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JP3670391B2 - Water purifier - Google Patents
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JP3670391B2 - Water purifier - Google Patents

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JP3670391B2
JP3670391B2 JP12919096A JP12919096A JP3670391B2 JP 3670391 B2 JP3670391 B2 JP 3670391B2 JP 12919096 A JP12919096 A JP 12919096A JP 12919096 A JP12919096 A JP 12919096A JP 3670391 B2 JP3670391 B2 JP 3670391B2
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tank
water
treatment
ozone
source water
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JPH09290283A (en
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秋路 原
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有限会社制電工業
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    • 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

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、処理槽の異なる複数の処理タンクを備え、上手側に設置した源水タンクを介し下手側の処理タンクから落差流下方式によって処理水を浄化処理するようにした浄水装置に関する。
【0002】
【従来の技術】
従来、湖や池,河川等の源水又は食品その他洗浄が行われた排水、並びにガソリンスタンド等の施設から排出される源水の浄化処理を行う浄水装置は、木炭及びゼオライトライト等を収容した複数の処理タンクを互いに連結し、その上手側の処理タンクから源水を給水ポンプで圧送供給し、最終の処理タンクから浄化水を強制排出するようにした浄水装置が知られている。
また近年このような浄水装置にオゾンを供給し殺菌等のオゾン処理を行うようにした浄水装置も知られている。
【0003】
【発明が解決しようとする課題】
然し、上記従来の構成による浄水装置は、大量の有機物や洗剤,油等種々の成分及び着色物等で汚染されている源水を処理する場合に、上手側の処理タンク内の木炭或いはゼオライト等の濾過体に対し、有機物や着色物また雑菌等が大量に付着すると共に該濾過体中を源水が強制的に圧送されるので、早期に目詰まり等が発生し易くその処理能力を低下させる欠点がある。
また各処理槽における処理が充分に行われないまま排出されるので、上記濾過体の交換を頻繁に行う必要を生じたり、各処理タンク内に大量の濾過体を収容しなければならない結果、浄水装置が大型化する不具合やランニングコストが高くなる等の問題がある。
【0004】
【課題を解決するための手段】
上記従来の問題点を解消するための本発明による浄水装置は、第1に源水の供給上手側から微生物による浄化処理作用を行う第1処理タンク5及び第2処理タンク6等からなる複数の処理タンク1と、該処理タンク1の下手側にオゾンが供給されてオゾン処理を行うオゾンタンク4を連結して源水の浄化を行う浄水装置Aにおいて、前記処理タンク1の上手側に源水を貯溜させる源水タンク2を設け、該源水タンク2から吸水ポンプ2Pによって第1タンク5に送水すると共に、第1処理タンク5から下手側の処理タンクを落差流下方式によって排水可能に連結し、且つ上記第1処理タンク5及び第2処理タンク6等の処理タンク1に、エアーとオゾンを選択可能に供給することにより、該処理タンク内の処理水を循環させながらバッキ処理とオゾン処理を行う補助タンク5T6Tを各別に併設してなることを特徴としている。
【0005】
に、処理タンク1の下手側に設置したオゾンタンク4から排水される処理水を源水タンク2に返流させて循環を繰り返して浄化処理させることを特徴としている。
【0006】
に、各処理タンク1及びオゾンタンク4を一側に列設すると共に他側に源水タンク2等を併設し、これらを一つの機台上に一体的に構成することを特徴としている。
【0007】
に、上手側の処理タンク1内に木炭5a又はゼオライト等の高多孔質微生物増床材を収容させると共に、下手側の処理タンク1内に瓦を粉砕した瓦片6aを収容させて浄水処理を行わせることを特徴としている。
【0008】
【発明の実施形態】
本発明の一実施形態を図面に基づいて説明する。図1は本発明に係わる浄水装置Aのカバーを外した内部構造を示し、図1〜図3に示すように該浄水装置Aは、平面視方形状の機台1a上で源水を収容可能な源水タンク(貯溜タンク)2を処理方向最上手側に設置すると共に、これに後続して立設固定した円筒容器状の複数の処理タンク1(5,6,4)のうち、上手側のものを適宜な大きさ(略10〜50mm程度)に粉砕した木炭5aを収容する木炭タンク(第1処理タンク)5にしている。
【0009】
