、この水位の低下に伴って各浸漬型膜分離装置1a〜1fが液面と共に徐々に下降する。したがって、図9及び図10に示すように、膜ユニット3の位置関係は低水位運転時のものに変わる。
【0026】
低水位の運転時においては、水位が仕切板17,17の上端より低下することで、仕切板17の上方に位置していた一つの浸漬型膜分離装置1aが2枚の仕切板17,17間によってトラップされる。そして、その仕切板17,17間を洗浄水槽14とし、浸漬型膜分離装置1aの洗浄を行い、残りの膜分離装置1b〜1fは濾過運転を行う。
【0027】
浸漬型膜分離装置1aの洗浄は、ポンプを停止し、図11に示すように、洗浄水槽14の仕切板17,17の区画内底部に接続したドレイン配管19の開閉バルブ20を開き、洗浄水槽14内の濃縮水を排出する。
【0028】
そして、次には洗浄水槽14に薬液を入れる。この薬液導入にあたっては、透過水槽15を利用して薬液を調合して入れることもできる。即ち、図11に示すように、中央部の透過水槽15内の仕切板17の上端よりも高い位置に中底23を設け、中底から上を薬液調整槽15aとし、中底には開閉弁21を取付け、常時は開閉弁21を開にし、各浸漬型膜分離装置1a〜1fが排水管で透過水槽15に排水する透過水を開閉弁21を通じ、中底の下に導入し、透過水槽の底から排水する。膜分離装置1aの洗浄を行うときは開閉弁21を閉じ、前述のドレイン配管の開閉バルブ20を開いて洗浄水槽内の濃縮水を排水する間、装置1b〜1fが排出する透過水を薬液調整槽15aに溜め、所定量溜ったらこれに薬品を加えて洗浄液を調整し、中底の直上に設けた洗浄水槽14への供給管24の弁22を開き、洗浄液を洗浄水槽14に供給する、なお、洗浄液の洗浄水槽への供給が終わったら開閉弁21は開にし、弁22は閉にする。
【0029】
こうして、洗浄水槽中の薬液に膜分離装置1aを、一定時間浸漬することにより膜ユニット3の膜面を洗浄し、十分に洗浄した後、洗浄水はドレイン配管19から排出し、次に原水を補給して高水位運転時の状態(図6)まで戻す。
【0030】
6基の浸漬型膜分離装置1a〜1fを一定方向に60°宛旋回させ、次の洗浄対象となる浸漬型膜分離装置1bを仕切板17,17の区画上に位置させる。前述した途切れた案内レール18は各膜分離装置1a〜1fを次の旋回位置であるレールの途切れた間隔に導くのをガイドする。尚、仕切板17,17の区画は、レールの途切れた間隔の1つの下方に設けられている(図7参照)。
【0031】
上記工程を繰り返すことにより、次の浸漬型膜分離装置1bも他の装置1a,1c〜1fが低水位運転時に同様に洗浄される。こうして、低水位運転時に膜分離装置が1基宛、順番に洗浄される。
【0032】
上記したように、本実施例では、円筒形の水槽13内に複数基の浸漬型膜分離装置1a〜1fを環状に配置して浮かせて、各浸漬型膜分離装置1を垂直方向の移動のみならず水平方向に移動できるようにすると共に、水槽13内にはその下部に、浸漬型膜分離装置1が納まる高さで、洗浄水槽14となるセクターを仕切板17で区画形成し、洗浄の必要時には、浸漬型膜分離装置1を1基宛、順番に水槽13内の洗浄水槽14へ移行し得るようにしたので、極めて簡単且つ自動的に膜面の洗浄ができる。
【0033】
なお、本発明にかかる浸漬型膜分離装置1は、反応槽,浸漬槽等の槽内に設けるものに限られるものではなく、湖沼、海水、河川等の自然界に浸漬する形態で使用することができる。例えば、浄水場、工場等の取水源に設けることができる。
【0034】
【発明の効果】
以上説明したように本発明によれば、保持手段により膜ユニットの全域を液面下に浸漬状態で保持し、結果的に膜ユニット全体が水面下となるように浮力体に取り付けているので、下部からの散気によるエアーリフト循環流が生じ、膜間の閉塞が防止でき、バブリングによる洗浄効果が向上する。また、膜ユニットが槽に固定されていないので、液面の上下に追随し、膜面が空気中に露出することがなく、疎水化しない。また液面に連動して垂直に移動できるばかりでなく、水平方向にも自由に動くことが可能となる。
【図面の簡単な説明】
【図1】本発明の基本的構成を示す浸漬型膜分離装置の第1の実施例の概略構成図である。
【図2】水面変動に伴なう膜ユニットの動きを示す説明図である。
【図3】複数の浸漬型膜分離装置を浮かせる第2の実施例における水槽の平面図である。
【図4】図3の水槽のA−A断面図である。
【図5】図3の水槽内に複数の浸漬型膜分離装置を環状に配置した形態における高水位運転時の状態を示す平面図である。
【図6】図5の水槽のB−B断面図である。
【図7】案内レールの配置を示す水槽の平面図である。
【図8】案内レールと浸漬型膜分離装置との配置関係を示す斜視図である。
【図9】低水位運転時の状態を示す平面図である。
【図10】図9の水槽のB−B断面図である。
【図11】洗浄水槽のドレイン時の状態を示す水槽の断面図である。
【符号の説明】
1 浸漬型膜分離装置
2 浸漬槽
3 膜ユニット
4 浮力体
5 連結部材
6 取付ベース
7 吸引ポンプ
8 吸引ポンプと膜ユニットとの間の配管
9 排水管
10 錘
11 散気管
12 ブロワー
13 円筒形水槽
14 洗浄水槽
15 透過水槽
15a 薬液調整槽
16 環状水槽部
17 仕切板
18 案内レール
19 ドレイン配管
20 開閉バルブ
21 閉鎖用開閉弁
22 連通用開閉弁
23 中底
24 供給管
[0001]
[Industrial application fields]
The present invention relates to a submerged membrane separator that performs a membrane separation process by immersing a membrane in a liquid, and more particularly to a submerged membrane separator with a buoyant body.
