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JP4178440B2 - Circulation type water supply and drainage equipment - Google Patents
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JP4178440B2 - Circulation type water supply and drainage equipment - Google Patents

Circulation type water supply and drainage equipment Download PDF

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JP4178440B2
JP4178440B2 JP2002019385A JP2002019385A JP4178440B2 JP 4178440 B2 JP4178440 B2 JP 4178440B2 JP 2002019385 A JP2002019385 A JP 2002019385A JP 2002019385 A JP2002019385 A JP 2002019385A JP 4178440 B2 JP4178440 B2 JP 4178440B2
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water
tank
storage tank
purification device
treatment tank
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JP2003211174A (en
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康豪 高嶋
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Description

【0001】
【発明の属する技術分野】
本発明は、各種施設や住宅などの生活系排水を浄化し循環させて再利用するとともに、雨水などを利用することによって、水道水の使用量をほぼゼロにしうる循環型給排水設備に関する。
【0002】
なお、本明細書において上水とは、厨房、浴室、洗面所などで使用する飲用可能な生活用水を言い、また、中水とは、トイレの便器に流す水や庭に散水する飲用とはならないがある程度きれいな水を言い、さらに、下水とは、上水や中水を使用した後のいわゆる汚水などを指すものである。
【0003】
また、本明細書においてバイオ処理とは、1)好気性菌類、嫌気性菌類、通性嫌気性菌類等すべての微生物群が共存・共栄・共生する微生物の生態系を創り上げること、2)複合微生物動態系において、すべての好気性及び嫌気性フザリウム属を不発生にすること、3)約20〜30億年以上前の古代菌の現生・発現により超高密度なエネルギーと情報の触媒作用が生じること、により、下水中に含まれる物質を分解消失することをいう。具体的には、微生物の持つ機能と基質と情報を利用し、あらゆる汚染物質の基礎に対して、その基質性に則した発酵法・増殖法・誘導法を駆使し、上記1)〜3)の状態にする。これを複合発酵法と呼ぶ。
【0004】
【従来の技術】
従来、各種施設や住宅などにおいては、上水道によって外部から取り入れた上水を、厨房の調理用水、トイレの流し水、洗面水、庭への散水などに使用し、使用後の下水は下水道によって浄水場に送り浄化処理した後、河川等に排水していた。また、地域によっては、前記浄水場の処理能力が不足して、下水を河川などに直接排水する場合もあった。
【0005】
【発明が解決しようとする課題】
上記のように上水道によって生活用水の供給を行い、下水道によって浄水場で浄化処理を行うというシステムの設備では、公共施設である上下水道設備に多額の経費がかかるだけでなく、下水を浄化処理する際には多量の汚泥が発生してその処理にも多大の手間と経費がかかるという問題があった。また、下水を河川などに直接排水すると、河川の汚染が進み、環境問題が発生するという問題がある。
【0006】
本発明は、前述の各問題を解消することを課題とし、該課題を解決した循環型給排水設備を提供することを目的とする。
【0007】
【課題を解決するための手段】
