JP3901441B2 - Septic tank operation - Google Patents
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Description
【0001】
【発明の属する技術分野】
本発明は、被処理水の原水を嫌気処理する嫌気処理槽を設けるとともに、微生物を担持させた状態で、被処理水とともに流動可能に形成してある担体を収容保持するとともに、気泡供給して前記担体を被処理水とともに流動させる散気部を設けてある前記担体流動槽とを設け、前記担体流動槽の下流側に前記担体流動槽内の被処理水を濾過する濾過槽とを設け、前記濾過槽からの汚泥及び被処理水を前記嫌気処理槽に移送可能にするエアリフトポンプを設けてある浄化槽の運転方法に関する。
【0002】
【従来の技術】
従来エアリフトポンプを備えた浄化槽において、前記エアリフトポンプが、前記担体流動槽から、浄化槽底部を経由して下流側に移流させられる被処理水を吸引可能に立設される縦管と、前記嫌気処理槽上側から前記担体流動槽上側にわたって横架姿勢で保持されるとともに前記縦管の上部に接続される横管と、前記縦管の下部に給気して被処理水を移流可能にする給気管とを備えて構成してあった。そして、この給気管には、ブロワ等からの給気によりエアを定常的に供給し、前記縦管内の被処理水を揚水し、被処理水及び汚泥を定常的に移送可能とする構成を採用したものが知られている。
そして、このような構成により、被処理水が前記担体流動槽により高度に好気処理され、酸性度が増しやすい傾向になるものの、再度嫌気処理することにより脱窒して酸性度が増しにくいようにコントロール可能に浄化槽を運転することができる。
【0003】
【発明が解決しようとする課題】
しかし、上述の構成の浄化槽においては、濾過槽を設け、汚泥を濾過した状態の被処理水を嫌気処理槽に移送することが出来る構成になっているために、通常時は主に被処理水の移送によって、被処理水の脱窒を進行させる機能が発揮させられると期待される。一方、前記濾過槽が目詰まりし始めると、前記濾過槽が正常に機能しなくなる虞があるために、これを防ぐ目的で前記濾過槽を再生処理するような場合がある。このような再生処理中には、大量の汚泥が発生するために、逆に、浄化槽から放流される処理水の水質に悪影響を与える虞が生じる。
【0004】
このような場合に、上述の従来の散気管によりこのような汚泥も含めて常時移送することが可能になるように運転しようとすると、比較的大量の被処理水を常時嫌気処理槽に移送する必要があるため、常に大容量で給気する必要があり、運転コストが高くなったり、常時好気的に処理された後の被処理水が嫌気濾床槽に流入する環境を形成することになるため、上流側の嫌気処理槽が定常的に好気性に偏った状態になって、微生物の育成環境が変化してしまう虞もあった。
【0005】
そこで、本発明の目的は、被処理水の循環を、浄化槽内の環境を好適な条件に維持した状態で持続させやすい浄化槽の運転方法を提供することにある。
【0006】
【課題を解決するための手段】
上記目的を達成するための本発明の浄化槽の運転方法の特徴構成は、被処理水の原水を嫌気処理する嫌気処理槽を設けるとともに、微生物を担持させた状態で、被処理水とともに流動可能に形成してある担体を収容保持するとともに、気泡供給して前記担体を被処理水とともに流動させる散気部を設けてある前記担体流動槽と、前記担体流動槽の下流側に前記担体流動槽内の被処理水を濾過する濾過槽とを設け、前記濾過槽からの汚泥及び被処理水を前記嫌気処理槽に移送可能にするエアリフトポンプを設けてある浄化槽の運転方法であって、
前記濾過槽には、担体を所定高さまで充填してある堆積濾過層と、前記堆積濾過層の下部には前記担体に散気して前記濾過槽内を攪拌可能にする散気管を設けておくと共に、前記エアリフトポンプに、前記担体流動槽から、浄化槽底部を経由して下流側に移流させられる被処理水を吸引可能に立設される縦管と、前記嫌気処理槽上側から前記担体流動槽上側にわたって横架姿勢で保持されるとともに前記縦管の上部に接続される横管と、前記縦管の下部に給気して被処理水を移流可能にする第一給気管と、前記縦管の下部に給気して汚泥を移送可能にする第二給気管とを備えさせ、前記第一給気管は常時作動状態とし、前記濾過槽の散気管の作動時に前記第二給気管から給気するように構成してある点にある。
【0009】
〔作用効果〕
つまり、前記エアリフトポンプが、前記担体流動槽から、浄化槽底部を経由して下流側に移流させられる被処理水を吸引可能に立設される縦管と、前記嫌気処理槽上側から前記担体流動槽上側にわたって横架姿勢で保持されるとともに前記縦管の上部に接続される横管と、前記縦管の下部に給気して被処理水を移流可能にする第一給気管と、前記縦管の下部に給気して汚泥を移送可能にする第二給気管とを備えて構成してあると、前記エアリフトポンプによって主に被処理水の循環を行いたい場合には、前記第一給気管を稼働状態にし、主に汚泥の移送を行いたい場合には、前記第二給気管を稼働状態にすることにより、エアリフトポンプの機能を切り替えることが可能になる。そのため、前記浄化槽の運転状況に応じて適切な水処理を選択することが出来、水処理性能を高く維持できる。
尚、両方の給気管をともに稼働状態とする場合は、一般的に汚泥移送を行う場合は、被処理水を移送する目的の場合に比べて大量の給気を行うことから、汚泥を移送する目的を主に達成するものとなる。従って、特に、通常は汚泥を移送する機能を期待せず、少ない頻度で汚泥移送機能を発揮させるような運転を行うような場合には、第一給気管は常時作動状態とし、必要な場合にのみ前記第二給気管を作動状態にするような制御をおこなうことによっても、同様の効果が期待できる。
