JP3669850B2 - Septic tank - Google Patents

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JP3669850B2
JP3669850B2 JP35737898A JP35737898A JP3669850B2 JP 3669850 B2 JP3669850 B2 JP 3669850B2 JP 35737898 A JP35737898 A JP 35737898A JP 35737898 A JP35737898 A JP 35737898A JP 3669850 B2 JP3669850 B2 JP 3669850B2
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tank
filtration
carrier
water
treated
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JP2000176475A (en
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八郎 佐藤
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Kubota Corp
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Kubota Corp
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【0001】
【発明の属する技術分野】
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し、気泡供給により前記担体を流動させる散気部を設けた担体流動槽を備えた浄化槽に関する。
【0002】
【従来の技術】
従来この種の浄化槽は、浄化槽本体を複数に仕切って前記担体流動槽を設けるとともに、その担体流動槽の下方に、前記担体流動槽において発生した汚泥と、前記担体とを堰き止めて濾過する濾過層を設け、被処理水を上方から果報に流通自在に構成したものが提案されている。このような構成により、前記担体流動槽から発生した汚泥を堰き止め、下流側への固形物の移流を防止しつつ、好気的に分解処理し、被処理水を浄化処理することができるものである。
【0003】
【発明が解決しようとする課題】
しかし、前記担体流動槽は前記濾過層の上方側に設けられていることから、たとえ、前記濾過層が目詰まりしたとしても、容易にメンテナンスすることは出来ず、例えば、浄化槽への被処理水の流入を遮断し、前記担体流動槽内の被処理水を全て抜き出す等の処理を行った後、前記担体流動槽及び濾過層を構成する各種部材を取り外すなどして、浄化槽全体の分解再組立を余儀なくされるような場合がある。そのため、前記濾過層に担体を充填してその担体による濾過を実現する構成として、前記濾過層の再生を容易にする構成とし、前記濾過層の目詰まりを低下させることが提案されているが、やはり、定期点検を励行せねば、前記浄化槽全体の分解再組立等が必要となるメンテナンスが必要になるという問題点が依然として残っていた。
従って、本発明の目的は、上記欠点に鑑み、メンテナンス容易に構成しながらも、上述の担体流動槽の機能を損なうことなく、被処理水を浄化することので着る浄化槽を提供することにある。
【0004】
【課題を解決するための手段】
この目的を達成するための本発明の浄化槽の特徴構成は、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を収容保持し、気泡供給により前記担体を流動させる散気部を設けた担体流動槽を備えるとともに、
汚泥を濾過する濾過槽と、
前記濾過槽を通過した被処理水を、貯留する処理水槽とを備え、
被処理水とともに流動可能に形成してある比重1以上1.2以下の多数の担体を、前記濾過槽の内部に収容し、前記担体を前記濾過槽内に沈降、堆積させた状態で堆積濾過層を形成自在に収容し、
前記担体流動槽と前記濾過槽とを仕切る第一隔壁に、被処理水の移流を許容しつつ、前記担体の移流を遮る移流壁部を設けるとともに、
前記濾過槽と前記処理水槽とを仕切り、前記堆積濾過層に臨む第二隔壁に、被処理水の移流を許容しつつ、前記担体の移流を遮る濾過壁部を設け
前記担体流動槽から前記濾過槽、前記処理水槽へと、この順に被処理水を移送自在に構成してある点にあり、
前記循環装置が散気装置であれば好ましく、
被処理水の移流する前記担体流動槽の上流側に沈殿分離槽又は夾雑物除去槽又は嫌気濾床槽等の被処理水が嫌気的に処理される嫌気処理槽を設け、前記濾過槽内から前記嫌気処理槽に被処理水を移送する移送手段を設けてあれば好ましく、前記移流壁部が前記第一隔壁の前記堆積濾過層の高さよりも低位置に設けてあってもよく、
前記移流壁部が前記第一隔壁の前記堆積濾過層の高さよりも低位置から高位置にわたって設けてあってもよく、
前記担体流動槽内から供給される気泡を、前記移流壁部の前記担体流動槽側面に沿って上方へ誘導できるように前記移流壁部を傾斜させて設けてあってもよく、
また、前記移流壁部の前記担体流動槽側下部に前記移流壁部に気泡供給する移流壁散気部を設けてあることが好ましい。
また、前記処理水槽から供給される気泡を、前記濾過壁部の前記処理水槽側面に沿って上方へ誘導できるように前記濾過壁部を傾斜させて設け、前記濾過壁部の前記処理水槽側下部に前記濾過壁部に気泡供給する濾過壁散気部を設けてあることが好ましい。
【0005】
〔作用効果〕
つまり、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し、気泡供給により前記担体を流動させる散気部を設けた担体流動槽を備えているから、前記担体に担持された微生物は、その担体流動槽内を循環しながら、気液と十分に接触し、被処理水を浄化しつつ活動させられる。