前記目的を達成するために、請求項1に記載した本発明の循環型給排水設備は、雨水などの中水を濾過した後に、二つの貯留槽に貯留し、必要に応じて前記各貯留槽から供給しうる水供給装置と、前記一方の貯留槽各別にから供給された中水を複合発酵により浄化して飲用可能な上水を得るための第1浄水装置と、前記他方の貯留槽の前記中水及び前記第1浄水装置からの上水をそれぞれ使用した後の下水を複合発酵により浄化して中水を得るための第2浄水装置とを備えた給排水設備を用いた循環型給排水設備であって、前記他方の貯留槽から送られた中水をトイレなどの中水使用場所に移送するとともに、この中水使用場所から送られた下水を第2浄水装置で順次浄化して前記他方の貯留槽に移送する一方、前記一方の貯留槽から送られた中水を第1浄水装置で浄化して飲用水となし、厨房などの上水使用場所に移送するとともに、この上水使用場所で出た下水を第2浄水装置に順次供給して浄化したうえ、前記他方の貯留槽に移送するように構成し、前記第1浄水装置及び第2浄水装置の装置本体には、所定の微生物を育成するとともに、エアーを送り込むようになした微生物処理槽と、シリカ触媒、カーボン触媒及びマテリアル触媒の鉱物触媒を積層してなる鉱物処理槽とを設け、前記微生物処理槽にて、あらかじめ水と、松、笹、梅、イチジク、桃、柿などの葉から抽出した抽出液と、オカラと、糖蜜とからなる原液から酵素を抽出してなる発酵を誘導するための酵素液を投入した被処理水を、槽内の微生物によりバイオ処理を行った後に、前記鉱物処理槽において、バイオ処理によって生成された固定窒素、生理活性物質、タンパク質結晶を消失させるように構成したものである。
【0008】
【発明の実施の形態】
以下に、本発明の好適な実施の形態を添付図面に基づいて詳細に説明する。ここにおいて、添付図面の図1は循環型給排水設備の概略図、図2は給排水設備を配備した施設の平面図、図3は給排水設備を配備した施設の正面図、図4は第1浄水装置の要部を縦断して示す正面図、図5は第1浄水装置における装置本体の横断平面図、図6は第1浄水装置における装置本体のエアー供給機構を示す横断平面図、図7は図4のA−A線断面図、図8は図4のB−B線断面図、図9は図4のC−C線断面図、図10は第2浄水装置の装置本体の縦断正面図、図11は第2浄水装置における装置本体の横断平面図、図12は第2浄水装置における本体装置のエアー供給機構を説明するための横断平面図、図13は図10のA−A線断面図、図14は図10のB−B線断面図、図15は図10のC−C線断面図、図16は図10のD−D線断面図ある。
【0009】
図1〜図3に示すように、給排水設備1は住居などの施設2に設置されるもので、中水たる雨水を受ける中水受槽3、第1貯留槽4、濾過槽5、第2貯留槽6、第3貯留槽7を、前記中水を順次移行しうるように送水パイプで連繋してなる水供給装置8と、この水供給装置8の中水を浄化して飲用可能な上水を得るための第1浄水装置9と、前記水供給装置8の前記中水あるいは前記上水を使用した後の水を浄化して中水を得るための第2浄水装置10とから構成する。第2貯留槽6と第1浄水装置9間、第3貯留槽7とトイレなどの中水使用場所11間、第1浄水装置9の後述するフィルター部材9bと厨房などの上水使用場所12間、前記上水使用場所12と第2浄水装置10の流量調整槽10c間、前記中水使用場所11と前記流量調整槽10b間、第2浄水装置10と第3貯留槽7間は、それぞれ循環パイプ13によって連繋する。第1貯留槽4、第2貯留槽6、第3貯留槽7には、それぞれ中水を送り出すためのポンプ4a,6a,7aを設け、また、第1貯留槽4にはポン4b及び送水パイプを介して放水部たる消火栓(図示せず)に連繋してある。なお、放水部は、庭や道路に散水するための散水栓(図示せず)であってもよい。
【0010】
前記住居などの施設2の一階のコンクリート屋根の上に設けた中水受槽3内には、土の上に芝を植設した芝層14、洗砂層15、シリカ層16を積層し、前記屋根の樋と第1貯留槽4間を導水パイプ17(図3参照)で連繋する。
【0011】
図4〜図9に示すように、第1浄水装置9は、タンク状の装置本体9aと、この装置本体9aで得た処理水を濾過するための、触媒用竹炭、SWAマテリアル、マイクロフィルター(図示せず)を順次通過するよう構成してなるフィルター部材9bと、前記装置本体9aに送り込む被処理水を一端貯水するとともに、送り込む水量を調整するための調整槽9cとからなる。この調整槽9cには、水90重量%、松、笹、梅、イチジク、桃、柿などの葉から抽出した抽出液6重量%、オカラ3重量%、糖蜜1重量%からなる原液から酵素を抽出してなる、発酵を誘導するための抗酸化物質を含む酵素液を定期的に投入する。
【0012】
前記酵素液の作成にあたっては、前述の松、笹、梅、イチジク、クリ、桃、柿の葉から抽出した抽出液、オカラ、糖蜜を混合した水溶液に、空気中から微生物が混入することによって、1ccあたりの微生物数(生菌数)が、初期状態において10〜10であったものが、10に増加して菌の死滅がなくなり、その後1020〜1030へと飛躍的に増大し、次に、この水溶液内で飛躍的に増殖した多数の微生物酵素が高密度化し、前記松、笹、梅、イチジク、クリ、桃、柿の葉に含まれる植物酵素とともに結合結晶化(合成融合)し、発酵を誘導するための抗酸化物質が生成される。この抗酸化物質を含む溶液を濾過して前記酵素液を得るのである。
【0013】
