JP4194730B2 - Sewage treatment equipment - Google Patents

Sewage treatment equipment Download PDF

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JP4194730B2
JP4194730B2 JP2000068208A JP2000068208A JP4194730B2 JP 4194730 B2 JP4194730 B2 JP 4194730B2 JP 2000068208 A JP2000068208 A JP 2000068208A JP 2000068208 A JP2000068208 A JP 2000068208A JP 4194730 B2 JP4194730 B2 JP 4194730B2
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electrolytic
sewage
scum
water
water surface
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JP2000068208A
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JP2001252671A (en
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淳一郎 佐藤
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淳一郎 佐藤
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Description

【0001】
【発明の属する技術分野】
本発明は、塗装工場における塗料ミストを含む汚水、または各種の生産工程において排出される汚水、例えば、金属前処理工程での汚水、染色工程での有色汚水、プリント基板製造工程での汚水等を薬品を用いることなく水とスラッジとに脱水分離処理する汚水装置に関するものである。
【0002】
【従来の技術】
従来の汚水処理の方法は、その殆どが薬品を用いた凝集沈澱法や酸化還元法であって、終段では生物処理、活性炭フィルタによる濾過処理、オゾン殺菌処理等がなされているが、いずれも高額の設備費を要し、また、広い設置スペースを要し、更には運転コストにも多くの費用を要して、小規模の企業者にとっては相当の負担増となって、事業経営を圧迫しかねないものとなっているのが現況である。
【0003】
【発明が解決しようとする課題】
本発明は、このような現況に鑑みなされたもので、その目的とするところは、従来装置に比して、その設備費用が安く、設置スペースも狭く、更には電力を含めてランニングコストが低減化できる小型にして、かつ効率的で使い易い汚水処理装置を提供することにある。
【0004】
【課題を解決するための手段】
この目的のため、請求項1に係る発明は、塗装工場における塗料ミストを含む汚水等の汚水が、溶解性アルミ電極を利用した電気分解により汚水とスカムとに分離されて一次処理される電解分離処理装置と、前記電解分離処理装置から加圧導入された一次処理水が、スラッジと水とに脱水分離されて二次処理される脱水処理装置とを備え、前記電解分離処理装置は、下部に汚水ピットからの汚水が流入する導入口を有し、内部には複数の溶解性アルミ電極板が間隔を有して並列状に配設された電解槽と、該電解槽に付設され、かつ電解槽において電解処理された水面上の浮遊スカムをスカム排出口を介して除去するスクレーパーを含むスカム排出手段と、前記電解槽に付設され、かつ前記スクレーパーによりスカムが確実に除去排出されるように前記電解槽内の水面を調整する水面調整板が内装された水面調整槽と、該水面調整槽からの一次処理電解水を受ける電解水受槽とを含み、前記脱水処理装置は、軸方向に二分割されて開閉可能に連結された外筒体と、該外筒体内に垂下配設された袋状濾布体とを含む構成を特徴とするものである。
【0005】
請求項2に係る発明は、前記電解分離処理装置における電解槽内が、第1の電解室と第2の電解室に区画形成されて、それぞれの電解室内にそれぞれ複数の溶解性アルミ電極板が配置され、また、前記脱水処理装置が2基並列に配置されている構成を特徴とするものである。
【0006】
【発明の実施の形態】
本発明の実施の形態について説明すると、本発明に係る汚水処理装置は、大別すると、塗装工場における塗料ミストを含む汚水等の汚水が、汚水とスカムとに分離されて一次処理される電解分離処理装置と、一次処理された電解水が二次処理される脱水処理装置とを備え、電解分離処理装置においては、溶解性アルミ電極を利用した電気分解により電解水とスカムに分離されて、電解水上に浮遊したスカムはスクレーパーにより除去排出されて一次処理がなされ、次いで、脱水処理装置において、高圧力ポンプ利用により水とスラッジ(脱水ケーキ)とに脱水分離されて二次処理がなされる。
【0007】
【実施例】
以下に具体的実施例について図面を参照し、その作用と共に説明する。
図1は全体のフロー図であり、図2は全体の概略正面図で、これら図において、汚水ピット1からの汚水はポンプ2により配管3、取入バルブ4を通って電解分離処理装置5に導入され、該電解分離処理装置5において、溶解性アルミ電極を利用した電気分解により電解水とスカムとに分離処理されて一次処理がなされる。
【0008】
図3に示されているように、電解分離処理装置5は電解槽6を含み、該電解槽6は、硬質合成樹脂材による一体成形品としての上面開口の箱型であって、その略中間内部は底板からの起立状仕切板7によって第1、第2の二つの電解室8、9に区画形成されるとともに、各電解室8、9の底部は、略漏斗状に形成され、第1の電解室8の略漏斗状部には汚水導入口が開口され、汚水ピット1からの汚水はこの下部導入口から導入される。電解室8、9内の対向する側板の下部には横に長い電極係止ブロック10が固定され、これら電極係止ブロック10の上方には、ブロック10と直交する長い複数の電極ガイドブロック11が適宜の間隔を有して縦方向に固定され、これらガイドブロック11、11間に上方よりそれぞれ方形板状の溶解性アルミ電極板12が差し込まれて並列状に配設されている。
【0009】