そして、汚泥を濾過する濾過槽と、前記濾過槽を通過した被処理水を、貯留する処理水槽とを備え、被処理水とともに流動可能に形成してある比重1以上1.2以下の多数の担体を、前記濾過槽の内部に収容し、前記担体を前記濾過槽内に沈降、堆積させた状態で堆積濾過層を形成自在に収容し、前記担体流動槽から前記濾過槽、前記処理水槽へと、この順に被処理水を移送自在に構成してあれば、前記多数の担体を容易に沈降堆積させることが出来、前記濾過槽内に前記堆積濾過層を形成させておくことが容易に出来るとともに、前記担体流動槽内で処理された被処理水は、濾過槽内に流入して担体濾過層を通過して前記処理水槽に移流することが出来るようになる。
【0006】
ここで、前記担体流動槽と前記濾過槽とを仕切る第一隔壁に、被処理水の移流を許容しつつ、前記担体の移流を遮る移流壁部を設けるとともに、前記濾過槽と前記処理水槽とを仕切り、前記堆積濾過層に臨む第二隔壁に、被処理水の移流を許容しつつ、前記担体の移流を遮る濾過壁部を設けてあるから、前記担体流動槽内の担体は前記濾過槽内に流入せず、しかも前記濾過槽内の担体も前記処理水槽に流入しないように規制される。また一方、前記担体流動槽内で発生した汚泥等は、被処理水とともに、前記担体流動槽から前記濾過槽に侵入するが、前記濾過壁部は、前記担体が沈降堆積したときの高さよりも低い位置に設けてあるから、前記被処理水は、堆積濾過層を通って前記濾過壁部を通過せねばならず、このとき、前記汚泥等は、前記担体に濾過されることになる。また、前記濾過槽は、前記担体流動槽とは第一隔壁によって区切って設けられるから、上部を解放状態に形成することが出来る。
またさらに、前記濾過槽内で、所定期間前記汚泥等を濾過した担体は、次第に目詰まりして次第に濾過機能が低下するとともに、前記汚泥の分解処理も滞りがちになるのであるが、前記濾過層内に前記濾過槽内に収容した担体を前記濾過槽内に循環させる循環装置を設けてあれば、前記担体を被処理水中で循環、攪拌すっることで、互いの担体同士が衝突しあう状況を作り、その衝突作用により前記担体に付着した汚泥を剥離させ、前記担体を再生し、再度濾過機能を復活させることができる。
【0007】
従って、担体流動法による水処理を効率よくするとともに、発生した汚泥の処理も効果的に行えるため、安定運転の継続に有利になるとともに、前記濾過層は上部開放形状に形成することが出来て、さらにメンテナンス容易とすることができた。
【0008】
ここで、前記循環装置を散気装置から構成してあれば、簡易な構成でありながらも、前記担体への気泡の供給による担体の洗浄再生効果も期待できることから、効率の良い担体の再生が行え、さらに、前記移送手段を設けてあれば、前記再生によって生じた汚泥等を沈殿分離槽又は強雑物除去槽又は嫌気濾床槽等の嫌気処理槽に移送して、より効果的な分解を図ることが出来る。
【0009】
また、前記移流壁部が前記第一隔壁の前記堆積濾過層の高さよりも低位置に設けてあれば、前記濾過槽を通過する被処理水は、確実に前記堆積濾過層を通過する構成になるので、確実な濾過を実現しやすい。
また、前記移流壁部が前記第一隔壁の前記堆積濾過層の高さよりも低位置から高位置にわたって設けてあるばあいには、前記濾過槽を攪拌して担体を再生したときに発生する剥離汚泥が、前記堆積濾過層の上部側から前記担体流動槽に逆流しやすく、汚泥処理効率の向上が期待できる。
尚、本発明にいう堆積濾過層の高さとは、前記濾過槽における担体が前記濾過槽内の攪拌後に自然に沈降して形成する堆積物の上面高さをいい、前記担体の量は、前記担体をほぼ全量沈降させたときの見かけ体積を基に調整することが出来る。
また、前記担体流動槽は、ほぼ常時流動状態を維持するのに対して、前記濾過槽は、間欠的に再生操作せねばならないことになるが、夜間等前記担体流動槽に新たな負荷が生じにくい時期を見計らって、前記濾過槽を攪拌操作し、担体から汚泥を分離した後、再び担体が沈降、堆積するのを待てば、生物処理の効率を低下させずに、浄化槽の定常運転を図ることが出来る。尚、前記担体の比重を1〜1.2程度に調整してあれば、これに要する時間を数分程度に抑えることが出来る。
【0010】
さらに、前記担体流動槽内から供給される気泡を、前記移流壁部の前記担体流動槽側面に沿って上方へ誘導できるように前記移流壁部を傾斜させて設けてあれば、前記担体流動槽内の被処理水の流れが、気泡とともに前記移流壁部に衝突することになるので、前記移流壁部を洗浄して汚泥等が付着して目詰まりが生じるのを抑制することが出来、やはり、浄化槽の定常的な安定運転を果たすのに寄与する。
また、前記移流壁部の前記担体流動槽側下部に前記移流壁部に気泡供給する移流壁散気部を設けてあれば、積極的に前記移流壁部に気泡を供給できるから、前記洗浄効果が大きく現れやすく好ましい。
また、前記処理水槽から供給される気泡を、前記濾過壁部の前記処理水槽側面に沿って上方へ誘導できるように前記濾過壁部を傾斜させて設け、前記濾過壁部の前記処理水槽側下部に前記濾過壁部に気泡供給する濾過壁散気部を設けてあれば、前記濾過壁部に汚泥等が付着したとしても、先と同様に前記濾過壁部を洗浄して目詰まり等を防止することが出来、浄化槽の定常的な安定運転を果たすのに寄与し、メンテナンス容易に構成することが出来る。
【0011】
尚、上述の構成で前記移流壁部と濾過壁部をともに傾斜して設けてあれば、前記濾過槽は上広がりに形成されるから、担体が攪拌操作により流動状態になり再び沈降堆積する際に、全体がほぐれながら上昇するとともに循環し始める状況を形成しやすく、かつ、ブロッキング現象か起きにくいので担体の再生が良好に行え、さらに、沈降堆積する際にも、移流壁部と濾過壁部の近傍において担体密度が低下して濾過効率が落ちるような不具合を招来しにくい。また、攪拌操作を散気装置によって実現する際には、ブロッキングが起きると気泡が移流壁部と濾過壁部を通じて濾過槽外へ逃げてしまう虞があるが、上述の構成によれば、このような現象を効率よく防止できる。尚、この際散気管は前記濾過槽底部のほぼ中央に位置することが望ましい。
【0012】
【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、上流側から嫌気処理槽N、好気処理槽E、処理水槽T1等を備え、前記嫌気処理槽Nは、沈殿分離槽N1及び嫌気濾床槽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から前記沈殿分離槽N1に流入するとともに、嫌気濾床槽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、前記沈殿槽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。