【0010】
また、大量の給気を伴う汚泥移送を機能させる場合には、前記縦管の内部に汚泥が付着していてもその汚泥をはぎ落として、洗浄する効果を発揮するので、前記縦管内壁面を常に清浄に維持して被処理水の循環水量を安定させ、好適な条件を維持した状態で持続させるのに寄与する。
【0011】
また、上述の構成において、前記濾過槽を前記担体流動槽に隣接して設けられる水処理槽内に、担体を所定高さまで充填してある堆積濾過層を形成して構成してある。
【0012】
前記堆積濾過層の下部には前記担体に散気して前記濾過槽内を攪拌可能にする散気管を設けてあると、この散気管による散気により前記濾過槽内に形成された堆積濾過層を、ほぐして攪拌し、担体に付着した固形成分は汚泥として剥離させることができる。
【0013】
このとき、前記汚泥は被処理水とともに前記濾過槽の下流側、処理水槽に移流することになり、前記エアリフトポンプが前記濾過槽から処理水槽に移流した汚泥を移送容易に配置してある状態では、そのエアリフトポンプによって処理水槽から、上流側の嫌気処理槽に汚泥が移送されることになる。ここで、浄化槽内に被処理水の原水が流入してこない状況を想定すると、浄化槽内での被処理水の流れは、嫌気処理槽から担体流動槽、濾過槽、処理水槽まで達し、前記嫌気処理槽に戻るという循環を繰り返すことになるから、前記濾過槽で発生した汚泥は、再び濾過槽にまで循環してくる途中で、嫌気処理槽を通過する際に、沈殿分離されて、前記エアリフトポンプによる汚泥移送を行っている間は、前記濾過槽で濾過される被処理水が清浄なものとなっている。また、このような状況で浄化槽に原水の流入があったとしても、前記汚泥移送にかかる被処理水移送量は、通常の原水流入量よりもきわめて多く設定することが出来、流入した原水は槽内の被処理水と十分混合され、生物処理されやすい状況が得られ、かつ、前記担体の再生も十分行えることになる。尚、これらをふまえると、前記汚泥移送は、被処理水の原水の流入の少ない時間帯に行われることが好ましいこともわかる。
さらに、前記再生処理の終わった担体は、例えば、水よりもその比重を大に形成してある場合、速やかに前記濾過槽内に堆積して堆積濾過層を形成するから、濾過機能の回復するまでに処理の不十分な被処理水が放流される虞も少ない。尚、前記担体の密度は、大きすぎると再生する際に散気によっても攪拌されにくくなり、小さすぎると堆積濾過層の形成までに時間を要するので、比重1.08〜1.2程度が好ましく、たとえば、比重1.2のものでは、80リットル/分程度の散気で攪拌されてほぐれ、散気終了後約25分程度で堆積濾過層が復旧される。
また、このようにして担体の再生処理を行った場合、比較的短時間でまとめて処理ができるので、前記嫌気処理槽に同時に移送される被処理水量も少なく抑制することが出来るので、上流側の嫌気処理槽の環境に悪影響が及ぶ虞を極力少なくできる点でもこのましい。
【0014】
また、前記濾過槽の散気管の散気状態に基づき前記エアリフトポンプの第2給気管によるエア供給を行うことにより、汚泥を浮遊させると同時に移送が行えるので、担体の再生処理が効率的に行われるために、たとえば、前記第一給気管への給気と第2給気管への給気とを切り替える切り替え装置と、前記散気管の散気と前記第二給気管への給気とを同期させる制御装置を設けるなどして、これらの協動をはかることが好ましい。
【0015】
【発明の実施の形態】
以下に本発明の実施の形態を図面に基づいて説明する。
本発明の浄化槽は、図1,2に示すように、上流側から嫌気処理槽N、好気処理槽E、処理水槽T1,T2等を備え、前記嫌気処理槽Nは、嫌気濾床槽第一室N1及び嫌気濾床槽第二室N2からなり、前記好気処理槽Eは、担体流動槽E1及び濾過槽E2からなる。被処理水の原水は、原水流入部Iから前記嫌気濾床槽第一室N1に流入するとともに、嫌気濾床槽第二室N2、担体流動槽E1、濾過槽E2、処理水槽T1の順に下流へ移送されつつ分解処理され、前記処理水槽T2の上方に設けた消毒槽Qを経た後、放流口Zから槽外に放流される。
【0016】
前記嫌気濾床槽第一室N1は、流入する被処理水の原水を貯留可能に構成してあり、その内部に嫌気性微生物を育成可能にしてある。前記嫌気濾床槽第一室N1に流入する被処理水の原水は、前記嫌気濾床槽第一室N1にて貯留されるとともに、嫌気分解され、主に、粗大な有機物の細分化が行われ、前記嫌気濾床槽第一室N1下部から前記嫌気濾床槽第二室N2の下部に移送される。また容易に分解されない汚泥等の固形分は前記嫌気濾床槽第一室N1下部に沈殿として、あるいは、嫌気濾床槽第一室N1上部にスカムとして貯留される。
前記嫌気濾床槽第二室N2は、嫌気濾床Fを備えるとともに、その嫌気濾床Fに嫌気性微生物を定着保持して育成させられる構成としてある。前記嫌気濾床槽第二室N2に流入した被処理水は、さらに嫌気処理を受け、固形物のほとんどない状態にまで分解された後、担体流動槽E1にオーバーフローで送られる。前記嫌気濾床槽Nと、前記担体流動槽E1との間はオーバーフロー部1によって被処理水を自然移流自在に構成されるとともに、そのオーバーフロー部1はスリット状部2を設けて、被処理水に移流可能に、かつ前記担体流動槽E1内の担体や汚泥が逆流するのを防止可能に構成してある。
【0017】
前記担体流動槽E1は、微生物を担持させた状態で、被処理水とともに流動可能に形成してある担体C1を収容保持するとともに、気泡供給により前記担体を流動させる散気管D1を設けて内装して散気部を設けてあり、前記散気管D1からの気泡供給により前記担体C1を前記担体流動槽E1内で流動させられる構成としてある。このような構成により、担体流動槽E1内に流入した被処理水は、好気性微生物による好気分解で浄化される。このような処理を受けた被処理水は、前記担体流動槽E1と、隣接する濾過槽E2とを仕切る第一隔壁W1に設けた移流壁部3を通じて、前記濾過槽E2に移流させられる。