[0002]
[Prior art]
Conventional submerged membrane separation devices generally employ a structure in which a membrane unit is firmly fixed in a tank by a water collecting pipe or a support member. In addition, a cylindrical filtration membrane as a membrane unit is attached to the lower part of the filtration membrane mounting seat, a water chamber is attached to the upper part in a liquid-tight manner by means of attachment screws, etc., and a reverse concave air chamber is formed below the filtration chamber. There is also a structure in which a membrane mounting seat is loaded in a filtration tank and floats by the buoyancy of an air chamber, and a vibration lever provided on the upper surface of the water chamber is moved up and down by an electromagnet to give vibration.
[0003]
[Problems to be solved by the invention]
However, in the conventional immersion type membrane separation apparatus in which the membrane unit is firmly fixed in the tank as described above or connected by a vibration lever, the membrane is exposed to the atmosphere when the liquid level is greatly lowered. May dry out or inhale air and destroy the membrane. Also, the installation work of the membrane unit required a great deal of labor and time.
[0004]
In addition, the conventional membrane separation device that floats the membrane mounting seat with the buoyancy of the air chamber can move the mounting seat up and down somewhat according to the liquid level up and down, but this mounting seat is connected by a vibration lever. Therefore, it cannot follow when the liquid level fluctuates greatly. Moreover, since the upper part of the membrane is exposed to the air, this membrane separation device cannot effectively use the membrane area.
[0005]
Furthermore, when suppressing the formation of the cake layer on the membrane surface by aeration from below the membrane unit, it is desirable to position the membrane unit in the vicinity of the liquid surface with the highest effect of suppressing the cake layer. None of the membrane separation devices can follow the top and bottom of the liquid level, and therefore, an efficient cake layer suppressing effect by aeration could not be expected.
[0006]
Accordingly, an object of the present invention is to provide a submerged membrane separation device in which the membrane unit is always located near the liquid surface following the vertical movement of the liquid surface and the exposure to the air above the membrane is eliminated. It is to do.
