Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3936564B2 - Apparatus for improving existing livestock wastewater storage tank and method for improving the same - Google Patents
[go: Go Back, main page]

JP3936564B2 - Apparatus for improving existing livestock wastewater storage tank and method for improving the same - Google Patents

Apparatus for improving existing livestock wastewater storage tank and method for improving the same Download PDF

Info

Publication number
JP3936564B2
JP3936564B2 JP2001306853A JP2001306853A JP3936564B2 JP 3936564 B2 JP3936564 B2 JP 3936564B2 JP 2001306853 A JP2001306853 A JP 2001306853A JP 2001306853 A JP2001306853 A JP 2001306853A JP 3936564 B2 JP3936564 B2 JP 3936564B2
Authority
JP
Japan
Prior art keywords
livestock wastewater
tank
membrane separation
sludge
tank body
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2001306853A
Other languages
Japanese (ja)
Other versions
JP2003112193A (en
Inventor
田中  理
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Maezawa Kasei Industries Co Ltd
Original Assignee
Maezawa Kasei Industries Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Maezawa Kasei Industries Co Ltd filed Critical Maezawa Kasei Industries Co Ltd
Priority to JP2001306853A priority Critical patent/JP3936564B2/en
Publication of JP2003112193A publication Critical patent/JP2003112193A/en
Application granted granted Critical
Publication of JP3936564B2 publication Critical patent/JP3936564B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Treatment Of Sludge (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、畜産排水が貯留される貯留槽と、この貯留槽に貯留された畜産排水を曝気する曝気手段とを備えた既設畜産排水貯留槽の改善装置およびその改善方法に関する。
【0002】
【従来の技術】
従来、中小規模の畜産農家などは、これら畜産農家が飼育する牛や豚などの家畜から排泄される畜産排泄物としての糞尿のうち、固形分をスクリーンで取り除いた排水である畜産排水を貯留槽としての尿溜め槽に流入させて、この尿溜め槽に貯留させ、この尿溜め槽に貯留させた畜産排水を、例えばブロワなどの曝気手段にて曝気して、この畜産排水を液肥化させたり、脱臭させたりしている。
【0003】
そして、この尿溜め槽に貯留された畜産排水を一定期間毎に、バキュームなどにより吸い出して、尿溜め槽にて処理された畜産排水を液肥として農地などに散布して利用したり、処理業者にて処分したりしている。
【0004】
ところが、畜産排水を処理業者で処分してもらうには多大な費用が掛かり、畜産排水を十分に液肥化させるには多大な時間を要するとともに、畜産排水から生成された液肥の利用先がないなどといった問題がある。
【0005】
また、既設の尿溜め槽を排水処理施設に変更するためには、この尿溜め槽を改修するためにこの尿溜め槽に貯留させた畜産排水を抜き出したり、この尿溜め槽への畜産排水の流入を一時的に停止させなければならないから、この尿溜め槽の処理能力の改善が容易ではない。
【0006】
【発明が解決しようとする課題】
上述したように、既設の尿溜め槽による畜産排水の処理能力を改善させるためには、多大な費用や時間が必要であるため、この既設の尿溜め槽による畜産排水の処理能力の改善が容易ではないという問題を有している。
【0007】
本発明は、このような点に鑑みなされたもので、既設畜産排水貯留槽による畜産排水の処理能力を容易に改善できる既設畜産排水貯留槽の改善装置およびその改善方法を提供することを目的とする。
【0008】
【課題を解決するための手段】
請求項1記載の既設畜産排水貯留槽の改善装置は、畜産排水が貯留される槽本体と、この槽本体に貯留された畜産排水を曝気する曝気手段と、畜産排水を前記槽本体へと流入させる流入管とを備えた既設畜産排水貯留槽の改善装置であって、前記槽本体に貯留された畜産排水が流入される膜分離槽と、この膜分離槽に流入された畜産排水を膜分離する膜分離手段と、前記膜分離槽内の汚泥を前記流入管へ返送する汚泥返送手段と、この汚泥返送手段にて返送される汚泥にオゾンを供給する供給手段とを具備し、前記汚泥返送手段は、前記膜分離槽内から吸い出され前記供給手段にてオゾンが供給された汚泥を前記流入管内へ返送させるものである。
【0009】
請求項2記載の既設畜産排水貯留槽の改善方法は、畜産排水が貯留される槽本体と、この槽本体に貯留された畜産排水を曝気する曝気手段と、畜産排水を前記槽本体へと流入させる流入管とを備えた既設畜産排水貯留槽の改善方法であって、前記槽本体に貯留された畜産排水が流入される膜分離槽を設け、この膜分離槽に流入された畜産排水を膜分離する膜分離手段を設け、前記膜分離槽内の汚泥を前記流入管へ返送する汚泥返送手段を設け、この汚泥返送手段にて返送される汚泥にオゾンを供給する供給手段を設け、前記膜分離槽内から吸い出し前記供給手段にてオゾンを供給した汚泥を、前記汚泥返送手段にて前記流入管内へ返送させるものである。
【0010】
そして、既設畜産排水貯留槽の槽本体に貯留され、この既設畜産排水貯留槽の曝気手段にて曝気された畜産排水を膜分離槽に流入させ、この膜分離槽に流入させた畜産排水を膜分離手段にて膜分離する。このとき、膜分離手段による畜産排水の膜分離により膜分離槽に汚泥が生じる。そこで、この汚泥を汚泥返送手段にて槽本体に返送させるとともに、この汚泥返送手段にて返送される汚泥に供給手段にてオゾンを供給する。この結果、既設畜産排水貯留槽に貯留された畜産排水がより効率良く処理される。また、既設畜産排水貯留槽の槽本体に貯留させた畜産排水を抜いたり、この槽本体への畜産排水の貯留を停止させたりすることなく、この既設畜産排水貯留槽に、膜分離槽、膜分離手段、汚泥返送手段および供給手段それぞれが取り付けられるから、この既設畜産排水貯留槽による畜産排水の処理能力が容易に改善される。
【0011】
また、汚泥返送手段にて返送される汚泥に供給手段がオゾンを供給するので、既設畜産排水貯留槽の槽本体に貯留された畜産排水に含まれる難分解性の物質がオゾンにてより分解されやすくなるから、この既設畜産排水貯留槽による畜産排水の処理能力がより改善される。
【0012】
さらに、畜産排水を槽本体へと流入させる流入管にオゾンを含んだ汚泥を返送させることにより、畜産排水の原水中に含まれる高濃度の難分解性物質が、槽本体内に流入して拡散してしまう前のより高濃度な状態でオゾンに接触する。このため、より効果的に畜産排水の酸化分解および脱臭が促進され、尿石やスケールなどの発生を防止できる。
【0013】
【発明の実施の形態】
以下、本発明の既設畜産排水貯留槽の改善装置に関連した実施の形態の構成を図1および図2を参照して説明する。
【0014】
図1および図2において、1は既設畜産排水貯留槽としての尿溜め槽で、この尿溜め槽1は、中小規模の畜産農家の敷地内などに既設され、この畜産農家が飼育する牛や豚などの家畜から排泄される畜産排泄物としての糞尿のうち、固形分をスクリーンで取り除いた排水である畜産排水Dを流入させて、この畜産排水Dを貯留させて浄化する。また、この尿溜め槽1は、図2に示すように、畜産排水Dが貯留される槽本体2を備えており、この槽本体2には、この槽本体2へと畜産排水Dを流入させる流入管3が取り付けられている。この結果、この流入管3の下流端には、槽本体2に畜産排水Dを流入させる流入口4が形成されている。
【0015】
また、槽本体2には、この槽本体2の内部に貯留された畜産排水Dを液肥化および脱臭させる曝気手段としての散気装置5が取り付けられている。
【0016】
この散気装置5は、槽本体2内における底面上に設置され、この底面を略閉塞する略円盤状の散気手段としての散気ディスク6を備えている。この散気ディスク6には、この散気ディスク6へと空気を供給する空気供給手段としてのブロワ7が散気管8を介して接続されている。そして、この散気管8の中間域には、この散気管8の内部を通過する空気の逆流を防止する図示しない逆止弁が取り付けられている。
【0017】
一方、既設の尿溜め槽1には、この尿溜め槽1の槽本体2内に貯留させた畜産排水Dを抜くことなく、さらには、この尿溜め槽1を取り壊すことなく、この尿溜め槽1の槽本体2内に貯留される畜産排水Dの処理能力を改善させて、この畜産排水Dの処理水を放流規制値以下にする新規追加設備としての改善装置11が後付けにて取り付けられている。
【0018】
この改善装置11は、図1に示すように、尿溜め槽1にて生物処理された畜産排水Dが流入されてこの畜産排水Dが貯留される膜分離槽12を備えている。この膜分離槽12は、尿溜め槽1の槽本体2に並設されている。また、この槽本体2と膜分離槽12との間には、この槽本体2に所定量の畜産排水Dが貯留された際に、この畜産排水D内の所定量より増加した一部の畜産排水Dを膜分離槽12へと越流させる越流手段としての越流部13が取り付けられている。
【0019】
さらに、膜分離槽12には、この膜分離槽12内に流入された畜産排水Dを曝気して、この畜産排水D中の溶存酸素量を向上させ、この畜産排水Dを生物処理させる曝気手段としての散気装置14が取り付けられている。また、この散気装置14は、後述のブロワ16により送り込まれた空気を膜分離槽12内の畜産排水D中に吐出させることにより、後述の膜分離装置21の分離膜23への汚泥Mの付着を防止する。
【0020】
そして、この散気装置14の散気ディスク15は、膜分離槽12内における底面上に設置されている。また、この散気ディスク15には、この散気ディスク15へと空気を供給する空気供給手段としてのブロワ16が散気管17を介して接続されている。そして、この散気管17の中間域には、この散気管17内を通過する空気の逆流を防止する図示しない逆止弁が取り付けられている。
【0021】
また、膜分離槽12内には、この膜分離槽12に流入された畜産排水Dを膜分離にて処理する膜分離手段としての膜分離装置21が取り付けられている。この膜分離装置21は、膜分離槽12内の畜産排水D中の固形分を濾過する。さらに、この膜分離装置21は、膜分離槽12内における略中心部に配設されている。また、この膜分離装置21には、この膜分離装置21にて膜分離された膜分離水としての処理水を河川などへと放流させる放流管22が取り付けられている。
【0022】
さらに、この膜分離装置21は、膜分離槽12に流入された畜産排水Dを膜分離する分離膜23を備えている。この分離膜23には、孔径が0.45μm以下の多数の孔が形成されている。
【0023】
また、膜分離槽12には、この膜分離槽12に流入された畜産排水Dを膜分離する際に濃縮される汚泥Mを吸い出して、この汚泥Mを尿溜め槽1の槽本体2に返送させる汚泥返送手段24が取り付けられている。この汚泥返送手段24は、膜分離槽12の外側面の下方に流入側が連通された細長円筒状の汚泥返送管25を備えている。この汚泥返送管25の流出側は、尿溜め槽1の槽本体2の上方に位置しており、この汚泥返送管25の流出側へと送られた汚泥Mを尿溜め槽1の槽本体2の内部へと返送する。
【0024】
ここで、汚泥返送手段24は、膜分離槽12に流入させた畜産排水Dにおける高濃度の微生物の活性化を維持するために、膜分離槽12内の畜産排水D中の活性汚泥Mの濃度(Mixed Liquor Suspended Solids:MLSS)を、15000mg/l程度にする。
【0025】