前記移流壁部3は、格子状又はスリット状に形成してあり、前記担体C1の移流を阻止するが汚泥や被処理水の移流を許容する構成にしてある。
【0018】
前記濾過槽E2は、水よりも比重の大きな担体C2を所定高さまで充填して構成してある。また、前記濾過槽E2とその濾過槽E2に隣接して設けられる前記処理水槽T1とを隔てる第二隔壁W2の前記所定高さよりも低位置には、被処理水を流通自在にする濾過壁部4を形成してある。これにより、前記濾過槽E2に移流する汚泥を含んだ被処理水は、前記担体C2の堆積した堆積濾過層Bを通過して濾過され、固形分をほとんど含まない状態となって、隣接する処理水槽T1に移流される。尚、前記第二隔壁W2は、上端部において、浄化槽側壁に接続され、平面視で前記処理水槽T1は、前記濾過槽E2の下方に隠れるように配置されている。
前記濾過壁部4は格子状もしくはスリット状に形成してあり、前記担体C2の移流を阻止するが汚泥や被処理水の移流を許容する構成にしてある。
さらに、構成される前記堆積濾過層Bの下部には前記担体C2に散気して前記濾過槽E2内を攪拌する攪拌装置としての散気管D2を設けてあり、夜間等浄化槽内への負荷の流入が少ない時間帯に、前記散気管D2からの散気を行い、担体の再生を行える構成としてある。
また、前記散気管D2には、移流壁部3に向かって散気し、散気による気泡が、前記移流壁部3を通過し、前記担体流動槽E1側で前記移流壁部3に沿って上昇させられるように構成した移流壁散気部Da、及び、同様に濾過壁部に向かって散気し、散気による気泡が、前記濾過壁部4を通過し、前記処理水槽T1側で前記濾過壁部4に沿って上昇させられるように構成してある濾過壁部散気部Dbを設けて、それぞれ、移流壁部3、濾過壁部4を洗浄して目詰まり等を防止する構成としてある。
【0019】
ここで、前記移流壁部3および濾過壁部4は、被処理水を必ず前記堆積濾過層Bの所定距離を通過させた後に移流させるべく、前記堆積濾過層Bの堆積上端部高さとなる所定高さよりも低位置に設けてあり、被処理水の移流を許容し、前記堆積濾過層Bにおける被処理水の濾過を可能とする構成であればよい。
尚、前記担体C1,C2は、いずれも被処理水とともに流動可能な比重1以上1.2以下に形成してある。
これにより、前記散気管D1のメンテナンスを行う等、散気管を浄化槽外ヘ取り出す必要がある場合でも、前記散気管は前記散気管挿入孔14を介して容易に挿脱することが出来、前記流出防止部材等をほとんど分解することなく作業を行うことが出来る。
【0020】
さらに、前記処理水槽T1には前記嫌気濾床槽第一室N1に被処理水を移送するエアリフトポンプAを設けてあり、前記担体C2の再生により生じた汚泥を、前記濾過槽E2内から前記嫌気濾床槽第一室N1へ被処理水とともに移送可能に構成してある。
前記エアリフトポンプAは、前記処理水槽T1の底部に下端開口部を有するとともに前記担体流動槽側上部に延設される縦管A1と、前記縦管A1上部の接続部から前記嫌気濾床槽第一室N1の上方にわたって横架される横管A2とを設けるとともに、前記縦管A1の下端部近郷に前記縦管A1の下部に給気して被処理水を移流可能にする第一給気管A3と、前記縦管A1の下部に給気して汚泥を移送可能にする第二給気管A4とを連設し、各給気管A3,A4から前記縦管A1内部に給気可能に構成してある。前記第一給気管A3の接続部は、前記第2給気管A4の接続部に比べ、より深位置に設けてあり、かつ、ほぼ常時10リットル/分の給気により約2リットル/分の被処理水移送が行える構成としてある、また、前記第二給気管A4は、前記第一給気管A3の接続部のやや上部に接続されており、前記散気管D2の作動時にのみ、一日一回10分程度、80リットル/分の給気を行って約60リットル/分の被処理水を移送し、前記濾過槽T1からの被処理水や汚泥分のほぼ全量を前記嫌気濾床槽第一室N1に移送させる構成としてある。
【0021】
これにより、具体的には、通常運転状態では、浄化槽内に流入した被処理水は、前記嫌気濾床槽第一、第二室N1,N2と順に嫌気処理を受けつつ移流し、前記担体流動槽E1に達する。そして溶解性BODなどが好気処理され、BOD源となる成分が生物膜によって酸化分解されることになる。さらに、前記濾過槽E2にて堆積濾過層Bを構成する担体Cにより濾過され、浮遊物を含まない清浄な被処理水が、処理水槽T1に移流し、浄化槽の底部近傍をくぐり、処理水槽T2を上昇し、最終的に浮遊成分をほとんど含まずかつBODが20mg/リットル以下の処理水が得られる。この処理水は、前記処理水槽2の上部に設けられた消毒槽Qに流入し、固形消毒剤Q1と接触して消毒された後槽外へ放流される。
一方同時に、前記生物膜処理によると、被処理水の清浄が酸性に偏り気味になるものと予想されるため、前記エアリフトポンプAにより酸性に偏りつつある被処理水を前記嫌気濾床槽第一室N1から再循環させることによって、硝酸性窒素成分が脱窒されて、前記処理水の酸性度が低下することが期待される。そのため、前記処理水槽においては、固形成分特にスカム等の発生しにくい状況を維持でき高度な水処理が実現可能となる。
【0022】
また、前記散気管D2を作動させているときには、前記濾過槽E2はほとんど機能せず、担体流動槽E1内で発生して前記濾過槽E2内で補足された固形成分が前記濾過槽E2内の担体から剥離され前記濾過槽E2内を循環することになる。この固形成分は、次第に前記処理水槽T1,T2に流入することになるが、前記エアリフトポンプAにより、大量の被処理水を前記嫌気濾床槽第一室N1に移送すると、この被処理水の移送を行っている間は、被処理水がほぼ全量前記嫌気濾床槽第一室から濾過槽Bまでを循環し続けるだけの被処理水処理が進行することになる。