【0013】
前記沈殿分離槽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。前記沈殿分離槽N1に流入する被処理水の原水は、前記沈殿分離槽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、前記沈殿分離槽N1下部からN1前記嫌気濾床槽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沈殿分離槽N1下部に沈殿としてあるいは、沈殿分離槽N1上部にスカムとして貯留される。
前記嫌気濾床槽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は櫛歯状部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。
【0014】
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、前記散気部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、前記担体流動槽と、隣接する濾過槽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、格子状又は櫛刃状に形成してあり、前記担体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。
また、前記第一隔壁W1の前記移流壁部3の下方には散気管Daを備えて移流壁散気部を設けてある。また、前記第一隔壁W1は前記移流壁部3とともに、前記移流壁散気部Daの上方側を覆う傾斜姿勢に設けてあり、前記移流壁部3に散気することにより前記移流壁部3の目詰まり等を防止する構成としてある。
【0015】
前記濾過槽E2は、水よりも比重の大きな担体C2を所定高さまで高密度に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。
前記濾過壁部4は格子状に形成してあり、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の下部には前記担体C2に散気して前記濾過槽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、前記第二隔壁W2の前記濾過壁部4の下方には散気管Dbを備えて移流壁散気部を設けてある。また、前記第二隔壁W2は前記濾過壁部4とともに、前記移流壁散気部の上方側を覆う傾斜姿勢に設けてあり、前記濾過壁部4に散気することにより前記濾過壁部4の目詰まり等を防止する構成としてある。
これにより、前記濾過槽E2は上方側が解放状態に設けられるから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。
【0016】
ここで、前記濾過壁部は、被処理水を必ず前記堆積濾過層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る。尚、前記移流壁部は、前記所定高さの上側にまで達する構成としてある、被処理水の移流を許容し、前記堆積濾過層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。
【0017】
さらに、前記担体流動槽E1には、前記沈殿分離槽N1に被処理水を移送するエアリフトポンプA1を設けてあり、水処理によって生じた汚泥を被処理水とともに前記沈殿分離槽N1に移送可能に構成してあるとともに、前記濾過槽E2には前記沈殿分離槽N1に被処理水を移送するエアリフトポンプA2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内から前記沈殿分離槽N1へ被処理水とともに移送することができる。
【0018】
前記処理水槽T1は、前記濾過槽E2を通過した清浄な上澄み部のみを外部に放流可能にし前記沈殿槽T2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。
【0019】
〔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V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。
【図面の簡単な説明】
【図1】本発明の浄化槽を示す縦断側面図
【図2】本発明の浄化槽を示す平面図
【図3】本発明の浄化槽を示す縦断正面図
【符号の説明】
E 好気処理槽
E1 担体流動槽
E2 濾過槽
I 原水流入部
N 嫌気処理槽
N1 沈殿分離槽
N2 嫌気濾床槽
T 処理水槽
Z 放流口
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a septic tank equipped with a carrier fluid tank that contains and holds a carrier that is formed so as to be able to flow together with water to be treated in a state where microorganisms are carried, and is provided with a diffuser that allows the carrier to flow by supplying bubbles.
[0002]
[Prior art]
