JP4046488B2 - Merged septic tank - Google Patents

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JP4046488B2
JP4046488B2 JP2001197950A JP2001197950A JP4046488B2 JP 4046488 B2 JP4046488 B2 JP 4046488B2 JP 2001197950 A JP2001197950 A JP 2001197950A JP 2001197950 A JP2001197950 A JP 2001197950A JP 4046488 B2 JP4046488 B2 JP 4046488B2
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tank
casing
water
treated
treatment
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JP2003010870A (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】
本発明は、少なくとも被処理水を好気処理する好気処理槽を内装する単独処理浄化槽である第一ケーシングから、被処理水を活性汚泥処理する活性汚泥処理槽を内装する第二ケーシングへと被処理水が移流自在になるように設けてある合併浄化槽に関する。
【0002】
【従来の技術】
従来、一般用の生活排水を処理する浄化槽としては、処理対象排水がし尿排水だけとする単独処理浄化槽と、処理対象排水がし尿排水だけでなく生活雑排水も処理可能な合併浄化槽が用いられている。
【0003】
単独処理浄化槽においては、処理対象排水がし尿排水のみであるので、台所、洗濯、浴室等から生じる生活雑排水はそのまま放流されており、湖沼等の閉鎖水域の水質汚濁の大きな原因となっている。この生活雑排水を適切に処理することは、閉鎖水域の水質汚濁の軽減に大きく貢献することは明らかであり、さらに、環境意識の向上に伴う水質の規制強化等により河川等に放流される排水の水質を向上させる浄化槽が望まれていた。そこで、単独処理浄化槽から、処理対象排水がし尿排水だけでなく生活雑排水も処理可能である合併浄化槽を用いることが考えられており、これにより、高い水質基準を満足させることができるようになっている。さらに、このような状況の下、単独処理浄化槽の新設廃止と、既設単独処理浄化槽の合併処理化を実現するための対策が模索されている。既設単独処理浄化槽の合併処理化を行うケースとしては、例えば、単独処理浄化槽を設置して間も無い、あるいは、土地の面積、形態等から既設の単独処理浄化槽を有効に活用して合併処理化をした方がよい時等が考えられる。
【0004】
このような既設単独処理浄化槽の合併処理化を実現した浄化槽としては、図4に示したように、既設単独処理浄化槽と、既設単独処理浄化槽とは別に地上設置された膜分離活性汚泥処理を行う後設の処理槽とを接続して合併処理可能にしたものが知られている(特開平11−169872号公報参照)。
【0005】
この既設単独処理浄化槽の合併処理化を実現した浄化槽は、流入口1から被処理水の原水が沈殿分離室2に流入するとともに、ばっ気室3、沈殿室4、消毒室5の順に下流へ移送されつつ分解処理されるように設けてある地下埋設の単独処理浄化槽7において、前記単独処理浄化槽7とは別に膜モジュール8と、前記膜モジュール8の下方に設置される散気管9とを有した膜処理槽10を地上設置し、前記ばっ気室3と前記膜処理槽10とを汚水汲上用のポンプ11を有した移送管12で連通させ、前記膜モジュール8と前記消毒槽5とを流出管13にて連通し、前記膜処理槽10底部と前記沈殿分離室2とを弁14を有した余剰汚泥返送管15にて連通して構成されていた。
【0006】
このような合併浄化槽において、生活雑排水及びし尿排水は、配管16、17から流入口1を介して前記沈殿分離室2に流入し、前記沈殿分離室2にて固液分離が行われる。固液分離した後の上澄み液は、前記ばっ気室3へと流入し、前記ポンプ11により前記移送管12を介して前記膜処理槽10へ流入させる。この時、前記ばっ気室3は、固液分離した後の上澄み液の流量を調整するための流量調整槽として機能するものであるため、単独処理浄化槽のみで用いられていた時のように、前記ばっ気室3内に接触材を設けて好気処理を行う必要はない。
前記膜処理槽10は、内部に前記膜モジュール8及び前記散気管9を内蔵しており、前記膜処理槽10上方に接続した前記移送管12から前記膜処理槽10に流入した上澄み液は、前記膜モジュール8にてミクロンサイズの固液分離を行い、前記流出管13より分離した処理水を前記消毒槽5へと移流させる。そして、前記消毒槽5に移流させた処理水は、塩素剤により滅菌処理を施した後に、流出口6より系外に放流される。
前記膜モジュール8にて前記消毒槽5へと移流しない汚泥は、前記膜モジュール8下方に設置した前記散気管9からの空気供給を受け、好気処理が行われる。しかし、全ての汚泥が好気処理により分解されることは少ないので、前記膜処理槽10底部に沈殿した汚泥(余剰汚泥)は、前記弁14を開弁し、前記余剰汚泥返送管15により、前記沈殿分離室2へと移送されるのである。
【0007】
このように既設単独処理浄化槽を有効活用して膜分離活性汚泥処理を行う膜処理槽を付設するだけで、活性汚泥処理されて十分BODの低下した被処理水を効率よく固液分離し、汚水を高度に浄化することが可能である合併浄化槽とすることができ、家庭から出される全ての生活排水を効率的に浄化し、放水基準値に適合するように処理することができる。
【0008】
【発明が解決しようとする課題】
上述した従来の合併浄化槽においては、既設単独処理浄化槽の前記ばっ気室が、後設の処理槽に対する流量調整槽として利用されていた。つまり、前記流量調整槽として機能させるばっ気室が、朝夕の特定時間に集中する流入処理水量のピーク量を吸収する構成としてあるために、通常は被処理水の水位を低水位LWL付近に抑える必要がある。そのため、前記ばっ気室空間の大部分は空の状態となり、地中埋設された既設単独処理浄化槽周囲の土圧の影響を受け易く、既設単独処理浄化槽の変形や破損の虞があった。このような既設単独処理浄化槽の変形や破損を避けるため、前記ばっ気室内部等において補強をすることが考えられるが、既設単独処理浄化槽内での補強作業が煩雑である点や、補強コストがかかるという点が障害となるため、既設単独処理浄化槽に手を加えて補強をすることは現実的にかなり困難であり、さらに、補強をしたとしても、長期的に耐え得るか疑問が残るという問題点があった。
【0009】
また、上述した合併浄化槽において、既設単独処理浄化槽に付設する後設の処理槽は、設置の際の工事費用や労力、更にメンテナンス時の負担等を考慮して地上又は半地上に設置される場合が多い。このような地上又は半地上に設置される処理槽は、主に、FRP(ガラス繊維強化プラスチック)やDCPD(ジシクロペンタジェン)等のプラスチックで形成されていた。また、前記処理槽は、温暖地においては、耐候性塗料を前記処理槽外表面に塗布し、寒冷地においては、前記処理槽の周囲を土盛りあるいはブロックで囲い土砂で覆うといった土木仕上げを施すことにより、周囲環境から保護されていた。
【0010】
しかし、前述のプラスチック製の処理槽においては、以下のような問題点があった。
(a)耐候性塗料を前記処理槽外表面に塗布したとしても、前記耐候性塗料が経年劣化して剥落する場合があった(耐候劣化)。このような劣化が生じると、前記FRPを用いた処理槽の場合は、樹脂が退化したり、ガラス繊維が露出したりする不都合を生じ易く、前記DCPDの場合は、表面が荒れたり、脆化が進行するという不都合が生じ易い。
(b)前記耐候劣化に加えて経時的なクリープ変形が生じるため、長期信頼性に欠ける(長期信頼性の欠如)。
(c)外的衝撃による破損の恐れがある(耐衝撃性の欠如)。
(d)前記処理槽のフレームは厚さ数ミリの板厚にすぎないため、冬期においては(特に寒冷地において)、外気の影響が前記処理槽内の微生物の活性を低下させる虞があり、さらに、前記処理槽内が凍結する虞がある。(断熱特性の欠如)。
【0011】
上記(a)耐候劣化、(b)長期信頼性の欠如については、前記処理槽のフレームにステンレス(sus)構造を採用することにより解決可能となるのであるが、この場合においても、(c)耐衝撃性の欠如、(d)断熱特性の欠如の問題点を解決するには至らなかった。また、前記ステンレス構造にした場合は、前記処理槽の製造コストが高価になるという欠点があった。