すると、処理水槽T1に流入した固形成分は、処理水槽T2側には侵入せず、嫌気濾床槽第一室N1に移送されることになり、順次下流側に移送されるにつれて沈殿貯留されることになり、結果として前記濾過槽E2が再生されるとともに、嫌気濾床槽Nによる汚泥の再処理、沈殿貯留が有効に図られることになる。
また、このように被処理水の大量移送を図るために前記縦管A1内に大量のエア供給を行うと、前記縦管A1内に付着した付着物等も剥離除去して移送することが可能となるので、前記エアリフトポンプAの詰まり防止にも寄与することになる。
【0023】
また、前記担体流動槽E1及び濾過槽E2の定常水位よりも上方側には浄化槽内に大量の被処理水が流入したとしても、槽内の担体C1,C2が他槽に流出しないように流出防止する流出防止部材10を、前記担体C1,C2よりも目の細かい網材11,11から構成してあり、複数に分割して前記マンホールHから取り出せる構成にしてある。また、前記流出防止部材10には、一部に開口12を設け、ダクト状の担体投入部13を延設してある。
これにより、前記担体流動槽E1及び濾過槽E2内に散気して被処理水の対流を形成したとしてもその流れは、前記流出防止部材10によって阻害されることなく円滑に流れるように形成される。また、前記担体流動槽E1及び濾過槽E2内に担体C1,C2を充填あるいは、担体C1,C2の交換を行うような場合には、前記担体投入部13を介して容易に投入、吸出しが可能となる。
【0024】
さらに、前記流出防止部材10には、前記散気管D1を挿脱自在にする散気管挿通孔14を設けてあり、前記散気管D1に連設されるエア供給管D1aには、前記散気管D1を前記担体流動槽E1内に位置固定した状態で、前記散気管挿通孔を蓋する蓋部材15を一体に連設して担体の流出を阻止する堰止機構を構成してある。尚、散気管D1や、エアリフトポンプAに対する給気配管等は、前記濾過槽の上方空間にまとめられ、前記担体流動槽E1の上部の配管を最小限に整理してある。
【0025】
これにより、前記担体流動槽E1および濾過槽E2は、上方側が解放状態に設けられ、かつ、上方空間から容易に担体交換、水質確認が出来る状態に配置されるため、メンテナンスの際には、前記浄化槽内を分解等することなく、前記蓋部材を給気管から脱離するだけで、前記挿通孔を開口させることが出来て、前記浄化槽に設けたマンホールHを介して上方側から容易に行える。また、この際、各種計測機器(pH計、BOD計等)を槽内に持ち込んで水質の検査等を行う場合にも、取り扱いに注意を要しにくく、作業性が向上する。
【0026】
尚、エアリフトポンプや、散気管へのエア供給はブロワから行われ、各管路へのエア供給切替は種々公知の切替制御装置を用いて、同期をはかるものとする。
【0027】
〔別実施形態〕
先の実施の形態では、前記移流壁部3及び濾過壁部4を前記第一、第二隔壁W1,W2に一体形成した構成を示したが、前記第一、第二隔壁W1,W2に対し着脱自在に構成してあっても良く、さらには、前記移流壁部3もしくは濾過壁部4を設けた前記第一、第二隔壁W1,W2を浄化槽に対して着脱自在に設けてあっても良い。また、図1においては各好気処理槽E1,E2を幅方向に並列に設けたが、長手方向に直列に設けるなど、平面視における配列は上述のものに限られるものではない。
【0028】
また、前記担体投入部13は、必須のものではないが、前記浄化槽の埋設状況に応じて前記マンホールHの近傍にまでダクト状に形成してあることが望ましい。
また、前記第一、第二給気管の前記縦管への接続部は必ずしも上下二段に設ける必要はなく、前記接続部で合流していても良く、また、上下位置が逆転していてもよい。
【図面の簡単な説明】
【図1】本発明の浄化槽の縦断側面図
【図2】本発明の浄化槽の要部斜視図
【図3】従来の浄化槽の要部斜視図
【符号の説明】
C1 担体
D1 散気部
E1 担体流動槽
10 流出防止部材[0001]
BACKGROUND OF THE INVENTION
The present invention provides an anaerobic treatment tank for anaerobically treating raw water to be treated, accommodates and holds a carrier that is formed to be flowable with the treated water in a state where microorganisms are supported, and supplies bubbles. A carrier flow tank provided with an air diffuser for flowing the carrier together with the water to be treated, and a filtration tank for filtering the water to be treated in the carrier fluid tank on the downstream side of the carrier fluid tank, the method of operation of the purification tank is provided with an air lift pump the sludge and treated water from the filtration tank to allow transfer to the anaerobic treatment tank.