またこの下手側のものを処理水の収容量と処理の性能を確保すると共に目詰まりを生じない範囲で、適宜な大きさ(略10〜20mm程度)に粉砕された瓦片6aを収容した瓦片タンク(第2処理タンク)6に構成すると共に、この下手側にオゾン発生器3から発生させたオゾンをエアーと適当量に混合させて供給するオゾンタンク(第3処理タンク)4となし、相隣るタンクを各連結管50,60を介して一連に連結し、源水タンク2から給水ポンプ2Pで給水される源水を連結管20を介して上記配設された処理タンク1に送給し、該処理タンク1の下手側から排出される処理水を排出管7によって源水タンク2内に還流(返流)するようにしている。
【0010】
尚、各処理タンク1の上部に開口する供給口10には通気口11を有する蓋12を開閉可能に取着し、木炭5a並びに瓦片6a等の濾過体を収容したメッシュ状の容器15を上記供給口10から挿脱することにより交換可能にしている。
また各処理タンク1の底部にはバルブ付のドレン13を設けて、必要によりタンク内の水と共に底部に溜まった蓄積物を排出し、タンク内を適時に清掃可能にしている。
上記浄水装置Aは、機台1a上の前面側に各処理タンク1を列設することにより、濾過体の交換及びメンテナンス作業を容易に行うことができるようにすると共に、その背後に源水タンク2を機体巾方向に設置することにより、源水の貯溜量を充分に確保しながら、機体をコンパクトに纏めて装置の小型化を図っている。
【0011】
上記処理タンク1の木炭タンク5は、その上部一側に前記連結管20の送水端を連結して給水口5Kを開設し、底部の送水口5Sとの間を木炭5aの収容部に形成している。
また瓦タンク6は、上記木炭タンク5の給水口5Kよりも落差hだけ低くなる位置に給水口6Kを開設し、上記送水口5Sと連結管50を介して連結すると共に、送水口5Sと略同高さに送水口6Sを開設してオゾンタンク4の底部と連結管60で連通し、後述する構成によって所定量の瓦片6aを収容している。
【0012】
一方、オゾンタンク4は、その上部に設けた送水口4Sの高さを前記瓦タンク6の給水口6Kよりも落差Hだけ低くなる部位に開設して排出管7を設けており、その端部を源水タンク2の還流口(給水口)2Kに連通させている。
またこのオゾンタンク4内には、低部から所定距離だけ離間させた給水口4Kの上部に、前記オゾン発生器3に連通する多数のノズル孔を有するガス管30をを臨設させて、オゾンタンク4内の底部からオゾンガスを小さな多数の気泡状態で供給するようにしている。
【0013】
そして、上記送水口4Sに連結する排出管7の送水端は、源水タンク2の給水口2Kに連結する高さを前記送水口4Sよりも落差H1だけ低くするように設置している。
尚、排出管7の管径は前記連結管50,60等の管径よりも大径にしてあり、上記落差h,H,H1によって奏される落差流下による自然濾過排出を円滑に行うようにしている。
1bは上記処理タンク1,源水タンク2及び関連機器等の周囲を覆うカバーであり、メンテナンス作業を容易に行うことができるように開閉可能に設置されている。1Cは浄水装置Aに設置される各種ポンプ並びにオゾン発生器3,エアーポンプ8等を手動操作及び自動制御可能にコントロールさせる制御盤である。
尚、図1に示すようにオゾン発生器3及びエアーポンプ8は制御盤1Cのボックス内空間を有効利用して収容設置することにより、機器の保護と装置のコンパクト化を合理的に図るようにしている。
【0014】
上記のように落差流下方式を以て連結される各タンクには以下に説明する付属装置及び機器を付設している。
即ち図4に示すように、源水タンク2は前記給水口2Kの上位に開設した給水口21に、適宜な源水所在地において源水が貯溜される源水槽22から、源水ポンプ23によって汲み上げられた源水を沈殿させる源水沈殿槽25の送水管26を連結している。
これにより、源水沈殿槽25の上層の源水を源水タンク2の収容量分だけ供給し、該源水タンク2内の源水を前述の処理タンク1で後述する処理方法によりバッチ的に浄化処理したのちに、源水タンク2内の処理水を排出ポンプ27によって排出管28を介し、機外に適宜設置される処理水貯溜槽29に排出するようにしている。
【0015】
また前述の木炭タンク5及び瓦タンク6には、下方から処理水を循環ポンプ5P,6Pによって吸い込み上方から繰り返し還元させると共に、エアーポンプ8と連結するエアー管80の多数のノズル孔を有するエアー送出部を下部に内装するバッキ処理用の補助タンク(バッキタンク)5T,6Tを併設し、上記木炭タンク5及び瓦タンク6内の底部部位からエアーを微細な気泡にして送り込むことによって、タンク内の木炭5a及び瓦片6a等の濾過体に住みつく微生物を活性化させると共に、有機物の分解を促進させることができるようにしている。
【0016】
また、この補助タンク5T,6Tには前記エアー管80を共用しオゾン発生3と切換可能に連結しており、切換弁(不図示)の操作によって補助タンク5T,6T内の処理水にオゾンを供給して殺菌等のオゾン処理を行うようにすることにより、ここで小容量のポンプ5P,6Pの送給によって時間をかけて緩やかにオゾン処理をしながら、各木炭タンク5及び瓦タンク6に循環を繰り返すようにしている。
これにより、該木炭タンク5及び瓦タンク6に直接的にオゾンを供給することによる弊害を防止しながら、別途併設した補助タンク5T,6T内でこの部における処理水の、バッキ処理と共にオゾン処理を簡単且つ良好に行うことができ、木炭タンク5及び瓦タンク6の処理負荷を軽減し装置の小型化を可能にすることができるようにしている。
【0017】
またこの実施形態においては、オゾンを補助タンク5T,6T並びにオゾンタンク4とで分担させてオゾン分散処理をさせるので、処理水に供給するオゾン濃度を100〜150PPM程度(在来の処理装置はオゾン濃度1000〜2000であり、オゾン処理後に排オゾン処理を必要としている。)と比較的低濃度にすると共に、大気を混入させてエアレーション効果を奏するようにさせることにより、有効な微生物を死滅させることなく活性にさせる状態で、水中の混入物の着色成分の分解及び雑菌の除去並びに鉄分を酸化させて、ヘドロの要因となる硫化鉄の発生を制御するようにしている。