そして、第1の電解室8の下部導入口からの汚水は、下部より上部に環流しながら溶解性アルミ電極板12により電気分解されて、汚水中のフロックはスカムAとして水面上に浮遊し、このスカムAは後述の手段により除去排出される。
【0010】
図3に示されているように、第1の電解室8の汚水は電気分解処理されながら仕切板7を超えて第2の電解室9に流入し、流入した電解水は、第2の電解室9内にして、かつ正面板と背面板間に仕切板7との間に間隔を有して平行に、しかも下部は漏斗状部の一部と平行にして形成されたガイド板13と仕切板7間を通って第2の電解室9の下部より上部に環流しながら第2の電解室9の溶解性アルミ電極板12により再度電気分解されて、電解水中のフロックはスカムAとして水面上に浮遊する。
【0011】
第1および第2の電解室8、9の水面上に浮遊したスカムAは、電解槽6の略中央上部に付設のスカム排出手段14により除去されて外部に排出される。
【0012】
スカム排出手段14は、大別すると、駆動部とスクレーパーを含み、駆動部15は、図6から図8に示されているように、下面開口の長い箱型状ハウジング15内の上方長手方向に、一端がベアリング軸台16により支持され、他端がハウジング15外面に取り付けの駆動モータ17の軸18と継手19を介して水平に連結されたボールネジ20が回転自在に設けられるとともに、該ボールネジ20には、ボールネジ20の正逆回転に伴って実線矢印方向に前進後退するボールナット21が、ブロック状のナットハウジング22内に固着された状態で螺合して取り付けられている。
【0013】
ボールネジ20の下方には、図7および図8に示されているように、ボールネジ20と平行にガイドレール23がハウジング15の側板の内面長手方向に固着されて配設されており、このガイドレール23にはスライドパック24がベアリング25を介して係合し、該スライドパック24とナットハウジング22は断面略Z字状のスライダー金具26の二つの片部27、28を介して連結され、ボールナット21と一体的に前進後退し、その前進後退は、ハウジング15の正面板内と背面板内のリミットスイッチ取付金具30に取り付けられたリミットスイッチ31により規制されている。
【0014】
ハウジング15下端開口部から外方に水平に突出したスライダー金具26の自由端片部29に、電解槽6の横幅よりもやや短いスクレーパー取付板32がボールネジ20と直交する如くに取り付けられるとともに、該スクレーパー取付板32には、その中間部位を除いた左右部位にそれぞれスクレーパー33が下向きに取り付けられている。
【0015】
このように構成されたスカム排出手段14は、図2、図3および図5に示されているように、ハウジング15の前後両端の側面が、電解槽6の正面側に突出させて一体成形のスカム排出口34の中央部に一体に起立形成された取付片35と、電解槽6の背面側中央部位に起立させた取付板36に取り付けられて、電解槽6の中央部に架設されている。
【0016】
そして、第1、第2の電解室8、9において電解処理された水面上に浮遊したスカムAは、駆動モータ17の回転力を受けて回転するボールネジ20と共動してボールナット21が前進後退するとともに、これと連動してスライドパック24がガイドレール23に沿って同方向に平行移動し、スライドパック24にスライダーZ金具26、スクレーパー取付板32を介して取り付けられたそれぞれのスクレーパー33によりスカム排出口34からスカム受槽37に排出される。
【0017】
なお、スカム排出のタイミングはタイマー(図示しない)により制御され、また、スクレーパー33の前進はスライドパック24が前方のリミットスイッチ31に接触することにより停止し、後退は後方のリミットスイッチ31に接触することにより停止する。
【0018】
スカムAの除去された第2の電解室9内の電解処理水は、図9に示されているように、第2の電解室9と水面調整槽38との共通側板に開口の横長孔39を通って水面調整槽38に流入する。
【0019】
水面調整槽38内には、図10および図11に示されているように、その底板上に幅いっぱいに固定板40が一体にして、かつ起立状に形成され、固定板40の前方両端縁には間隔を置いて平行に左右ガイド板41が一体にして、かつ起立状に形成され、これら固定板40と左右ガイド板41間には上方より水面調整板42が実線矢印で示す上下方向に摺動可能として差し込まれている。そして、水面調整板42を適宜に上方に可動し、止め具43により固定板40に衝止することによって水面調整板42を所定位置で一時的に固定し、電解槽6(第1の電解室8と第2の電解室9)内の汚水の水面が、スクレーパー33によるスカムAの除去排出に適合した水面になるよう調整される。
【0020】
なお、固定板40と水面調整板42は共にその上辺がV字状に形成された三角堰となっているが、これは水面調整槽38内に流れ込んでいる流量が外部から容易に目測し得るようにしたからである。
【0021】
電解槽6から水面調整槽38に流入の電解水は、流出孔から配管44を介して電解水受槽45に移送される。
【0022】
第1の電解室8と第2の電解室9の底部はそれぞれドレンバルブ46、47を介して配管48と接続され、また、配管48はスカム受槽37と接続されて、スカム受槽37からの汚水、各電解室8、9からのドレンは配管48を通って汚水ピット1に戻るよう配管されている。
【0023】
電解水受槽45からの一次処理水は、配管49、給水ストップバルブ50を介し高圧力ポンプ51により配管52、給水ストップバルブ53、三方ロータリーバルブ54、配管55、分岐配管56、脱水ストップバルブ57を介して2基の脱水処理装置58に高圧移送され、該脱水処理装置58においてスラッジ(脱水ケーキ)と水とに脱水分離されて二次処理がなされる。
【0024】
2基の脱水処理装置58は同一構成であって、図12および図13に示されているように、軸方向に二分割されて複数の開閉金具62により開閉可能に連結され、かつ上下の開口部端縁にはつば部60を有し、また、自由端縁軸方向にそれぞれつば部61を有し、全体が図13に想像線で示されているように、開閉金具62を介して開かれ、また、つば部61の接合部がボルト、ナット等の固着具63により締着されて閉塞される外筒体59を含んでいる。
【0025】