さらに、この汚泥返送管25の中間部には、この汚泥返送管25を用いて膜分離槽12の底面部に堆積した汚泥Mを吸い出す汚泥返送ポンプ26が取り付けられている。また、汚泥返送管25の汚泥返送ポンプ26よりも下流側には、この汚泥返送管25内を通過する汚泥Mに空気を供給する供給手段としての汚泥曝気手段であるエジェクタ27が取り付けられている。このエジェクタ27には、外部から空気を汚泥返送管25の内部へと導入させる導入口28が開口されている。また、このエジェクタ27は、散気装置5による槽本体2内の畜産排水Dの曝気を助け、この畜産排水Dの溶存酸素量を向上させる。
【0026】
次に、上記関連した実施の形態の既設尿溜め槽の改善方法について説明する。
【0027】
まず、図2に示す既設の尿溜め槽1の槽本体2に隣接させて膜分離槽12を構築する。
【0028】
そして、この膜分離槽12と槽本体2との間に越流部13を形成するとともに、この膜分離槽12に汚泥返送手段24を取り付ける。
【0029】
この後、この膜分離槽12に散気装置14を取り付けるとともに、膜分離装置21を取り付けて、図1に示す畜産排水処理設備を構築する。
【0030】
次に、上記関連した実施の形態の畜産排水の処理方法を説明する。
【0031】
まず、家畜などの排泄物のうち固形分と分離された尿だけが流入管3からこの尿溜め槽1の槽本体2内に畜産排水Dが貯留される。
【0032】
すると、この槽本体2内に貯留された畜産排水Dは、この槽本体2内で散気装置5にて曝気され、この畜産排水D中の溶存酸素量が向上されて生物処理される。
【0033】
そして、槽本体2内に貯留された畜産排水Dの液面が越流部13より上昇すると、この畜産排水Dの一部が越流部13から膜分離槽12内へと越流してこの膜分離槽12内に流入される。
【0034】
すると、この膜分離槽12内に流入された畜産排水Dは、この膜分離槽12内で散気装置14にてさらに曝気され、この畜産排水D中の溶存酸素量が向上されて生物処理が促進される。
【0035】
さらに、この膜分離槽12内に流入された畜産排水Dは、膜分離装置21にて膜分離される。そして、この膜分離装置21にて膜分離された処理水は、放流管22にて河川などへと放流される。
【0036】
また、膜分離装置21による畜産排水Dの膜分離により膜分離槽12の底部に汚泥Mが沈殿する。この汚泥Mは、汚泥返送手段24にて尿溜め槽1の槽本体2へと返送される。このとき、汚泥返送手段24のエジェクタ27により汚泥返送管25内を流れる汚泥Mに空気を取り込ませて、この汚泥Mが返送される尿溜め槽1の槽本体2中の畜産排水Dの溶存酸素量を向上させる。
【0037】
上述したように、上記関連した実施の形態によれば、既設の尿溜め槽1の槽本体2に貯留させた畜産排水Dを抜いたり、この槽本体2への畜産排水Dの貯留を停止させたりすることなく、この既設の尿溜め槽1の下流側に改善装置11を増設できるから、既設の尿溜め槽1をそのまま使用でき、この尿溜め槽1の槽本体2に貯留された畜産排水Dの処理能力を容易に向上させて改善できるとともに、この改善装置11により尿溜め槽1の槽本体2に貯留される畜産排水Dの処理水を河川などに放流できる。よって、尿溜め槽1の槽本体2に貯留させた畜産排水Dを、バキュームなどで汲み出して、液肥として利用するとの名目で農地などに散布する必要がなくなる。
【0038】
また、尿溜め槽1の槽本体2に貯留させた畜産排水Dを膜分離槽12に流入させて膜分離装置21で膜分離するので、尿溜め槽1の槽本体2に貯留させた畜産排水Dを膜分離以外の方法でさらに処理する場合に比べ、最小限の設備で良好な畜産排水処理設備へと変更できる。よって、改善装置11のコンパクトかつ施工が容易であるので、既設の尿溜め槽1の改善の施工性を向上できる。
【0039】
さらに、膜分離槽12に汚泥返送管25を接続して、この汚泥返送管25にエジェクタ27を取り付けて、この汚泥返送管25内を通過する汚泥Mに空気を取り込ませることにより、既設の尿溜め槽1に設けた散気装置5の散気管8やブロワ7を改造などして、この散気装置5による散気効率を向上させることなく、この尿溜め槽1の槽本体2に貯留させた畜産排水D中の溶存酸素量を適切な値に向上できる。
【0040】
次に、本発明の実施の形態の構成を図3を参照して説明する。
【0041】
この図2に示す改善装置11は、基本的には図1および図2に示す改善装置11と同様であるが、さらに上流の尿溜め槽1の流入管3に汚泥返送管25の下流端を接続させて、この流入管3に膜分離槽12内に沈殿する汚泥Mを返送する。
【0042】
また、汚泥返送手段24の汚泥返送管25に接続されたエジェクタ27の導入口28には、図示しないオゾン発生装置が接続されており、このオゾン発生装置にて発生したオゾン(O)を、汚泥返送管25内を通過する汚泥Mに接触させる。
【0043】
この結果、この図2に示す改善装置11は、尿溜め槽1の槽本体2から越流部13にて越流した畜産排水Dが膜分離槽12に流入され、この膜分離槽12内に流入された畜産排水Dが膜分離装置21にて膜分離されるとともに、この膜分離装置21による膜分離にて生じる汚泥Mが汚泥返送手段24にて尿溜め槽1の槽本体2へと返送されるので、図1および図2に示す改善装置11と同様の作用効果を奏することができる。
【0044】
さらに、汚泥返送管25の下流端を尿溜め槽1の流入管3に接続させて、この汚泥返送管25にて返送される汚泥Mをさらに上流に返送することにより、尿溜め槽1の槽本体2に貯留される畜産排水D中の溶存酸素量をより向上できるから、この槽本体2による畜産排水Dの処理をより効率良くでき、既設の尿溜め槽1による畜産排水Dの処理能力をより改善できる。
【0045】
また、オゾン発生装置にて発生したオゾンを、汚泥返送管25内を通過する汚泥Mに取り込ませることにより、このオゾンが有する強力な酸化作用にて、尿溜め槽1の槽本体2に貯留された畜産排水Dに含まれる難分解性の物質がより分解されやすくなるから、尿溜め槽1による畜産排水Dの処理能力をより改善できる。
【0046】
すなわち、尿溜め槽1の流入管3にオゾンを含んだ汚泥Mを返送させることにより、畜産排水Dの原水中に含まれる高濃度の難分解性物質が、尿溜め槽1の槽本体2内に流入して拡散してしまう前のより高濃度な状態でオゾンに接触するから、より効果的に畜産排水Dの酸化分解および脱臭を促進でき、尿溜め槽1や改善装置11への尿石やスケールなどの発生を防止できる。
【0047】
なお、上記各実施の形態では、尿溜め槽1の槽本体2に貯留させた畜産排水Dを越流部13にて膜分離槽12に越流させているが、尿溜め槽1の槽本体2内に貯留された畜産排水Dをポンプアップなどにて膜分離槽12へと送ってもよい。
【0048】
また、汚泥返送ポンプ26とエジェクタ27とを別体として構成したが、これら汚泥返送ポンプ26およびエジェクタ27を一体として構成してもよい。
【0049】
【発明の効果】
請求項1記載の既設畜産排水貯留槽の改善装置および請求項2記載の既設畜産排水貯留槽の改善方法によれば、既設畜産排水貯留槽の槽本体に貯留され、この既設畜産排水貯留槽の曝気手段にて曝気された畜産排水を膜分離槽に流入させ、この膜分離槽に流入させた畜産排水を膜分離手段にて膜分離すると、膜分離手段による畜産排水の膜分離により膜分離槽に汚泥が生じるので、この汚泥を汚泥返送手段にて槽本体に返送させるとともに、この汚泥返送手段にて返送される汚泥に供給手段にてオゾンを供給すれば、既設畜産排水貯留槽に貯留された畜産排水をより効率良く処理でき、また、既設畜産排水貯留槽の槽本体に貯留させた畜産排水を抜いたり、この槽本体への畜産排水の貯留を停止させたりすることなく、この既設畜産排水貯留槽に、膜分離槽、膜分離手段、汚泥返送手段および供給手段それぞれが取り付けられるから、この既設畜産排水貯留槽による畜産排水の処理能力を容易に改善できる。
【0050】
また、汚泥返送手段にて返送される汚泥に供給手段にてオゾンを供給すれば、既設畜産排水貯留槽の槽本体に貯留された畜産排水に含まれる難分解性の物質がオゾンにてより分解されやすくなるから、この既設畜産排水貯留槽による畜産排水の処理能力をより改善できる。
【0051】
さらに、畜産排水を槽本体へと流入させる流入管にオゾンを含んだ汚泥を返送させることにより、畜産排水の原水中に含まれる高濃度の難分解性物質が、槽本体内に流入して拡散してしまう前のより高濃度な状態でオゾンに接触するから、より効果的に畜産排水の酸化分解および脱臭を促進でき、尿石やスケールなどの発生を防止できる。
【図面の簡単な説明】
【図1】 本発明の既設畜産排水貯留槽の改善装置の関連した実施の形態を示す説明図である。
【図2】 同上既設畜産排水貯留槽を示す説明図である。
【図3】 本発明の実施の形態の既設畜産排水貯留槽の改善装置を示す説明図である。
【符号の説明】
1 既設畜産排水貯留槽としての尿溜め槽
2 槽本体
3 流入管
5 曝気手段としての散気装置
11 改善装置
12 膜分離槽
21 膜分離手段としての膜分離装置
24 汚泥返送手段
27 供給手段としてのエジェクタ
D 畜産排水
M 汚泥
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an improvement device for an existing livestock wastewater storage tank including a storage tank in which livestock wastewater is stored and aeration means for aeration of livestock wastewater stored in the storage tank, and a method for improving the same .
[0002]
[Prior art]
Conventionally, small and medium-sized livestock farmers have stored livestock wastewater, which is drainage from which solids have been removed from the excreta as livestock excretion excreted from livestock such as cattle and pigs raised by these livestock farmers. The livestock wastewater stored in the urine reservoir is aerated by aeration means such as a blower, and the livestock wastewater is liquefied. Or deodorizing.
[0003]
And the livestock wastewater stored in this urine storage tank is sucked out by vacuum etc. at regular intervals, and the livestock wastewater processed in the urine storage tank is sprayed and used as liquid manure on farmland etc. Or dispose of it.
[0004]
However, it takes a lot of money to dispose of livestock wastewater at a processing company, and it takes a lot of time to fully fertilize livestock wastewater, and there is no use of liquid fertilizer generated from livestock wastewater. There is a problem.
[0005]
In addition, in order to change the existing urine storage tank to a wastewater treatment facility, the livestock wastewater stored in the urine storage tank is withdrawn in order to renovate the urine storage tank, or the livestock drainage to this urine storage tank is removed. Since the inflow must be temporarily stopped, it is not easy to improve the processing capacity of the urine tank.
[0006]
[Problems to be solved by the invention]
As described above, in order to improve the processing capacity of livestock wastewater using the existing urine tank, it is necessary to spend a great deal of time and money, so it is easy to improve the processing capacity of livestock wastewater using this existing urine tank. It has a problem of not.