Conventionally, this type of septic tank is provided with the carrier fluid tank by dividing the septic tank body into a plurality of pieces, and under the carrier fluid tank, sludge generated in the carrier fluid tank and the carrier are filtered for damming and filtering. There has been proposed a structure in which a layer is provided so that water to be treated can be freely distributed from above to fruit reports. With such a configuration, the sludge generated from the carrier fluidized tank can be dammed and the aeration can be decomposed and the water to be treated can be purified while preventing the advection of solids downstream. It is.
[0003]
[Problems to be solved by the invention]
However, since the carrier fluid tank is provided above the filtration layer, even if the filtration layer is clogged, it cannot be easily maintained. After removing the water to be treated and extracting all of the water to be treated in the carrier fluid tank, the various parts constituting the carrier fluid tank and the filtration layer are removed, and the entire septic tank is disassembled and reassembled. May be forced to. Therefore, it is proposed that the filtration layer is filled with a carrier and the filtration by the carrier is realized, the filtration layer is easily regenerated, and the clogging of the filtration layer is reduced. After all, if periodic inspection is not carried out, there still remains a problem that maintenance that requires disassembly and reassembly of the entire septic tank becomes necessary.
Accordingly, an object of the present invention is to provide a septic tank that can be worn by purifying the water to be treated without impairing the function of the above-described carrier flow tank, while maintaining easy maintenance, in view of the above drawbacks.
[0004]
[Means for Solving the Problems]
To achieve this object, the septic tank according to the present invention is characterized in that a carrier that is formed so as to be able to flow together with the water to be treated is contained and held in a state where microorganisms are supported, and the carrier is made to flow by supplying bubbles. With a carrier fluid tank provided with a gas part,
A filtration tank for filtering sludge;
A treated water tank for storing treated water that has passed through the filtration tank;
A large number of carriers having a specific gravity of 1 or more and 1.2 or less formed so as to be able to flow together with the water to be treated are accommodated in the filtration tank, and the carrier is sedimented and deposited in the filtration tank. Contains the layer formably,
The first partition partitioning the carrier fluid tank and the filtration tank is provided with a convection wall that blocks the advection of the carrier while allowing the advection of water to be treated.