上記の処理が行われた処理水は難性分解成分を、事前にオゾンで強制的に酸化分解して分解を高められた状態になって、木炭タンク5及び瓦タンク6に格別に供給され、ここで上記処理により吸着され易い状態に分解された有機物等の処理が良好に行われる。従って、農薬や洗剤等の化学的物質により汚染された源水をも良好に処理することができる等の利点を有する。
【0018】
尚、木炭タンク5はその内部に10〜20ミリ程度に単粒化された木炭5aが通水可能に積層収容されており、木炭5aの表面及び内部の気孔に前記オゾンタンク4により処理負荷を軽減された状態の、源水の含有物中特に有機物が良好に吸着される。
そしてこの処理過程において、該有機物を分解するミジンコ等の微生物を良好に発生定住させ好適に増殖させることができ、木炭5aによる源水の有機物の吸着分解並びに鉄分の吸着を促進した状態で、下方に位置する送水口5Sから次位の瓦タンク6に送水する。
【0019】
また図3(B)に示すように瓦タンク6内には、多数の通水孔15bを有するステンレス製円筒状の容器15を足15aを介して着脱可能に設置しており、該容器15の内部には、廃棄用の瓦或いは素焼状態で不用品とされる瓦を有効利用する上で、これを10〜20mm程度に砕いて単粒化させた状態で通水可能に積層収容している。
上記瓦片6aは固形化された多孔質土質であるところから微生物の好適な増床を提供し、この場で活性化する微生物によって処理水を良好に浄化し、前工程の木炭5aで未処理な成分を気孔に吸収させて除去しながら次位のオゾンタンク4に送給する等の特徴を有している。
【0020】
また、上述の廃棄用瓦はその処分に困窮している現状において、第2処理タンクとしての処理材(濾過体)として該瓦の有効処分の用途を開くと共に、廉価な浄化装置を提供することができる等の利点がある。
一方オゾンタンク4は、底部から供給される処理水に対しガス管30によって下方からオゾンを微細な気泡となして供給されるので、給水口4Kから送給される供給初期の処理水を優先的に脱色脱臭殺菌、酸化有機分解作用等のオゾン処理を行わせながら上方に至り、上記給水口4Kから送給される処理水を良好に処理すると共に、送水口4Sから残留オゾンの少ない状態となし循環されて次位に行われる処理タンク1の処理負荷を軽くし良好に行うようにしている。
【0021】
また、上記オゾンタンク4から送水される処理水は長い経路に設定された排出管7を経て源水タンク2に送給するとよく、この場合には源水タンク2に至る間に残留オゾンは具合よく低減されると共に、給水口2Kから源水タンク2内に循環貯溜される間においても残留オゾンは低減されるので、該源水タンク2から木炭タンク5へ送られる循環処理水の残留オゾンは皆無又は僅少となり、下手側の木炭タンク5等内に生息する微生物に悪影響を与えることが防止されるものである。
【0022】
叙上のように構成した浄化装置Aはあらかじめ設定された制御盤1Cの指令によって、源水タンク2内に貯溜された所定量の源水を給水ポンプ2Pで木炭タンク5に供給しながら、これより下手側となる瓦タンク6及びオゾンタンク4並びに水位が低下している上記源水タンク2に、既述の落差h,H,H1によって奏される落差流下方式によって各タンクの処理水を緩やかに流下送給し、源水タンク2から再び一つの給水ポンプ2Pによって送出され、循環処理を所定時間内に適数回繰り返したのち、設定処理済の浄水を源水タンク2内から排出ポンプ27によって機外に排出することによって一連の浄化処理を良好に完了することができる。
【0023】
そして、こののちは設定された指令によって源水槽22の源水を再び源水タンク2に供給し前述と同様に浄化処理を連続的に行う。
この様な浄化処理に当たり、最上手側の処理タンクに源水タンク2から源水を給水ポンプ2Pで供給し、これより下手側の各処理タンクに対してはポンプによる圧送を避け、既述のような落差流下方式による送水を行って自然排出を行わせて、緩やかに所定回数だけ循環させるようにしているので、各処理タンク1においてそれぞれの浄化処理が充分に行われた状態で一連の処理を簡単且つ良好に行うことができる。
【0024】
また上記浄水装置Aの運転中において、給水ポンプ2Pのトラブルにより給水が行われなくなったような場合に、木炭タンク5及び瓦タンク6並びにオゾンタンク4内に適正な水位を維持することができるので、これら各処理タンク1が空になることによる濾過体の乾燥によって、有効な微生物を死滅させたりガス分の発生を良好に防止することができる。
【0025】
尚、図示例による源水タンク2は源水収容量1500程度となし、これを3〜5時間内において10〜15回程度循環処理させたところ、化学的酸素要求量は源水370mg/に対し処理水は6.6mg/であり、ノルマルヘキサン抽出物質含有量は源水210mg/に対し0.6mg/程度で、また透視度は源水1度に対し30度以上と極めて好結果であると共に、処理水は一つの給水ポンプ2Pを用い落差流下方式となして次位の処理タンクに送給するようにしたので、浄化装置Aの構成を簡潔で廉価に、且つ小型化を図りながら制作することができると共に、ランニングコストを低減することができた。
【0026】
また源水タンク2と各処理タンク1とは機台1a上に既述の配置を以て設置構成することにより、源水タンク2を有した浄化装置Aをコンパクトに纏まりよく製作することができると共に、装置の運搬移動及び設置作業等を簡単且つ良好に行うことができる等の利点がある。
尚、本実施形態では処理水を循環させてバッチ的に処理をするものを示したが、各処理タンク等の処理能力を拡大させることにより、源水を循環させることなく上手側から連続的に処理させて排水するようにしてもよい。
【0027】
【発明の効果】
本発明は以上のように構成したことにより次のような効果を奏する。