[0007]
This invention is made in view of such a point, and it aims at providing the improvement apparatus of the existing livestock wastewater storage tank which can improve the processing capacity of the livestock wastewater by the existing livestock wastewater storage tank, and its improvement method To do.
[0008]
[Means for Solving the Problems]
The apparatus for improving an existing livestock wastewater storage tank according to claim 1 includes a tank body in which livestock wastewater is stored, aeration means for aeration of livestock wastewater stored in the tank body, and the livestock wastewater flowing into the tank body An apparatus for improving an existing livestock wastewater storage tank provided with an inflow pipe , wherein a membrane separation tank into which livestock wastewater stored in the tank body flows, and a livestock wastewater that has flowed into the membrane separation tank are subjected to membrane separation and membrane separation means for, comprising a sludge return means to return your sludge of the membrane separation tank to the inlet pipe, and a supply means for supplying ozone into the sludge that is returned by this sludge return means, the sludge returning means, the ozone is supplied sludge by the membrane is sucked from the separation tank in the supply means, it is intended to return to the inlet pipe.
[0009]
The method for improving an existing livestock wastewater storage tank according to claim 2 is a tank body in which livestock wastewater is stored, an aeration means for aeration of livestock wastewater stored in the tank body, and the livestock wastewater flowing into the tank body A method for improving an existing livestock wastewater storage tank provided with an inflow pipe, wherein a membrane separation tank into which livestock wastewater stored in the tank body is introduced is provided, and the livestock wastewater flowing into the membrane separation tank is formed into a membrane A membrane separation means for separating, a sludge return means for returning sludge in the membrane separation tank to the inflow pipe, a supply means for supplying ozone to the sludge returned by the sludge return means, The sludge sucked out from the separation tank and supplied with ozone by the supply means is returned to the inflow pipe by the sludge return means.
[0010]
Then, the livestock wastewater stored in the tank body of the existing livestock wastewater storage tank and aerated by the aeration means of the existing livestock wastewater storage tank is caused to flow into the membrane separation tank, and the livestock wastewater that has flowed into the membrane separation tank is converted into a membrane. The membrane is separated by a separation means. At this time, sludge is generated in the membrane separation tank by membrane separation of livestock wastewater by the membrane separation means. Therefore, the sludge is returned to the tank body by the sludge return means, and ozone is supplied to the sludge returned by the sludge return means by the supply means. As a result, the livestock wastewater stored in the existing livestock wastewater storage tank is processed more efficiently. In addition, without removing the livestock wastewater stored in the tank body of the existing livestock wastewater storage tank or stopping the storage of livestock wastewater in this tank body, this existing livestock wastewater storage tank can be equipped with a membrane separation tank, membrane Since each of the separation means, the sludge return means and the supply means is attached, the processing capacity of livestock wastewater by this existing livestock wastewater storage tank is easily improved.
[0011]
In addition, since the supply means supplies ozone to the sludge returned by the sludge return means, the hardly decomposable substances contained in the livestock wastewater stored in the tank body of the existing livestock wastewater storage tank are further decomposed by ozone. Since it becomes easy, the processing capacity of the livestock wastewater by this existing livestock wastewater storage tank is improved more.
[0012]
Furthermore, by returning sludge containing ozone to the inflow pipe through which livestock wastewater flows into the tank body, high-concentration refractory substances contained in the raw water of livestock wastewater flow into the tank body and diffuse. It comes in contact with ozone in a higher concentration state before it is done. For this reason, oxidative decomposition and deodorization of livestock wastewater are promoted more effectively, and generation of urine stones and scales can be prevented.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the configuration of an embodiment related to the improvement device for an existing livestock wastewater storage tank of the present invention will be described with reference to FIGS. 1 and 2.
[0014]
1 and 2, reference numeral 1 denotes a urine storage tank as an existing livestock drainage storage tank. This urine storage tank 1 is already installed on the grounds of small and medium-sized livestock farmers, and cattle and pigs raised by this livestock farmer. The livestock wastewater D, which is wastewater from which solid content has been removed with a screen, is introduced into the excreta excreted from livestock such as livestock excreta, and the livestock wastewater D is stored and purified. Further, as shown in FIG. 2, the urine storage tank 1 includes a tank body 2 in which livestock wastewater D is stored, and the livestock wastewater D flows into the tank body 2 into the tank body 2. An inflow pipe 3 is attached. As a result, at the downstream end of the inflow pipe 3, an inflow port 4 through which the livestock wastewater D flows into the tank body 2 is formed.