【0012】
また、(d)断熱特性の欠如の問題点は、発泡材等の断熱材を使用して前記処理槽の断熱特性を向上させることが考えられるが、この場合も前記処理槽の製造コストが高価になるという欠点があった。また、前述のように土木仕上げを施すことにより前記処理槽を周囲環境から保護することが考えられるが、これは労力がかかり、さらに施工のためのコストがかかるという問題点があった。
【0013】
従って、本発明の目的は、既設の単独処理浄化槽をそのまま活用するか、あるいは簡便な改造を施した状態で活用することができ、かつ外環境に対する耐性が高い合併浄化槽を提供することにある。
【0014】
【課題を解決するための手段】
〔構成1〕
この目的を達成するための本発明の特徴構成は、請求項1に記載のように、
少なくとも被処理水を好気処理する好気処理槽を内装する単独処理浄化槽である第一ケーシングから、被処理水を活性汚泥処理する活性汚泥処理槽を内装する第二ケーシングへと被処理水が移流自在になるように設けてある合併浄化槽において、
生活雑排水を流入させる生活雑排水配管が前記第二ケーシングに接続してあると共に、前記第二ケーシングに、被処理水を貯留して流量を調整する流量調整槽を前記活性汚泥処理槽の上流に設けてあると共に、夾雑物を除去する夾雑物除去槽を前記流量調整槽の上流に設けてあり、前記好気処理槽の曝気を停止してある点にあり、その作用効果は以下の通りである。
【0015】
〔作用効果1〕
つまり、生活雑排水を流入させる生活雑排水配管が前記第二ケーシングに接続してあるため、台所、洗濯、浴室等から生じる排水である生活雑排水は、前記第二ケーシングに直接流入させることができる。そのため、既設単独処理浄化槽である前記第一ケーシングにおいて被処理水の流量を調整する必要が無くなり、前記好気処理槽において接触材等の部材が設けられている状態のまま活用できる。この時、既設単独処理浄化槽である前記第一ケーシングは、し尿排水のみを受入れ、前記好気処理槽では比較的高水位である通常水位のまま処理を行うことができる。そのため、前記好気処理槽空間の大部分が空の状態になることは殆ど無くなり、前記好気処理槽内部の被処理水の水圧が既設単独処理浄化槽周囲の土圧と拮抗状態を保つことができるため、既設単独処理浄化槽の変形や破損の虞はほとんどなくなるのである。そのため、既設単独処理浄化槽の強度を増すための補強工事をすることなく、既設単独処理浄化槽をそのまま活用することができる。この時、一般的には、前記好気処理槽へのばっ気を停止した状態で使用するため、既設単独処理浄化槽を沈澱分離槽あるいは嫌気処理槽として用いることになる。
【0016】
そして、既設単独処理浄化槽である前記第一ケーシングは、し尿排水中の固体成分を沈殿させることにより分離させる沈澱分離槽としての機能を発揮した後、負荷の低減した被処理水を後設の前記第二ケーシングに自然移流させることができるのである。
【0017】
また、前記第二ケーシングにおいて、被処理水を貯留して流量を調整する流量調整槽を前記活性汚泥処理槽の上流に設けることにより、前記第二ケーシングに直接流入した生活雑排水の流入負荷を緩衝することができ、これにより、朝夕の特定時間に集中する流入処理水量のピーク量を吸収することができる。そのため、前記活性汚泥処理槽の活性汚泥処理を安定して行うことができる。
【0018】
このように、前記第二ケーシングにおいて生活雑排水の流入負荷を緩衝する前記流量調整槽を設けることにより、既設単独処理浄化槽において被処理水の流量調整を行う必要がないため、既設単独処理浄化槽をそのまま活用することができる。そのため、少なくとも被処理水を好気処理する好気処理槽を内装する単独処理浄化槽が既に設置されている状況において生活雑排水の合併処理化を行う際には、上述の構成を有する第二ケーシングのみを付設設置して既設単独処理浄化槽に接続すればよいので、新たに合併浄化槽を敷設するのに比べて、設置労力やコストが低減できる。さらに、既設単独処理浄化槽を掘り起こした時の廃棄物処理の問題を回避できる。
【0019】
さらに、上述の構成を有する第二ケーシングを既設単独処理浄化槽に接続した場合は、前記移送管、前記流出管、前記余剰汚泥返送管といった複数の配管で接続する必要が無いため、複雑な配管工事を行う必要が無く、その分設置労力やコストが低減できる
また、前記第二ケーシングにおいて、夾雑物を除去する夾雑物除去槽を前記流量調整槽の上流に設けることにより、前記第二ケーシングに流入した食物残渣等の夾雑物を除去することができる。
また、前記夾雑物除去槽が前記流量調整槽の上流に設けられているため、前記夾雑物除去槽は前記活性汚泥処理槽の上流に設けられることになる。これにより、前記活性汚泥処理槽に夾雑物が流入することはほとんど無くなり、前記活性汚泥処理槽内における活性汚泥処理に悪影響を与える可能性が低くなる。つまり、前記活性汚泥処理槽では、前記活性汚泥処理槽内に負荷が大きく好気処理されにくい固形分等が流入しにくい状態で活性汚泥処理が進行することになるので、前記活性汚泥処理槽の水処理能力をより高く維持できる。そのため、前記活性汚泥処理槽での処理効率の向上が期待される。
【0020】
〔構成
この目的を達成するための本発明の特徴構成は、請求項に記載のように、
少なくとも被処理水を好気処理する好気処理槽を内装する単独処理浄化槽である第一ケーシングから、被処理水を活性汚泥処理する活性汚泥処理槽を内装する第二ケーシングへと被処理水が移流自在になるように設けてある合併浄化槽において、
生活雑排水を流入させる生活雑排水配管が前記第一ケーシングに接続してあると共に、前記第二ケーシングに対して、被処理水を貯留して流量を調整する流量調整槽を前記活性汚泥処理槽の上流に、夾雑物を除去する夾雑物除去槽を前記流量調整槽の上流にそれぞれ設けてある点にあり、その作用効果は以下の通りである。
【0021】
〔作用効果
つまり、生活雑排水を流入させる生活雑排水配管が前記第一ケーシングに接続してあることにより、生活雑排水は、前記第一ケーシングにし尿排水と共に流入する。そして、前記第一ケーシングは、し尿排水中の固形分の沈殿分離や、し尿排水中のトイレットペーパー等の夾雑物、及び生活雑排水中の食物残渣等の夾雑物を沈殿除去する夾雑物除去槽としての機能を発揮した後、被処理水を後設の前記第二ケーシングに自然移流させることができるのである。つまり、前記第一ケーシングにおいて夾雑物除去等の前処理をされた被処理水を前記第二ケーシングの前記活性汚泥処理槽で活性汚泥処理することができるので、前記活性汚泥処理槽では、負荷が大きく好気処理されにくい夾雑物等の固形分が流入しにくい状態で活性汚泥処理が進行することになるので、前記活性汚泥処理槽の水処理能力をより高く維持できる。
また、生活雑排水配管の前記第一ケーシングへの接続は、後述の実施例2で記載したように前記第一ケーシングに生活雑排水流入口を開けるといった簡単な改造を加えるだけで行うことができる。
【0022】
また、前記第二ケーシングにおいて、被処理水を貯留して流量を調整する流量調整槽を設けてあることから、前記第一ケーシングに流入した生活雑排水の流入負荷を前記第二ケーシングの前記流量調整槽において緩衝することができるため、既設単独処理浄化槽である前記第一ケーシングにおいて被処理水の流量を調整する必要が無くなり、前記好気処理槽において接触材等の部材が設けられている状態のまま活用できるのであるから、既設単独処理浄化槽の前記好気処理槽では比較的高水位である通常水位のまま処理を行うことができる。そのため、前記好気処理槽空間の大部分が空の状態になることは殆ど無くなり、前記好気処理槽内部の被処理水の水圧が既設単独処理浄化槽周囲の土圧と拮抗状態を保つことができるため、前記既設単独処理浄化槽の変形や破損の虞はほとんどなくなるのである。そのため、前記既設単独処理浄化槽の強度を増すための補強工事をすることなく、前記既設単独処理浄化槽をそのまま活用することができる。この時、一般的には、前記好気処理槽へのばっ気を停止した状態で使用するため、既設単独処理浄化槽を沈澱分離槽あるいは嫌気処理槽として用いることになる。
【0023】
また、前記流量調整槽が前記活性汚泥処理槽の上流に設けられていることから、朝夕の特定時間に集中する流入処理水量のピーク量を吸収することができるため、前記活性汚泥処理槽の活性汚泥処理を安定して行うことができるのである。