請求項1の発明により、源水を一旦源水タンクに貯めた状態において給水ポンプによって第1処理タンクに送水し、第1処理タンクから下手側の各タンクに落差流下方式によって送水すると共に、第1処理タンク等に補助タンクを併設し各別にバッキ処理を行わせるようにしたので、各タンクにおいて緩やかに送水し微生物による処理並びにオゾンによる処理を充分に行わせることができ、ランニングコストの低い浄化処理を良好に行うと共に、簡潔な構成で廉価型の浄水装置を提供することができる。
【0028】
炭や瓦片等を収容する処理タンク毎に併設された補助タンクにオゾンを供給し、該補助タンク内で処理水を緩やかに時間をかけてオゾン処理を行い各処理タンクに循環還流させることにより、各処理タンクに直接的にオゾンを供給することによる弊害を防止しながら、処理水のバッキ処理と共にオゾン処理を簡単且つ良好に行い、処理タンクの処理負荷を軽減し装置の小型化を図ることができる。
【0029】
請求項の発明により、最上手側の処理タンクに源水タンクから源水を給水ポンプで供給し、これより下手側の各処理タンクに対してはポンプによる圧送を避けて落差流下方式による送水を行って循環させるようにしたので、各処理タンクにおける浄化処理を充分に行うことができ一連の処理を良好に行うと共に浄水装置の小型化を図ることができる。
【0030】
請求項の発明により、機台の一側に列設した各処理タンクとオゾンタンクの他側に源水タンクを一体的に併設することにより、源水タンクを有した浄化装置をコンパクトに纏まりよく製作すると共に、装置の運搬移動及び設置作業等を簡単且つ容易に行うことができる。
【0031】
請求項の発明により、処理水を、上手側の木炭等の高多孔質微生物増床材を収容させた処理タンクで処理したのちに、瓦片を収容させた下手側の処理タンクによって良好に浄水処理を行わせることができる。
また上記処理にあたり瓦を粉砕させて収容される瓦片は、微生物の好適な増床を提供し微生物を活性化させて処理水を良好に浄化すると共に、廃棄用瓦の有効処分の用途を開きながら廉価な浄化装置を提供することができる。
【図面の簡単な説明】
【図1】 本発明の浄水装置を一部破断をして示す正面図。
【図2】 図1の平面図。
【図3】 (A)は図1の側面図。(B)は瓦タンクの断面図。
【図4】 図1の構成及び源水の処理形態を示す回路図。
【符号の説明】
1 処理タンク
1a 機台
1C 制御盤
2 源水タンク
2P 給水ポンプ
3 オゾン発生器
4 第3タンク(オゾンタンク)
5 第1タンク(木炭タンク)
5a 木炭
6 第2タンク(瓦タンク)
6a 瓦片
5T,6T 補助タンク
7 排出管
8 エアーポンプ
27 排出ポンプ
50,60 連結管
A 浄水装置
h,H,H1 落差
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a water purifier that includes a plurality of treatment tanks having different treatment tanks, and purifies treated water from a lower-side treatment tank through a source water tank installed on the upper side by a falling flow method.
[0002]
[Prior art]
Conventionally, water purifiers that purify source water from lakes, ponds, rivers, etc. or wastewater that has been washed, and source water discharged from facilities such as gas stations, contain charcoal, zeolite lights, etc. There is known a water purifier in which a plurality of processing tanks are connected to each other, source water is pumped and supplied from a processing tank on the upper side by a water supply pump, and purified water is forcibly discharged from the final processing tank.
In recent years, a water purifier that supplies ozone to such a water purifier and performs ozone treatment such as sterilization is also known.
[0003]
[Problems to be solved by the invention]
However, the water purifier according to the above-described conventional configuration, when treating source water contaminated with a large amount of various organic substances, detergents, oils and other various components and colored substances, charcoal or zeolite in the upper treatment tank, etc. A large amount of organic matter, coloring matter, or various bacteria adheres to the filter body, and the source water is forcibly pumped through the filter body. There are drawbacks.