装置本体9aは、その内部を、第1処理室18(バイオ触媒槽)と第2処理室19(バイオ触媒槽)からなる微生物処理槽20、鉱物を用いて浄化作用を発揮する鉱物処理槽21、処理水貯水槽22に区画し、前記各第1、第2処理室18,19の各下部にエアー吐出部18a,19aを、また各両側部にエアー吐出部18b,19bを配置する。さらに、前記装置本体9aは、前記鉱物処理槽21の下部にエアー吐出部21a,21bを配置するとともに、前記第1処理室18と第2処理室19間、この第2処理室19と鉱物処理槽21間、この鉱物処理槽21と処理水貯水槽22間の各仕切壁23上部には、それぞれ処理された処理水が順次移行しうる水路24a,24b,24cを設ける。図5に示すように、前記水路24aの出口端は、第2処理室19の下部に開口し、また、前記水路24bの出口端は、鉱物処理21の下部に開口し、さらに、前記水路24cは仕切壁23の上部を貫通する透孔で構成されている。前記エアー吐出部18a,18b,21aは第1エアーパイプ25aにより、また、前記エアー吐出部18b,19b,21bは、第1エアーパイプ25bにより、それぞれ外部のエアー供給装置(図示せず)からエアーの供給を受けるように構成する。前記各第1、第2エアーパイプ25a,25bには、第1処理室18に係る各エアー吐出部18a,18bと第2処理室19に係るエアー吐出部19a,19bと鉱物処理21のエアー吐出部21a,21bにエアーを送り込むか否かを切り換えるべく、エアーの遮断及び通過を切り換えるための切替弁(図示せず)を設けてある。
【0014】
また、前記各第1、第2処理室18,19は、藻、菌類が現生・発現するためのバイオ加工を施した不織布26a,26bを所定間隔を置いて吊り下げるとともに、上部から光を照射するための図示しない光源を有する。
【0015】
各第1、第2処理室18,19には、好気性菌類の乳酸菌、酵母菌等、嫌気性菌類の乳酸菌、放線菌、アゾトバクター、アミロバクター、根瘤菌等を育成するための菌床が投入されており、これらによるバイオ処理によって、好気性・嫌気性フザリウム属を抑制し、発生した塩基類をタンパク化させて結晶体となすものである。また、第1処理室18には、前記第2貯留槽6にから伸びる循環パイプ13と接続する導水パイプ27を設け、この導水パイプ27の内端を、第1処理室18下部に臨ましめる。
【0016】
鉱物を用いて浄化作用を発揮する鉱物処理槽21は、シリカ触媒28とカーボン触媒層29とマテリアル触媒30とを積層してなり、前記第1、第2処理室18、19内でバイオ処理された処理水に含まれる窒素(N)、生理活性物質、タンパク質結晶を、無機性媒体(C・SiO2 ,Ti,Fe,Al,Cu,Mg,Li,Be,etc)により、消失させる作用を発揮する。具体的には、シリカ触媒28では、前記処理水に含まれる固定窒素、生理活性物質、タンパク質結晶(酵素結合結晶)は、無機性触媒体であるイオン(C・SiO )に衝突することにより、プラスイオン化したものが炭素イオン(C)に吸着される。また、前記カーボン触媒29では、残留したすべての水素基(H )をカーボン触媒29に含まれる無機性触媒体である炭素(C)に吸着させる。さらに前記マテリアル触媒30にてすべての触媒作用が終了する。
【0017】
前記第1処理室18と鉱物処理槽21間には、鉱物処理槽21から第1処理室18に処理水を返送するための返送パイプ31が配置してある。この返送パイプ31は、鉱物処理槽21内の処理水のバイオ処理不足を補うべく、前記処理水を鉱物処理槽21から第1処理室18に返送して再度の複合発酵および触媒処理による各浄化を行うためのものである。
【0018】
処理水貯水槽22は、鉱物処理槽21で触媒処理された処理水を装置本体9aから前記フィルター部材9bに送り出すための排水機構を設けてある。この排水機構は、モータ32と先端を処理水貯水槽22下部に臨ましめた吸上パイプ33とからなり、この吸上パイプ33は、前記フィルター部材9bに連繋する連繋パイプ34に接続してある。
【0019】
なお、図4、図5中の符号35は、水位が上がり過ぎた際に処理水を外部に排出する、処理水貯水槽22上部に設けたオーバーフローパイプ、符号36は、第1、第2微生物処理槽18,19及び鉱物処理槽21上部に設けた開口部である。
【0020】
次に、上記浄水装置1により雨水の処理を行う工程を説明する。まず、調整槽9cに第2貯留槽6内の雨水を流し込み、酵素液を投入して所定時間経過後に、この被処理水を導水パイプ27から第1処理室18に徐々に流入させるとともに、エアー吐出部18a,18b,19a,19bから所定の前記切替弁を操作してエアーを吐出させる。第1処理室18では、好気性菌類の乳酸菌、酵母菌等による発酵系優先微生物群処理と、前記好気性菌類及び嫌気性菌類の乳酸菌、放線菌による発酵及び発酵合成系微生物群処理と、主に嫌気性菌類による発酵合成系微生物群処理により、抗酸化作用による酸化、変敗、腐敗の抑制、アミノ酸、糖類、ビタミン、ミネラル等の生理活性物質の生成及び大腸菌、雑菌、一般細菌の抑制、ストレプトマイセス・ペニシリウム等抗生物質の生成及びウイルス、病原菌、リケッチャーの滅菌、増殖抑制を行う。また、第1、第2処理室18,19では、不織布26a,26bに現生・発現した光合成菌、藻菌類、光合成微生物が、光源(図示せず)の光によって、炭酸ガス、窒素ガスを取り込んで光合成等のエネルギー置換及び交換を行う。すなわち、このバイオ処理とエネルギー置換及び交換によって、被処理水のほぼ完全な酸化、変敗、腐敗を断ち切り、好気性・嫌気性フザリウム属を消滅させ、微生物の全ての有害作用を有効作用に導く。換言すれば、前記バイオ処理によって、前記各菌の共存、共栄、共生を可能とし、微生物の有効作用を引き出して、酸化、変敗、腐敗を断ち切るのである。