外筒体59の上部には、中央部に一次処理電解水の導入口65を有する上部閉塞板64が、その外周縁部とつは部60との接合部に対するボルト、ナット等の固着具66をもって固着され、外筒体下部はその中央部に排水口68を有する下部閉塞板67に、その外周縁部とつば部61との接合部に対するボルト、ナット等の固着具69をもって固着されている。
【0026】
下部閉塞板67上には、下部閉塞板67よりもやや小径にして、かつ排水口68と適合する排水口71を有する台座70が固着され、該台座70上の中央部には、排水口71を囲繞して金網等による上面が閉塞し、かつ下面開口の水抜用内筒体72が立設固着されるとともに、該水抜用内筒体72の外周部には、袋状濾布体73が設けられている。
【0027】
袋状濾布体73は、1ミクロン以上の微粒子の補集が可能な濾布体であって、胴部74と該胴部74から二股状に分岐した長足状袋部75を有する、所謂衣服のズボン形状であって、胴部74が上部閉塞板64の下面に導入口65を囲繞して取付板77により取り付けられるとともに、分岐部が水抜用内筒体72の上面部で支持され、二つの長足状袋部75は図13に想像線で示されているように、横断面略半円状にして垂下され、それぞれの下端部は幾重にも折り畳まれて折畳み部76とされて密閉状態とされている。また、袋状濾布体73と外筒体59の間には水切用網状筒体78が設けられている。
【0028】
そして、2基の脱水処理装置58は、受皿79上に配置されている。各配管、バルブを通って導入口65より圧入された一次処理水は、図12に矢印で示されているように、袋状濾布体73の胴部74から両方の長足状袋部75を流れ落ちながら、水は水抜用内筒体72内を流れ落ち、一部は水切用網状筒体78に入る。一方、一次処理水中に含まれているスラッジBは、折畳み部76により密閉されているそれぞれの長足状袋部75に補集される。
【0029】
袋状濾布体73により濾過された二次処理水は、排出口71、68から受皿79に集められ、更に2基による二次処理水は共通の排水口より濾過水受槽80に貯留され、濾過水返送ポンプ81により汚水ピット1に返送される。
【0030】
このようにして脱水処理がなされた後、三方ロータリーバルブ54が切替えられて一次処理水の圧入が停止され、次いで、電磁バルブ82の作動によりコンプレッサー83からの圧縮空気が各導入口65から各袋状濾布体73内に導入されて、各長足状袋部75内に溜まっているスラッジBは圧縮空気による圧力振動により圧縮され、これが完全なケーキ状態になるまで自動的に繰り返される。この場合において、スラッジの容量、限度の判断は圧力スイッチおよび指示計84により、またはタイマー等による運転時間の管理により決定される。このように電解分離処理装置5による汚水の一次処理と脱水処理装置58による二次処理は、電解電源を含む制御盤85の操作により自動的に行われる。
【0031】
袋状濾布体73内のスラッジBが完全なケーキ状態になると、運転が停止されて、外筒体59を固定している上下閉塞板64、67の各固着具66、69が外されるとともに、外筒体59を閉塞しているつば部61の固着具63が外され、外筒体59は開閉金具62を支点として図13に想像線で示されているように、手動で開かれ、中の長足状袋部75が取り出されて、折畳み部76が開放されて脱水ケーキ(スラッジB)が取り出される。
【0032】
【発明の効果】
しかして、本発明によれば、電解分離処理装置と脱水処理装置との組合わせ装置であるから、全体的に小型化が可能で、設備費用も安く、また、設置スペースも狭くて済むものである。
【0033】
また、電解分離処理装置は、溶解性アルミ電極を用いた電解構造であるから、混合、乳化状態にある汚水の分解が容易であり、また、水素ガスによる殺菌作用も含め水の浄化が進行する。
【0034】
また、電解槽には、水面調整手段を有する水面調整槽が付設されているから、電解槽内の水位は常に良好に調整保持されて、汚水面上に分離浮遊してきたスカムを確実にスクレーパーで除去排出することができる。
【0035】
また、脱水処理装置においては、薬品は不要で、微細粒子の補集が可能な袋状濾布体内に一次処理水を高圧力で流し入れてスラッジを脱水分離し、更に圧縮空気を入れて圧力振動を与えるものであるから、脱水効率が向上し、スラッジのケーキ化が良好になされる。
【0036】
また、脱水処理装置において、ケーキ化されたスラッジの袋状濾布体からの取り出しは、外筒体が軸方向に開閉可能となっているから、容易に取り出すことができる。
【図面の簡単な説明】
【図1】本発明に係る汚水処理装置の一例でのフロー図である。
【図2】本発明の一例での概略正面図である。
【図3】電解分離装置の要部を示す一部断面の正面図である。
【図4】溶解性アルミ電極板の配列状態を示す部分的拡大横断図である。
【図5】電解室部分を示す一部断面の正面図である。
【図6】スカム排出手段の部分を示す一部省略の正面図である。
【図7】スカム排出手段の要部を示す一部断面の側面図である。
【図8】スカム排出手段におけるスライダーZ金具と他の構成部材との取り付け状態を示す一部省略の断面図である。
【図9】一部を断面し、かつ一部を省略して示す電解槽と水面調整槽の側面図である。
【図10】水面調整手段の一例を示す正面図である。
【図11】図10の一部省略の縦断面図である。
【図12】脱水処理装置の一例を示す一部省略の縦断面図である。
【図13】図12の横断面図である。
【符号の説明】
1 汚水ピット
5 電解分離処理装置
6 電解槽
7 仕切板
8 第1の電解室
9 第2の電解室
12 溶解性アルミ電極板
14 スカム排出手段
33 スクレーパー
34 スカム排出口
38 水面調整槽
39 横長孔
42 水面調整板
45 電解水受槽
58 脱水処理装置
59 外筒体
73 袋状濾布体
A スカム
B スラッジ
[0001]
BACKGROUND OF THE INVENTION
The present invention includes sewage containing paint mist in a paint factory, or sewage discharged in various production processes, such as sewage in a metal pretreatment process, colored sewage in a dyeing process, and sewage in a printed circuit board manufacturing process. The present invention relates to a sewage apparatus that performs dehydration and separation into water and sludge without using chemicals.