The filtration tank and the treated water tank are partitioned, and a second partition wall facing the deposited filtration layer is provided with a filtration wall portion that allows the treatment water to flow while blocking the transfer of the carrier, and the filtration from the carrier flow tank. To the tank, the treated water tank, the water to be treated is configured to be freely transferred in this order,
Preferably, the circulation device is a diffuser,
An anaerobic treatment tank in which the treated water is treated anaerobically, such as a sedimentation separation tank, a contaminant removal tank, or an anaerobic filter bed tank, is provided upstream of the carrier flow tank to which the treated water is transferred. Preferably, there is provided a transfer means for transferring the water to be treated to the anaerobic treatment tank, and the advection wall portion may be provided at a position lower than the height of the deposited filtration layer of the first partition wall,
The advection wall portion may be provided from a lower position to a higher position than the height of the deposition filtration layer of the first partition wall,
The advancing wall portion may be provided to be inclined so that the bubbles supplied from the inside of the carrier fluidizing tank can be guided upward along the side surface of the carrier fluidizing tank of the advancing wall portion,
Moreover, it is preferable to provide the advection wall aeration part which supplies a bubble to the advection wall part in the carrier flow tank side lower part of the advection wall part.
In addition, the filtration wall portion is provided to be inclined so that air bubbles supplied from the treatment water tank can be guided upward along the side surface of the treatment water tank of the filtration wall portion, and the treatment water tank side lower portion of the filtration wall portion It is preferable that a filtration wall diffuser for supplying bubbles to the filtration wall is provided.
[0005]
[Function and effect]
In other words, in a state where microorganisms are supported, a carrier fluid tank is provided that holds and holds a carrier that is formed to be flowable together with the water to be treated, and is provided with an air diffuser that causes the carrier to flow by supplying bubbles. The microorganisms carried on the carrier are allowed to act while purifying the water to be treated while sufficiently contacting the gas and liquid while circulating in the carrier fluid tank.
And it is provided with the filtration tank which filters sludge, and the treated water tank which stores the to-be-treated water which passed the said filtration tank, and has many specific gravity 1 or more and 1.2 or less formed so that it can flow with treated water A carrier is accommodated inside the filtration tank, and a sedimentation filtration layer is freely formed in a state where the carrier is settled and deposited in the filtration tank, from the carrier flow tank to the filtration tank and the treated water tank. If the water to be treated is configured to be transportable in this order, the large number of carriers can be easily settled and deposited, and the deposited filtration layer can be easily formed in the filtration tank. At the same time, the water to be treated that has been treated in the carrier fluidized tank can flow into the filtration tank, pass through the carrier filtration layer, and be transferred to the treated water tank.
[0006]
Here, the first partition partitioning the carrier flow tank and the filtration tank is provided with a convection wall portion that blocks the transfer of the carrier while allowing the transfer of the water to be treated, and the filtration tank and the treatment water tank. And the second partition wall facing the deposition filtration layer is provided with a filtration wall portion that allows the transfer of the water to be treated and blocks the transfer of the support, so that the support in the support fluid tank is the filter tank. In addition, the carrier in the filtration tank is regulated so as not to flow into the treated water tank. On the other hand, sludge and the like generated in the carrier fluid tank enter the filtration tank from the carrier fluid tank together with the water to be treated, but the filtration wall portion is higher than the height when the carrier is sedimented. Since it is provided at a low position, the water to be treated must pass through the filtration wall portion through the deposited filtration layer, and at this time, the sludge and the like are filtered by the carrier. Moreover, since the said filtration tank is divided and provided with the said carrier flow tank by the 1st partition, it can form an upper part in an open state.
Furthermore, the carrier that has filtered the sludge and the like for a predetermined period in the filtration tank is gradually clogged and the filtration function gradually decreases, and the sludge decomposition treatment tends to be delayed. If a circulation device for circulating the carrier accommodated in the filtration tank is provided in the filtration tank, the carriers collide with each other by circulating and stirring the carrier in the water to be treated. The sludge adhering to the carrier is peeled off by the collision action, the carrier is regenerated, and the filtration function can be restored again.
[0007]
Accordingly, the water treatment by the carrier flow method can be efficiently performed and the generated sludge can be treated effectively, which is advantageous for continuation of stable operation and the filtration layer can be formed in an open top shape. Furthermore, maintenance could be made easier.
[0008]
Here, if the circulation device is composed of an air diffuser, it is possible to expect an effect of washing and regeneration of the carrier by supplying bubbles to the carrier, although it is a simple structure. If the transfer means is provided, the sludge generated by the regeneration is transferred to an anaerobic treatment tank such as a sedimentation separation tank, a strong substance removal tank or an anaerobic filter bed tank, and more effective decomposition. Can be planned.
[0009]
Further, if the advection wall portion is provided at a position lower than the height of the deposition filtration layer of the first partition wall, the water to be treated that passes through the filtration tank surely passes through the deposition filtration layer. Therefore, it is easy to achieve reliable filtration.
