JP3768054B2 - Septic tank partition wall structure - Google Patents
Septic tank partition wall structure Download PDFInfo
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Description
【0001】
【発明の属する技術分野】
本発明は、複数の水処理槽を並設し、上流側槽と下流側槽とを仕切る仕切壁に、前記上流側槽から前記下流側槽に被処理水を溢流させる溢流部を設けた浄化槽の仕切壁構造に関する。
【0002】
【従来の技術】
従来、浄化槽の仕切壁は、下端部に上流側槽の定常水位が位置するように、開口部を前記仕切壁の所定位置に開口形成、あるいは、前記仕切壁の上端部側から切り欠き形成されているものが知られている。
また、前記開口部に、前記下流側槽から上流側槽への被処理水の逆流を防止すべく、前記開口部を閉塞可能な揺動板を設け、前記揺動板を、前記下流側槽側に揺動自在に取り付け、揺動姿勢で前記開口部が開口状態になり溢流部が形成され、垂下姿勢で前記開口部を覆うとともに前記開口部周縁部により前記上流側槽側への揺動が規制されるように構成してあるものが知られている。
【0003】
【発明が解決しようとする課題】
上述の単に開口部を形成して溢流部が形成されている前者の浄化槽の仕切壁の構造によると、浄化槽内部に被処理水の原水が大量に流入した場合に、前記開口部により規制されるべき水位よりも高くなり、前記上流側槽と下流側槽との間で被処理水が循環する空間が大きくなるとともに、それに伴い、両槽間での被処理水の逆流循環が大規模に発生することになる。
【0004】
しかし、このような被処理水の大量流入があった場合には、前記上流側槽から、下流側槽への被処理水流入は許容する必要があるものの、特に下流側槽が被処理水を好気処理する槽であるような場合、汚泥濃度を比較的高濃度に維持して処理する必要があるなどの理由から、前記汚泥が前記下流側槽から上流側槽へ浮遊汚泥が大量に返送されることは好ましくなく、安定に被処理水処理を行うには、汚泥の逆流循環を抑制する必要性がある。
【0005】
そのため、このような傾向を防ぐべく前記揺動板を設けてある構成が採用されるのであるが、このようにすると、被処理水の大量流入を受けた場合にも被処理水の移流が前記上流側槽から下流側槽に向かって起きるように形成すべく、前記揺動板を設けた後者の構造が考えられているのであるが、このような場合には、前記上流側槽及び下流側槽が前記開口部で規制される水位よりもやや高い水位を保っている状態の水位を維持しているような場合には、被処理水の定常的な返送移流が図れず、被処理水の生物処理を行う上で好ましくない状況も想定される。
また、前記被処理水の大量流入が設計時点で想定した最大量を超えた様な場合、前記下流側槽への前記被処理水の大量移流が直接影響するため、前記上流側槽でその被処理水の大量流入を緩衝させることも必要になる。
そこで、前記仕切壁に開口部を設け、単に、前記上流側槽と下流側槽とがの定常水位にある状態で仕切る構成とし、前記上流側槽と下流側槽との間の被処理水の移流をすべてエアリフトポンプのような被処理水移送手段に負担させ、前記上流側槽では、槽内への被処理水の大量移流を一時貯留できる構成をとり、下流側槽への悪影響を緩衝しながらも、前記下流側槽からの汚泥成分の返送等を良好に維持することが検討されているが、前記被処理水返送手段を配設するために浄化槽の構造が複雑になるとともに初期設備費、運転経費が割高になるという不都合があった。
【0006】
従って、本発明の目的は、上記欠点に鑑み、仕切壁の改良により、簡単安価な構成により、浄化槽内に大量の被処理水流入があった場合にも、上流側槽で緩衝しつつ、通常時にも安定な被処理水処理が出来るような浄化槽を提供する点にある。
【0007】
【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仕切壁構造の特徴構成は、複数の水処理槽を並設し、上流側槽と下流側槽とを仕切る仕切壁に、前記上流側槽から前記下流側槽に被処理水を溢流させる溢流部を設けた浄化槽の仕切壁構造であって、前記仕切壁に開口部を設け、前記開口部よりも狭い通水口を形成してある揺動板を設け、前記揺動板を、前記上流側槽側に揺動自在に取り付け、揺動姿勢で前記開口部が開口状態になり溢流部が形成され、垂下姿勢で前記開口部の少なくとも一部を覆うとともに、前記開口部周縁部により前記下流側槽側への揺動が規制され、かつ、前記開口部の開口度が制限されて、前記通水口が溢流部に形成されるように設け、さらに、前記揺動板の上方側に、前記上流側槽の水位が上昇した場合に、前記上流側槽から前記下流側槽に被処理水を溢流させる溢流部を形成してある点にある。
【0008】
〔作用効果〕
つまり、複数の水処理槽を並設し、上流側槽と下流側槽とを仕切る仕切壁に、前記上流側槽から前記下流側槽に被処理水を溢流させる溢流部を設けた浄化槽において、前記下流側槽に散気装置を設けてあれば、前記下流側槽では、被処理水の好気処理が行えるとともに、発生する汚泥を前記上流側槽内で浮遊させることが出来る。
ここで、前記仕切壁に開口部を設けてあれば、上流側槽から下流側槽への被処理水の自然移流が図れるとともに、前記上流側槽側に揺動自在に取り付け、揺動姿勢で前記開口部が開口状態になり溢流部が形成され、垂下姿勢で前記開口部の少なくとも一部を覆うとともに、前記開口部周縁部により前記下流側槽側への揺動が規制され、かつ、前記開口部の開口度が制限されて、前記通水口が溢流部に形成されるように揺動板が設けてあれば、 前記上流側槽の水位が前記下流側槽の水位よりも高くなった場合に、両槽の水頭差により、前記揺動板が、垂下姿勢になり、前記仕切壁の周縁部に押圧され、前記開口部を覆うとともに前記開口部周縁部により前記下流側槽側への揺動が規制される。このとき、前記上流側槽の水位が急激に上昇して、前記揺動板の上端部よりも高水位に達すると、その揺動板の上端部側よりも上方の被処理水は、その揺動板の上方側を溢流部として前記下流側槽へ移流することになる。ここで、移流させられる被処理水は、通常負荷が少ないため、大量移流した被処理水の移流を緩和しつつ、かつ、負荷の少ない被処理水の早期移流を促すこととなり、被処理水の処理の適正化が図れる。また、上流側槽の被処理水の水位が前記揺動板の上端部に達しない場合でも、前記水位が前記通水口よりも上部にあれば、前記通水口により溢流部が形成されるようになる。すると、前記開口部は狭められ、水頭差の関係から前記上流側槽の被処理水は優先的に前記通水口を通過するので、前記下流側槽から上流側槽への被処理水の返送を抑制しながら、前記上流側槽からの被処理水の移流を図れることになる。