[0002]
[Prior art]
Most of the conventional sewage treatment methods are coagulation-precipitation method and oxidation-reduction method using chemicals, and biological treatment, filtration treatment with activated carbon filter, ozone sterilization treatment, etc. are made at the final stage. Large equipment costs, a large installation space, and a lot of operating costs also add a considerable burden to small businesses, putting pressure on business management It is the current situation that has become impossible.
[0003]
[Problems to be solved by the invention]
The present invention has been made in view of such a current situation, and the object of the present invention is that the equipment cost is lower, the installation space is smaller, and the running cost including electric power is reduced as compared with the conventional apparatus. An object of the present invention is to provide an efficient and easy-to-use sewage treatment apparatus that can be made compact.
[0004]
[Means for Solving the Problems]
For this purpose, the invention according to claim 1 is an electrolytic separation in which sewage such as sewage containing paint mist in a coating factory is separated into sewage and scum by electrolysis using a soluble aluminum electrode. A treatment device, and a dehydration device in which primary treated water introduced under pressure from the electrolytic separation treatment device is dehydrated and separated into sludge and water and subjected to a secondary treatment, and the electrolytic separation treatment device is disposed at a lower portion. An electrolytic cell having an inlet through which sewage from the sewage pit flows, a plurality of soluble aluminum electrode plates arranged in parallel at intervals, and an electrolytic cell attached to the electrolytic cell and electrolyzed A scum discharge means including a scraper for removing floating scum on the water surface electrolyzed in the tank through a scum discharge port; and attached to the electrolytic tank, and the scum is surely removed and discharged by the scraper. A water surface adjustment tank equipped with a water surface adjustment plate for adjusting the water surface in the electrolysis tank, and an electrolyzed water receiving tank that receives primary treated electrolyzed water from the water surface adjustment tank, and the dehydration apparatus is arranged in the axial direction. The present invention is characterized in that it includes an outer cylinder that is divided into two parts and that is connected to be openable and closable, and a bag-like filter cloth that is suspended from the outer cylinder.