[0015]
The tank body 2 is provided with an aeration device 5 as aeration means for liquid fertilizing and deodorizing the livestock wastewater D stored in the tank body 2.
[0016]
The air diffuser 5 is provided on a bottom surface in the tank body 2 and includes an air diffuser disk 6 as a substantially disk-shaped air diffuser that substantially closes the bottom surface. A blower 7 serving as an air supply means for supplying air to the diffuser disk 6 is connected to the diffuser disk 6 via an air diffuser 8. A check valve (not shown) that prevents the backflow of air passing through the inside of the air diffuser 8 is attached to an intermediate region of the air diffuser 8.
[0017]
On the other hand, in the existing urine reservoir 1, the urine reservoir 1 is collected without removing the livestock drainage D stored in the tank body 2 of the urine reservoir 1, and further without demolishing the urine reservoir 1. The improvement device 11 as a new additional equipment is installed later to improve the processing capacity of the livestock wastewater D stored in the tank body 2 of 1 and make the treated water of the livestock wastewater D below the discharge regulation value. Yes.
[0018]
As shown in FIG. 1, the improvement device 11 includes a membrane separation tank 12 into which livestock wastewater D biologically treated in the urine storage tank 1 flows and the livestock wastewater D is stored. The membrane separation tank 12 is arranged in parallel with the tank body 2 of the urine reservoir 1. In addition, when a predetermined amount of livestock wastewater D is stored in the tank body 2 between the tank body 2 and the membrane separation tank 12, a part of the livestock increased from the predetermined amount in the livestock wastewater D. An overflow section 13 is attached as overflow means for allowing the drainage D to overflow into the membrane separation tank 12.
[0019]
Further, the membrane separation tank 12 is aerated by aeration of the livestock wastewater D flowing into the membrane separation tank 12 to improve the amount of dissolved oxygen in the livestock wastewater D and biologically treating the livestock wastewater D. As a diffuser 14 is attached. In addition, the air diffuser 14 discharges air fed by a blower 16 described later into the livestock wastewater D in the membrane separation tank 12, thereby allowing the sludge M to be applied to the separation membrane 23 of the membrane separator 21 described later. Prevent adhesion.
[0020]
The diffuser disk 15 of the diffuser 14 is installed on the bottom surface in the membrane separation tank 12. A blower 16 serving as an air supply means for supplying air to the diffuser disk 15 is connected to the diffuser disk 15 via an air diffuser 17. A check valve (not shown) that prevents the backflow of air passing through the air diffuser 17 is attached to an intermediate region of the air diffuser 17.
[0021]
Further, in the membrane separation tank 12, a membrane separation device 21 is attached as a membrane separation means for processing livestock wastewater D flowing into the membrane separation tank 12 by membrane separation. The membrane separation device 21 filters the solid content in the livestock wastewater D in the membrane separation tank 12. Further, the membrane separation device 21 is disposed at a substantially central portion in the membrane separation tank 12. The membrane separation device 21 is provided with a discharge pipe 22 for discharging treated water as membrane separation water separated by the membrane separation device 21 to a river or the like.
[0022]
Further, the membrane separation device 21 is provided with a separation membrane 23 for membrane separation of livestock wastewater D flowing into the membrane separation tank 12. In the separation membrane 23, a large number of holes having a hole diameter of 0.45 μm or less are formed.
[0023]
Further, the membrane separation tank 12 sucks out the sludge M concentrated when the livestock wastewater D flowing into the membrane separation tank 12 is subjected to membrane separation, and returns the sludge M to the tank body 2 of the urine storage tank 1. The sludge returning means 24 is attached. The sludge return means 24 includes an elongated cylindrical sludge return pipe 25 having an inflow side communicating with the lower side of the outer surface of the membrane separation tank 12. The outflow side of the sludge return pipe 25 is located above the tank body 2 of the urine storage tank 1, and the sludge M sent to the outflow side of the sludge return pipe 25 is stored in the tank body 2 of the urine storage tank 1. Return to the inside.
[0024]
Here, the sludge returning means 24 is used to maintain the activation of high-concentration microorganisms in the livestock wastewater D flowing into the membrane separation tank 12, and the concentration of the activated sludge M in the livestock wastewater D in the membrane separation tank 12 (Mixed Liquor Suspended Solids: MLSS) is set to about 15000 mg / l.
[0025]
Further, a sludge return pump 26 for sucking out the sludge M accumulated on the bottom surface of the membrane separation tank 12 using the sludge return pipe 25 is attached to an intermediate portion of the sludge return pipe 25. Further, an ejector 27 that is a sludge aeration means as a supply means for supplying air to the sludge M passing through the sludge return pipe 25 is attached to the sludge return pipe 25 downstream of the sludge return pump 26. . The ejector 27 has an introduction port 28 through which air is introduced from the outside into the sludge return pipe 25. Further, the ejector 27 helps the aeration of the livestock wastewater D in the tank body 2 by the air diffuser 5 and improves the dissolved oxygen amount of the livestock wastewater D.