Further, in the case where the advection wall portion is provided from a position lower than a height of the deposited filtration layer of the first partition wall, the separation that occurs when the carrier is regenerated by stirring the filtration tank. Sludge tends to flow backward from the upper side of the sedimentation filtration layer to the carrier flow tank, and an improvement in sludge treatment efficiency can be expected.
The height of the deposited filtration layer referred to in the present invention refers to the height of the upper surface of the deposit formed by the carrier in the filtration tank naturally settled after stirring in the filtration tank, and the amount of the carrier is The volume can be adjusted based on the apparent volume when the carrier is almost completely settled.
Further, while the carrier fluid tank maintains a fluid state almost always, the filtration tank must be regenerated intermittently, but a new load is generated in the carrier fluid tank such as at night. In anticipation of difficult times, the filtration tank is agitated and sludge is separated from the carrier. After waiting for the carrier to settle and deposit again, steady operation of the septic tank is attempted without lowering the biological treatment efficiency. I can do it. If the specific gravity of the carrier is adjusted to about 1 to 1.2, the time required for this can be suppressed to about several minutes.
[0010]
Furthermore, if the advancing wall portion is inclined and provided so that the bubbles supplied from the inside of the advancing carrier portion can be guided upward along the side surface of the advancing carrier portion of the advancing wall portion, Since the flow of the water to be treated collides with the advection wall part together with bubbles, it is possible to suppress clogging due to sludge adhering by washing the advection wall part, This contributes to the steady and stable operation of the septic tank.
Further, if the advection wall diffuser for supplying bubbles to the advection wall is provided at the lower part of the advection wall on the side of the carrier flow tank, bubbles can be positively supplied to the advection wall. Is easy to appear and is preferable.
In addition, the filtration wall portion is provided to be inclined so that air bubbles supplied from the treatment water tank can be guided upward along the side surface of the treatment water tank of the filtration wall portion, and the treatment water tank side lower portion of the filtration wall portion If there is a filtration wall diffuser for supplying air bubbles to the filtration wall, even if sludge adheres to the filtration wall, the filtration wall is washed to prevent clogging and the like. This contributes to the steady and stable operation of the septic tank, and can be configured easily.
[0011]
Note that if the advection wall portion and the filtration wall portion are both inclined in the above-described configuration, the filtration tank is formed so as to expand upward. In addition, it is easy to form a situation where the whole ascends loosely and starts to circulate, and the blocking phenomenon does not easily occur, so that the carrier can be regenerated well. In the vicinity of, it is difficult to cause a problem that the carrier density is lowered and the filtration efficiency is lowered. In addition, when the stirring operation is realized by the air diffuser, if blocking occurs, bubbles may escape to the outside of the filtration tank through the advection wall portion and the filtration wall portion. Can be effectively prevented. In this case, it is desirable that the air diffuser is located at substantially the center of the bottom of the filtration tank.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below with reference to the drawings.
The septic tank of the present invention comprises an anaerobic treatment tank N, an aerobic treatment tank E, a treated water tank T1, etc. from the upstream side, and the anaerobic treatment tank N comprises a precipitation separation tank N1 and an anaerobic filter bed tank N2, and the aerobic treatment tank The processing tank E includes a carrier fluid tank E1 and a filtration tank E2. The raw water to be treated flows into the sedimentation separation tank N1 from the raw water inflow section I, and is decomposed while being transferred downstream in the order of the anaerobic filter bed tank N2, the carrier flow tank E1, the filtration tank E2, and the treated water tank T1. After passing through the disinfection tank Q provided above the settling tank T2, it is discharged from the discharge port Z to the outside of the tank.
[0013]
The sedimentation separation tank N1 is configured to be able to store raw water to be treated, and is capable of growing anaerobic microorganisms therein. The raw water to be treated that flows into the precipitation separation tank N1 is stored in the precipitation separation tank N1 and is anaerobically decomposed, and mainly coarse organic matter is subdivided, and the lower part of the precipitation separation tank N1 From N1 to the lower part of the anaerobic filter bed tank N2. Solids such as sludge that are not easily decomposed are stored as precipitates in the lower part of the precipitation separation tank N1 or as scum in the upper part of the precipitation separation tank N1.