【0024】
このように、前記第二ケーシングにおいて生活雑排水の流入負荷を緩衝する前記流量調整槽を設けることにより、既設単独処理浄化槽において被処理水の流量調整を行う必要がないため、既設単独処理浄化槽をそのまま活用することができる。そのため、少なくとも被処理水を好気処理する好気処理槽を内装する単独処理浄化槽が既に設置されている状況において生活雑排水の合併処理化を行う際には、上述の構成を有する第二ケーシングのみを付設設置して既設単独処理浄化槽に接続すればよいので、新たに合併浄化槽を敷設するのに比べて、設置労力やコストが低減できる。さらに、既設単独処理浄化槽を掘り起こした時の廃棄物処理の問題を回避できる。
【0025】
さらに、上述の構成を有する第二ケーシングを既設単独処理浄化槽に接続した場合は、前記移送管、前記流出管、前記余剰汚泥返送管といった複数の配管で接続する必要が無いため、複雑な配管工事を行う必要が無く、その分設置労力やコストが低減できる。
【0026】
また、槽内の清掃は、主に前記第一ケーシングについて行えば良く、前記第二ケーシングについては、必要が生じた時のみ汚泥引き抜き等の処理を行えばよいので、清掃に要する労力やコストを低減することができる。
【0028】
そして、前記第二ケーシングにおいて、夾雑物を除去する夾雑物除去槽を前記流量調整槽の上流に設けることにより、前記第二ケーシングに流入した食物残渣等の夾雑物を除去することができる。
また、前記夾雑物除去槽が前記流量調整槽の上流に設けられているため、前記夾雑物除去槽は前記活性汚泥処理槽の上流に設けられることになる。これにより、前記活性汚泥処理槽に夾雑物が流入することはほとんど無くなり、前記活性汚泥処理槽内における活性汚泥処理に悪影響を与える可能性が低くなる。つまり、前記活性汚泥処理槽では、前記活性汚泥処理槽内に負荷が大きく好気処理されにくい固形分等が流入しにくい状態で活性汚泥処理が進行することになるので、前記活性汚泥処理槽の水処理能力をより高く維持できる。そのため、前記活性汚泥処理槽での処理効率の向上が期待される。
【0029】
〔構成
この目的を達成するための本発明の特徴構成は、請求項に記載したように、上記構成の何れか1項に記載の合併浄化槽において、
前記夾雑物除去槽に下端部に開口部のある移流管を設け、前記移流管の上端部に、前記夾雑物除去槽を所定水位以上にする前記被処理水を前記流量調整槽以外へ案内する案内路を設けてある点にあり、その作用効果は以下の通りである。
【0030】
〔作用効果
つまり、前記夾雑物除去槽及び前記流量調整槽の水位が異常に高い場合に、槽内に大量流入した低負荷被処理水をそのまま前記消毒槽に移送したり、一時貯留槽に貯留することができるのである。
【0033】
【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が、本発明は、これらによって限定されるものではない。
本発明の合併浄化槽は図1に示すように、地下埋設してある第一ケーシングX1と第二ケーシングX2とを備え、前記第一ケーシングX1から前記第二ケーシングX2に接続管H1を介して被処理水を移送自在に形成してある。
【0034】
前記第一ケーシングX1は、被処理水が流入する流入口1、被処理水の原水を受ける沈殿分離室2、ばっ気室3、沈殿室4、消毒室5をこの順に被処理水が移流自在になるように構成してあり、し尿排水をオーバーフローにより移流させる。前記ばっ気室3を経た被処理水は、前記沈殿室4で沈殿処理されて、固形成分を含まない状態にされた処理排水が前記消毒室5を経て、前記第一ケーシングX1外へ移送される構成にしてある。このような第一ケーシングX1としては、既設の単独処理浄化槽をそのまま適用することが出来る。
【0035】
また、前記第一ケーシングX1は、上述の構成に限らず、し尿単独処理浄化槽であれば、前記沈澱分離槽を嫌気処理槽に置き換えた構成であっても適用可能であり、さらに、ばっ気槽、沈殿槽、消毒槽からなる全ばっ気槽のような構成でも適用可能である。これらは、少なくとも被処理水を好気処理する好気処理槽を内装するし尿単独処理浄化槽である。この時、好気処理槽である前記ばっ気槽へのばっ気を停止した状態で使用するため、前記し尿単独処理浄化槽を沈澱分離槽あるいは嫌気処理槽として用いることになる。
【0036】
前記第二ケーシングX2には、上流側から夾雑物除去槽N1、流量調整槽E1、膜分離槽E2、汚泥濃度調整槽P、消毒槽Qが設けられている。
【0037】
前記夾雑物除去槽N1は、前記第二ケーシング内に流入した被処理水を受けて、その被処理水から沈殿する固形物および液面に発生するスカム等の固体成分や食物残渣等の夾雑物を分離しつつ、内部に生息する嫌気性菌により被処理水を嫌気処理し、移流管Fを介して前記流量調整槽E1に移流自在に構成してある。この夾雑物除去槽N1が後述の膜分離槽E2の上流に設けてあることから、前記膜分離槽E2に夾雑物が流入することはほとんど無くなることにより前記膜分離槽E2における活性汚泥処理に悪影響を与える可能性が低くなる。そのため、前記膜分離槽E2での処理効率の向上が期待される。
前記移流管Fは、夾雑物除去槽N1の幅方向中央部に開口部F1を設けた移流管であり、前記夾雑物除去槽N1の基準水位以上になった被処理水が濾材F2により濾過されて前記開口部F1から前記流量調整槽E1に流入するように構成したものである。また、前記移流管Fの上部には前記基準水位よりもやや上方の所定水位に達した被処理水を前記流量調整槽槽E1以外へ案内する第一、第二案内路G1、G2を設けてある。
前記移流管F上部に設けた第一案内路G1は、前記消毒槽Qに連通接続されており、被処理水を前記膜分離槽E2を介さずに前記消毒槽Qに供給可能にする越流機構を構成している。前記夾雑物除去槽N1及び前記流量調整槽E1の水位が異常に高い場合に、槽内に大量流入した低負荷被処理水をそのまま前記消毒槽Qに移送することができるようになっている。また、前記第二案内路G2は、前記第一ケーシングX1及び前記第二ケーシングX2とは別体に設けた一時貯留槽Tに連通接続してあり、前記低負荷被処理水を前記一時貯留槽Tに貯留することができるように構成してある。
【0038】
前記流量調整槽E1は、前記夾雑物除去槽N1から流入した被処理水を脱窒菌により嫌気処理しつつ、被処理水を貯留してLWL〜HWLの範囲で流量を調節可能な流量調整部を有する。これにより、被処理水の流入負荷を緩衝することができ、朝夕の特定時間に集中する流入処理水量のピーク量を吸収することができる構成としてある。そのため、前記膜分離槽E2の活性汚泥処理を安定して行うことができる。
また、前記流量調整槽E1には、計量装置A1および移送用エアリフトポンプA2を内装してなり、前記被処理水の膜分離処理量に対応して定常的に被処理水を前記膜分離槽E2に移送管A3を介して移送する構成にしてある。
【0039】
前記膜分離槽E2は、多数の平膜を並設してなる膜分離装置Mを内装してあり、さらに前記膜分離槽E2内には好気性菌が育成されている。前記好気性菌が凝集してフロックを形成して活性汚泥となり、被処理水の有機成分を好気分解するのである。その膜分離装置Mの下方には、前記膜分離装置Mに気泡を供給してその膜面に汚泥等が付着するのを防止し、且つ、前記膜分離槽E2内に循環流を形成しながら前記好気性菌に酸素を供給する散気装置Dを内装してある。
前記膜分離装置Mのそれぞれの平膜は、被処理水導通部を内方に有する樹脂製の支持板の両表面に濾過膜部材を接着形成するとともに、前記被処理水導通部に連通する集水管M1を連設してある。前記集水管M1は吸引ポンプA4に連通接続され、この吸引ポンプA4を運転して吸引操作する事で被処理水が前記平膜の前記濾過膜部材を通過して、その濾過膜部材によって被処理水中の汚泥等が除去され、このように膜分離処理して高度に浄水された被処理水を前記消毒槽Qへ送りだすのである。
【0040】
尚、前述の吸引ポンプA4の下流側には、揚水配管101を介して地上にて再利用可能なように構成することが可能である。例えば、給水部102としての屋根散水設備が接続し、冬には屋根上の雪の融雪に、夏には屋根の冷却の用に供される。また、屋根散水するだけでなく、空調用冷却水用もしくはトイレ用洗浄水等にも使用することができる。
【0041】
前記汚泥濃度調整槽Pには、前記膜分離槽E2からの循環液に含まれる汚泥を貯留し、さらに、前記汚泥濃度調整槽Pからの脱離液を硝化液と共に前記流量調整槽E1に移送する汚泥移送管G3を配置している。
【0042】