つまり、前記上流側槽と下流側槽との関係に基づき、適切な被処理水の循環をはかり、外部環境に放出される水質をより一層浄化できることになる。
一方、前記上流側槽の水位が前記下流側槽の水位と同等になった場合には、前記揺動板の揺動に伴って、前記上流側槽と前記下流側槽との間で双方向の被処理水の移流が起きやすい状況が作られる。そのため、浮遊汚泥の返送循環が効率よくはかられるとともに、水処理の効率化を図りやすくできる。
【0009】
【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及び担体濾過槽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、担体濾過槽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T1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。
【0010】
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に溢流で送られる。前記嫌気濾床槽第二室N2と、前記担体流動槽E1との間は溢流部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、その溢流部1は櫛歯状に形成してある開口部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内の担体が逆流するのを防止可能に構成してある。前記開口部は、下端を前記嫌気濾床槽第一室N1の最低水位に設け、上端を前記嫌気濾床槽第二室N2の最高水位以上にまで延設してある。
【0011】
前記嫌気濾床槽第二室N2と、前記担体流動槽E1との間の仕切壁W0において前記開口部2の上流側槽に相当する前記嫌気濾床槽第二室N2側には、図3に示すように、前記開口部2よりも狭い通水口aを形成してある揺動板Xを設け、前記揺動板を、前記上流側槽側に揺動自在に取り付け、揺動姿勢で前記開口部2が開口状態になり溢流部2aが形成され、垂下姿勢で前記開口部2を覆うとともに、前記開口部2周縁部により前記下流側槽である担体流動槽E1側への揺動が規制され、かつ、前記通水口aにより溢流部2aが形成されるように設けてある。
さらに、前記揺動板Xの上端部に、前記嫌気濾床槽第二室N2の水位が上昇した場合に、前記上流側槽から前記下流側槽に被処理水を溢流させる溢流部2aを形成してあるとともに、前記浄化槽内に大量の被処理水の原水が流入したような場合には、前記溢流部2aからの被処理水の溢流により、前記上流側槽の水位が前記揺動板Xの上方側の所定位置で規制される構成としてある。
【0012】
具体的には上下長さ100mm幅10mmのスリットが、多数形成されている開口部2の下部を覆う揺動板Xを設けて、その上端部の水平軸心周りに揺動自在に取付け、その揺動板Xの上下方向の中央部には、直径13〜20mmの孔部を形成して通水口aを設けてある。この通水口は前記揺動板Xの幅方向に多数並設してあり、流量抑制が可能になるように設定してある。これにより、前記通水口aを通過した被処理水が、前記開口部2を通過して前記上流側槽から下流側槽に移流する構成としてある。
【0013】
これにより、前記嫌気路床槽N2の水位が、低位置にある場合は、被処理水が、前記通水口aを越えないレベルで維持され、被処理水の流通のない状態で水処理され、
定常位置にある場合は、前記揺動板が、前記下流側槽内の散気装置によるバブリングの影響等により容易に揺動して、前記開口部を溢流部として、前記担体流動槽E1と前記嫌気濾床槽第二室N2との間で、被処理水の流動があり、浮遊汚泥の返送が良好に行われ、
高位置にある場合は、前記揺動板が前記開口部を覆い、揺動規制された状態になりながら、前記通水口を介して前記嫌気濾床槽第二室N2N1から前記担体流動槽への被処理水移流が緩やかに行われる。
さらに水位が上昇した場合には、被処理水が前記揺動板の上端部を溢流部として比較的急激に行われることになる。そのため、大量流入し微生物処理のあまり必要のない被処理水の早期処理を行えるようになる。
【0014】
従って、前記水位が低位置の状態から高位置の状態までの空間が浄化槽に対して被処理水が大量流入した場合にその被処理水を一時貯留する貯留空間として働くことになる。
【0015】
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、隣接する担体濾過槽E2とを仕切る第一隔壁W1に設けた移流壁部3を通じて、前記担体濾過槽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。
【0016】
前記担体濾過槽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、前記担体濾過槽E2とその担体濾過槽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、前記担体濾過槽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、前記担体濾過槽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に散気して前記担体濾過槽E2内を攪拌する攪拌装置としての逆洗管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、前記逆洗管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、前記逆洗管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。
【0017】