The anaerobic filter bed tank N2 includes an anaerobic filter bed F, and is configured to fix and grow anaerobic microorganisms on the anaerobic filter bed F. The water to be treated which has flowed into the anaerobic filter bed tank N2 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 so that water to be treated can be naturally transferred, and the overflow portion 1 is provided with a comb-like portion 2 to be treated. It is configured such that it can be transferred to water and the carrier and sludge in the carrier flow tank E1 can be prevented from flowing back.
[0014]
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, and the carrier C1 is caused to flow in the carrier flow tank E1 by supplying bubbles from the air diffuser. 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 and the adjacent filtration tank.
The advection wall portion 3 is formed in a lattice shape or a comb blade shape, and is configured to prevent the advancing of the carrier but to permit the advancing of sludge and water to be treated.
Further, an aeration wall diffuser is provided below the advection wall 3 of the first partition wall W1 with an aeration tube Da. The first partition wall W <b> 1 is provided in an inclined posture covering the upper side of the advection wall diffuser Da together with the advection wall 3, and the advection wall 3 is diffused by aeration. It is configured to prevent clogging and the like.
[0015]
The filtration tank E2 is configured by filling a carrier C2 having a specific gravity greater than that of water to a predetermined height at a high density. Moreover, the filtration wall part 4 which makes a to-be-processed water flow freely is formed in the position lower than the said predetermined height of the said filtration tank E2 and the 2nd partition W2 provided adjacent to the filtration tank E2. 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 filtration wall 4 is formed in a lattice shape, and prevents the advection of the carrier C2, but allows the advection of sludge and water to be treated.
Further, an aeration pipe D2 as a stirring device for agitating the inside of the filtration tank by aerating the carrier C2 is provided at the lower part of the deposited filtration layer so that the load flows into the septic tank such as at night. The carrier is regenerated by performing aeration from the diffusion tube D2 in a short time zone.
In addition, an aeration wall diffuser is provided below the filtration wall 4 of the second partition wall W2 with a diffuser tube Db. In addition, the second partition wall W2 is provided in an inclined posture that covers the upper side of the advection wall diffuser together with the filter wall 4 and diffuses into the filter wall 4 to thereby The configuration prevents clogging and the like.
Thereby, since the upper side of the filtration tank E2 is provided in an open state, the maintenance can be easily performed from the upper side through the manhole H provided in the septic tank without disassembling the inside of the septic tank.
[0016]
Here, the filtration wall portion is provided at a position lower than a predetermined height that is the height of the deposition upper end portion of the deposition filtration layer so that the water to be treated must be transferred after passing through a predetermined distance of the deposition filtration layer. is there. In addition, the said advection wall part should just be the structure which accept | permits the advection of to-be-processed water as the structure which reaches to the upper side of the said predetermined height, and enables filtration of the to-be-processed water in the said sedimentation filtration layer.
The carriers C1 and C2 are each 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.
[0017]
Further, the carrier flow tank E1 is provided with an air lift pump A1 for transferring the water to be treated to the precipitation separation tank N1, so that the sludge generated by the water treatment can be transferred to the precipitation separation tank N1 together with the water to be treated. In addition, the filtration tank E2 is provided with an air lift pump A2 for transferring the water to be treated to the precipitation separation tank N1, and the sludge generated by the regeneration of the carrier C2 is extracted from the filtration tank E2 into the filtration tank E2. It can transfer with the to-be-processed water to the sedimentation separation tank N1.
[0018]
The treated water tank T1 allows only the clean supernatant that has passed through the filtration tank E2 to be discharged to the outside, flows into the disinfection tank Q provided at the upper part of the settling tank T2, and contacts the solid disinfectant Q1 to disinfect. After that, it is discharged out of the tank.
[0019]
[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 V 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.
[Brief description of the drawings]
FIG. 1 is a vertical side view showing a septic tank according to the present invention. FIG. 2 is a plan view showing a septic tank according to the present invention.