尚、前記膜分離槽E2における汚泥量の目安としては、5000〜15000mg/リットルの範囲であることが適切な活性汚泥処理を維持する上で好ましく、しかも、膜分離装置M内の平膜の膜面が汚染されにくい状態を維持できるのである。
【0043】
このように、第一ケーシングX1と第二ケーシングX2が移流自在になるように設けると共に、前記第一ケーシングX1と前記第二ケーシングX2とを地下埋設して合併処理浄化槽とすることにより、前記第一ケーシングX1においては、ポンプ装置等の動力を使用すること無く、後設の前記第二ケーシングX2に被処理水を自然移流により移送することができる。
【0044】
このような合併浄化槽において、図2に示したように、生活雑排水配管H2より生活雑排水を前記第二ケーシングX2に流入させる構成とすることができる。この時、前記生活雑排水配管H2は、直接前記第二ケーシングX2と接続させて前記第一ケーシングX1の排水と生活雑排水とを別々に第二ケーシングX2に流入させてもよいし、前記第一ケーシングX1と前記第二ケーシングX2とを接続する前記接続管H1と合流させて(破線部分)、前記第一ケーシングX1の排水と生活雑排水とをまとめて第二ケーシングX2に流入させてもよい。
【0045】
このように生活雑排水配管H2を設けることにより、既設の単独処理浄化槽である前記第一ケーシングを改造することなく合併処理可能な浄化槽を提供することができる。この時、前記第一ケーシングX1は、し尿排水のみを受入れ、し尿排水中の固体成分を沈殿させることにより分離させる沈澱分離槽としての機能を発揮した後、負荷の低減した被処理水を後設の前記第二ケーシングX2に自然移流させることができるのである。
【0046】
上述した合併浄化槽において、前記第二ケーシングX2において前記流量調整槽E1を設けることにより、既設単独処理浄化槽において被処理水の流量調整を行う必要がないため、前記第一ケーシングX1は既設単独処理浄化槽をそのまま活用することができる。つまり、前記第一ケーシングX1は既設単独処理浄化槽の前記ばっ気室3において接触材等の部材が設けられている状態のまま活用できるのであるから、前記ばっ気室3では比較的高水位である通常水位のまま処理を行うことができる。そのため、前記ばっ気室3空間の大部分が空の状態になることは殆ど無くなり、前記ばっ気室3内部の被処理水の水圧が前記第一ケーシングX1周囲の土圧と拮抗状態を保つことができるため、前記第一ケーシングX1の変形や破損の虞はほとんどなくなるのである。そのため、前記第一ケーシングX1は、強度を増すための補強工事をすることなく既設単独処理浄化槽をそのまま活用することができる。この時、一般的には、前記ばっ気室3へのばっ気を停止した状態で使用するため、前記既設単独処理浄化槽を沈澱分離槽あるいは嫌気処理槽として用いることになる。
【0047】
そのため、被処理水を好気処理するばっ気室3を内装する単独処理浄化槽が既に設置されている状況において生活雑排水の合併処理化を行う際には、上述の構成を有する第二ケーシングX2のみを付設設置して既設単独処理浄化槽に接続すればよいので、新たに合併浄化槽を敷設するのに比べて、設置労力やコストが低減でき、さらに、既設単独処理浄化槽である前記第一ケーシングX1を掘り起こした時の廃棄物処理の問題も回避できる。
【0048】
さらに、上述の構成を有する第二ケーシングX2を既設単独処理浄化槽に接続した場合は、図4における前記移送管12、前記流出管13、前記余剰汚泥返送管15といった複数の配管で接続する必要が無いため、複雑な配管工事を行う必要が無く、その分設置労力やコストが低減できる。
【0049】
また、前記第二ケーシングX2が地中埋設されているため、前記第二ケーシングX2が直接外気に晒されることが無くなる。これにより、前記耐候劣化が生じる虞は殆ど無く、前記第二ケーシングX2周囲の土が前記第二ケーシングX2の荷重を支えて分散することになるのでクリープ変形が生じ難く、そのため、長期信頼性を有したケーシングとすることができ、外部から衝撃が加わってケーシングが破損する虞は殆ど無くなる。
【0050】
さらに、前記第二ケーシングX2が地中埋設されているため、寒冷地の冬期における外気温の影響を受け難くなる。そのため、前記第二ケーシングX2内の被処理水が凍結する虞は殆ど無いため被処理水の活性汚泥処理及び膜分離処理が行えなくなることを防止でき、外気の影響により前記第二ケーシングX2内の膜分離槽E2内の微生物の活性が低下する虞が少なくなるため、前記膜分離槽E2における生物反応効率の低下を防止することができる。そのため、前記膜分離槽E2での処理効率の向上が期待される。
【0051】
〔別実施形態〕
以下に別実施形態を説明する。
上述した地下埋設してある第一ケーシングX1と第二ケーシングX2を有する合併処理浄化槽において、図3に示したように、生活雑排水配管H3より生活雑排水を前記第一ケーシングX1に流入させる構成とすることができる。
【0052】
この時、生活雑排水配管H3の前記第一ケーシングX1への接続は、前記第一ケーシングX1に前記流入口1とは別の生活雑排水流入口を開けるといった簡単な改造を加えるだけで行うことができる。あるいは、前記生活雑排水配管H3を、既設のし尿排水配管H4と合流させて(破線部分)、し尿排水と生活雑排水とをまとめて第一ケーシングX1に流入させる構成とすれば、前記第一ケーシングX1に改造を加える必要がない。
【0053】
そして、前記第一ケーシングX1は、し尿排水中の固形分の沈殿分離や、し尿排水中のトイレットペーパー等の夾雑物及び生活雑排水中の夾雑物を沈殿除去する夾雑物除去槽としての機能を発揮した後、後設の前記第二ケーシングX2に被処理水を自然移流させることができるのである。
【0054】
つまり、前記第一ケーシングX1の既設単独処理浄化槽で夾雑物除去等の前処理をされた被処理水を前記第二ケーシングX2の膜分離槽E2で活性汚泥処理することができるので、前記膜分離槽E2では、前記膜分離槽E2内に負荷が大きく好気処理されにくい固形分等が流入しにくい状態で活性汚泥処理が進行することになるので、前記膜分離槽E2の水処理能力をより高く維持できる。
【0055】
この時、槽内の清掃は、主に前記第一ケーシングX1について行えば良いので、清掃に要する労力やコストを低減することができる。また、前記第二ケーシングX2の清掃においては、必要が生じた時のみ前記夾雑物除去槽N1及び前記汚泥濃度調整槽Pの汚泥引き抜き等の処理を行えばよい。
【図面の簡単な説明】
【図1】本発明の合併浄化槽の概略図。
【図2】本発明の合併浄化槽の配管系を示した概略図。
【図3】本発明の合併浄化槽の配管系を示した別実施形態の概略図。
【図4】従来の合併浄化槽の概略図。
【符号の説明】
X1 第一ケーシング
X2 第二ケーシング
2 沈殿分離室
3 ばっ気室
N1 夾雑物除去槽
E1 流量調整槽
E2 膜分離槽
H2〜3 生活雑排水配管
[0001]
BACKGROUND OF THE INVENTION
The present invention is from a first casing, which is a single treatment septic tank, in which an aerobic treatment tank for aerobically treating treated water is used, to a second casing, in which an activated sludge treatment tank for treating activated water is treated. It is related with the merged septic tank provided so that to-be-processed water can move freely.
[0002]
[Prior art]
Conventionally, as a septic tank for treating general-purpose domestic wastewater, a single-treatment septic tank that only treats wastewater and urine drainage, and a combined septic tank that can treat not only wastewater to be treated but also sewage wastewater can be used. Yes.