[0007]
[Means for Solving the Problems]
The present invention has been proposed in order to achieve the above object, and the invention according to claim 1 is directed to an immersion tank, a membrane unit immersed in the immersion tank, and a buoyancy that floats the membrane unit in a liquid. and body, and a mounting base over scan fixing the該浮force body, a suction pump mounted on the base over the scan with said mounting, a pipe for connecting the membrane unit and the suction pump suction side, the suction pump discharge side An immersion membrane separation device including a provided drainage pipe. The invention according to claim 2 is the submerged membrane separation apparatus according to claim 1, wherein a weight is attached to the lower part of the membrane unit. Further, in the invention according to claim 3, the immersion tank has a separate cylinder standing at the center of the cylindrical water tank, the inside of the cylinder is partitioned as a permeated water tank, and the outside of the cylinder is defined as an annular water tank part, The submerged membrane separation according to claim 1 or 2, wherein a partition plate is provided to form a cleaning unit, and a pipe for discharging water in the cleaning unit and a chemical solution supply pipe to the cleaning unit are provided to immerse the membrane unit. Device. Further, an invention according to claim 4, wherein, provided the different radii arcuate Interrupted guide rails on the upper surface opening portion of the annular water tank unit in a horizontal direction, to constitute a mounting base on the guide rail so as to slide guided claims Item 4. The immersion membrane separation apparatus according to Item 3 . The invention according to claim 5 is the submerged membrane separation apparatus according to any one of claims 3 and 4, wherein a drain pipe provided on the discharge side of the suction pump is passed through a permeate tank in the cylinder.
[0008]
[Action]
By the holding means including the weight of the membrane unit, the entire area of the membrane unit is held in a submerged state under the liquid surface, and as a result, the membrane unit is attached to the buoyant body so as to be under the water surface. As a result, an air lift circulation flow is generated by the air diffused from below the membrane unit, so that the clogging between the membranes can be prevented and the cleaning effect by bubbling is improved. Moreover, since the membrane unit is not fixed to the tank, the membrane unit follows the liquid surface up and down, and the membrane is not exposed to the air and is not hydrophobized. In addition to being able to move vertically in conjunction with the liquid level, it is also possible to move freely in the horizontal direction.
[0009]
【Example】
Embodiments of the present invention will be described below with reference to the drawings.
A submerged membrane separation apparatus 1 shown in FIG. 1 is a basic embodiment of the present invention, and a membrane unit 3 is immersed in the immersion tank 2 in a state of being floated by the buoyancy of a buoyant body 4. The membrane unit 3 is, for example, a submerged flat membrane, a hollow fiber membrane, or a unit thereof, and has two buoyant bodies 4 on the upper part, so that the membrane unit 3 is always levitated near the liquid surface, and the liquid level changes. The position can be changed according to the condition.
[0010]
The buoyancy body 4 has an appropriate shape such as a sphere or a polyhedron, but has a large volume compared to its own weight, for example, by hollowing the inside or filling with foamed polystyrene. The buoyancy body 4 may have any shape and structure as long as the buoyancy body 4 can give sufficient buoyancy to the membrane unit 3, and the number of attachments is not limited.
[0011]
Reference numeral 5 denotes a connecting member that connects the membrane unit 3 and the buoyant body 4. As the connecting member 5, a flexible member such as a strip or a member integrated with the membrane unit 3 by a rigid structure is appropriately used. You may select and use. Further, the distance between the buoyancy body 4 and the upper end of the membrane unit 3 can be freely set, and it is sufficient that the upper end of the membrane does not protrude from the liquid surface into the air.
[0012]
Two buoyancy bodies 4 provided on the upper part of the membrane unit 3 are fixed to a plate-like mounting base 6. A suction pump 7 is mounted on the mounting base 6, and a suction side pipe of the suction pump 7 is mounted. 8 is connected to the membrane unit 3 as a water collecting pipe, and a drain pipe 9 with a flexible tube is connected to the discharge side on the discharge side, and suction filtration is performed using the water depth difference of the membrane unit 3 and the suction force of the suction pump 7. The permeated water that has passed through the membrane of the membrane unit 3 is collected by the pipe 8 and drained from the drain pipe 9.