[0005]
In the invention according to claim 2, the inside of the electrolytic cell in the electrolytic separation treatment apparatus is partitioned into a first electrolytic chamber and a second electrolytic chamber, and a plurality of soluble aluminum electrode plates are provided in each electrolytic chamber. The dehydration apparatus is arranged in parallel, and two of the dehydration processing apparatuses are arranged in parallel.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
DESCRIPTION OF EMBODIMENTS Embodiments of the present invention will be described. The sewage treatment apparatus according to the present invention can be broadly divided into electrolytic separation in which sewage such as sewage containing paint mist in a coating factory is separated into sewage and scum and subjected to primary treatment. A treatment device and a dehydration treatment device for secondary treatment of the electrolyzed water subjected to the primary treatment. In the electrolytic separation treatment device, the electrolyzed water is separated into electrolyzed water and scum by electrolysis using a soluble aluminum electrode. The scum floating on the water is removed and discharged by a scraper and subjected to a primary treatment, and then dehydrated and separated into water and sludge (dehydrated cake) using a high pressure pump in a dehydration processing device, and subjected to a secondary treatment.
[0007]
【Example】
Specific examples will be described below with reference to the drawings, together with the operation thereof.
FIG. 1 is an overall flow diagram, and FIG. 2 is an overall schematic front view. In these drawings, sewage from the sewage pit 1 passes through a pipe 3 and an intake valve 4 by a pump 2 to an electrolytic separation treatment device 5. Introduced and electrolyzed using a soluble aluminum electrode, the electrolytic separation treatment apparatus 5 separates the electrolyzed water and scum into primary treatment.
[0008]
As shown in FIG. 3, the electrolytic separation treatment apparatus 5 includes an electrolytic cell 6, and the electrolytic cell 6 is a box shape with an upper surface opening as an integrally molded product made of a hard synthetic resin material, and is substantially in the middle. The interior is partitioned and formed into first and second electrolysis chambers 8 and 9 by an upright partition plate 7 from the bottom plate, and the bottoms of the electrolysis chambers 8 and 9 are formed in a substantially funnel shape. A sewage introduction port is opened in a substantially funnel-shaped portion of the electrolysis chamber 8, and sewage from the sewage pit 1 is introduced from this lower introduction port. A horizontally long electrode locking block 10 is fixed to the lower part of the opposing side plates in the electrolysis chambers 8 and 9. Above these electrode locking blocks 10, a plurality of long electrode guide blocks 11 orthogonal to the block 10 are provided. A rectangular plate-like soluble aluminum electrode plate 12 is inserted between the guide blocks 11 and 11 from above, and arranged in parallel.
[0009]
And the sewage from the lower inlet of the first electrolysis chamber 8 is electrolyzed by the soluble aluminum electrode plate 12 while circulating from the lower part to the upper part, and the floc in the sewage floats on the water surface as scum A, This scum A is removed and discharged by means described later.
[0010]
As shown in FIG. 3, the sewage in the first electrolysis chamber 8 flows into the second electrolysis chamber 9 over the partition plate 7 while being electrolyzed, and the electrolyzed water that flows in the second electrolysis chamber A guide plate 13 and a partition formed in the chamber 9 and in parallel with a space between the front plate and the rear plate with a space between the partition plate 7 and with the lower portion parallel to a part of the funnel-shaped portion. Electrolysis is again performed by the soluble aluminum electrode plate 12 in the second electrolysis chamber 9 while circulating between the plates 7 from the lower portion to the upper portion of the second electrolysis chamber 9, and the floc in the electrolyzed water becomes scum A on the surface of the water. To float.
[0011]
The scum A floating on the water surface of the first and second electrolysis chambers 8 and 9 is removed by the scum discharge means 14 attached to the substantially upper center of the electrolytic cell 6 and discharged to the outside.
[0012]
The scum discharge means 14 roughly includes a drive unit and a scraper, and the drive unit 15 is arranged in the upper longitudinal direction in the box-shaped housing 15 having a long bottom opening, as shown in FIGS. A ball screw 20 having one end supported by the bearing shaft 16 and the other end connected horizontally to the shaft 18 of the drive motor 17 attached to the outer surface of the housing 15 via a joint 19 is rotatably provided. A ball nut 21 that advances and retreats in the direction of the solid arrow in accordance with forward and reverse rotation of the ball screw 20 is screwed and attached in a state of being fixed in a block-shaped nut housing 22.