[0003]
In the single treatment septic tank, the wastewater to be treated is only human wastewater, so daily wastewater from the kitchen, laundry, bathroom, etc. is discharged as it is, which is a major cause of water pollution in closed water areas such as lakes and marshes. . It is clear that proper treatment of this domestic wastewater greatly contributes to the reduction of water pollution in closed water areas, and further, wastewater discharged into rivers, etc. due to the strengthening of water quality regulations accompanying the improvement of environmental awareness. A septic tank that improves the quality of water has been desired. Thus, it is considered to use a combined septic tank that can treat not only human wastewater but also daily wastewater from a single treatment septic tank, which makes it possible to satisfy high water quality standards. ing. Furthermore, under such circumstances, measures for realizing the abolition of the new single treatment septic tank and the merger processing of the existing single treatment septic tank are being sought. Examples of cases where an existing single treatment septic tank is to be merged are, for example, shortly after the installation of a single treatment septic tank, or the existing single treatment septic tank is effectively utilized from the area, form, etc. of the land. There are times when it is better to do.
[0004]
As shown in FIG. 4, the septic tank that realizes the combined processing of such existing single-treatment septic tanks performs membrane separation activated sludge treatment that is installed on the ground separately from the existing single-process septic tank and the existing single-process septic tank. There is known one that is connected to a subsequent processing tank so that it can be merged (see JP-A-11-169872).
[0005]
In the septic tank that realizes the combined processing of the existing single processing septic tank, raw water to be treated flows into the sedimentation separation chamber 2 from the inlet 1 and goes downstream in the order of the aeration chamber 3, the sedimentation chamber 4, and the disinfection chamber 5. In the single-treatment septic tank 7 buried underground so as to be decomposed while being transported, a membrane module 8 and an air diffuser 9 installed below the membrane module 8 are provided separately from the single-process septic tank 7. The membrane treatment tank 10 is installed on the ground, the aeration chamber 3 and the membrane treatment tank 10 are communicated with each other by a transfer pipe 12 having a pump 11 for pumping up sewage, and the membrane module 8 and the disinfection tank 5 are connected. The effluent pipe 13 communicated, and the bottom of the membrane treatment tank 10 and the sedimentation separation chamber 2 communicated with an excess sludge return pipe 15 having a valve 14.
[0006]
In such a combined septic tank, miscellaneous wastewater and human wastewater drainage flows from the pipes 16 and 17 into the precipitation separation chamber 2 through the inlet 1, and solid-liquid separation is performed in the precipitation separation chamber 2. The supernatant liquid after solid-liquid separation flows into the aeration chamber 3, and flows into the membrane treatment tank 10 through the transfer pipe 12 by the pump 11. At this time, since the aeration chamber 3 functions as a flow rate adjusting tank for adjusting the flow rate of the supernatant liquid after solid-liquid separation, as in the case where it is used only in the single processing septic tank, It is not necessary to provide an aerobic treatment by providing a contact material in the aeration chamber 3.
The membrane treatment tank 10 incorporates the membrane module 8 and the diffuser tube 9 inside, and the supernatant liquid flowing into the membrane treatment tank 10 from the transfer pipe 12 connected above the membrane treatment tank 10 is: The membrane module 8 performs micron-sized solid-liquid separation, and the treated water separated from the outflow pipe 13 is transferred to the disinfection tank 5. The treated water transferred to the disinfecting tank 5 is sterilized with a chlorine agent and then discharged out of the system from the outlet 6.
The sludge that is not transferred to the disinfection tank 5 by the membrane module 8 is supplied with air from the air diffuser 9 installed below the membrane module 8 and is subjected to aerobic treatment. However, since all the sludge is rarely decomposed by the aerobic treatment, the sludge settled on the bottom of the membrane treatment tank 10 (excess sludge) opens the valve 14 and the surplus sludge return pipe 15 It is transferred to the precipitation separation chamber 2.
[0007]
In this way, simply by installing a membrane treatment tank for membrane separation activated sludge treatment by effectively utilizing the existing single treatment septic tank, the treated water that has been treated with activated sludge and has a sufficiently reduced BOD is efficiently separated into solid and liquid. Can be made into a combined septic tank that can be highly purified, and all domestic wastewater discharged from the household can be efficiently purified and treated so as to meet the water discharge standard value.
[0008]
[Problems to be solved by the invention]
In the conventional merged septic tank described above, the aeration chamber of the existing single processing septic tank is used as a flow rate adjusting tank for the subsequent processing tank. In other words, since the aeration chamber functioning as the flow rate adjusting tank is configured to absorb the peak amount of the inflow treated water concentrated at a specific time in the morning and evening, the water level of the treated water is normally suppressed to the vicinity of the low water level LWL. There is a need. Therefore, most of the aeration chamber space is in an empty state, easily affected by earth pressure around the existing single treatment septic tank buried in the ground, and there is a risk of deformation or breakage of the existing single treatment septic tank. In order to avoid such deformation and breakage of the existing single treatment septic tank, it is conceivable to reinforce the inside of the aeration chamber etc., but the reinforcement work in the existing single treatment septic tank is complicated and the reinforcement cost is Because this is an obstacle, it is actually quite difficult to reinforce existing single-treatment septic tanks, and there is still a question of whether they can withstand long-term even if they are reinforced. There was a point.
[0009]
In addition, in the merged septic tank described above, the subsequent processing tank attached to the existing single processing septic tank is installed on the ground or semi-ground in consideration of the construction cost and labor at the time of installation, the burden at the time of maintenance, etc. There are many. Such treatment tanks installed on the ground or semi-ground are mainly formed of plastics such as FRP (glass fiber reinforced plastic) and DCPD (dicyclopentagen). In addition, the treatment tank is applied with a weather-resistant paint on the outer surface of the treatment tank in a warm region, and in a cold region, the treatment tank is subjected to a civil engineering finish such as surrounding the treatment tank with a pile or a block and covering with earth and sand. It was protected from the surrounding environment.
[0010]
However, the above-described plastic processing tank has the following problems.
(A) Even if the weather-resistant paint was applied to the outer surface of the treatment tank, the weather-resistant paint sometimes deteriorated over time (weather-resistant deterioration). When such deterioration occurs, in the case of the processing tank using the FRP, the resin is likely to deteriorate or the glass fiber is exposed, and in the case of the DCPD, the surface is roughened or embrittled. The inconvenience of progressing is likely to occur.
(B) Since creep deformation with time occurs in addition to the weather resistance deterioration, the long-term reliability is lacking (lack of long-term reliability).
(C) There is a risk of damage due to external impact (lack of impact resistance).
(D) Since the frame of the treatment tank is only a few millimeters thick, in winter (especially in cold regions), the influence of outside air may reduce the activity of microorganisms in the treatment tank, Furthermore, there is a possibility that the inside of the processing tank will freeze. (Lack of thermal insulation properties).
[0011]
The above (a) deterioration of weather resistance and (b) lack of long-term reliability can be solved by adopting a stainless steel (sus) structure in the frame of the treatment tank, but in this case as well, (c) The problem of lack of impact resistance and (d) lack of heat insulation properties could not be solved. Further, when the stainless steel structure is used, the manufacturing cost of the treatment tank is expensive.
[0012]
In addition, (d) the problem of lack of heat insulation properties may be to improve the heat insulation properties of the treatment tank by using a heat insulating material such as a foam, but in this case also, the manufacturing cost of the treatment tank is expensive. There was a drawback of becoming. In addition, it is conceivable to protect the treatment tank from the surrounding environment by applying a civil engineering finish as described above, but this has a problem that it takes labor and costs for construction.
[0013]
Accordingly, an object of the present invention is to provide a combined septic tank that can be used as it is, or can be used in a state of simple modification, and has high resistance to the external environment.
[0014]
[Means for Solving the Problems]
    [Configuration 1]
  The characteristic configuration of the present invention to achieve this object is as described in claim 1.
  Water to be treated is transferred from the first casing, which is an independent treatment septic tank, in which an aerobic treatment tank for aerobically treating the water to be treated to a second casing in which an activated sludge treatment tank for treating the treated water is activated. In the merged septic tank that is set up so that it can freely move,
  A household wastewater pipe for allowing household wastewater to flow in is connected to the second casing, and a flow rate adjustment tank for storing the treated water and adjusting the flow rate is provided upstream of the activated sludge treatment tank in the second casing. Set up inIn addition, a contaminant removal tank for removing contaminants is provided upstream of the flow rate adjustment tank.In other words, the aeration of the aerobic treatment tank is stopped, and the effects thereof are as follows.