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。
【0018】
さらに、前記処理水槽T1には、図2,3に示すように、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、前記担体濾過槽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。
【0019】
また、前記担体流動槽E1及び担体濾過槽E2の定常水位よりもやや下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が他槽に流出しないように流出防止する担体保持部材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、浄化槽の周壁あるいは隔壁に接着固定してある。また、前記担体保持部材10には、一部に開口12を設けるとともに、開閉自在な蓋部材13a を流出防止部材13として前記開口を開閉自在に取付けて開閉機構を形成してある。
これにより、前記担体流動槽E1及び担体濾過槽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、前記担体保持部材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及び担体濾過槽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、被処理水を引き抜き水位を低下させた後、前記開口12を担体投入部として用い、容易に担体を投入、吸出しが可能となるので、容易にメンテナンスできる構成となっている。
【0020】
さらに、前記担体保持部材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14を蓋する流出防止部材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、前記担体濾過槽B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。
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D1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、前記担体保持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。
【0021】
前記処理水槽T1では、被処理水のうち前記担体濾過槽E2を通過した清浄な上澄み部のみを外部に放流可能にするとともに、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。
【0022】
これにより、前記担体流動槽E1および担体濾過槽E2は、上方空間から容易に担体交換出来る状態に配置されるため、メンテナンスの際には、前記浄化槽内を大幅に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。
【0023】
〔別実施の形態〕
先の実施の形態では、担体流動槽E1と、嫌気濾床槽第二室N2との間に揺動板を採用したが、これに限らず、急激な被処理水移流に対して流量調整して移流水量を安定化させる必要のある槽と、その上流側槽との間を仕切る仕切壁W0に採用してもよい。いずれにしても、被処理水移送ポンプを設けなくても、上流側槽と下流側槽との間で被処理水の穏やかな移送を維持しつつ被処理水を貯留し、さらに、被処理水の大量流入時には、溢流を許容し、前記上流側槽の貯水量を緩和することのできる構成が達成できる。
このような場合、前記開口部は、スリット状に設けてある以外に、単に前記仕切壁W0を切り欠き、その一部に揺動板を設けてあってもよい。
【0024】
また、図5に示すように、嫌気濾床槽第一室N1と、嫌気濾床槽第二室N2との間に、被処理水を定常的に移送する移送ポンプA2を設けてあってもよく、このような場合、浄化槽内への被処理水の原水流入が少ない時期に、被処理水を下流側の嫌気濾床槽第二室N2に移送処理し、被処理水の大量流入を許容する被処理水貯留空間Sを形成自在にする構成を採用しても良い。このような構成によると被処理水の原水流入の少ない時期には、嫌気濾床槽第一室N1内の水位は、LWLまで低下し、被処理水の原水大量流入を受け入れ可能な状態を形成するとともに、被処理水の大量流入を受けて水位がHWLにまで達したときには、先の実施の形態同様に被処理水の処理効率の適正化が図れる事になり、さらに、被処理水の原水流入に対する緩衝能力を向上させられる。
【図面の簡単な説明】
【図1】浄化槽の縦断側面図
【図2】浄化槽の要部斜視図
【図3】浄化槽の要部断面図
【図4】揺動板の作用説明図
【図5】別実施の形態の浄化槽の縦断側面図
【符号の説明】
X 揺動板
W0 仕切壁
2 開口部
a 通水口
2a 溢流部[0001]
BACKGROUND OF THE INVENTION
In the present invention, a plurality of water treatment tanks are arranged side by side, and an overflow portion for overflowing the water to be treated from the upstream tank to the downstream tank is provided in a partition wall that partitions the upstream tank and the downstream tank. The present invention relates to a partition wall structure of a septic tank.
[0002]
[Prior art]
Conventionally, the partition wall of the septic tank is formed with an opening at a predetermined position of the partition wall or a notch from the upper end side of the partition wall so that the steady water level of the upstream tank is located at the lower end. What is known.