[0013]
As shown in FIGS. 7 and 8, a guide rail 23 is fixed below the ball screw 20 in parallel with the ball screw 20 in the longitudinal direction of the inner surface of the side plate of the housing 15. The slide pack 24 is engaged with the nut 23 via a bearing 25, and the slide pack 24 and the nut housing 22 are connected via two pieces 27 and 28 of a slider metal fitting 26 having a substantially Z-shaped cross section. The forward / backward movement is integrated with the limit switch 31 attached to the limit switch mounting bracket 30 in the front plate and the rear plate of the housing 15.
[0014]
A scraper mounting plate 32 that is slightly shorter than the lateral width of the electrolytic cell 6 is attached to the free end piece 29 of the slider fitting 26 that protrudes horizontally from the lower end opening of the housing 15 so as to be orthogonal to the ball screw 20. On the scraper mounting plate 32, scrapers 33 are respectively attached to the left and right parts excluding the intermediate part.
[0015]
As shown in FIGS. 2, 3, and 5, the scum discharging means 14 configured as described above is integrally formed by projecting the front and rear side surfaces of the housing 15 to the front side of the electrolytic cell 6. It is attached to an attachment piece 35 that is integrally formed upright at the center of the scum discharge port 34 and an attachment plate 36 that is erected at the central portion on the back side of the electrolytic cell 6, and is installed in the central part of the electrolytic cell 6. .
[0016]
Then, the scum A floating on the water surface electrolyzed in the first and second electrolysis chambers 8 and 9 moves together with the ball screw 20 that rotates by receiving the rotational force of the drive motor 17 and the ball nut 21 advances. In conjunction with this, the slide pack 24 is translated in the same direction along the guide rail 23, and each scraper 33 is attached to the slide pack 24 via a slider Z metal fitting 26 and a scraper mounting plate 32. It is discharged from the scum discharge port 34 to the scum receiving tank 37.
[0017]
The timing of discharging the scum is controlled by a timer (not shown), and the advancement of the scraper 33 is stopped when the slide pack 24 contacts the front limit switch 31, and the backward movement contacts the rear limit switch 31. Stop by.
[0018]
As shown in FIG. 9, the electrolytically treated water in the second electrolysis chamber 9 from which the scum A has been removed is a horizontally elongated hole 39 having an opening in the common side plate of the second electrolysis chamber 9 and the water surface adjustment tank 38. It flows into the water surface adjustment tank 38 through.
[0019]
As shown in FIGS. 10 and 11, the fixing plate 40 is integrally formed upright on the bottom plate in the water surface adjustment tank 38 in an upright manner, and both front edges of the fixing plate 40 are formed. The left and right guide plates 41 are integrally formed upright in parallel with an interval, and a water level adjusting plate 42 is formed between the fixed plate 40 and the left and right guide plates 41 in the vertical direction indicated by a solid line arrow from above. It is inserted as slidable. Then, the water level adjustment plate 42 is appropriately moved upward, and the water level adjustment plate 42 is temporarily fixed at a predetermined position by stopping against the fixing plate 40 by the stopper 43, and the electrolytic cell 6 (first electrolytic chamber). 8 and the second electrolysis chamber 9) are adjusted so that the water level of the sewage is suitable for the removal and discharge of the scum A by the scraper 33.
[0020]
Both the fixed plate 40 and the water surface adjustment plate 42 are triangular weirs whose upper sides are formed in a V shape, and this allows the flow rate flowing into the water surface adjustment tank 38 to be easily measured from the outside. It was because it did so.
[0021]
The electrolyzed water flowing into the water surface adjustment tank 38 from the electrolyzer 6 is transferred to the electrolyzed water receiving tank 45 through the pipe 44 from the outflow hole.
[0022]
The bottoms of the first electrolysis chamber 8 and the second electrolysis chamber 9 are connected to a pipe 48 via drain valves 46 and 47, respectively, and the pipe 48 is connected to a scum receiving tank 37 so that sewage from the scum receiving tank 37 is obtained. The drains from the electrolysis chambers 8 and 9 are piped so as to return to the sewage pit 1 through the pipe 48.
[0023]
The primary treated water from the electrolyzed water receiving tank 45 is connected to a pipe 52, a water supply stop valve 53, a three-way rotary valve 54, a pipe 55, a branch pipe 56, and a dehydration stop valve 57 through a pipe 49 and a water supply stop valve 50. To the two dehydration treatment devices 58, and the dehydration treatment device 58 is dehydrated and separated into sludge (dehydrated cake) and water for secondary treatment.
[0024]
As shown in FIGS. 12 and 13, the two dehydration processing devices 58 are divided into two parts in the axial direction and connected so as to be openable and closable by a plurality of opening and closing metal fittings 62, as well as upper and lower openings. A flange 60 is provided at the end of each part, and a flange 61 is provided in each axial direction of the free edge. The entire part is opened via an opening / closing bracket 62 as indicated by an imaginary line in FIG. In addition, the joint portion of the collar portion 61 includes an outer cylindrical body 59 that is fastened and closed by a fixing tool 63 such as a bolt or a nut.