In addition, since the treatment in each treatment tank is discharged without being sufficiently performed, it is necessary to frequently replace the filter body, or a large amount of filter body must be accommodated in each treatment tank. There are problems such as an increase in the size of the apparatus and an increase in running cost.
[0004]
[Means for Solving the Problems]
A water purifier according to the present invention for solving the above-mentioned conventional problems is a plurality of first treatment tanks 5 and second treatment tanks 6 that perform a purification treatment action by microorganisms from the first supply side of source water. In the water purifier A that purifies the source water by connecting the treatment tank 1 and the ozone tank 4 that performs ozone treatment by supplying ozone to the lower side of the treatment tank 1, the source water is placed on the upper side of the treatment tank 1. A source water tank 2 is provided for storing water, and water is supplied from the source water tank 2 to the first tank 5 by the water absorption pump 2P, and the lower processing tank is connected to the first processing tank 5 so as to be drainable by a falling flow method. and the processing tank 1 of the like first processing tank 5 and the second treatment tank 6, by selectably supplying air and ozone, aeration process while circulating the treated water in the treatment tank Auxiliary tank 5T performing ozone treatment, a 6T are characterized by being parallel in each separate.
[0005]
Second , it is characterized in that the treated water drained from the ozone tank 4 installed on the lower side of the treatment tank 1 is returned to the source water tank 2 and repeatedly purified to be purified.
[0006]
Third , the treatment tanks 1 and the ozone tank 4 are arranged on one side and the source water tank 2 and the like are provided on the other side, and these are integrally configured on one machine base. .
[0007]
Fourth , a highly porous microbial flooring material such as charcoal 5a or zeolite is accommodated in the upper processing tank 1, and a tile piece 6a obtained by pulverizing tiles is accommodated in the lower processing tank 1 to purify the water. It features processing.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
An embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows the internal structure of the water purification apparatus A according to the present invention with the cover removed. As shown in FIGS. 1 to 3, the water purification apparatus A can accommodate source water on a machine base 1a having a plan view. An upper water source tank (storage tank) 2 is installed on the uppermost side in the processing direction, and the upper side of the plurality of cylindrical container-like processing tanks 1 (5, 6, 4) fixed upright after this. A charcoal tank (first treatment tank) 5 is provided for containing charcoal 5a pulverized to an appropriate size (approximately 10 to 50 mm).
[0009]
Further, the tile on the lower side contains the tile pieces 6a pulverized to an appropriate size (approximately 10 to 20 mm) within a range in which the amount of treated water and the performance of the treatment are ensured and clogging does not occur. It is configured as a single tank (second processing tank) 6, and there is an ozone tank (third processing tank) 4 that supplies ozone generated from the ozone generator 3 to the lower side by mixing it with air in an appropriate amount. Adjacent tanks are connected in series via the connecting pipes 50 and 60, and source water supplied from the source water tank 2 by the feed water pump 2P is sent to the treatment tank 1 arranged above via the connecting pipe 20. The treated water discharged from the lower side of the treatment tank 1 is returned (returned) into the source water tank 2 through the discharge pipe 7.
[0010]
In addition, a lid 12 having a vent 11 is detachably attached to the supply port 10 that opens at the top of each processing tank 1, and a mesh-like container 15 containing a charcoal 5 a and a filter piece such as a tile piece 6 a is provided. Replacement is possible by inserting / removing from the supply port 10.
In addition, a drain 13 with a valve is provided at the bottom of each processing tank 1 to discharge accumulated matter accumulated at the bottom together with water in the tank as needed, so that the inside of the tank can be cleaned in a timely manner.
The water purifier A can arrange the treatment tanks 1 on the front side of the machine base 1a so that the filter can be easily replaced and maintained, and the source water tank is located behind the tanks. By installing 2 in the width direction of the machine body, the machine body is made compact and the apparatus is downsized while securing a sufficient amount of source water.
[0011]
The charcoal tank 5 of the processing tank 1 is connected to the water supply end of the connecting pipe 20 on the upper one side thereof to open a water supply port 5K, and is formed between the bottom water supply port 5S as a charcoal 5a accommodating portion. ing.
Further, the tile tank 6 is provided with a water supply port 6K at a position lower than the water supply port 5K of the charcoal tank 5 by a drop h, and is connected to the water supply port 5S via a connecting pipe 50, and is substantially the same as the water supply port 5S. A water supply port 6S is opened at the same height and communicates with the bottom of the ozone tank 4 by a connecting pipe 60, and a predetermined amount of tile pieces 6a are accommodated by a configuration described later.
[0012]
On the other hand, the ozone tank 4 is provided with a discharge pipe 7 by opening the water supply port 4 </ b> S provided at the upper part thereof at a position lower than the water supply port 6 </ b> K of the tile tank 6 by a drop H. Is communicated with the reflux port (water supply port) 2K of the source water tank 2.
In the ozone tank 4, a gas pipe 30 having a number of nozzle holes communicating with the ozone generator 3 is provided on the upper portion of the water supply port 4 </ b> K spaced apart from the lower portion by a predetermined distance. The ozone gas is supplied in the state of a large number of small bubbles from the bottom of the inside 4.
[0013]
The water supply end of the discharge pipe 7 connected to the water supply port 4S is installed so that the height connected to the water supply port 2K of the source water tank 2 is lower than the water supply port 4S by a drop H1.