【0021】
続いて、第1処理室18の水路24aより、被処理水は水路24aから第2処理室19に移行し、この第2処理室19でも前記第1処理室18の場合と同様のバイオ処理と光合成によるエネルギー置換及び交換が行われる。
【0022】
続いて、第2処理室19より、処理水が水路24bを経て鉱物処理21に流入する。この鉱物処理槽21では、マテリアル触媒30とカーボン触媒29とシリカ触媒28が、これらに含まれる無機性触媒体(C・SiO,Ti,Fe,Al,Cu,Mg,Li,Be,etc)を用いたイオン触媒により、バイオ処理により発生した固定窒素、生理活性物質、タンパク質結晶の消失を行う。
【0023】
続いて、鉱物処理21より、処理水(飲用可能な上水)は水路24cから処理水貯水槽22に流れ込む。この処理水は、モータ32でポンプを駆動し、吸上パイプ33で前記処理水を汲み上げ、触媒用竹炭、SWAマテリアル、マイクロフィルターを積層(図示せず)してなるフィルター部材9bにてさらに濾過し、飲用水として上水使用場所13に送水する。なお、第1処理室18への被処理水の導入は連続的になされる。
【0024】
また、上水使用場所11で使用した後の下水(汚水)は、送水パイプ13を経て第2浄水装置10に送られる。なお、前記のようにして得られた鉱物処理槽21内の処理水になお不要物質が存在する場合には、返送パイプ31によって前記第1処理室18に戻され、再度バイオ処理と鉱物を用いた触媒処理を施すことが可能である。
【0025】
図1及び図10に示すように、第2浄水装置10は、タンク形状の装置本体10aと、この装置本体10aに送りこまれる下水の流量を、装置本体10aで効果的に処理するように調整するための第1流量調整槽10bと、第2流量調整10cとからなる。この第1流量調整槽10bには、前述した第1浄水装置9で使用したものと同じ酵素液を定期的に投入する。
【0026】
図10〜図16に示すように、装置本体10aの内部を仕切壁37,38,39,40,41によって、第1微生物処理槽42、第2微生物処理槽43、第3微生物処理槽44、第4微生物処理槽45、第5微生物処理槽46、鉱物処理槽47に区画し、前記各第1〜第5微生物処理槽42〜46の各下部にエアー吐出部42a,43a,44a,45a,46aを配置し、また、第5微生物処理槽46の両側部にもエアー吐出部46bを配置し、さらに、前記鉱物処理槽47下部にエアー吐出部47aを配置する。前記仕切壁37,38,39上部には、第1微生物処理槽42から第2微生物処理槽43へ、第2微生物処理槽43から第3微生物処理槽44へ、第3微生物処理槽44から第4微生物処理槽45へ、それぞれ処理水を移行させるための水路48aを設ける。前記各水路48aの各出口側の第2〜第4微生物処理槽43〜45には、各水路48aを通って移行させた各処理水を第2〜第4微生物処理槽43〜45下部に誘導するための断面半円状の誘導管49をそれぞれ設ける。また、装置本体10a上部には前記各槽に対応するように、内部の各部材の保守管理のために開口部50を設けてある。
【0027】
図12に明示したように、エアー吐出部42a,43a,44a,45a,47aは、第1エアーパイプ51aにより、また、前記エアー吐出部46a,46bは第2エアーパイプ51bによりそれぞれ外部のエアー供給装置(図示せず)からエアーの供給を受けるように構成する。
【0028】
図10に明示したように、第1微生物処理槽42は、内部にあらかじめ好気性菌類の乳酸菌、酵母菌が優先的に現生するための菌床が投入され、また、隔壁52により内部を二分し下部で連通する二つの処理室53a,53bに分割し、装置本体10a端部側の処理室53aには、外部から被処理水である汚水を、前記端部側処理室53a下部に導入する導水管54を設ける。この導水管54は、連繋パイプ55によって前記第2流量調整槽10cに連繋してある(図1参照)。
【0029】
また、第2、第3微生物処理槽43,44には、前記好気性菌類と嫌気性菌類の乳酸菌、放線菌、アゾトバクター、アミロバクター、根瘤菌が優先的に現生するための菌床が投入されている。
【0030】
図2及び図11に明示したように、第4微生物処理槽45には、前記嫌気性菌類が優先的に現生するための菌床が投入されるとともに、その側部壁には、処理水に含まれる各種菌類を沈殿させるための沈殿槽56に連繋した処理水取出孔57を設ける。
【0031】