[0015]
[Operation effect 1]
In other words, since the daily wastewater pipe for allowing the daily wastewater to flow in is connected to the second casing, the daily wastewater that is drained from the kitchen, laundry, bathroom, etc. can be directly flowed into the second casing. it can. Therefore, it is not necessary to adjust the flow rate of the water to be treated in the first casing, which is an existing single treatment purification tank, and the first aerobic treatment tank can be utilized with a member such as a contact material provided. At this time, the first casing, which is an existing single-treatment septic tank, accepts only human wastewater, and the aerobic treatment tank can perform the treatment with the normal water level being a relatively high water level. Therefore, most of the aerobic treatment tank space is almost never emptied, and the water pressure of the water to be treated inside the aerobic treatment tank is kept in an antagonistic state with the earth pressure around the existing single treatment septic tank. Therefore, there is almost no risk of deformation or breakage of the existing single treatment septic tank. Therefore, the existing single treatment septic tank can be used as it is without performing a reinforcement work for increasing the strength of the existing single treatment septic tank. At this time, in general, since the aerobic treatment tank is used in a state where aeration is stopped, the existing single treatment purification tank is used as a precipitation separation tank or an anaerobic treatment tank.
[0016]
And said 1st casing which is an existing single processing septic tank, after exhibiting the function as a sedimentation separation tank that separates solid components in human wastewater by precipitation, the treated water with reduced load is installed in the above-mentioned It can be naturally advected to the second casing.
[0017]
Further, in the second casing, by providing a flow rate adjusting tank for storing the treated water and adjusting the flow rate upstream of the activated sludge treating tank, the inflow load of domestic wastewater directly flowing into the second casing is reduced. It can be buffered, so that the peak amount of the inflow treated water concentrated at a specific time in the morning and evening can be absorbed. Therefore, the activated sludge treatment of the activated sludge treatment tank can be performed stably.
[0018]
In this way, by providing the flow rate adjustment tank that buffers the inflow load of domestic wastewater in the second casing, it is not necessary to adjust the flow rate of the treated water in the existing single treatment septic tank. It can be used as it is. Therefore, the second casing having the above-described configuration is to be used when merging wastewater in a situation where a single treatment septic tank that has at least an aerobic treatment tank for aerobically treating treated water is already installed. Therefore, installation labor and cost can be reduced compared to newly laying a merged septic tank. Further, it is possible to avoid the problem of waste disposal when the existing single treatment septic tank is dug up.
[0019]
  Furthermore, when the second casing having the above-described configuration is connected to the existing single treatment septic tank, it is not necessary to connect with a plurality of pipes such as the transfer pipe, the outflow pipe, and the excess sludge return pipe, so that complicated piping work There is no need to perform installation, and installation labor and cost can be reduced accordingly..
AlsoIn the second casing, it is possible to remove contaminants such as food residues flowing into the second casing by providing a contaminant removal tank for removing contaminants upstream of the flow rate adjustment tank.
  Further, since the contaminant removal tank is provided upstream of the flow rate adjustment tank, the contaminant removal tank is provided upstream of the activated sludge treatment tank. Thereby, impurities hardly flow into the activated sludge treatment tank, and the possibility of adversely affecting the activated sludge treatment in the activated sludge treatment tank is reduced. That is, in the activated sludge treatment tank, the activated sludge treatment proceeds in a state in which solids or the like that are difficult to be aerobically treated due to a large load are difficult to flow into the activated sludge treatment tank. Water treatment capacity can be maintained higher. Therefore, the improvement of the processing efficiency in the said activated sludge processing tank is anticipated.
[0020]
    〔Constitution2]
  In order to achieve this object, the characterizing features of the present invention are as follows.2As described in
  Water to be treated is transferred from the first casing, which is an independent treatment septic tank, in which an aerobic treatment tank for aerobically treating the water to be treated to a second casing in which an activated sludge treatment tank for treating the treated water is activated. In the merged septic tank that is set up so that it can freely move,
  A household wastewater pipe for allowing household wastewater to flow is connected to the first casing, and a flow rate adjustment tank for storing treated water and adjusting the flow rate with respect to the second casing is the activated sludge treatment tank. The waste removal tank for removing the foreign substances is provided upstream of the flow rate adjustment tank, and the operation and effects thereof are as follows.
[0021]
    [Function and effect2]
  In other words, the daily wastewater pipe into which the daily wastewater flows is connected to the first casing, so that the daily wastewater flows into the first casing together with the urine drainage. And the said 1st casing is a contaminant removal tank which carries out the sediment separation of the solid content in a human waste water, the foreign materials, such as toilet paper in a human waste water, and the food residue in a domestic waste water. After exhibiting the function, the water to be treated can be naturally advected to the subsequent second casing. In other words, since the water to be treated that has been subjected to the pretreatment such as the removal of contaminants in the first casing can be activated sludge treatment in the activated sludge treatment tank of the second casing, the load in the activated sludge treatment tank is Since the activated sludge treatment proceeds in a state in which solids such as contaminants that are largely difficult to be aerobic hardly flow in, the water treatment capacity of the activated sludge treatment tank can be maintained higher.
  In addition, the connection of the household wastewater piping to the first casing can be performed only by adding a simple modification such as opening the daily wastewater inlet to the first casing as described in Example 2 described later. .
[0022]
Further, since the second casing is provided with a flow rate adjusting tank for storing the treated water and adjusting the flow rate, the inflow load of the domestic wastewater that has flowed into the first casing is set to the flow rate of the second casing. Since it can be buffered in the adjustment tank, there is no need to adjust the flow rate of the water to be treated in the first casing, which is an existing single treatment purification tank, and a member such as a contact material is provided in the aerobic treatment tank Since the aerobic treatment tank of the existing single treatment septic tank can be used as it is, the treatment can be performed with the normal water level being relatively high. Therefore, most of the aerobic treatment tank space is almost never emptied, and the water pressure of the water to be treated inside the aerobic treatment tank is kept in an antagonistic state with the earth pressure around the existing single treatment septic tank. Therefore, there is almost no risk of deformation or breakage of the existing single processing septic tank. Therefore, the existing single processing septic tank can be used as it is without performing a reinforcement work for increasing the strength of the existing single processing septic tank. At this time, in general, since the aerobic treatment tank is used in a state where aeration is stopped, the existing single treatment purification tank is used as a precipitation separation tank or an anaerobic treatment tank.
[0023]
In addition, since the flow rate adjustment tank is provided upstream of the activated sludge treatment tank, it can absorb the peak amount of the inflow treated water concentrated at a specific time in the morning and evening, so that the activated sludge treatment tank can be activated. Sludge treatment can be performed stably.
[0024]
In this way, by providing the flow rate adjustment tank that buffers the inflow load of domestic wastewater in the second casing, it is not necessary to adjust the flow rate of the treated water in the existing single treatment septic tank. It can be used as it is. Therefore, the second casing having the above-described configuration is to be used when merging wastewater in a situation where a single treatment septic tank that has at least an aerobic treatment tank for aerobically treating treated water is already installed. Therefore, installation labor and cost can be reduced compared to newly laying a merged septic tank. Further, it is possible to avoid the problem of waste disposal when the existing single treatment septic tank is dug up.
[0025]
Furthermore, when the second casing having the above-described configuration is connected to the existing single treatment septic tank, it is not necessary to connect with a plurality of pipes such as the transfer pipe, the outflow pipe, and the excess sludge return pipe, so that complicated piping work There is no need to perform the operation, and installation labor and cost can be reduced accordingly.
[0026]
Further, the cleaning of the tank may be performed mainly for the first casing, and the second casing may be subjected to a process such as sludge extraction only when necessary, so that labor and cost required for cleaning are reduced. Can be reduced.
[0028]
  AndIn the second casing, it is possible to remove contaminants such as food residues flowing into the second casing by providing a contaminant removal tank for removing contaminants upstream of the flow rate adjustment tank.