[0026]
Next, the improvement method of the existing urine reservoir of the related embodiment will be described.
[0027]
First, the membrane separation tank 12 is constructed adjacent to the tank body 2 of the existing urine tank 1 shown in FIG.
[0028]
Then, an overflow section 13 is formed between the membrane separation tank 12 and the tank body 2, and a sludge return means 24 is attached to the membrane separation tank 12.
[0029]
Thereafter, the aeration device 14 is attached to the membrane separation tank 12, and the membrane separation device 21 is attached to construct the livestock wastewater treatment facility shown in FIG.
[0030]
Next, the processing method of the livestock wastewater of the said related embodiment is demonstrated.
[0031]
First, livestock wastewater D is stored in the tank body 2 of the urine storage tank 1 from the inflow pipe 3 only from the urine separated from the solid content of excrement such as livestock.
[0032]
Then, the livestock wastewater D stored in the tank body 2 is aerated by the aeration device 5 in the tank body 2, and the amount of dissolved oxygen in the livestock wastewater D is improved to be biologically treated.
[0033]
When the liquid level of the livestock wastewater D stored in the tank body 2 rises from the overflow section 13, a part of the livestock wastewater D overflows from the overflow section 13 into the membrane separation tank 12 and this membrane. It flows into the separation tank 12.
[0034]
Then, the livestock wastewater D that has flowed into the membrane separation tank 12 is further aerated in the membrane separation tank 12 by the air diffuser 14, and the amount of dissolved oxygen in the livestock wastewater D is improved so that the biological treatment can be performed. Promoted.
[0035]
Further, the livestock wastewater D flowing into the membrane separation tank 12 is subjected to membrane separation by the membrane separation device 21. Then, the treated water membrane-separated by the membrane separation device 21 is discharged into a river or the like through a discharge pipe 22.
[0036]
In addition, the sludge M is precipitated at the bottom of the membrane separation tank 12 by the membrane separation of the livestock wastewater D by the membrane separation device 21. This sludge M is returned to the tank body 2 of the urine reservoir 1 by the sludge return means 24. At this time, air is taken into the sludge M flowing in the sludge return pipe 25 by the ejector 27 of the sludge return means 24, and dissolved oxygen in the livestock wastewater D in the tank body 2 of the urine reservoir 1 to which this sludge M is returned. Improve the amount.
[0037]
As described above, according to the related embodiment, the livestock wastewater D stored in the tank body 2 of the existing urine tank 1 is removed, or the storage of the livestock wastewater D in the tank body 2 is stopped. Therefore, the improvement device 11 can be added to the downstream side of the existing urine storage tank 1, so that the existing urine storage tank 1 can be used as it is, and the livestock wastewater stored in the tank body 2 of the urine storage tank 1 is used. The treatment capacity of D can be easily improved and improved, and this improvement device 11 can discharge the treated water of livestock wastewater D stored in the tank body 2 of the urine tank 1 to a river or the like. Therefore, it is not necessary to pump the livestock wastewater D stored in the tank body 2 of the urine storage tank 1 with vacuum or the like and to spray it on farmland in the name of using it as liquid fertilizer.
[0038]
Moreover, since the livestock wastewater D stored in the tank body 2 of the urine tank 1 is flowed into the membrane separation tank 12 and membrane-separated by the membrane separation device 21, the livestock wastewater stored in the tank body 2 of the urine tank 1 is stored. Compared with the case where D is further processed by a method other than membrane separation, it can be changed to a good livestock wastewater treatment facility with minimum facilities. Therefore, since the improvement device 11 is compact and easy to install, the improvement workability of the existing urine reservoir 1 can be improved.
[0039]
Furthermore, the sludge return pipe 25 is connected to the membrane separation tank 12, an ejector 27 is attached to the sludge return pipe 25, and air is taken into the sludge M passing through the sludge return pipe 25, so that the existing urine is collected. The air diffuser 8 and the blower 7 of the air diffuser 5 provided in the reservoir 1 are modified so that the efficiency of the air diffused by the air diffuser 5 is not improved and stored in the tank body 2 of the urine reservoir 1. The amount of dissolved oxygen in the livestock wastewater D can be improved to an appropriate value.
[0040]
Next, the configuration of an embodiment of the present invention will be described with reference to FIG.
[0041]
The improvement device 11 shown in FIG. 2 is basically the same as the improvement device 11 shown in FIGS. 1 and 2, except that the downstream end of the sludge return pipe 25 is connected to the inflow pipe 3 of the upstream urine reservoir 1. The sludge M precipitated in the membrane separation tank 12 is returned to the inflow pipe 3 by being connected.
[0042]
Further, an ozone generator (not shown) is connected to the inlet 28 of the ejector 27 connected to the sludge return pipe 25 of the sludge return means 24, and ozone (O 3 ) generated by this ozone generator is The sludge is brought into contact with the sludge M passing through the sludge return pipe 25.
[0043]