In addition, a swing plate capable of closing the opening is provided in the opening to prevent backflow of the water to be treated from the downstream tank to the upstream tank, and the swing plate is connected to the downstream tank. swingably to the side, the opening in the swing posture overflow portion becomes an opening state is formed, the by Ri before SL on the upstream side tank opening peripheral portion covers the opening in the hanging position There are known ones that are configured to be restricted from swinging to the side.
[0003]
[Problems to be solved by the invention]
According to the structure of the partition wall of the former septic tank where the overflow part is formed simply by forming an opening as described above, when a large amount of raw water to be treated flows into the septic tank, it is regulated by the opening. The water level becomes higher than the water level to be treated, and the space in which the water to be treated circulates between the upstream side tank and the downstream side tank becomes large. Will occur.
[0004]
However, when there is a large inflow of water to be treated in this way, it is necessary to allow the inflow of water to be treated from the upstream side tank to the downstream side tank. In the case of an aerobic tank, the sludge is returned from the downstream tank to the upstream tank in large quantities because it is necessary to maintain the sludge concentration at a relatively high level. It is not preferable to perform the treatment water treatment stably, and it is necessary to suppress the backflow circulation of the sludge.
[0005]
Therefore, in order to prevent such a tendency, a configuration in which the swing plate is provided is adopted. However, in this case, even when a large amount of water to be treated is received, the advection of the water to be treated is In order to form the latter so as to occur from the upstream side tank toward the downstream side tank, the latter structure provided with the swing plate is considered. In such a case, the upstream side tank and the downstream side are considered. If the tank is maintained at a level that is slightly higher than the level regulated by the opening, the water to be treated cannot be steadily returned and transferred, An unfavorable situation is also assumed when performing biological treatment.
In addition, when a large amount of the water to be treated exceeds the maximum amount assumed at the time of design, a large amount of the water to be treated is directly affected by the downstream side tank. It is also necessary to buffer large inflows of treated water.