[0002]
[Prior art]
In a conventional septic tank equipped with an air lift pump, the air lift pump is erected so as to be able to suck up water to be treated that is transferred from the carrier flow tank to the downstream side via the bottom of the septic tank, and the anaerobic treatment A horizontal pipe that is held in a horizontal posture from the upper side of the tank to the upper side of the carrier flow tank and connected to the upper part of the vertical pipe, and an air supply pipe that supplies the lower part of the vertical pipe to allow the water to be treated to be transferred And was configured. And this air supply pipe adopts a configuration that allows air to be constantly supplied by supplying air from a blower or the like, pumps the water to be treated in the vertical pipe, and allows the water to be treated and sludge to be steadily transferred. Is known.
And, with such a configuration, the water to be treated is highly aerobically treated by the carrier fluidized tank, and the acidity tends to increase, but it is difficult to increase the acidity by denitrifying by anaerobic treatment again. The septic tank can be operated in a controllable manner.
[0003]
[Problems to be solved by the invention]
However, in the septic tank having the above-described configuration, a filtration tank is provided so that the treated water in a state in which sludge is filtered can be transferred to the anaerobic treatment tank. It is expected that the function of advancing the denitrification of the water to be treated will be exhibited by the transfer of. On the other hand, if the filtration tank starts to be clogged, the filtration tank may not function normally. Therefore, the filtration tank may be regenerated for the purpose of preventing this. During such a regeneration process, a large amount of sludge is generated, which may adversely affect the quality of the treated water discharged from the septic tank.
[0004]
In such a case, if an attempt is made to operate such that the above-described conventional air diffuser can always transport such sludge, a relatively large amount of water to be treated is always transported to the anaerobic treatment tank. Because it is necessary, it is necessary to always supply air with a large capacity, which increases the operating cost or forms an environment in which treated water after being always aerobically treated flows into the anaerobic filter bed tank Therefore, the anaerobic treatment tank on the upstream side is steadily biased to aerobic condition, and there is a possibility that the growth environment of microorganisms may change.
[0005]
Then, the objective of this invention is providing the operating method of the septic tank which is easy to maintain the circulation of to-be-processed water in the state which maintained the environment in a septic tank on the suitable conditions.
[0006]
[Means for Solving the Problems]
The characteristic configuration of the operation method of the septic tank of the present invention for achieving the above object is to provide an anaerobic treatment tank for anaerobically treating the raw water to be treated, and to flow with the treated water in a state where microorganisms are supported. The carrier fluidized tank that contains and holds the formed carrier and is provided with an air diffuser for supplying bubbles to flow the carrier together with the water to be treated, and in the carrier fluidized tank on the downstream side of the carrier fluidized tank A filtration tank for filtering the water to be treated, and a method of operating a septic tank provided with an air lift pump that enables transfer of sludge and water to be treated from the filtration tank to the anaerobic treatment tank,
The filtration tank is provided with a deposition filtration layer filled with a carrier up to a predetermined height, and an air diffusion tube is provided below the deposition filtration layer to diffuse the carrier and allow the inside of the filtration tank to be stirred. In addition, a vertical pipe installed to be able to suck water to be treated from the carrier flow tank to the downstream side through the bottom of the purification tank to the air lift pump , and the carrier flow tank from the upper side of the anaerobic treatment tank A horizontal pipe that is held in a horizontal position over the upper side and connected to the upper part of the vertical pipe, a first air supply pipe that supplies air to the lower part of the vertical pipe to allow the water to be treated to flow, and the vertical pipe A second air supply pipe for supplying sludge to the lower part of the air supply , the first air supply pipe being always in an operating state, and supplying air from the second air supply pipe when the air diffuser pipe of the filtration tank is in operation It is in the point which is constituted so that .
[0009]
[Function and effect]
That is, the air lift pump has a vertical pipe installed so as to be able to suck water to be treated from the carrier flow tank to the downstream side through the bottom of the purification tank, and the carrier flow tank from above the anaerobic treatment tank. A horizontal pipe that is held in a horizontal position over the upper side and connected to the upper part of the vertical pipe, a first air supply pipe that supplies air to the lower part of the vertical pipe to allow the water to be treated to flow, and the vertical pipe A second air supply pipe for supplying sludge to the lower part of the air supply, and when the water to be treated is mainly circulated by the air lift pump, the first air supply pipe In the operation state, the sludge is mainly transferred, and the function of the air lift pump can be switched by setting the second air supply pipe to the operation state. Therefore, an appropriate water treatment can be selected according to the operation status of the septic tank, and the water treatment performance can be maintained high.
In addition, when both supply pipes are in an operating state, in general, when sludge is transferred, sludge is transferred because a large amount of air is supplied compared to the case of transferring the water to be treated. The objective is mainly achieved. Therefore, in particular, the first air supply pipe is always in an operating state, when the operation that allows the sludge transfer function to be performed with a low frequency is not expected, and the first air supply pipe is always in an operating state. The same effect can be expected by controlling the second air supply pipe to the operating state only.
[0010]
In addition, when sludge transfer with a large amount of air supply is made to function, even if sludge adheres to the inside of the vertical pipe, the sludge is removed and the effect of cleaning is exhibited. Always keep it clean to stabilize the amount of circulating water to be treated and contribute to maintaining it in a state of maintaining suitable conditions.
[0011]
In the configuration described above, the filtration tank the carrier fluidizing tank water treatment tank provided adjacent to, Ru Thea configured to form a deposited filtration layer are filled with a charge of material to a predetermined height.
[0012]
When a diffusion tube is provided below the deposition filtration layer to diffuse the carrier and allow the inside of the filtration tank to be stirred, the deposition filtration layer formed in the filtration tank by the diffusion of the diffusion tube The solid component adhering to the carrier can be peeled off as sludge.