As a result, in the improvement device 11 shown in FIG. 2, the livestock wastewater D overflowed from the tank body 2 of the urine storage tank 1 in the overflow section 13 flows into the membrane separation tank 12, and enters the membrane separation tank 12. The inflow of livestock wastewater D is separated by the membrane separation device 21 and the sludge M generated by the membrane separation by the membrane separation device 21 is returned to the tank body 2 of the urine storage tank 1 by the sludge return means 24. Therefore, the same operational effects as the improvement device 11 shown in FIGS. 1 and 2 can be obtained.
[0044]
Further, the downstream end of the sludge return pipe 25 is connected to the inflow pipe 3 of the urine storage tank 1, and the sludge M returned by the sludge return pipe 25 is returned further upstream, whereby the tank of the urine reservoir 1 is obtained. Since the amount of dissolved oxygen in the livestock wastewater D stored in the main body 2 can be further improved, the treatment of the livestock wastewater D by the tank body 2 can be made more efficient, and the processing capacity of the livestock wastewater D by the existing urine reservoir 1 can be increased. It can be improved.
[0045]
In addition, the ozone generated by the ozone generator is taken into the sludge M passing through the sludge return pipe 25, so that it is stored in the tank body 2 of the urine storage tank 1 by the strong oxidizing action of this ozone. Since the hardly decomposable substance contained in the livestock wastewater D is more easily decomposed, the processing capacity of the livestock wastewater D by the urine storage tank 1 can be further improved.
[0046]
That is, by returning the sludge M containing ozone to the inflow pipe 3 of the urine storage tank 1, the high-concentration hardly decomposable substance contained in the raw water of the livestock wastewater D is contained in the tank body 2 of the urine storage tank 1. Since it comes into contact with ozone in a higher concentration before it flows into and diffuses, it can more effectively promote oxidative degradation and deodorization of the livestock wastewater D, and urine stones to the urine tank 1 and the improvement device 11 And scale can be prevented.
[0047]
In each of the above embodiments, the livestock wastewater D stored in the tank body 2 of the urine tank 1 is overflowed to the membrane separation tank 12 at the overflow section 13. The livestock wastewater D stored in 2 may be sent to the membrane separation tank 12 by pumping up or the like.
[0048]
Further, although the sludge return pump 26 and the ejector 27 are configured as separate bodies, the sludge return pump 26 and the ejector 27 may be configured as a single unit.
[0049]
【The invention's effect】
According to the improvement device of the existing livestock drainage storage tank according to claim 1 and the improvement method of the existing livestock drainage storage tank according to claim 2 , the tank is stored in the tank body of the existing livestock drainage storage tank. When the livestock wastewater aerated by the aeration means flows into the membrane separation tank and the livestock wastewater flowed into the membrane separation tank is separated by the membrane separation means, the membrane separation tank is separated by the membrane separation of the livestock wastewater by the membrane separation means. If sludge is returned to the tank body by the sludge return means and ozone is supplied to the sludge returned by the sludge return means, the sludge is stored in the existing livestock wastewater storage tank. The livestock wastewater can be treated more efficiently, and the existing livestock wastewater can be treated without removing the livestock wastewater stored in the tank body of the existing livestock wastewater storage tank or stopping the storage of livestock wastewater in the tank body. Wastewater storage The membrane separation tank, the membrane separation unit, since each sludge return means and supply means are attached, the processing capacity of the livestock waste water according to the existing livestock waste water reservoir can be easily improved.
[0050]
In addition, if ozone is supplied by the supply means to the sludge returned by the sludge return means, the hardly decomposable substances contained in the livestock wastewater stored in the tank body of the existing livestock wastewater storage tank are further decomposed by ozone. Since it becomes easy to be done, the processing capacity of livestock wastewater by this existing livestock wastewater storage tank can be improved more.
[0051]
Furthermore, by returning sludge containing ozone to the inflow pipe through which livestock wastewater flows into the tank body, high-concentration refractory substances contained in the raw water of livestock wastewater flow into the tank body and diffuse. Since it comes into contact with ozone in a higher concentration state before it is consumed, the oxidative decomposition and deodorization of livestock wastewater can be promoted more effectively, and the occurrence of urine stones and scales can be prevented.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram showing a related embodiment of an improvement device for an existing livestock wastewater storage tank of the present invention.
FIG. 2 is an explanatory view showing an existing livestock drainage storage tank as described above.
FIG. 3 is an explanatory diagram showing an improvement device for an existing livestock wastewater storage tank according to an embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Urine reservoir tank as existing livestock drainage storage tank 2 Tank main body 3 Inflow pipe 5 Aeration device as aeration means
11 Improvement device
12 Membrane separation tank
21 Membrane separation device as membrane separation means
24 Sludge return means
27 Ejector as supply means D Livestock drainage M Sludge