  Further, since the contaminant removal tank is provided upstream of the flow rate adjustment tank, the contaminant removal tank is provided upstream of the activated sludge treatment tank. Thereby, impurities hardly flow into the activated sludge treatment tank, and the possibility of adversely affecting the activated sludge treatment in the activated sludge treatment tank is reduced. That is, in the activated sludge treatment tank, the activated sludge treatment proceeds in a state in which solids or the like that are difficult to be aerobically treated due to a large load are difficult to flow into the activated sludge treatment tank. Water treatment capacity can be maintained higher. Therefore, the improvement of the processing efficiency in the said activated sludge processing tank is anticipated.
[0029]
    〔Constitution3]
  In order to achieve this object, the characterizing features of the present invention are as follows.3As described above, the above configuration1~2In the merged septic tank described in any one of
  The contaminant removal tank is provided with an advection pipe having an opening at the lower end, and the treated water that brings the contaminant removal tank to a predetermined water level or higher is guided to the upper end of the advection pipe to other than the flow rate adjustment tank. A guide path is provided, and the function and effect thereof are as follows.
[0030]
    [Function and effect3]
  That is, when the water level of the contaminant removal tank and the flow rate adjustment tank is abnormally high, the low-load treated water that has flowed into the tank in large quantities can be transferred to the disinfection tank as it is or stored in the temporary storage tank. It can be done.
[0033]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below with reference to the drawings, but the present invention is not limited thereto.
As shown in FIG. 1, the merged septic tank of the present invention comprises a first casing X1 and a second casing X2 embedded underground, and is covered from the first casing X1 to the second casing X2 via a connecting pipe H1. The treated water is formed so as to be transportable.
[0034]
In the first casing X1, the water to be treated can freely flow through the inlet 1 into which the water to be treated flows, the sedimentation separation chamber 2 that receives the raw water to be treated, the aeration chamber 3, the sedimentation chamber 4, and the disinfection chamber 5 in this order. The human wastewater is advected by overflow. The treated water that has passed through the aeration chamber 3 is precipitated in the sedimentation chamber 4 and treated wastewater that does not contain solid components is transferred to the outside of the first casing X1 through the disinfection chamber 5. The configuration is as follows. As such a first casing X1, an existing single processing septic tank can be applied as it is.
[0035]
In addition, the first casing X1 is not limited to the above-described configuration, but can be applied to a configuration in which the precipitation separation tank is replaced with an anaerobic processing tank as long as it is a human waste treatment tank. It is also possible to apply a configuration such as a complete aeration tank comprising a sedimentation tank and a disinfection tank. These are at least an aerobic treatment tank for aerobic treatment of water to be treated, and a urine single treatment purification tank. At this time, since the aeration to the aeration tank, which is an aerobic treatment tank, is used in a stopped state, the human waste single treatment purification tank is used as a precipitation separation tank or an anaerobic treatment tank.
[0036]
The second casing X2 is provided with a contaminant removal tank N1, a flow rate adjustment tank E1, a membrane separation tank E2, a sludge concentration adjustment tank P, and a disinfection tank Q from the upstream side.
[0037]
The contaminant removal tank N1 receives the water to be treated which has flowed into the second casing, and precipitates from the water to be treated and solids such as scum generated on the liquid surface and impurities such as food residues. The water to be treated is anaerobically treated by anaerobic bacteria that inhabit the inside, and can be transferred to the flow rate adjusting tank E1 via the advection tube F. Since the contaminant removal tank N1 is provided upstream of the membrane separation tank E2 described later, the contaminants hardly flow into the membrane separation tank E2, thereby adversely affecting the activated sludge treatment in the membrane separation tank E2. Is less likely to give Therefore, improvement of the processing efficiency in the membrane separation tank E2 is expected.
The advection pipe F is a advection pipe provided with an opening F1 in the central portion in the width direction of the contaminant removal tank N1, and the water to be treated that has reached the reference water level of the contaminant removal tank N1 is filtered by the filter medium F2. And is configured to flow into the flow rate adjusting tank E1 from the opening F1. In addition, first and second guide paths G1 and G2 for guiding the water to be treated that has reached a predetermined water level slightly above the reference water level to other than the flow rate adjusting tank E1 are provided on the upper part of the advection pipe F. is there.
The first guide path G1 provided in the upper part of the advection pipe F is connected to the sterilization tank Q so as to supply water to be treated to the sterilization tank Q without passing through the membrane separation tank E2. The mechanism is configured. When the water levels of the contaminant removal tank N1 and the flow rate adjusting tank E1 are abnormally high, the low-load treated water that has flowed into the tank in large quantities can be transferred to the disinfection tank Q as it is. The second guide path G2 is connected to a temporary storage tank T provided separately from the first casing X1 and the second casing X2, and the low-load treated water is supplied to the temporary storage tank. T can be stored in T.
[0038]
The flow rate adjustment tank E1 has a flow rate adjustment unit capable of storing the treated water and adjusting the flow rate in the range of LWL to HWL while anaerobically treating the treated water flowing from the contaminant removal tank N1 with denitrifying bacteria. Have. Thereby, it is set as the structure which can buffer the inflow load of to-be-processed water, and can absorb the peak amount of the inflow treated water amount which concentrates on the morning and evening specific time. Therefore, the activated sludge treatment of the membrane separation tank E2 can be performed stably.
The flow rate adjusting tank E1 includes a metering device A1 and a transfer air lift pump A2, and the water to be treated is steadily supplied to the membrane separation tank E2 in accordance with the amount of the membrane to be treated. It is configured to be transferred through the transfer pipe A3.
[0039]
The membrane separation tank E2 includes a membrane separation apparatus M having a large number of flat membranes arranged in parallel, and aerobic bacteria are grown in the membrane separation tank E2. The aerobic bacteria aggregate to form flocs to become activated sludge, which aerobically decomposes organic components of the water to be treated. Below the membrane separator M, bubbles are supplied to the membrane separator M to prevent sludge and the like from adhering to the membrane surface, and a circulation flow is formed in the membrane separator E2. An air diffuser D for supplying oxygen to the aerobic bacteria is incorporated.
Each flat membrane of the membrane separation device M is formed by adhering and forming a filtration membrane member on both surfaces of a resin-made support plate having a to-be-treated water conducting portion on the inside, and communicating with the to-be-treated water conducting portion. A water pipe M1 is provided continuously. The water collecting pipe M1 is connected in communication with a suction pump A4. By operating the suction pump A4 and performing a suction operation, the water to be treated passes through the filtration membrane member of the flat membrane and is treated by the filtration membrane member. The sludge in the water is removed, and the water to be treated, which has been subjected to membrane separation treatment and highly purified in this way, is sent to the sterilization tank Q.
[0040]
The downstream side of the suction pump A4 can be configured to be reusable on the ground via the pumping pipe 101. For example, a roof watering facility as the water supply unit 102 is connected, and is used for melting snow on the roof in winter and for cooling the roof in summer. Moreover, it can be used not only for watering the roof but also for cooling water for air conditioning or washing water for toilets.
[0041]
The sludge concentration adjusting tank P stores sludge contained in the circulating liquid from the membrane separation tank E2, and further transfers the desorbed liquid from the sludge concentration adjusting tank P to the flow rate adjusting tank E1 together with the nitrification liquid. The sludge transfer pipe G3 is arranged.
[0042]
The amount of sludge in the membrane separation tank E2 is preferably in the range of 5000 to 15000 mg / liter in order to maintain an appropriate activated sludge treatment, and the membrane of the flat membrane in the membrane separator M The surface can be kept from being contaminated.
[0043]
As described above, the first casing X1 and the second casing X2 are provided so as to be freely transferred, and the first casing X1 and the second casing X2 are buried underground to form a combined treatment septic tank. In one casing X1, water to be treated can be transferred to the second casing X2 provided later by natural advection without using power from a pump device or the like.
[0044]
In such a combined septic tank, as shown in FIG. 2, it can be set as the structure which flows a miscellaneous wastewater into said 2nd casing X2 from the miscellaneous wastewater piping H2. At this time, the miscellaneous wastewater pipe H2 may be directly connected to the second casing X2 so that the wastewater from the first casing X1 and the miscellaneous wastewater flow into the second casing X2 separately. Even if the connecting pipe H1 that connects the one casing X1 and the second casing X2 is joined (broken line part), the waste water from the first casing X1 and the domestic waste water are collectively flowed into the second casing X2. Good.
[0045]
By providing the household wastewater pipe H2 in this way, it is possible to provide a septic tank that can be merged without modifying the first casing, which is an existing single-process septic tank. At this time, the first casing X1 accepts only human wastewater and exhibits a function as a sedimentation separation tank that separates the solid components in the human wastewater by sedimentation. The second casing X2 can be naturally advected.