The diameter of the discharge pipe 7 is larger than the diameters of the connecting pipes 50, 60, etc., so that the natural filtration and discharge by the drop flow produced by the drops h, H, H1 can be performed smoothly. ing.
A cover 1b covers the periphery of the processing tank 1, the source water tank 2, related equipment, and the like, and is installed to be openable and closable so that maintenance work can be easily performed. 1C is a control panel for controlling various pumps installed in the water purifier A, the ozone generator 3, the air pump 8 and the like so that they can be manually operated and automatically controlled.
In addition, as shown in FIG. 1, the ozone generator 3 and the air pump 8 are accommodated and installed by effectively using the space in the box of the control panel 1C so that the equipment can be protected and the apparatus can be made compact. ing.
[0014]
As described above, each of the tanks connected by the drop flow method is provided with an attachment device and equipment described below.
That is, as shown in FIG. 4, the source water tank 2 is pumped by a source water pump 23 from a source water tank 22 in which source water is stored at an appropriate source water location to a water inlet 21 opened above the water inlet 2K. The water supply pipe 26 of the source water settling tank 25 for precipitating the generated source water is connected.
As a result, the source water in the upper layer of the source water settling tank 25 is supplied by the amount accommodated in the source water tank 2, and the source water in the source water tank 2 is batch-processed by the processing method described later in the processing tank 1 described above. After the purification treatment, the treated water in the source water tank 2 is discharged by a discharge pump 27 through a discharge pipe 28 to a treated water storage tank 29 that is appropriately installed outside the apparatus.
[0015]
Further, the charcoal tank 5 and the tile tank 6 suck in treated water from below by circulation pumps 5P and 6P and repeatedly reduce the treated water from above, and also have an air delivery having a plurality of nozzle holes of an air pipe 80 connected to the air pump 8. Auxiliary tanks (Tack tanks) 5T and 6T for the back treatment are installed in the lower part, and air is sent in the form of fine bubbles from the bottom parts of the charcoal tank 5 and the tile tank 6 so that the charcoal in the tank The microorganisms that live on the filter body such as 5a and the tiles 6a are activated, and the decomposition of the organic matter can be promoted.
[0016]
The auxiliary tanks 5T and 6T share the air pipe 80 and are connected to the ozone generator 3 so as to be switchable. By operating a switching valve (not shown), ozone is added to the treated water in the auxiliary tanks 5T and 6T. Are supplied to each of the charcoal tanks 5 and the tile tanks 6 while the ozone treatment is performed slowly over time by feeding the small-capacity pumps 5P and 6P. The circulation is repeated.
This prevents ozone from being directly supplied to the charcoal tank 5 and the tile tank 6 while performing ozone treatment along with the back-up treatment of the treated water in the auxiliary tanks 5T and 6T provided separately. This can be performed easily and satisfactorily, and the processing load on the charcoal tank 5 and the tile tank 6 can be reduced, and the apparatus can be downsized.
[0017]
In this embodiment, ozone is distributed by the auxiliary tanks 5T and 6T and the ozone tank 4 to perform ozone dispersion treatment, so that the ozone concentration supplied to the treated water is about 100 to 150 PPM (conventional treatment equipment uses ozone). The concentration is 1000 to 2000, and the exhaust ozone treatment is necessary after the ozone treatment.) The effective concentration of microorganisms is killed by mixing the air and producing an aeration effect. In an activated state, decomposition of colored components of contaminants in water, removal of germs and oxidation of iron are controlled to control the generation of iron sulfide that causes sludge.
The above process is performed treated water flame decomposition component, advance is forced to a state of increased oxidative degradation to biodegradation with ozone, it is particularly supplied to the charcoal tank 5 and tiles tank 6 Here, the treatment of the organic matter or the like decomposed to be easily adsorbed by the above treatment is performed well. Therefore, there is an advantage that the source water contaminated with chemical substances such as agricultural chemicals and detergents can be treated well.
[0018]
In addition, the charcoal tank 5 contains therein the charcoal 5a which is made into a single grain of about 10 to 20 mm so as to allow water to pass therethrough, and the ozone tank 4 imposes a treatment load on the surface of the charcoal 5a and the pores inside. Particularly, organic substances are favorably adsorbed among the contents of the source water in a reduced state.
And in this treatment process, microorganisms such as daphnia that decompose the organic matter can be well generated and settled, and can be suitably grown, and in the state of promoting the adsorption and decomposition of the organic matter of the source water by the charcoal 5a and the adsorption of iron, Water is supplied from the water supply port 5S located at the next to the next tile tank 6.
[0019]
Further, as shown in FIG. 3B, a stainless steel cylindrical container 15 having a large number of water passage holes 15b is detachably installed in the tile tank 6 through legs 15a. Inside the waste tile or the tile that is discarded in the unglazed state is effectively used, and is stacked and accommodated so that it can be passed through in a state of being crushed to about 10 to 20 mm into a single grain. .
Since the tile 6a is a solidified porous soil, it provides a suitable expansion of microorganisms, and the treated water is well purified by the microorganisms activated on the spot, and is not treated with the charcoal 5a in the previous step. It is characterized by being fed to the next ozone tank 4 while absorbing and removing various components in the pores.