Claims (2)

畜産排水が貯留される槽本体と、この槽本体に貯留された畜産排水を曝気する曝気手段と、畜産排水を前記槽本体へと流入させる流入管とを備えた既設畜産排水貯留槽の改善装置であって、
前記槽本体に貯留された畜産排水が流入される膜分離槽と、
この膜分離槽に流入された畜産排水を膜分離する膜分離手段と、
前記膜分離槽内の汚泥を前記流入管へ返送する汚泥返送手段と、
この汚泥返送手段にて返送される汚泥にオゾンを供給する供給手段とを具備し、
前記汚泥返送手段は、前記膜分離槽内から吸い出され前記供給手段にてオゾンが供給された汚泥を前記流入管内へ返送させる
ことを特徴とした既設畜産排水貯留槽の改善装置。
An apparatus for improving an existing livestock wastewater storage tank, comprising a tank body in which livestock wastewater is stored, aeration means for aeration of livestock wastewater stored in the tank body, and an inflow pipe for allowing livestock wastewater to flow into the tank body Because
A membrane separation tank into which livestock wastewater stored in the tank body flows,
Membrane separation means for membrane separation of livestock wastewater flowing into the membrane separation tank;
And sludge return means to return your sludge of the membrane separation tank to the inlet pipe,
This sludge is sent back by the sludge return means comprise a supply means for supplying ozone,
It said sludge return means, the membrane is sucked from the separation tank the sludge ozone is supplied at a delivery unit, improving apparatus existing livestock wastewater storage tank which is characterized in that is returned to the inlet pipe.
畜産排水が貯留される槽本体と、この槽本体に貯留された畜産排水を曝気する曝気手段と、畜産排水を前記槽本体へと流入させる流入管とを備えた既設畜産排水貯留槽の改善方法であって、A method for improving an existing livestock wastewater storage tank comprising a tank body in which livestock wastewater is stored, aeration means for aeration of livestock wastewater stored in the tank body, and an inflow pipe for allowing livestock wastewater to flow into the tank body Because
前記槽本体に貯留された畜産排水が流入される膜分離槽を設け、Provide a membrane separation tank into which livestock wastewater stored in the tank body flows,
この膜分離槽に流入された畜産排水を膜分離する膜分離手段を設け、Membrane separation means for membrane separation of livestock wastewater flowing into this membrane separation tank is provided,
前記膜分離槽内の汚泥を前記流入管へ返送する汚泥返送手段を設け、Providing a sludge return means for returning the sludge in the membrane separation tank to the inflow pipe;
この汚泥返送手段にて返送される汚泥にオゾンを供給する供給手段を設け、A supply means for supplying ozone to the sludge returned by this sludge return means is provided.
前記膜分離槽内から吸い出し前記供給手段にてオゾンを供給した汚泥を、前記汚泥返送手段にて前記流入管内へ返送させるThe sludge sucked out from the membrane separation tank and supplied with ozone by the supply means is returned to the inflow pipe by the sludge return means.
ことを特徴とする既設畜産排水貯留槽の改善方法。The improvement method of the existing livestock drainage storage tank characterized by this.
JP2001306853A 2001-10-02 2001-10-02 Apparatus for improving existing livestock wastewater storage tank and method for improving the same Expired - Lifetime JP3936564B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001306853A JP3936564B2 (en) 2001-10-02 2001-10-02 Apparatus for improving existing livestock wastewater storage tank and method for improving the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001306853A JP3936564B2 (en) 2001-10-02 2001-10-02 Apparatus for improving existing livestock wastewater storage tank and method for improving the same