[0013]
Also, a weight 10 is suspended below the membrane unit 3 as one component of a holding unit that immerses the membrane surface of the membrane unit 3 under the liquid level over the entire area. This is a case where the weight of the membrane unit 3 is light relative to the volume, that is, the specific gravity is light. A weight 10 is attached under the membrane unit 3 with the buoyant body 4 so that the membrane surface does not float in the atmosphere. It is. Therefore, even when the weight 10 is not attached, the weight of the membrane unit 3 itself serves as the holding means.
[0014]
As shown in FIG. 2, the membrane unit 3 floating below the liquid surface by such a configuration moves in the vertical direction in conjunction with the vertical movement of the liquid surface level in the immersion bath 2, or easily in the horizontal direction. Or move. In addition, since the diffuser pipe 11 which comprises a part of aeration apparatus is arrange | positioned under the membrane unit 3, the air sent from the blower 12 is sent in a liquid from the diffuser pipe 11, and by this bubble, The cake layer growing on the film surface of the film unit 3 can be peeled off. Further, even if the membrane unit 3 moves in the vertical direction or the horizontal direction according to the level of the liquid level, a flexible tube is interposed in the middle of the drain pipe 9, and the pipe is bent sufficiently. Therefore, there is no trouble in draining the permeated water from the membrane unit 3.
[0015]
Moreover, according to the present Example, it is not necessary to provide the fixing member with respect to the tank 2, and since there is no component embedded in the immersion tank 2, maintenance management is easy. And by attaching the buoyancy body 4, the membrane unit 3 can be positioned under a certain water level even under conditions where the liquid level varies.
[0016]
By aeration from the air diffuser 11 below the membrane unit 3, the membrane filtration in the bubble rising airflow can suppress the formation of the cake on the membrane surface and is the most efficient, and the membrane unit is placed in the water tank where the water level fluctuates. The relative position of the membrane unit 3 varies depending on the water level under the condition that the 3 is buried and fixed, but if the membrane unit 3 is installed near the water surface where the suppression effect of the cake layer is highest as in this embodiment, the buoyancy of the buoyant body The membrane unit 3 can be positioned under conditions where there is always destruction of bubbles and accompanying vibration of water. Therefore, the cake layer hardly grows on the membrane surface, which is suitable for suction membrane filtration. Moreover, since it has such an effect, it is suitable for the use conditions which carry out membrane filtration over 24 hours on the use conditions which discharge | emit only in the daytime period.
[0017]
Furthermore, since the suction pump 7 is provided on the mounting base of the buoyant body 4, the suction pump 7 is fixed on the land, piped to the membrane unit 3 that is far away, and a conventional membrane separation device that performs suction filtration. In comparison, the efficiency can be increased. That is, as the suction pipe becomes longer, the pipe resistance increases and the true suction filtration pressure in the membrane unit 3 is reduced. However, if the suction pump 7 is arranged on the upper part of the membrane unit 3 as in this embodiment, the suction pipe is always provided. The pipe resistance can be kept small. Therefore, membrane filtration can be performed efficiently.
[0018]
In addition, when obtaining purified water without turbidity by membrane filtration from a lake or the like, it is preferable because only water with low turbidity concentration near the water surface can be separated. In other words, it is advantageous in that coarse particles that hinder membrane filtration are precipitated by natural sedimentation, and only the most turbid and diluted target water is always subjected to filtration.
[0019]
As described above, the membrane unit 3 can be moved horizontally under conditions above a certain water level, and the membrane module can be moved and cleaned using this, and the movement in the horizontal direction and the vertical direction can be combined to the washing water tank. Can be moved automatically. Examples thereof will be described below.