[0013]
At this time, the sludge will be transferred to the treated water tank, downstream of the filtration tank, together with the water to be treated, and in the state where the air lift pump is easily arranged to transfer the sludge transferred from the filtration tank to the treated water tank. Then, sludge is transferred from the treated water tank to the anaerobic treatment tank on the upstream side by the air lift pump. Here, assuming that the raw water to be treated does not flow into the septic tank, the flow of the treated water in the septic tank reaches from the anaerobic treatment tank to the carrier flow tank, the filtration tank, and the treated water tank. Since the circulation of returning to the treatment tank is repeated, the sludge generated in the filtration tank is precipitated and separated when passing through the anaerobic treatment tank while circulating to the filtration tank again, and the air lift While the sludge is transferred by the pump, the water to be treated filtered in the filtration tank is clean. Further, even if raw water flows into the septic tank in such a situation, the amount of treated water transferred for the sludge transfer can be set to be much larger than the normal raw water inflow, It is sufficiently mixed with the water to be treated, and it is easy to be biologically treated, and the carrier can be sufficiently regenerated. In view of these, it is understood that the sludge transfer is preferably performed in a time zone in which the raw water to be treated is little inflow.
Furthermore, when the carrier having undergone the regeneration treatment has a specific gravity greater than that of water, for example, it quickly accumulates in the filtration tank to form a deposited filtration layer, so that the filtration function is restored. There is little possibility that the water to be treated that is insufficiently treated will be discharged. If the density of the carrier is too large, it is difficult to stir even by aeration during regeneration, and if it is too small, it takes time to form the deposited filtration layer. Therefore, a specific gravity of about 1.08 to 1.2 is preferable. For example, in the case of a specific gravity of 1.2, it is stirred and loosened with an air diffuse of about 80 liters / minute, and the deposited filtration layer is restored about 25 minutes after the end of the air diffuse.
Further, when the carrier regeneration process is performed in this way, the process can be performed collectively in a relatively short time, so that the amount of water to be treated that is simultaneously transferred to the anaerobic treatment tank can be suppressed, so that the upstream side This is also preferable in that the possibility of adversely affecting the environment of the anaerobic treatment tank is minimized.
[0014]
Further, by supplying air through the second air supply pipe of the air lift pump based on the air diffusion state of the filter tank, sludge can be suspended and transferred at the same time, so that the carrier regeneration process can be performed efficiently. For example, the switching device that switches between the supply of air to the first supply pipe and the supply of air to the second supply pipe, and the diffusion of the diffusion pipe and the supply of air to the second supply pipe are synchronized. It is preferable to achieve these cooperations by providing a control device.
[0015]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below with reference to the drawings.
As shown in FIGS. 1 and 2, the septic tank of the present invention comprises an anaerobic treatment tank N, an aerobic treatment tank E, treated water tanks T1, T2, and the like from the upstream side. It consists of one chamber N1 and an anaerobic filter bed tank second chamber N2, and the aerobic treatment tank E consists of a carrier flow tank E1 and a filtration tank E2. The raw water to be treated flows into the first anaerobic filter bed tank N1 from the raw water inflow section I, and downstream in the order of the anaerobic filter bed tank second chamber N2, the carrier flow tank E1, the filter tank E2, and the treated water tank T1. It is decomposed while being transferred to the tank, and after passing through the disinfection tank Q provided above the treated water tank T2, it is discharged from the outlet Z to the outside of the tank.
[0016]
The anaerobic filter bed first chamber N1 is configured to be capable of storing raw water to be treated, and is capable of growing anaerobic microorganisms therein. The raw water to be treated flowing into the first anaerobic filter bed first chamber N1 is stored in the first anaerobic filter bed first chamber N1 and is anaerobically decomposed, mainly to divide coarse organic matter. And transferred from the lower part of the first anaerobic filter bed tank N1 to the lower part of the second chamber N2 of the anaerobic filter bed tank. Solids such as sludge that are not easily decomposed are stored as precipitates in the lower part of the anaerobic filter bed first chamber N1 or as scum in the upper part of the anaerobic filter bed first chamber N1.
The anaerobic filter bed second chamber N2 is provided with an anaerobic filter bed F, and anaerobic microorganisms are fixed and grown on the anaerobic filter bed F. The water to be treated which has flowed into the second chamber N2 of the anaerobic filter bed is further subjected to anaerobic treatment, decomposed to a state having almost no solid matter, and then sent to the carrier flow tank E1 by overflow. Between the anaerobic filter bed tank N and the carrier fluidized tank E1, the overflow portion 1 is configured to allow free movement of the treated water, and the overflow portion 1 is provided with a slit-like portion 2 to provide the treated water. The carrier and sludge in the carrier fluid tank E1 can be prevented from flowing back.
[0017]
The carrier fluid tank E1 accommodates and holds a carrier C1 that is formed so as to be able to flow together with the water to be treated in a state where microorganisms are supported, and is provided with an air diffuser D1 that allows the carrier to flow by supplying bubbles. An air diffuser is provided to allow the carrier C1 to flow in the carrier flow tank E1 by supplying bubbles from the air diffuser D1. With such a configuration, the water to be treated flowing into the carrier fluid tank E1 is purified by aerobic decomposition by aerobic microorganisms. The treated water that has undergone such treatment is transferred to the filtration tank E2 through the transfer wall portion 3 provided in the first partition wall W1 that partitions the carrier flow tank E1 and the adjacent filtration tank E2.
The advection wall portion 3 is formed in a lattice shape or a slit shape, and is configured to prevent the advection of the carrier C1, but to permit the advection of sludge and water to be treated.