Publications (2)

Publication Number Publication Date
JP2003112193A JP2003112193A (en) 2003-04-15
JP3936564B2 true JP3936564B2 (en) 2007-06-27

Family

ID=19126421

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001306853A Expired - Lifetime JP3936564B2 (en) 2001-10-02 2001-10-02 Apparatus for improving existing livestock wastewater storage tank and method for improving the same

Country Status (1)

Country Link
JP (1) JP3936564B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4253301B2 (en) * 2003-05-02 2009-04-08 大栄株式会社 Purification processing equipment
JP5448287B2 (en) * 2006-01-19 2014-03-19 三菱レイヨン株式会社 Membrane separation activated sludge treatment equipment
JP5183538B2 (en) * 2009-03-19 2013-04-17 日成プラント株式会社 Surplus sludge reduction device

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3052350B2 (en) * 1990-08-01 2000-06-12 栗田工業株式会社 Organic wastewater treatment equipment
JP3383498B2 (en) * 1995-11-30 2003-03-04 株式会社荏原製作所 Organic wastewater treatment method
JP3738377B2 (en) * 1997-03-24 2006-01-25 ユニチカ株式会社 Wastewater treatment method
JP3763444B2 (en) * 1999-01-19 2006-04-05 株式会社荏原製作所 Organic wastewater treatment method
JP2001087786A (en) * 1999-09-27 2001-04-03 Yoshimoto Pole Kk Sewage treating apparatus

Also Published As

Publication number Publication date
JP2003112193A (en) 2003-04-15

Similar Documents

Publication Publication Date Title
US6383369B2 (en) Waste and wastewater treatment and recycling system
CN102046256A (en) Backwash unsaturated wastewater filter device
JPH11221582A (en) Wastewater purification equipment
US6165359A (en) High strength wastewater treatment system
US4439317A (en) Sewage treatment system
US4350587A (en) Sewage treatment system
JP3936564B2 (en) Apparatus for improving existing livestock wastewater storage tank and method for improving the same
JP3744425B2 (en) Membrane separation wastewater treatment equipment
JP2002102662A (en) Livestock wastewater treatment system and solid-liquid separation method in primary settling basin, aeration tank and anaerobic tank to be used for the same
WO1988005334A1 (en) Methods and apparatus for liquid filtration
JP4381556B2 (en) Merger processing septic tank
JPS6254072B2 (en)
CN208577593U (en) A kind of combination MBR sewage treatment unit
JP4444430B2 (en) Method of merger treatment of single treatment septic tank
CN221701334U (en) A continuous circulation integrated biochemical tower for sewage treatment
JP3693135B2 (en) Integration of existing single treatment septic tank
CN218969044U (en) Combined domestic sewage treatment machine
JP2003010897A (en) Manure processing apparatus and manure processing method
CN211078813U (en) High-efficient intelligent sewage disinfection filter equipment
JPH01231994A (en) Sewage treatment equipment
JP2002346580A (en) Combination of existing individual treatment septic tank
JP4230089B2 (en) Merger processing septic tank
KR950013317B1 (en) Biological waste water treatment method
JP4960784B2 (en) ceramic
JPS6274489A (en) Recirculation aeration type sewage treatment apparatus

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040723

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20060126

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060301

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060405

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060816

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060908

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20070307

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20070323

R150 Certificate of patent or registration of utility model

Ref document number: 3936564

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100330

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110330

Year of fee payment: 4

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110330

Year of fee payment: 4

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110330

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120330

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120330

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130330

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130330

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140330

Year of fee payment: 7