Therefore, an opening is provided in the partition wall, and the upstream tank and the downstream tank are simply partitioned in a state where they are at a steady water level, and water to be treated between the upstream tank and the downstream tank is configured. All the advection is borne by the treated water transfer means such as an air lift pump, and the upstream tank is configured to be able to temporarily store a large amount of treated water into the tank to buffer the adverse effects on the downstream tank. However, it has been studied to maintain the return of the sludge component from the downstream tank well, but the structure of the septic tank becomes complicated and the initial equipment cost is increased due to the provision of the treated water return means. There was an inconvenience that the operating cost was expensive.
[0006]
Therefore, in view of the above-mentioned drawbacks, the object of the present invention is to provide an ordinary tank while buffering in the upstream tank even when there is a large amount of water to be treated in the septic tank due to the improvement of the partition wall and a simple and inexpensive configuration. It is in the point which provides the septic tank which can perform the to-be-processed water treatment stable sometimes.
[0007]
[Means for Solving the Problems]
In order to achieve this object, the characteristic configuration of the partition wall structure of the septic tank of the present invention includes a plurality of water treatment tanks arranged side by side, and a partition wall that partitions an upstream tank and a downstream tank from the upstream tank to the partition wall. water to be treated on the downstream side tank a partition wall structure of the septic tank provided with an overflow section for overflow, the openings provided in the partition wall, swinging it has a narrow water passage opening than the opening A moving plate is provided, and the swing plate is swingably attached to the upstream tank side, and the opening portion is opened and an overflow portion is formed in the swinging posture, and at least the opening portion is formed in the hanging posture. together with part of the cover, the swing of the opening peripheral edge portion by Ri front Symbol downstream tank side is restricted, and the opening degree of the opening is restricted, the through water outlet is formed in the overflow portion Furthermore, when the water level of the upstream tank rises above the swing plate, the upstream side Lies in is formed an overflow section for overflow of the treated water into the downstream vessel from.
[0008]
[Function and effect]
In other words, a septic tank in which a plurality of water treatment tanks are arranged side by side, and an overflow section is provided on the partition wall that separates the upstream tank and the downstream tank from the upstream tank to overflow the treated water from the upstream tank. In this case, if an aeration device is provided in the downstream tank, the downstream tank can perform aerobic treatment of the water to be treated, and the generated sludge can be suspended in the upstream tank.
Here, if the partition wall is provided with an opening, natural advection of the water to be treated from the upstream side tank to the downstream side tank can be achieved, and the upstream side tank side is swingably attached, the opening is overflow portion is formed becomes the opening state, covers at least a portion of the opening in the hanging position, the swing of the opening peripheral edge portion by Ri front Symbol downstream tank side is restricted And if the opening degree of the said opening part is restrict | limited and the rocking | fluctuation plate is provided so that the said water flow opening may be formed in an overflow part, the water level of the said upstream tank is higher than the water level of the said downstream tank. The swinging plate is in a suspended position due to the difference in water head between the two tanks, and is pressed against the peripheral edge of the partition wall to cover the opening and the downstream side by the peripheral edge of the opening. Swinging to the tank side is restricted. At this time, when the water level of the upstream tank rises rapidly and reaches a higher water level than the upper end of the swing plate, the water to be treated above the upper end of the swing plate is swung. The upper side of the moving plate is transferred to the downstream tank as an overflow portion. Here, the treated water to be advected has a low normal load, so that the advection of the treated water with less load is promoted while relaxing the advection of the treated water that has been abundantly transferred. Processing can be optimized. In addition, even when the water level of the water to be treated in the upstream tank does not reach the upper end of the swing plate, if the water level is above the water inlet, an overflow portion is formed by the water inlet. become. Then, the opening is narrowed, and the treated water in the upstream side tank preferentially passes through the water flow port due to the difference in water head, so that the treated water is returned from the downstream side tank to the upstream side tank. While suppressing, the advection of the to-be-processed water from the said upstream tank can be aimed at.
That is, based on the relationship between the upstream tank and the downstream tank, the water to be treated is appropriately circulated, and the water quality released to the external environment can be further purified.
On the other hand, when the water level of the upstream tank becomes equal to the water level of the downstream tank, the two-way between the upstream tank and the downstream tank is accompanied by the swing of the swing plate. The situation where the advection of to-be-treated water tends to occur is created. Therefore, the return circulation of floating sludge can be efficiently carried out, and the efficiency of water treatment can be facilitated.