[0018]
The filtration tank E2 is configured by filling a carrier C2 having a specific gravity greater than that of water up to a predetermined height. Moreover, the filtration wall part which distribute | circulates to-be-processed water freely in the position lower than the said predetermined height of the 2nd partition W2 which separates the said filtration tank E2 and the said treated water tank T1 provided adjacent to the said filtration tank E2. 4 is formed. As a result, the water to be treated containing sludge that is transferred to the filtration tank E2 is filtered through the deposited filtration layer B on which the carrier C2 is deposited, so that the solid water is hardly contained, and the adjacent treatment is performed. It is transferred to the water tank T1. The second partition wall W2 is connected to the septic tank side wall at the upper end, and the treated water tank T1 is arranged to be hidden under the filtration tank E2 in a plan view.
The filtration wall portion 4 is formed in a lattice shape or a slit shape, and prevents the advancing of the carrier C2, but allows the advancing of sludge and water to be treated.
Furthermore, an aeration pipe D2 as a stirring device for agitating the inside of the filtration tank E2 by agitating the carrier C2 is provided below the constructed filtration layer B, and the load on the septic tank such as at night is reduced. In the time zone when there is little inflow, the carrier is regenerated by performing aeration from the diffusion tube D2.
In addition, air diffuses toward the advection wall portion 3 in the aeration tube D2, and bubbles due to the aeration pass through the advection wall portion 3, and along the advection wall portion 3 on the carrier flow tank E1 side. The advection wall diffuser Da configured to be raised, and similarly diffused toward the filtration wall, and air bubbles due to the aeration pass through the filtration wall 4 and the treatment water tank T1 side As the structure which provides the filtration wall part aeration part Db comprised so that it can be raised along the filtration wall part 4, and wash | cleans the advection wall part 3 and the filtration wall part 4, respectively, and prevents clogging etc. is there.
[0019]
Here, the advection wall part 3 and the filtration wall part 4 have a predetermined upper end height of the deposition filtration layer B so that the water to be treated must be allowed to flow after passing a predetermined distance of the deposition filtration layer B. What is necessary is just the structure which is provided in the position lower than height, accept | permits the advection of to-be-processed water, and enables filtration of the to-be-processed water in the said deposition filtration layer B. FIG.
Each of the carriers C1 and C2 is formed to have a specific gravity of 1 or more and 1.2 or less that can flow together with the water to be treated.
Thereby, even when it is necessary to take the diffuser tube out of the septic tank, for example, when the diffuser tube D1 is maintained, the diffuser tube can be easily inserted and removed through the diffuser
[0020]
Further, the treated water tank T1 is provided with an air lift pump A for transferring the treated water to the anaerobic filter bed first chamber N1, and the sludge generated by the regeneration of the carrier C2 is collected from the filtration tank E2 into the treated water tank T1. It can be transferred to the first chamber N1 of the anaerobic filter bed tank together with the water to be treated.
The air lift pump A has a lower end opening at the bottom of the treated water tank T1 and a vertical pipe A1 extended to the upper part on the carrier flow tank side, and a connection part of the upper part of the vertical pipe A1 to the anaerobic filter bed tank first. A first air supply pipe that is provided with a horizontal pipe A2 that extends horizontally over the upper part of the chamber N1 and that supplies water to the lower part of the vertical pipe A1 to the lower part of the vertical pipe A1 so that the water to be treated can be transferred A3 and a second air supply pipe A4 that supplies air to the lower part of the vertical pipe A1 and allows sludge to be transferred are connected in series, and each air supply pipe A3, A4 can supply air into the vertical pipe A1. It is. The connection portion of the first air supply pipe A3 is provided at a deeper position than the connection portion of the second air supply pipe A4, and the cover is approximately 2 liters / minute by supplying air of 10 liters / minute almost always. The second supply pipe A4 is connected to a slightly upper part of the connection part of the first supply pipe A3, and is once a day only when the diffuser pipe D2 is operated. About 10 minutes, 80 liters / minute of air is supplied, and about 60 liters / minute of treated water is transferred, and almost all of the treated water and sludge from the filtration tank T1 is transferred to the anaerobic filter bed tank 1 It is configured to be transferred to the chamber N1.
[0021]
Thus, specifically, in a normal operation state, the water to be treated that has flowed into the septic tank is transferred to the anaerobic filter bed tank first and second chambers N1 and N2 while being subjected to anaerobic treatment in this order. Reach tank E1. And soluble BOD etc. are aerobically processed and the component used as a BOD source is oxidatively decomposed | disassembled by a biofilm. Further, the clean water to be treated which is filtered by the carrier C constituting the sedimentation filtration layer B in the filtration tank E2 and does not contain suspended matters is transferred to the treatment water tank T1, passes through the vicinity of the bottom of the purification tank, and the treatment water tank T2. And finally, treated water containing almost no suspended components and BOD of 20 mg / liter or less is obtained. This treated water flows into the disinfecting tank Q provided in the upper part of the treated water tank 2, and after being disinfected in contact with the solid disinfectant Q1, it is discharged outside the tank.
At the same time, according to the biofilm treatment, it is expected that the purification of the water to be treated is likely to be biased toward acidity. Therefore, the water to be treated that is being biased toward acidity by the air lift pump A is removed from the first anaerobic filter bed tank 1. By recirculating from the chamber N1, it is expected that the nitrate nitrogen component is denitrified and the acidity of the treated water is lowered. Therefore, in the treated water tank, it is possible to maintain a state in which solid components, particularly scum, are hardly generated, and it is possible to realize advanced water treatment.
[0022]
Further, when the air diffuser D2 is operated, the filtration tank E2 hardly functions, and solid components generated in the carrier flow tank E1 and captured in the filtration tank E2 are contained in the filtration tank E2. It peels from the carrier and circulates in the filtration tank E2. This solid component gradually flows into the treated water tanks T1 and T2. When a large amount of treated water is transferred to the first anaerobic filter bed tank N1 by the air lift pump A, the treated water While the transfer is being performed, the treatment water treatment proceeds so that almost all of the treatment water continues to circulate from the first chamber of the anaerobic filter bed tank to the filtration tank B.