[0020]
3 to 11 show an embodiment in which a plurality of submerged membrane separators 1 having the above-described basic configuration are provided. Each submerged membrane separator 1a to 1f is not only moved in the vertical direction but also in the horizontal direction. It can move and is configured to move manually or automatically to a washing water tank 14 formed at one location in the cylindrical water tank 13.
[0021]
FIG. 3 is a plan view of the cylindrical water tank 13, and FIG. 4 is an AA cross-sectional view of the water tank 13. The cylindrical water tank 13 is provided with a separate cylinder at the center to define the inside of the cylinder as a permeated water tank 15, and the outside of the cylinder as an annular water tank part 16, and an annular water tank part around the permeated water tank 15. 16, two partition plates 17 are arranged at a predetermined interval in the circumferential direction as shown in the figure, and are extended from the bottom of the water tank 13 to the height of the lower half, so that one submerged membrane separation is performed. A cleaning water tank 14 capable of storing the apparatus 1 is partitioned. In the annular water tank section 16, a plurality of, in this embodiment, six submerged membrane separation devices 1 are arranged at equal intervals in the circumferential direction.
[0022]
5 and 6 show the positional relationship of each of the submerged membrane separators 1 during high water level operation. The six submerged membrane separators 1a to 1f are arranged in a water tank above the partition plate 17. A drainage pipe 9 a made of a flexible tube from the suction pump 7 passes through a permeate tank 15 in the center. Therefore, all of the permeated water filtered by the membrane units 3 of the submerged membrane separators 1a to 1f is once collected in the permeated water tank 15 through the drain pipe 9a, and is separately collected from the permeated water tank 15 through a separate pipe. Drained. In FIG. 5, the partition plate 17 is represented by a dotted line to indicate that the partition plate 17 is below the water surface.
[0023]
Further, as shown in FIGS. 7 and 8, a circular arc-shaped guide rail 18 having a different radius is provided in the upper surface opening of the annular water tank portion 16 in the horizontal direction, and each submerged membrane separation device 1 is provided on the guide rail 18. The mounting base 6 is slidably guided. The means for moving the six submerged membrane separation devices 1 in the annular water tank 16 in the horizontal direction may be manually operated, but a rotating arm that presses the mounting base of each submerged membrane separation device 1 (FIG. (Not shown) is preferably configured so that it can be moved mechanically, for example, by providing it in the radial direction of the annular water tank section 16.
[0024]
Next, the cleaning automation process in the apparatus having the above-described configuration will be described.
[0025]
As shown in FIG. 6, when each submerged membrane separator 1 is operated at a high water level, the water level is reduced by the amount of permeated water that has been membrane-filtered, and each submerged membrane separator 1a is reduced as the water level decreases. ˜1f gradually descends with the liquid level. Therefore, as shown in FIGS. 9 and 10, the positional relationship of the membrane unit 3 changes to that at the time of low water level operation.
[0026]
During operation at a low water level, the water level drops from the upper ends of the partition plates 17 and 17, so that one submerged membrane separation device 1 a located above the partition plate 17 has two partition plates 17 and 17. Trapped by between. And between the partition plates 17 and 17 is used as the washing water tank 14, the submerged membrane separation apparatus 1a is washed, and the remaining membrane separation apparatuses 1b to 1f perform the filtration operation.
[0027]
Cleaning of the submerged membrane separation apparatus 1a stops the pump, and opens the opening / closing valve 20 of the drain pipe 19 connected to the partition bottoms of the partition plates 17 and 17 of the cleaning water tank 14, as shown in FIG. The concentrated water in 14 is discharged.