[0009]
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 includes an anaerobic treatment tank N, an aerobic treatment tank E, a treated water tank T1, and the like from the upstream side, and the anaerobic treatment tank N is an anaerobic filter bed tank first chamber. N1 and the anaerobic filter bed tank second chamber N2, and the aerobic treatment tank E includes a carrier fluidization tank E1 and a carrier filtration tank E2. The raw water to be treated flows from the raw water inflow part I into the first anaerobic filter bed tank N1, and in the order of the anaerobic filter bed tank second chamber N2, the carrier flow tank E1, the carrier filter tank E2, and the treated water tank T1. It is decomposed while being transferred downstream, passes through a disinfection tank Q provided above the treated water tank T1, and then discharged from the discharge port Z to the outside of the tank.
[0010]
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. Further, 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 fluidization tank E1 as an overflow. Between the anaerobic filter bed second chamber N2 and the carrier flow tank E1, the overflow portion 1 is configured to allow natural flow of the water to be treated, and the overflow portion 1 is formed in a comb shape. The
[0011]
In the anaerobic filter bed tank second chamber N2 side corresponding to the upstream tank of the
Further, the upper end portion of the swing plate X, before SL when the water level in the anaerobic filter bed chamber second chamber N2 rises, the overflow portion to the overflow water to be treated to said downstream vessel from the
[0012]
Specifically, an oscillating plate X that covers the lower part of the
[0013]
Thereby, when the water level of the anaerobic roadbed tank N2 is at a low position, the water to be treated is maintained at a level not exceeding the water inlet a, and the water is treated without the flow of the water to be treated.
When in the steady position, the swinging plate easily swings due to the bubbling effect of the air diffuser in the downstream side tank, and the opening is used as an overflow part. Between the anaerobic filter bed tank second chamber N2, there is a flow of water to be treated, and the return of floating sludge is satisfactorily performed,
When in the high position, the swing plate covers the opening and is in a swing-controlled state, while the anaerobic filter bed second chamber N2N1 passes through the water inlet to the carrier flow tank. The treated water advection is performed slowly.
When the water level further rises, the water to be treated is relatively abruptly used with the upper end portion of the swing plate as an overflow portion. For this reason, it becomes possible to perform early treatment of water to be treated that flows in a large amount and does not require much microbial treatment.
[0014]
Therefore, when a large amount of water to be treated flows into the septic tank, the space between the low water level and the high water state serves as a storage space for temporarily storing the water to be treated.
[0015]
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 carrier filtration tank E2 through the advection wall portion 3 provided in the first partition wall W1 that partitions the carrier flow tank E1 and the adjacent carrier filtration tank E2. .
The advection wall portion 3 is formed in a lattice shape or a slit shape, and is configured to prevent the advancing of the carrier but to permit the advancing of sludge and water to be treated.
[0016]
The carrier 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. Further, a filtration for allowing the water to be treated to flow freely at a position lower than the predetermined height of the second partition wall W2 separating the carrier filtration tank E2 and the treated water tank T1 provided adjacent to the carrier filtration tank E2. A
The
Further, a backwash pipe D2 as a stirring device for agitating the inside of the carrier filtration tank E2 by aeration of the carrier C2 is provided at the lower part of the deposited filtration layer B to be constructed. The carrier can be regenerated by performing aeration from the backwash tube D2 in a time zone when the inflow of the load is small.
In addition, the backwash pipe D2 diffuses toward the advection wall portion 3, 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 aeration part Da configured to be raised and the air diffused toward the filtration wall part in the same manner, and air bubbles caused by the aeration pass through the
[0017]
Here, the advection wall part 3 and the
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.
[0018]
Further, as shown in FIGS. 2 and 3, 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, which is generated by the regeneration of the carrier C2. The sludge can be transferred together with the water to be treated from the inside of the carrier filtration tank E2 to the anaerobic filter bed tank first chamber N1.