図15に明示したように、第5微生物処理槽46は、前述の第1浄水槽9における微生物処理槽20で使用したものと同じ複数の不織布58を所定間隔を置いて吊り下げるとともに、その側壁には前記沈殿槽56に連繋する受水口59を設けてある。この受水口59の出口端は、第5微生物処理槽46の下部に開口している。
【0032】
鉱物処理槽47は、シリカ触媒62、カーボン触媒61、マテリアル触媒60を積層してなり、前記第5微生物処理槽46内でバイオ処理された処理水に含まれる固定窒素、生理活性物質、タンパク質結晶を、無機性媒体(C・SiO2 ,Ti,Fe,Al,Cu,Mg,Li,Be,etc)により、消失させる作用を発揮する。具体的には、シリカ触媒62において、固定窒素、生理活性物質、タンパク質結晶がC・SiOに衝突することにより、プラスイオン化したもの炭素(C)に吸着され、また、カーボン触媒61において、残留したすべての水素基(H+)を炭素(C)に吸着させ、マテリアル触媒60において、すべての消失が触媒作用が終わる。なお、図10〜図12中、符号63はオーバーフローパイプである。
【0033】
次に、上記第2浄水装置10で浄水を得る過程を説明する。まず、第1、第2流量調整槽10b,10cを経て第1微生物処理槽42の処理室53aに汚水を徐々に導入すると、第1微生物処理槽42より、水路48aを経て第2微生物処理槽43の下部に流入し、さらに第3、第4微生物処理槽44,45に移流される。この第4微生物処理槽44より、処理水は、処理水取出孔57から沈殿槽56に入り、この沈殿槽56より、受水口59から第5微生物処理槽46の下部に入る。また、第5微生物処理槽46より、水路48bを通って鉱物処理槽47の下部に移送される。
【0034】
そして、第1微生物処理槽42では、エアーを供給されて、好気性菌類の乳酸菌、酵母菌による発酵系優先微生物群処理が進み、抗酸化作用による酸化、変敗、腐敗の抑制及び固形物の液状化が行われる。
【0035】
第2微生物処理槽43では、前記好気性菌類及び嫌気性菌類の乳酸菌、放線菌による発酵及び発酵合成系微生物群処理が進み、主に嫌気性菌類による発酵合成系微生物群とが同時に進行するバイオ処理により、アミノ酸、糖類、ビタミン、ミネラル等の生理活性物質の生成が行われる。
【0036】
第3微生物処理槽44では、発酵合成系微生物群処理が進み、好気性の雑菌類及び嫌気性の細菌、ウイルス、病原菌、リケッチャーの滅菌、増殖抑制が行なわれる。
【0037】
第4微生物処理槽45では、処理水に主に嫌気性菌類が存在し、合成系優先微生物群処理が行われ、これを前記沈殿槽56に送り込んで、各種菌類を沈殿させる。沈殿した菌類は第一微生物処理槽へ返送され、そこで再び活動し始める。そして、沈殿槽56から第5微生物処理槽46に流入した処理水には、ほぼ菌類が存在しない。
【0038】
第5微生物処理槽46では、不織布26a,26bに現生・発現した光合成菌、藻菌類、光合成微生物が、光源(図示せず)からの光によって、炭酸ガス、窒素ガスを取り込んで光合成等のエネルギー置換及び交換を行う。すなわち、このバイオ処理とエネルギー置換及び交換によって、被処理水のほぼ完全な酸化、変敗、腐敗を断ち切り、好気性・嫌気性フザリウム属を消滅させ、微生物の全ての有害作用を有効作用に導く。換言すれば、前記バイオ処理によって、前記各菌の共存、共栄、共生を可能とし、微生物の有効作用を引き出して、酸化、変敗、腐敗を断ち切るのである。
【0039】
続いて、上記第5微生物処理槽46の処理水が水路48bを経て鉱物処理47に入ると、前記第1浄水装置9の鉱物処理槽21の場合と同様に、積層したマテリアル触媒60、カーボン触媒61、シリカ触媒62が、これらに含まれる無機性触媒体(C・SiO2 ,Ti,Fe,Al,Cu,Mg,Li,Be B etc)を用いたイオン触媒により、固定窒素(N)、生理活性物質、タンパク質結晶の消失を行う
【0040】
すなわち、前記マテリアル触媒60では、前記微生物処理槽45で処理された処理水をより浄化する作用を発揮する。また、前記カーボン触媒61では、タンパク結晶の衝突により、残留したすべての水素基(H)をカーボン触媒61に含まれる無機性触媒体である炭素(C)に吸着させる。さらにシリカ触媒62では、被処理水中の固定窒素、生理活性物質、タンパク結晶が、シリカ触媒62に含まれる無機性触媒体であるイオン(C・SiO)に衝突することにより、プラスイオン化したものを炭素イオン(C)に吸着させる。
【0041】
このようにして得られた中水は、再度トイレ用水などとして使用すべく、前記水供給装置の8の第3貯留槽7(図1参照)に循環パイプ13(図1参照)に送り出す。
【0042】
以上のように構成した給排水設備1による循環型給排水設備は、水供給装置8において、中水を受ける雨水受槽3、第1貯留槽4、濾過層5を経て、第2貯留槽6及び第3貯留槽7に中水を貯留し、この第3貯留槽7の中水を、トイレなどの使用場所11に送って使用し、使用後の下水を、第2浄水装置10で中水に浄化して前記第3貯留槽7に返送する一方、前記第2貯留槽6の中水を、第1上水装置9で上水に浄化して、厨房などの上水使用場所12に送って使用し、使用後の下水を、前記中水使用場所11から出た下水といっしょに、第2浄水装置10に送って浄化し、前記第3貯留槽7に返送するのである。