[0028]
Next, a chemical solution is put into the washing water tank 14. In introducing the chemical solution, the chemical solution can be prepared by using the permeated water tank 15. That is, as shown in FIG. 11, an insole 23 is provided at a position higher than the upper end of the partition plate 17 in the permeate tank 15 in the center, and the top from the insole is a chemical solution adjusting tank 15 a, and an open / close valve is provided in the insole 21, the on-off valve 21 is normally opened, and the permeated water that each of the submerged membrane separators 1 a to 1 f drains into the permeate tank 15 through the drain pipe is introduced to the bottom of the insole through the on-off valve 21. Drain from the bottom. When cleaning the membrane separation device 1a, the on-off valve 21 is closed, and the permeated water discharged from the devices 1b to 1f is adjusted with the chemical solution while the on-off valve 20 of the drain pipe is opened to drain the concentrated water in the washing water tank. When a predetermined amount of water is stored in the tank 15a, chemicals are added thereto to adjust the cleaning liquid, the valve 22 of the supply pipe 24 to the cleaning water tank 14 provided immediately above the inner bottom is opened, and the cleaning liquid is supplied to the cleaning water tank 14. When the supply of the cleaning liquid to the cleaning water tank is finished, the on-off valve 21 is opened and the valve 22 is closed.
[0029]
Thus, the membrane surface of the membrane unit 3 is washed by immersing the membrane separation device 1a in the chemical solution in the washing water tank for a certain period of time, and after sufficiently washing, the washing water is discharged from the drain pipe 19, and then the raw water is removed. Replenish and return to the state during high water level operation (Fig. 6).
[0030]
The six submerged membrane separators 1a to 1f are swung to 60 ° in a fixed direction, and the submerged membrane separator 1b to be cleaned next is positioned on the partition plate 17,17. The interrupted guide rail 18 described above guides each membrane separation device 1a to 1f to guide to the interrupted interval of the rail which is the next turning position. In addition, the partition of the partition plates 17 and 17 is provided in one downward direction of the space | interval which the rail interrupted (refer FIG. 7).
[0031]
By repeating the above process, the other submerged membrane separation apparatus 1b is also cleaned in the same manner when the other apparatuses 1a and 1c to 1f are operated at a low water level. In this way, one membrane separator is sequentially cleaned at the time of low water level operation.
[0032]
As described above, in this embodiment, a plurality of submerged membrane separators 1a to 1f are annularly arranged and floated in a cylindrical water tank 13, and each submerged membrane separator 1 is moved only in the vertical direction. In addition, the water tank 13 can be moved in a horizontal direction, and a sector which becomes a washing water tank 14 is partitioned by a partition plate 17 at a height at which the submerged membrane separation device 1 is accommodated in the lower part of the water tank 13. When necessary, the submerged membrane separator 1 can be transferred to the washing water tank 14 in the water tank 13 in order and to the one, so that the membrane surface can be cleaned very easily and automatically.
[0033]
The submerged membrane separation apparatus 1 according to the present invention is not limited to those provided in a reaction tank, a dipping tank, or the like, but can be used in a form that is immersed in the natural world such as lakes, seawater, and rivers. it can. For example, it can be provided in a water intake source such as a water purification plant or a factory.
[0034]
【The invention's effect】
As described above, according to the present invention, the whole area of the membrane unit is held under the liquid level by the holding means, and as a result, the whole membrane unit is attached to the buoyant body so as to be under the water surface. An air lift circulation flow is generated by air diffusion from the lower part, blocking between the membranes can be prevented, and the cleaning effect by bubbling is improved. Further, since the membrane unit is not fixed to the tank, it follows the top and bottom of the liquid level, the membrane surface is not exposed to the air, and is not hydrophobized. In addition to being able to move vertically in conjunction with the liquid level, it is also possible to move freely in the horizontal direction.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram of a first embodiment of a submerged membrane separation apparatus showing a basic configuration of the present invention.
FIG. 2 is an explanatory diagram showing the movement of a membrane unit accompanying water surface fluctuations.
FIG. 3 is a plan view of a water tank in a second embodiment for floating a plurality of submerged membrane separation devices.
4 is a cross-sectional view taken along the line AA of the water tank of FIG. 3. FIG.
5 is a plan view showing a state at the time of high water level operation in a form in which a plurality of submerged membrane separation devices are annularly arranged in the water tank of FIG. 3;
6 is a BB cross-sectional view of the water tank of FIG.
FIG. 7 is a plan view of a water tank showing the arrangement of guide rails.
FIG. 8 is a perspective view showing a positional relationship between a guide rail and a submerged membrane separation device.