[0020]
Moreover, in the present situation where the above-mentioned waste tiles are difficult to dispose of, the use of effective disposal of the tiles as a treatment material (filter body) as a second treatment tank is opened, and an inexpensive purification device is provided. There are advantages such as being able to.
On the other hand, since the ozone tank 4 is supplied with ozone as fine bubbles from below by the gas pipe 30 with respect to the treated water supplied from the bottom, the treated water at the initial stage of supply supplied from the water supply port 4K is given priority. In this state, the treated water supplied from the water supply port 4K is treated well and the residual ozone is low from the water supply port 4S while performing ozone treatment such as decolorization, deodorization sterilization, and oxidative organic decomposition. The processing load of the processing tank 1 that is circulated and performed next is lightened so as to be performed satisfactorily.
[0021]
The treated water sent from the ozone tank 4 may be sent to the source water tank 2 through the discharge pipe 7 set in a long path. In this case, the residual ozone is in a certain condition while reaching the source water tank 2. Since the residual ozone is also reduced while being circulated and stored in the source water tank 2 from the water supply port 2K, the residual ozone of the circulated treated water sent from the source water tank 2 to the charcoal tank 5 is reduced. There is no or very little, and it is possible to prevent adverse effects on microorganisms that live in the lower charcoal tank 5 or the like.
[0022]
The purifier A configured as described above is configured to supply a predetermined amount of source water stored in the source water tank 2 to the charcoal tank 5 by the water supply pump 2P in accordance with a preset command from the control panel 1C. The treated water in each tank is gently fed into the tile tank 6 and the ozone tank 4 on the lower side and the above-mentioned source water tank 2 where the water level is lowered by the above-described head-down method represented by the heads h, H, H1. Then, the water is sent again from the source water tank 2 by one water pump 2P, and the circulation process is repeated an appropriate number of times within a predetermined time. Then, the set purified water is discharged from the source water tank 2 to the discharge pump 27 A series of purification processes can be satisfactorily completed by discharging to outside the machine.
[0023]
Thereafter, the source water in the source water tank 22 is supplied again to the source water tank 2 according to the set command, and the purification process is continuously performed in the same manner as described above.
In such a purification process, the source water is supplied from the source water tank 2 to the uppermost processing tank by the feed water pump 2P, and pumping of each lower processing tank is avoided by the pump. Since the water is discharged by such a head-down method and is naturally discharged and is circulated gently a predetermined number of times, a series of treatments are performed in a state where each purification treatment is sufficiently performed in each treatment tank 1. Can be performed easily and satisfactorily.
[0024]
Further, when the water purification apparatus A is in operation, water supply can no longer be performed due to a trouble with the water supply pump 2P, so that an appropriate water level can be maintained in the charcoal tank 5, the tile tank 6, and the ozone tank 4. By drying the filter body due to the emptying of each of these treatment tanks 1, effective microorganisms can be killed or generation of gas components can be satisfactorily prevented.
[0025]
Note that source water tank 2 source water carrying capacity 1500 l about the pear according to the illustrated example where was which was 10 to 15 times the circulation processing within 3-5 hours, chemical oxygen demand source water 370 mg / l to treated water is 6.6 mg / l, n-hexane extract content of about 0.6 mg / l to the source water 210 mg / l, also the perspective of the relative once the source water 30 degrees or more exceedingly In addition to the good results, the treated water was supplied to the next treatment tank by using a single feed water pump 2P and was sent to the next treatment tank, so the configuration of the purification device A was simplified, inexpensive and downsized. As well as being able to produce while trying, we were able to reduce running costs.
[0026]
Moreover, the source water tank 2 and each processing tank 1 can be manufactured in a compact and well-structured purification apparatus A having the source water tank 2 by configuring the above-described arrangement on the machine base 1a. There is an advantage that the apparatus can be transported, installed, and the like easily and satisfactorily.
In this embodiment, the treatment water is circulated and treated in batches. However, by expanding the treatment capacity of each treatment tank and the like, it is continuously possible from the upper side without circulating the source water. You may make it process and drain.
[0027]
【The invention's effect】
The present invention configured as described above has the following effects.
According to the first aspect of the present invention, the source water is once stored in the source water tank, and is fed to the first treatment tank by the feed pump, and is fed from the first treatment tank to each of the lower tanks by the drop flow method. Since an auxiliary tank is attached to each treatment tank, etc., and a separate back-up treatment is performed, water can be fed slowly in each tank to allow sufficient treatment with microorganisms and treatment with ozone, and purification with low running costs It is possible to provide a low-priced water purifier with a simple configuration while performing the treatment satisfactorily.
[0028]
Ozone is supplied to the auxiliary tank provided together for each processing tank containing the charcoal and tile pieces like, circulating reflux to each processing tank conducted ozone treatment over slowly time treated water in the auxiliary tank Thus, while preventing the harmful effects of supplying ozone directly to each treatment tank, the ozone treatment is performed easily and well together with the back water treatment of the treatment water, reducing the treatment load on the treatment tank and reducing the size of the apparatus. be able to.