【0043】
なお、本発明は上記実施形態になんら限定されるものではなく、例えば、中水は雨水に代えて川水や湖水でもよい。
【0044】
【発明の効果】
以上のように、請求項1に記載した本発明によれば、雨水や川水などの中水を利用して飲用水などを得るとともに、上水あるいは中水を使用した後の下水は、悪臭を消失し、余剰汚泥を不発生又は軽減しつつ浄化して再利用するので、従来のような公的な上下水道設備や浄化設備に全てを頼らないでも生活水を確保できるほか、上下水道設備費を軽減でき、加えて、下水を浄化した後の中水を河川に排出しても環境上問題がないどころか、魚が現生し、水鳥が飛ぶ等の自然回帰現象が起こるうえ、効果的なバイオ処理を行わせることができるという効果を奏する。
【図面の簡単な説明】
【図1】循環型給排水設備の概略図。
【図2】給排水設備を配備した施設の平面図。
【図3】給排水設備を配備した施設の正面図。
【図4】第1浄水装置おける装置本体の縦断正面図。
【図5】第1浄水装置における装置本体の横断平面図。
【図6】第1浄水装置における装置本体のエアー供給機構を示す横断平面図。
【図7】図4のA−A線断面図。
【図8】図4のB−B線断面図。
【図9】図4のC−C線断面図。
【図10】第2浄水装置における要部を縦断して示す正面図。
【図11】第2浄水装置における装置本体の横断平面図。
【図12】第2浄水装置における本体装置のエアー供給機構を示す横断平面図。
【図13】図10のA−A線断面図。
【図14】図10のB−B線断面図。
【図15】図10のC−C線断面図。
【図16】図10のD−D線断面図。
【符号の説明】
1 給排水設備
2 施設
3 中水受槽
4 第1貯留槽
5 濾過タンク
6 第2貯留槽
7 第3貯留槽
8 水供給装置
9 第1浄水装置
9a 装置本体
9b フィルター部材
9c 調整槽
10 第2浄水装置
10a 装置本体
10b 第1流量調整槽
10c 第2流量調整槽
11 中水使用場所
12 上水使用場所
13 循環パイプ
14 土、芝層
16 シリカ層
15 洗砂層
17 導水パイプ
18 第1処理室
19 第2処理室
20 微生物処理槽
21 鉱物処理槽
22 処理水貯水槽
23 仕切壁
24a,24b、24c 水路
25a 第1エアーパイプ
25b 第2エアーパイプ
26a,26b 不織布
27 導水管
28 シリカ触
29 カーボン触
30 マテリアル触
31 返送パイプ
32 モータ
33 吸上パイプ
34 連繋パイプ
35 オーバーフローパイプ
36 開口部
37,38,39,40,41 仕切壁
42 第1微生物処理槽
43 第2微生物処理槽
44 第3微生物処理槽
45 第4微生物処理槽
46 第5微生物処理槽
47 鉱物処理槽
42a,43a,44a,45a,46a,46b,47a エアー吐出部
48a,48b 水路
49 誘導管
50 開口部
51a 第1エアーパイプ
51b 第2エアーパイプ
52 隔壁
53a,53b 処理室
54 導水管
55 連繋パイプ
56 沈殿槽
57 ゴミ取出孔
58 不織布
59 処理水取出孔
60 マテリアル触媒
61 カーボン触媒
62 シリカ触媒
63 オーバーフローパイプ
[0001]
BACKGROUND OF THE INVENTION
  The present invention relates to a circulation type water supply and drainage facility that can purify and circulate life-related wastewater such as various facilities and houses, and can reuse water by using rainwater and the like, so that the amount of tap water used can be made almost zero.
[0002]
  In this specification, drinking water refers to drinking water that can be used in kitchens, bathrooms, washrooms, etc., and medium water refers to drinking water that flows in the toilet bowl or water sprayed in the garden. This means water that is clean to some extent, and sewage refers to so-called sewage after use of clean water or medium water.