FIG. 9 is a plan view showing a state during low water level operation.
10 is a cross-sectional view of the water tank of FIG. 9 taken along the line BB.
FIG. 11 is a cross-sectional view of the water tank showing a state when the cleaning water tank is drained.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Submerged membrane separator 2 Immersion tank 3 Membrane unit 4 Buoyant body 5 Connecting member 6 Mounting base 7 Suction pump 8 Pipe 9 between the suction pump and the membrane unit Drain pipe 10 Weight 11 Aeration pipe 12 Blower 13 Cylindrical water tank 14 Washing water tank 15 Permeated water tank 15a Chemical solution adjusting tank 16 Annular water tank part 17 Partition plate 18 Guide rail 19 Drain pipe 20 Opening / closing valve 21 Opening / closing valve 22 Closing open / close valve 23 Middle bottom 24 Supply pipe

Claims (5)

浸漬槽と、該浸漬槽内に浸漬された膜ユニットと、該膜ユニットを液中で浮かせる浮力体と、該浮力体を固定する取付べースと、該取付べース上に搭載された吸引ポンプと、該膜ユニットと吸引ポンプ吸引側とを接続する配管と、吸引ポン吐出側に設けた排水管とを含む浸漬膜分離装置。An immersion tank, a membrane unit immersed in the immersion tank, a buoyant body that floats the membrane unit in a liquid, a mounting base that fixes the buoyant body, and a mounting base mounted on the mounting base a suction pump, and piping connecting the the membrane unit suction pump suction side, submerged membrane separator including the provided suction pump discharge side drain pipe. 膜ユニットの下部に錘を取り付けた請求項1記載の浸漬膜分離装置。  The submerged membrane separator according to claim 1, wherein a weight is attached to a lower portion of the membrane unit. 浸漬槽は円筒形水槽の中央部に別途円筒が立設されて該円筒内が透過水槽、円筒の外側が環状水槽部として区画され、前記環状水槽部内に仕切板が設けられて洗浄部となり、洗浄部内の水の排出用配管と、洗浄部への薬液供給管が設けられてなり、前記膜ユニットを浸漬させた請求項1又は2記載の浸漬膜分離装置。  The immersion tank has a separate cylinder standing at the center of the cylindrical water tank, the inside of the cylinder is divided as a permeated water tank, the outside of the cylinder is defined as an annular water tank part, a partition plate is provided in the annular water tank part, and becomes a cleaning part, The submerged membrane separation apparatus according to claim 1 or 2, wherein a pipe for discharging water in the cleaning unit and a chemical solution supply pipe to the cleaning unit are provided, and the membrane unit is immersed. 環状水槽部の上面開口部に半径の異なる円弧状の途切れた案内レールを水平方向に設け、該案内レールに取付ベースを摺動案内するように構成した請求項3に記載の浸漬膜分離装置。The submerged membrane separation device according to claim 3, wherein a guide rail having an arc-like shape with different radii is provided in a horizontal direction at an upper surface opening of the annular water tank portion, and a mounting base is slidably guided on the guide rail. 吸引ポンプの吐出側に設けた排水管を円筒内の透過水槽に通した請求項3,4のいずれか1項に記載の浸漬膜分離装置。The submerged membrane separation apparatus according to any one of claims 3 and 4, wherein a drain pipe provided on the discharge side of the suction pump is passed through a permeate tank in a cylinder.
JP21679194A 1994-08-19 1994-08-19 Immersion membrane separator Expired - Fee Related JP3661206B2 (en)

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JP6482448B2 (en) * 2015-10-08 2019-03-13 日立造船株式会社 Osmotic intake unit
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CN115893650A (en) * 2022-11-28 2023-04-04 苏州乐净环境科技有限公司 Floating MBR filtering device, floating MBR filtering system and filtering method thereof
CN117263429A (en) * 2023-09-22 2023-12-22 威海智洁环保技术有限公司 Membrane method water treatment device and method based on ultrafiltration membrane and efficient cleaning method of ultrafiltration membrane component

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