Then, the solid component that has flowed into the treated water tank T1 does not enter the treated water tank T2 side, but is transferred to the anaerobic filter bed tank first chamber N1, and is precipitated and stored as it is sequentially transferred to the downstream side. As a result, the filtration tank E2 is regenerated, and sludge reprocessing and sediment storage by the anaerobic filter bed tank N are effectively achieved.
In addition, when a large amount of air is supplied into the vertical pipe A1 in order to transfer a large amount of water to be treated in this way, it is possible to peel off and remove deposits and the like adhering to the vertical pipe A1. Therefore, this contributes to prevention of clogging of the air lift pump A.
[0023]
Further, even if a large amount of water to be treated flows into the septic tank above the steady water level of the carrier flow tank E1 and the filtration tank E2, the carriers C1 and C2 in the tank flow out so as not to flow into other tanks. The
Thereby, even if it diffuses in the said carrier flow tank E1 and the filtration tank E2 and forms the convection of to-be-processed water, the flow is formed so that it may flow smoothly, without being inhibited by the said
[0024]
Further, the
[0025]
As a result, the carrier fluid tank E1 and the filtration tank E2 are arranged in a state in which the upper side is provided in an open state and the carrier can be easily replaced and the water quality can be confirmed from the upper space. By simply removing the lid member from the air supply pipe without disassembling the inside of the septic tank, the insertion hole can be opened and can be easily performed from above via the manhole H provided in the septic tank. At this time, even when various measuring devices (pH meter, BOD meter, etc.) are brought into the tank for water quality inspection and the like, it is difficult to pay attention to handling and workability is improved.
[0026]
Air supply to the air lift pump and the diffuser pipe is performed from the blower, and air supply switching to each pipe line is synchronized using various known switching control devices.
[0027]
[Another embodiment]
In the previous embodiment, the structure in which the advection wall portion 3 and the filtration wall portion 4 are integrally formed with the first and second partition walls W1 and W2 is shown. The first and second partition walls W1 and W2 provided with the advection wall portion 3 or the filtration wall portion 4 may be detachably provided with respect to the septic tank. good. Moreover, although each aerobic processing tank E1, E2 was provided in parallel in the width direction in FIG. 1, the arrangement | sequence in planar view, such as providing in series in a longitudinal direction, is not restricted to the above-mentioned thing.
[0028]
Moreover, although the said carrier injection | throwing-in
Further, the connecting portion of the first and second air supply pipes to the vertical pipe is not necessarily provided in two upper and lower stages, and may be joined at the connecting section, or the vertical position may be reversed. Good.
[Brief description of the drawings]
FIG. 1 is a longitudinal side view of a septic tank according to the present invention. FIG. 2 is a perspective view of essential parts of the septic tank of the present invention. FIG. 3 is a perspective view of essential parts of a conventional septic tank.
C1 Carrier D1 Air diffuser E1
Claims (1)
前記濾過槽には、担体を所定高さまで充填してある堆積濾過層と、前記堆積濾過層の下部には前記担体に散気して前記濾過槽内を攪拌可能にする散気管を設けておくと共に、前記エアリフトポンプに、前記担体流動槽から、浄化槽底部を経由して下流側に移流させられる被処理水を吸引可能に立設される縦管と、前記嫌気処理槽上側から前記担体流動槽上側にわたって横架姿勢で保持されるとともに前記縦管の上部に接続される横管と、前記縦管の下部に給気して被処理水を移流可能にする第一給気管と、前記縦管の下部に給気して汚泥を移送可能にする第二給気管とを備えさせ、前記第一給気管は常時作動状態とし、前記濾過槽の散気管の作動時に前記第二給気管から給気する浄化槽の運転方法。An anaerobic treatment tank for anaerobically treating the raw water to be treated is provided, and a carrier that is formed so as to be able to flow with the treated water is accommodated in a state where microorganisms are supported, and bubbles are supplied to cover the carrier. Sludge from the filtration tank is provided with the carrier flow tank provided with a diffuser for flowing together with the treated water, and a filtration tank for filtering the treated water in the carrier flow tank on the downstream side of the carrier flow tank. And an operation method of a septic tank provided with an air lift pump that enables transfer of water to be treated to the anaerobic treatment tank,
The filtration tank is provided with a deposition filtration layer filled with a carrier up to a predetermined height, and an air diffusion tube is provided below the deposition filtration layer to diffuse the carrier and allow the inside of the filtration tank to be stirred. In addition, a vertical pipe installed to be able to suck water to be treated from the carrier flow tank to the downstream side through the bottom of the purification tank to the air lift pump , and the carrier flow tank from the upper side of the anaerobic treatment tank A horizontal pipe that is held in a horizontal position over the upper side and connected to the upper part of the vertical pipe, a first air supply pipe that supplies air to the lower part of the vertical pipe to allow the water to be treated to flow, and the vertical pipe A second air supply pipe for supplying sludge to the lower part of the air supply , the first air supply pipe being always in an operating state, and supplying air from the second air supply pipe when the air diffuser pipe of the filtration tank is in operation To operate the septic tank .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000294298A JP3901441B2 (en) | 2000-09-27 | 2000-09-27 | Septic tank operation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000294298A JP3901441B2 (en) | 2000-09-27 | 2000-09-27 | Septic tank operation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002102873A JP2002102873A (en) | 2002-04-09 |
| JP3901441B2 true JP3901441B2 (en) | 2007-04-04 |
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|---|---|---|---|
| JP2000294298A Expired - Fee Related JP3901441B2 (en) | 2000-09-27 | 2000-09-27 | Septic tank operation |
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| JP (1) | JP3901441B2 (en) |
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