[0046]
In the merged septic tank described above, the flow rate adjusting tank E1 is provided in the second casing X2, so that it is not necessary to adjust the flow rate of the water to be treated in the existing single process septic tank. Can be used as is. That is, since the first casing X1 can be utilized in a state where a member such as a contact material is provided in the aeration chamber 3 of the existing single processing septic tank, the aeration chamber 3 has a relatively high water level. The treatment can be carried out with the normal water level. Therefore, most of the space of the aeration chamber 3 is almost never empty, and the water pressure of the water to be treated inside the aeration chamber 3 is kept in an antagonistic state with the earth pressure around the first casing X1. Therefore, there is almost no risk of deformation or breakage of the first casing X1. Therefore, the first casing X1 can utilize the existing single-treatment septic tank as it is without reinforcing work for increasing the strength. At this time, in general, since the aeration to the aeration chamber 3 is stopped, the existing single treatment septic tank is used as a precipitation separation tank or an anaerobic treatment tank.
[0047]
Therefore, in the situation where the single treatment septic tank that houses the aeration chamber 3 that aerobically treats the water to be treated is already installed, the second casing X2 having the above-described configuration is used for the combined treatment of domestic wastewater. Therefore, it is possible to reduce installation labor and cost as compared to newly laying a combined septic tank, and further, the first casing X1 which is an existing singly processed septic tank. The problem of waste disposal when digging up can also be avoided.
[0048]
Further, when the second casing X2 having the above-described configuration is connected to the existing single processing septic tank, it is necessary to connect with a plurality of pipes such as the transfer pipe 12, the outflow pipe 13, and the excess sludge return pipe 15 in FIG. Since there is no need for complicated piping work, installation labor and cost can be reduced accordingly.
[0049]
Further, since the second casing X2 is buried in the ground, the second casing X2 is not directly exposed to the outside air. As a result, there is almost no risk of the weather resistance deterioration, and since the soil around the second casing X2 supports and disperses the load of the second casing X2, creep deformation hardly occurs, and thus long-term reliability is ensured. The casing can be provided, and there is almost no risk of damage to the casing due to external impact.
[0050]
Furthermore, since the second casing X2 is buried in the ground, it is difficult to be affected by the outside air temperature in the winter in a cold region. Therefore, since there is almost no possibility that the water to be treated in the second casing X2 will freeze, it is possible to prevent the activated sludge treatment and membrane separation treatment of the water to be treated from being performed, and the inside of the second casing X2 due to the influence of outside air. Since there is less possibility that the activity of the microorganisms in the membrane separation tank E2 is reduced, it is possible to prevent a decrease in biological reaction efficiency in the membrane separation tank E2. Therefore, improvement of the processing efficiency in the membrane separation tank E2 is expected.
[0051]
[Another embodiment]
Another embodiment will be described below.
In the merged treatment septic tank having the first casing X1 and the second casing X2 buried underground, as shown in FIG. 3, a configuration in which household wastewater flows into the first casing X1 from the household wastewater pipe H3. It can be.
[0052]
At this time, the connection to the first casing X1 of the domestic miscellaneous drainage pipe H3 is performed only by adding a simple modification such as opening a miscellaneous drainage inlet different from the inlet 1 to the first casing X1. Can do. Alternatively, if the daily wastewater drain pipe H3 is joined with the existing human wastewater drainage pipe H4 (broken line portion), the wastewater drainage and the daily wastewater are collectively flowed into the first casing X1. There is no need to modify the casing X1.
[0053]
The first casing X1 has a function as a contaminant removal tank that precipitates and separates solids in human wastewater, and impurities such as toilet paper in human wastewater and household wastewater. After being demonstrated, the water to be treated can be naturally advected to the second casing X2 provided later.
[0054]
That is, since the water to be treated which has been pretreated such as removing foreign substances in the existing single treatment septic tank of the first casing X1 can be treated with activated sludge in the membrane separation tank E2 of the second casing X2, the membrane separation In the tank E2, since the activated sludge process proceeds in a state where it is difficult for a solid content or the like that is heavily loaded and difficult to be aerobic to flow into the membrane separation tank E2, the water treatment capacity of the membrane separation tank E2 is further increased. Highly maintainable.
[0055]
At this time, since the cleaning in the tank may be performed mainly for the first casing X1, labor and cost required for cleaning can be reduced. Further, in the cleaning of the second casing X2, it is only necessary to perform processing such as sludge extraction from the contaminant removal tank N1 and the sludge concentration adjustment tank P only when necessary.
[Brief description of the drawings]
FIG. 1 is a schematic view of a combined septic tank of the present invention.
FIG. 2 is a schematic view showing a piping system of a combined septic tank according to the present invention.
FIG. 3 is a schematic view of another embodiment showing the piping system of the combined septic tank of the present invention.
FIG. 4 is a schematic diagram of a conventional merged septic tank.
[Explanation of symbols]
X1 first casing
X2 Second casing
2 Precipitation separation chamber
3 Aeration room
N1 contaminant removal tank
E1 Flow adjustment tank
E2 membrane separation tank
H2-3 Daily life drainage piping

Claims (3)

少なくとも被処理水を好気処理する好気処理槽を内装する単独処理浄化槽である第一ケーシングから、被処理水を活性汚泥処理する活性汚泥処理槽を内装する第二ケーシングへと被処理水が移流自在になるように設けてある合併浄化槽において、
生活雑排水を流入させる生活雑排水配管が前記第二ケーシングに接続してあると共に、前記第二ケーシングに、被処理水を貯留して流量を調整する流量調整槽を前記活性汚泥処理槽の上流に設けてあると共に、夾雑物を除去する夾雑物除去槽を前記流量調整槽の上流に設けてあり、前記好気処理槽の曝気を停止してある合併浄化槽
Water to be treated is transferred from the first casing, which is an independent treatment septic tank, in which an aerobic treatment tank for aerobically treating the water to be treated to a second casing in which an activated sludge treatment tank for treating the treated water is activated. In the merged septic tank that is set up so that it can freely move,
A household wastewater pipe for allowing household wastewater to flow in is connected to the second casing, and a flow rate adjustment tank for storing the treated water and adjusting the flow rate is provided upstream of the activated sludge treatment tank in the second casing. the provided Oh Rutotomoni, Ri Oh provided contaminant removal bath to remove contaminants upstream of the flow regulation tank, septic tanks where the are stops aeration aerobic treatment tank.
少なくとも被処理水を好気処理する好気処理槽を内装する単独処理浄化槽である第一ケーシングから、被処理水を活性汚泥処理する活性汚泥処理槽を内装する第二ケーシングへと被処理水が移流自在になるように設けてある合併浄化槽において、
生活雑排水を流入させる生活雑排水配管が前記第一ケーシングに接続してあると共に、前記第二ケーシングに対して、被処理水を貯留して流量を調整する流量調整槽を前記活性汚泥処理槽の上流に、夾雑物を除去する夾雑物除去槽を前記流量調整槽の上流にそれぞれ設けてある合併浄化槽。
Water to be treated is transferred from the first casing, which is an independent treatment septic tank, in which an aerobic treatment tank for aerobically treating the water to be treated to a second casing in which an activated sludge treatment tank for treating the treated water is activated. In the merged septic tank that is set up so that it can freely move,
A household wastewater pipe for allowing household wastewater to flow is connected to the first casing, and a flow rate adjustment tank for storing treated water and adjusting the flow rate with respect to the second casing is the activated sludge treatment tank. A combined septic tank in which a contaminant removal tank for removing impurities is provided upstream of the flow rate adjustment tank.
前記夾雑物除去槽に下端部に開口部のある移流管を設け、前記移流管の上端部に、前記夾雑物除去槽を所定水位以上にする前記被処理水を前記流量調整槽以外へ案内する案内路を設けてある請求項又はに記載の合併浄化槽。The contaminant removal tank is provided with an advection pipe having an opening at the lower end, and the treated water that brings the contaminant removal tank to a predetermined water level or higher is guided to the upper end of the advection pipe to other than the flow rate adjustment tank. The merged septic tank according to claim 1 or 2 , wherein a guide path is provided.
JP2001197950A 2001-06-29 2001-06-29 Merged septic tank Expired - Fee Related JP4046488B2 (en)

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