[0019]
Moreover, even if a large amount of water to be treated flows into the septic tank slightly below the steady water level of the carrier flow tank E1 and the carrier filtration tank E2, the carrier C1 in the tank flows out so as not to flow into other tanks. The
Thereby, even if air is diffused into the carrier flow tank E1 and the carrier filtration tank E2 to form convection of the water to be treated, the flow is formed so as to flow smoothly without being inhibited by the
[0020]
Further, the
Thereby, even when it is necessary to take the diffuser tube out of the septic tank, for example, when performing maintenance of the diffuser tube D1, the diffuser tube D1 can be easily inserted and removed through the diffuser
[0021]
In the treated water tank T1, only the clean supernatant part that has passed through the carrier filtration tank E2 in the treated water can be discharged to the outside, and flows into the disinfecting tank Q provided in the upper part, and the solid disinfectant Q1 After contact is disinfected, it is discharged out of the tank.
[0022]
As a result, the carrier flow tank E1 and the carrier filtration tank E2 are arranged in a state in which the carrier can be easily replaced from the upper space. Therefore, during maintenance, the septic tank is not greatly decomposed and the like. It can be easily performed from the upper side through a manhole H provided at the top.
[0023]
[Another embodiment]
In the previous embodiment, the swing plate was adopted between the carrier flow tank E1 and the anaerobic filter bed second chamber N2. However, the present invention is not limited to this, and the flow rate is adjusted for abrupt water advection. Thus, the partition wall W0 may be used to partition between the tank that needs to stabilize the amount of advection water and the upstream tank. In any case, the treated water is stored while maintaining the gentle transfer of the treated water between the upstream tank and the downstream tank without providing the treated water transfer pump. When a large amount of water flows in, it is possible to achieve a configuration that allows overflow and relaxes the amount of water stored in the upstream tank.
In such a case, in addition to providing the opening in a slit shape, the partition wall W0 may be simply cut out and a swing plate may be provided in a part thereof.
[0024]
Moreover, as shown in FIG. 5, even if the transfer pump A2 which steadily transfers to-be-processed water is provided between the anaerobic filter bed tank first chamber N1 and the anaerobic filter bed tank second chamber N2. Well, in such a case, when the raw water inflow of the treated water into the septic tank is small, the treated water is transferred to the second anaerobic filter bed second chamber N2 on the downstream side, and a large amount of treated water is allowed to flow. You may employ | adopt the structure which makes the to-be-processed water storage space S formed freely. According to such a configuration, the water level in the first chamber N1 of the anaerobic filter bed tank is lowered to LWL at a time when the raw water inflow of the treated water is small, and a state in which a large amount of raw water inflow of the treated water can be accepted At the same time, when the water level reaches HWL due to a large inflow of water to be treated, the treatment efficiency of the water to be treated can be optimized as in the previous embodiment. Buffer capacity against inflow can be improved.
[Brief description of the drawings]
FIG. 1 is a vertical side view of a septic tank. FIG. 2 is a perspective view of the main part of the septic tank. FIG. 3 is a cross-sectional view of the main part of the septic tank. Vertical side view
X Swing plate
Claims (2)
前記仕切壁に開口部を設け、
前記開口部よりも狭い通水口を形成してある揺動板を設け、
前記揺動板を、前記上流側槽側に揺動自在に取り付け、揺動姿勢で前記開口部が開口状態になり溢流部が形成され、垂下姿勢で前記開口部の少なくとも一部を覆うとともに、前記開口部周縁部により前記下流側槽側への揺動が規制され、かつ、前記開口部の開口度が制限されて、前記通水口が溢流部に形成されるように設けてある浄化槽の仕切壁構造。A partition of a septic tank in which a plurality of water treatment tanks are arranged in parallel and an overflow portion is provided on a partition wall that separates the upstream tank and the downstream tank from the upstream tank to overflow the treated water from the upstream tank. A wall structure,
An opening is provided in the partition wall,
The swinging plate is provided that is formed a narrow water passage opening than the opening,
The swing plate is swingably attached to the upstream tank side, and the opening is in an open state in a swinging posture to form an overflow portion, and at least a part of the opening is covered in a hanging posture. swinging Previous Symbol downstream tank side Ri by the opening peripheral edge portion is restricted, and the opening degree of the opening is restricted, provided as the through Mizuguchi is formed overflow portion partition wall structure of the septic tank are.
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JP2000003300A JP3768054B2 (en) | 2000-01-12 | 2000-01-12 | Septic tank partition wall structure |
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JP2000003300A JP3768054B2 (en) | 2000-01-12 | 2000-01-12 | Septic tank partition wall structure |
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JP3768054B2 true JP3768054B2 (en) | 2006-04-19 |
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