[0025]
At the upper part of the outer cylinder 59, there is an upper closing plate 64 having an inlet 65 for primary treated electrolyzed water at the center, and a fixing tool 66 such as a bolt or nut for the joint between the outer peripheral edge and the part 60. The lower part of the outer cylindrical body is fixed to a lower closing plate 67 having a drain outlet 68 at the center thereof with fixing tools 69 such as bolts and nuts for the joint between the outer peripheral edge part and the collar part 61. .
[0026]
A pedestal 70 having a drain port 71 that is slightly smaller in diameter than the lower block plate 67 and that matches the drain port 68 is fixed on the lower block plate 67, and a drain port 71 is provided at the center on the pedestal 70. The drainage inner cylinder 72 is fixed upright and the bag-like filter cloth body 73 is formed on the outer peripheral portion of the drainage inner cylinder 72. Is provided.
[0027]
The bag-like filter cloth body 73 is a filter cloth body capable of collecting fine particles of 1 micron or more, and has a trunk portion 74 and a long leg-like bag portion 75 branched from the trunk portion 74 into a bifurcated shape. The body portion 74 is attached to the lower surface of the upper closing plate 64 by surrounding the introduction port 65 by the attachment plate 77, and the branch portion is supported by the upper surface portion of the draining inner cylinder 72. As shown by an imaginary line in FIG. 13, the two long-legged bag portions 75 are suspended in a substantially semicircular cross section, and each lower end portion is folded several times into a folded portion 76 to be sealed. It is said that. In addition, a draining reticulated cylinder 78 is provided between the bag-like filter cloth 73 and the outer cylinder 59.
[0028]
The two dehydration processing devices 58 are disposed on a tray 79. The primary treated water that has been press-fitted from the introduction port 65 through the pipes and valves passes through both the long-legged bag portions 75 from the trunk portion 74 of the bag-like filter cloth body 73 as indicated by arrows in FIG. While flowing down, water flows down in the draining inner cylinder 72, and a part enters the draining reticulated cylinder 78. On the other hand, the sludge B contained in the primary treated water is collected in each long-legged bag portion 75 sealed by the folding portion 76.
[0029]
The secondary treated water filtered by the bag-like filter cloth body 73 is collected in the receiving tray 79 from the discharge ports 71 and 68, and the secondary treated water by two units is further stored in the filtered water receiving tank 80 from the common drain port, The filtrate is returned to the sewage pit 1 by the filtered water return pump 81.
[0030]
After the dehydration process is performed in this manner, the three-way rotary valve 54 is switched to stop the press-fitting of the primary treated water, and the compressed air from the compressor 83 is then sent from each inlet 65 to each bag by the operation of the electromagnetic valve 82. The sludge B introduced into the filter cloth body 73 and accumulated in the long leg-like bag portions 75 is compressed by pressure vibration caused by compressed air, and is automatically repeated until it becomes a complete cake state. In this case, the determination of the sludge capacity and limit is determined by the pressure switch and indicator 84 or by management of the operation time by a timer or the like. Thus, the primary treatment of sewage by the electrolytic separation treatment device 5 and the secondary treatment by the dehydration treatment device 58 are automatically performed by operating the control panel 85 including the electrolytic power source.
[0031]
When the sludge B in the bag-shaped filter cloth body 73 is in a complete cake state, the operation is stopped and the fixing members 66 and 69 of the upper and lower closing plates 64 and 67 fixing the outer cylinder body 59 are removed. At the same time, the fixing member 63 of the collar portion 61 closing the outer cylindrical body 59 is removed, and the outer cylindrical body 59 is manually opened as indicated by an imaginary line in FIG. The long legged bag portion 75 is taken out, the folding portion 76 is opened, and the dehydrated cake (sludge B) is taken out.
[0032]
【The invention's effect】
Therefore, according to the present invention, since it is a combination device of an electrolytic separation treatment device and a dehydration treatment device, the overall size can be reduced, the equipment cost is low, and the installation space can be reduced.
[0033]
In addition, since the electrolytic separation treatment apparatus has an electrolytic structure using a soluble aluminum electrode, it is easy to decompose sewage in a mixed and emulsified state, and water purification proceeds including sterilization by hydrogen gas. .
[0034]
In addition, since the electrolyzer is equipped with a water surface adjustment tank having a water surface adjusting means, the water level in the electrolyzer is always adjusted and maintained well, and the scum separated and floated on the sewage surface can be surely secured with a scraper. Can be removed and discharged.
[0035]
In addition, in the dehydration processing equipment, no chemicals are required and the sludge is dewatered and separated by pouring primary treated water at a high pressure into the bag-shaped filter cloth that can collect fine particles, and pressure vibration is caused by adding compressed air. Therefore, dewatering efficiency is improved and sludge cake formation is achieved.