[0003]
  In this specification, biotreatment means 1) creation of an ecosystem of microorganisms in which all microbial groups such as aerobic fungi, anaerobic fungi, facultative anaerobic fungi coexist, prosper, and coexist. To eliminate all aerobic and anaerobic Fusarium species in microbial dynamics 3) Catalysis of ultra-high density energy and information due to the emergence and expression of ancient fungi about 2 to 3 billion years ago This means that the substances contained in sewage are decomposed and lost. Specifically, using the functions, substrates and information of microorganisms, and using the fermentation, growth, and induction methods according to the substrate properties for the basis of all pollutants, the above 1) to 3) To the state. This is called a complex fermentation method.
[0004]
[Prior art]
  Conventionally, in various facilities and houses, water taken from outside by water supply is used for cooking water in kitchens, toilet flushing, wash water, sprinkling water in gardens, etc. Sewage after use is purified by sewerage. After being sent to the site and purified, it was drained into rivers. In some areas, the treatment capacity of the water purification plant is insufficient, and sewage is drained directly into rivers.
[0005]
[Problems to be solved by the invention]
  In the system equipment that supplies domestic water through the water supply and cleans up at the water treatment plant through the sewer as described above, it not only costs a large amount of water and sewage equipment, which is a public facility, but also purifies the sewage. In some cases, a large amount of sludge was generated, and the treatment of the sludge was very troublesome and expensive. In addition, if sewage is drained directly into a river or the like, there is a problem that pollution of the river advances and environmental problems occur.
[0006]
  This invention makes it a subject to eliminate each above-mentioned problem, and aims at providing the circulation type water supply / drainage equipment which solved this subject.
[0007]
[Means for Solving the Problems]
  In order to achieve the above object, the circulation type water supply and drainage system according to the first aspect of the present invention is configured to supply middle water such as rainwater.After filtration, in two storage tanksStore and if necessaryFrom each storage tankA water supply device capable of supplying;For each of the one storage tankA first water purifier for purifying the intermediate water supplied from the above by complex fermentation to obtain drinking water, andThe other storage tankSaid medium water and saidFrom the first water purification deviceWaterRespectivelyA circulation type water supply and drainage facility using a water supply and drainage facility comprising a second water purification device for purifying sewage after use by complex fermentation to obtain middle water,The other storage tankThe sewage sent from the place where the intermediate water is used is sequentially purified by the second water purifier and transferred to the place where the water is used.The other storage tankWhile being transferred toOne storage tankThe first water purifier purifies the middle water sent from the water and transfers it to drinking water, and transfers it to a drinking water use place such as a kitchen. The sewage discharged from this drinking water use place is sequentially supplied to the second water purifier. And purifyThe other storage tankConfigured to be transported toThe main body of the first water purification device and the second water purification device is laminated with a microorganism treatment tank that grows predetermined microorganisms and feeds air, and a silica catalyst, a carbon catalyst, and a mineral catalyst of a material catalyst. A stock solution consisting of water, an extract previously extracted from leaves such as pine, persimmon, plum, fig, peach, persimmon, okara, and molasses. The water to be treated with the enzyme solution for inducing fermentation obtained by extracting the enzyme from the biotreatment with microorganisms in the tank, and then in the mineral treatment tank, fixed nitrogen produced by biotreatment, Disappear bioactive substances and protein crystalsIt is comprised so that.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
  Preferred embodiments of the present invention will be described below in detail with reference to the accompanying drawings. Here, FIG. 1 of the attached drawings is a schematic view of the circulation type water supply and drainage equipment, FIG. 2 is a plan view of the facility provided with the water supply and drainage equipment, FIG. 3 is a front view of the facility provided with the water supply and drainage equipment, and FIG. FIG. 5 is a cross-sectional plan view of the apparatus main body in the first water purifier, FIG. 6 is a cross-sectional plan view showing the air supply mechanism of the apparatus main body in the first water purifier, and FIG. 4 is a cross-sectional view taken along line AA of FIG. 4, FIG. 8 is a cross-sectional view taken along line BB of FIG. 4, FIG. 9 is a cross-sectional view taken along line CC of FIG. 11 is a cross-sectional plan view of the main body of the second water purifier, FIG. 12 is a cross-sectional plan view for explaining the air supply mechanism of the main body of the second water purifier, and FIG. 13 is a cross-sectional view taken along line AA in FIG. 14 is a cross-sectional view taken along line BB in FIG. 10, FIG. 15 is a cross-sectional view taken along line CC in FIG. 10, and FIG. There sectional view taken along line D-D.