[0029]
According to the second aspect of the present invention, the source water is supplied from the source water tank to the uppermost processing tank by the feed water pump, and the pumping of the lower processing tanks to the lower processing tank is avoided and the water is supplied by the head-down method. Therefore, the purification treatment in each treatment tank can be sufficiently performed, and a series of treatments can be performed satisfactorily and the water purification apparatus can be downsized.
[0030]
According to the invention of claim 3 , the purification tank having the source water tank is compactly gathered by integrally providing the source water tank on the other side of each ozone treatment tank and the treatment tank arranged in one side of the machine base. It can be manufactured well, and the apparatus can be transported and installed easily and easily.
[0031]
According to the invention of claim 4 , after treating the treated water in the treatment tank containing the highly porous microbial flooring material such as the charcoal on the upper side, the treated water is favorably improved by the lower treatment tank containing the tile fragments. Water purification treatment can be performed.
In addition, the tile pieces that are housed by crushing the tiles for the above treatment provide a suitable expansion floor for microorganisms, activate the microorganisms, purify the treated water well, and open up the use of effective disposal of waste tiles. However, an inexpensive purification device can be provided.
[Brief description of the drawings]
FIG. 1 is a front view of a water purification device according to the present invention, partially broken away.
FIG. 2 is a plan view of FIG.
FIG. 3A is a side view of FIG. (B) is sectional drawing of a tile tank.
FIG. 4 is a circuit diagram showing the configuration of FIG. 1 and the form of treatment of source water.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Processing tank 1a Machine stand 1C Control panel 2 Source water tank 2P Water supply pump 3 Ozone generator 4 3rd tank (ozone tank)
5 First tank (charcoal tank)
5a Charcoal 6 Second tank (tile tank)
6a tile 5T, 6T auxiliary tank 7 discharge pipe 8 air pump 27 discharge pump 50, 60 connecting pipe A water purifier h, H, H1 head

Claims (4)

源水の供給上手側から微生物による浄化処理作用を行う第1処理タンク(5)及び第2処理タンク(6)等からなる複数の処理タンク(1)と、該処理タンク(1)の下手側にオゾンが供給されてオゾン処理を行うオゾンタンク(4)を連結して源水の浄化を行う浄水装置(A)において、前記処理タンク(1)の上手側に源水を貯溜させる源水タンク(2)を設け、該源水タンク(2)から吸水ポンプ(2P)によって第1タンク(5)に送水すると共に、第1処理タンク(5)から下手側の処理タンクを落差流下方式によって排水可能に連結し、且つ上記第1処理タンク(5)及び第2処理タンク(6)等の処理タンク(1)に、エアーとオゾンを選択可能に供給することにより、該処理タンク内の処理水を循環させながらバッキ処理とオゾン処理を行う補助タンク(5T),(6T)を各別に併設してなる浄水装置。A plurality of treatment tanks (1) composed of a first treatment tank (5), a second treatment tank (6) and the like that perform a purification treatment action by microorganisms from the upper side of the source water supply, and the lower side of the treatment tank (1) In a water purifier (A) that purifies source water by connecting an ozone tank (4) that is supplied with ozone to perform ozone treatment, a source water tank that stores the source water on the upper side of the treatment tank (1) (2) is provided, and water is fed from the source water tank (2) to the first tank (5) by the water absorption pump (2P), and the lower processing tank is drained from the first processing tank (5) by the head-down method. The processing water in the processing tank is connected to the processing tank (1), such as the first processing tank (5) and the second processing tank (6), so that air and ozone can be selected. and aeration process while circulating Auxiliary tank performing Dzong process (5T), water purification device comprising features to each other (6T). 処理タンク(1)の下手側に設置したオゾンタンク(4)から排水される処理水を源水タンク(2)に返流させて循環を繰り返して浄化処理させる請求項1の浄水装置。The water purifier according to claim 1, wherein the treated water drained from the ozone tank (4) installed on the lower side of the treatment tank (1) is returned to the source water tank (2) and repeatedly circulated for purification treatment. 各処理タンク(1)及びオゾンタンク(4)を一側に列設すると共に他側に源水タンク(2)等を併設し、これらを一つの機台上に一体的に構成する請求項1又は2の浄水装置。The processing tanks (1) and the ozone tanks (4) are arranged on one side and a source water tank (2) is provided on the other side, and these are integrally configured on one machine base. Or 2 water purifier. 上手側の処理タンク(1)内に木炭(5a)又はゼオライト等の高多孔質微生物増床材を収容させると共に、下手側の処理タンク(1)内に瓦を粉砕した瓦片(6a)を収容させて浄水処理を行わせる請求項1又は2又は3の浄水装置。A tile piece (6a) in which a highly porous microbial flooring material such as charcoal (5a) or zeolite is accommodated in the upper processing tank (1) and the tiles are crushed in the lower processing tank (1). The water purifier according to claim 1, 2 or 3, wherein the water purifying treatment is carried out.
JP12919096A 1996-04-25 1996-04-25 Water purifier Expired - Lifetime JP3670391B2 (en)

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JP3670391B2 true JP3670391B2 (en) 2005-07-13

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