E aerobic treatment tank E1 carrier flow tank E2 filtration tank I raw water inflow section N anaerobic treatment tank N1 sedimentation separation tank N2 anaerobic filter bed tank T treated water tank Z outlet

Claims (8)

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し、気泡供給により担体を流動させる散気部を設けた担体流動槽を備えるとともに、
汚泥を濾過する濾過槽と、
濾過槽を通過した被処理水を、貯留する処理水槽とを備え、
被処理水とともに流動可能に形成してある比重1以上1.2以下の多数の担体を、濾過槽の内部に収容し、担体を濾過槽内に沈降、堆積させた状態で堆積濾過層を形成自在に収容し、
担体流動槽と濾過槽とを仕切る第一隔壁に、被処理水の移流を許容しつつ、担体の移流を遮る移流壁部を設けるとともに、
濾過槽と処理水槽とを仕切り、前記堆積濾過層に臨む第二隔壁に、被処理水の移流を許容しつつ、前記担体の移流を遮る濾過壁部を設け
前記濾過槽内に収容した担体を前記濾過槽内に循環させる循環装置を設け、
前記担体流動槽から前記濾過槽、前記処理水槽へと、この順に被処理水を移送自在に構成してある浄化槽。
In a state where microorganisms are supported, a carrier fluid tank is provided that contains and holds a carrier that is formed to be flowable together with the water to be treated, and is provided with an air diffuser that allows the carrier to flow by supplying bubbles.
A filtration tank for filtering sludge;
A treated water tank for storing treated water that has passed through the filtration tank,
A large number of carriers having a specific gravity of 1 or more and 1.2 or less formed to flow with the water to be treated are accommodated in the filtration tank, and the deposited filtration layer is formed in a state where the carrier is settled and deposited in the filtration tank. To accommodate freely,
In the first partition partitioning the carrier fluid tank and the filtration tank, while providing the advection wall portion that blocks the advection of the carrier while allowing the advection of the water to be treated,
A filter tank and a treated water tank are partitioned, and a second partition wall facing the deposited filtration layer is provided with a filtration wall portion that blocks the transfer of the carrier while allowing the transfer of water to be treated, and the carrier accommodated in the filtration tank Providing a circulation device for circulation in the filtration tank;
A septic tank constructed such that the water to be treated can be transferred in this order from the carrier fluid tank to the filtration tank and the treated water tank.
前記循環装置が散気装置である請求項1に記載の浄化槽。The septic tank according to claim 1, wherein the circulation device is an air diffuser. 被処理水の移流する前記担体流動槽の上流側に嫌気処理槽を設け、前記濾過槽内から前記嫌気処理槽に被処理水を移送する移送手段を設けた請求項1に記載の浄化槽。The septic tank according to claim 1, wherein an anaerobic treatment tank is provided upstream of the carrier flow tank to which the water to be treated is transferred, and a transfer means for transferring the water to be treated from the filtration tank to the anaerobic treatment tank. 前記移流壁部が前記第一隔壁の前記堆積濾過層の高さよりも低位置に設けてある請求項1又は2に記載の浄化槽。The septic tank according to claim 1 or 2, wherein the advection wall portion is provided at a position lower than a height of the deposition filtration layer of the first partition wall. 前記移流壁部が前記第一隔壁の前記堆積濾過層の高さよりも低位置から高位置にわたって設けてある請求項1〜3のいずれかに記載の浄化槽。The septic tank according to any one of claims 1 to 3, wherein the advection wall portion is provided from a lower position to a higher position than a height of the deposition filtration layer of the first partition wall. 前記担体流動槽内から供給される気泡を、前記移流壁部の前記担体流動槽側面に沿って上方へ誘導できるように前記移流壁部を傾斜させて設けてある請求項1〜4のいずれかに記載の浄化槽。The advection wall portion is provided so as to be inclined so that bubbles supplied from within the carrier flow vessel can be guided upward along the side surface of the carrier flow vessel of the advection wall portion. The septic tank described in 1. 前記移流壁部の前記担体流動槽側下部に前記移流壁部に気泡供給する移流壁散気部を設けてある請求項5に記載の浄化槽。The septic tank according to claim 5, wherein a convection wall aeration section for supplying bubbles to the convection wall section is provided at a lower part of the convection wall section on the carrier flow tank side. 前記処理水槽から供給される気泡を、前記濾過壁部の前記処理水槽側面に沿って上方へ誘導できるように前記濾過壁部を傾斜させて設け、前記濾過壁部の前記処理水槽側下部に前記濾過壁部に気泡供給する濾過壁散気部を設けてある請求項6に記載の浄化槽。The filtration wall portion is provided to be inclined so that air bubbles supplied from the treatment water tank can be guided upward along the side surface of the treatment water tank of the filtration wall portion, and the treatment water tank side lower portion of the filtration wall portion The septic tank according to claim 6, wherein a filtration wall aeration part for supplying bubbles to the filtration wall part is provided.
JP35737898A 1998-12-16 1998-12-16 Septic tank Expired - Lifetime JP3669850B2 (en)

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