[0036]
Moreover, in the dehydration apparatus, the cake sludge can be easily removed from the bag-like filter cloth body because the outer cylinder body can be opened and closed in the axial direction.
[Brief description of the drawings]
FIG. 1 is a flowchart of an example of a sewage treatment apparatus according to the present invention.
FIG. 2 is a schematic front view of an example of the present invention.
FIG. 3 is a partial cross-sectional front view showing the main part of the electrolytic separation apparatus.
FIG. 4 is a partially enlarged cross-sectional view showing an arrangement state of soluble aluminum electrode plates.
FIG. 5 is a partial cross-sectional front view showing an electrolytic chamber portion.
FIG. 6 is a partially omitted front view showing a portion of scum discharge means.
FIG. 7 is a partial cross-sectional side view showing the main part of the scum discharge means.
FIG. 8 is a partially omitted cross-sectional view showing a state where the slider Z metal fitting and other components are attached in the scum discharge means.
FIG. 9 is a side view of an electrolytic cell and a water surface adjustment tank, partially cut away and partially omitted.
FIG. 10 is a front view showing an example of water surface adjusting means.
11 is a longitudinal sectional view of FIG. 10 partially omitted.
FIG. 12 is a partly omitted longitudinal sectional view showing an example of a dehydrating apparatus.
13 is a cross-sectional view of FIG.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Sewage pit 5 Electrolytic separation processing apparatus 6 Electrolysis tank 7 Partition plate 8 1st electrolysis chamber 9 2nd electrolysis chamber 12 Soluble aluminum electrode plate 14 Scum discharge means 33 Scraper 34 Scum discharge port 38 Water surface adjustment tank 39 Horizontal long hole 42 Water surface adjustment plate 45 Electrolyzed water receiving tank 58 Dehydration processing device 59 Outer cylinder 73 Bag-shaped filter cloth body A Scum B Sludge

Claims (2)

塗装工場における塗料ミストを含む汚水等の汚水が、溶解性アルミ電極を利用した電気分解により汚水とスカムとに分離されて一次処理される電解分離処理装置と、
前記電解分離処理装置から加圧導入された一次処理水が、スラッジと水とに脱水分離されて二次処理される脱水処理装置とを備え、
前記電解分離処理装置は、下部に汚水ピットからの汚水が流入する導入口を有し、内部には複数の溶解性アルミ電極板が間隔を有して並列状に配設された電解槽と、該電解槽に付設され、かつ電解槽において電解処理された水面上の浮遊スカムをスカム排出口を介して除去するスクレーパーを含むスカム排出手段と、前記電解槽に付設され、かつ前記スクレーパーによりスカムが確実に除去排出されるように前記電解槽内の水面を調整する水面調整板が内装された水面調整槽と、該水面調整槽からの一次処理電解水を受ける電解水受槽とを含み、
前記脱水処理装置は、軸方向に二分割されて開閉可能に連結された外筒体と、該外筒体内に垂下配設された袋状濾布体とを含む構成を特徴とする汚水処理装置。
An electrolytic separation treatment apparatus in which sewage such as sewage containing paint mist in a paint factory is separated into sewage and scum by electrolysis using a soluble aluminum electrode,
The primary treatment water introduced under pressure from the electrolytic separation treatment device comprises a dehydration treatment device that is dehydrated and separated into sludge and water and subjected to secondary treatment,
The electrolytic separation treatment apparatus has an introduction port through which sewage from a sewage pit flows at the lower part, and an electrolytic cell in which a plurality of soluble aluminum electrode plates are arranged in parallel with intervals therebetween, A scum discharge means including a scraper attached to the electrolytic cell and removing floating scum on the water surface electrolyzed in the electrolytic cell through a scum discharge port; and a scum attached to the electrolytic cell, Including a water surface adjustment tank equipped with a water surface adjustment plate for adjusting the water surface in the electrolytic cell so as to be surely removed and discharged, and an electrolyzed water receiving tank for receiving primary treated electrolyzed water from the water surface adjustment tank,
The dewatering apparatus includes an outer cylinder that is divided into two in the axial direction and connected so as to be openable and closable, and a bag-like filter cloth body that is suspended in the outer cylinder. .
前記電解分離処理装置における電解槽内が、第1の電解室と第2の電解室に区画形成されて、それぞれの電解室内にそれぞれ複数の溶解性アルミ電極板が配置され、また、前記脱水処理装置が2基並列に配置されている構成を特徴とする請求項1の汚水処理装置。The electrolytic cell in the electrolytic separation processing apparatus is partitioned into a first electrolytic chamber and a second electrolytic chamber, and a plurality of soluble aluminum electrode plates are disposed in the respective electrolytic chambers. 2. The sewage treatment apparatus according to claim 1, wherein two apparatuses are arranged in parallel.
JP2000068208A 2000-03-13 2000-03-13 Sewage treatment equipment Expired - Lifetime JP4194730B2 (en)

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