[0009]
  As shown in FIGS. 1 to 3, the water supply / drainage equipment 1 is installed in a facility 2 such as a residence, and includes a middle water receiving tank 3, a first storage tank 4, a filtration tank 5, and a second storage tank that receive rainwater as middle water. A water supply device 8 formed by linking the tank 6 and the third storage tank 7 with a water supply pipe so that the intermediate water can be transferred in sequence, and drinking water that is purified by purifying the intermediate water of the water supply device 8 After using the first water purifier 9 for obtaining the water and the intermediate water or the clean water of the water supply device 8underIt comprises the 2nd water purifier 10 for purifying water and obtaining middle water. Between the second storage tank 6 and the first water purification device 9, between the third storage tank 7 and the middle water use place 11 such as a toilet, between the filter member 9b described later of the first water purification apparatus 9 and the upper water use place 12 such as a kitchen. , Between the water use place 12 and the flow rate adjustment tank 10c of the second water purification apparatus 10, between the intermediate water use place 11 and the flow rate adjustment tank 10b, and between the second water purification apparatus 10 and the third storage tank 7 respectively. They are connected by a pipe 13. The first storage tank 4, the second storage tank 6, and the third storage tank 7 are respectively provided with pumps 4a, 6a, and 7a for sending out middle water, and the first storage tank 4 has a pump.TheIt is connected with a fire hydrant (not shown) which is a water discharge part via 4b and a water supply pipe. The water discharge part may be a water spigot (not shown) for watering the garden or road.
[0010]
  In the middle water receiving tank 3 provided on the concrete roof on the first floor of the facility 2 such as the residence, a lawn layer 14, a sand-washed layer 15 and a silica layer 16 in which grass is planted on the soil are laminated, The roof gutter and the first storage tank 4 are connected by a water guide pipe 17 (see FIG. 3).
[0011]
  As shown in FIGS. 4-9, the 1st water purifier 9 is a tank-shaped apparatus main body 9a, the bamboo charcoal for catalyst, SWA material, and a microfilter (for filtering the treated water obtained with this apparatus main body 9a. The filter member 9b is configured to sequentially pass through (not shown) and the adjustment tank 9c for storing the treated water to be fed into the apparatus main body 9a and adjusting the amount of the water to be fed. In this adjustment tank 9c, the enzyme is extracted from a stock solution consisting of 90% by weight of water, 6% by weight of an extract extracted from leaves such as pine, persimmon, plum, fig, peach and persimmon, 3% by weight of okara and 1% by weight of molasses. Extracted,To induce fermentationPeriodically add an enzyme solution containing an antioxidant.
[0012]
  In the preparation of the enzyme solution, by extracting microorganisms from the air into the aqueous solution mixed with the extract extracted from the above-mentioned pine, bamboo shoot, plum, fig, chestnut, peach, bamboo leaf, okara, molasses, The number of microorganisms per 1 cc (viable bacteria count) is 10 in the initial state.7-108Was 109And the number of bacteria disappears, and then 1020-1030The plant enzymes contained in the pine, persimmon, plum, fig, chestnut, peach, and persimmon leaves Together with crystallization (synthesis fusion),To induce fermentationAntioxidants are produced. The enzyme solution is obtained by filtering the solution containing the antioxidant.
[0013]
  The apparatus main body 9a has a microbial treatment tank 20 composed of a first treatment chamber 18 (biocatalyst tank) and a second treatment chamber 19 (biocatalyst tank),Demonstrates purification using mineralsIt is divided into a mineral processing tank 21 and a treated water storage tank 22, and air discharge portions 18a and 19a are provided at the lower portions of the first and second treatment chambers 18 and 19, respectively, and air discharge portions 18b and 19b are provided at both sides. Deploy. Further, the apparatus main body 9a has air discharge portions 21a and 21b arranged below the mineral processing tank 21, and between the first processing chamber 18 and the second processing chamber 19, and between the second processing chamber 19 and the mineral processing. Water channels 24a, 24b, and 24c through which treated water can be sequentially transferred are provided between the tanks 21 and above the partition walls 23 between the mineral treatment tank 21 and the treated water storage tank 22, respectively. As shown in FIG. 5, the outlet end of the water channel 24a opens to the lower part of the second treatment chamber 19, and the outlet end of the water channel 24b is mineral processing.TankFurther, the water channel 24 c is formed by a through-hole penetrating the upper part of the partition wall 23. The air discharge portions 18a, 18b, and 21a are supplied from the external air supply device (not shown) by the first air pipe 25a, and the air discharge portions 18b, 19b, and 21b are supplied from the external air supply device (not shown) by the first air pipe 25b. To receive the supply. In each of the first and second air pipes 25a and 25b, air discharge portions 18a and 18b related to the first processing chamber 18, air discharge portions 19a and 19b related to the second processing chamber 19, and mineral processing.TankA switching valve (not shown) for switching between blocking and passing of air is provided in order to switch whether or not to send air to the 21 air discharge portions 21a and 21b.
[0014]
  Each of the first and second processing chambers 18 and 19 suspends the nonwoven fabrics 26a and 26b subjected to bioprocessing for algae and fungi to be present and expressed at predetermined intervals and emits light from the top. It has a light source (not shown) for irradiating.
[0015]
  In each of the first and second processing chambers 18 and 19, a fungus bed for growing anaerobic lactic acid bacteria, yeast, etc., anaerobic lactic acid bacteria, actinomycetes, azotobacter, amylobacter, root-knot fungus, etc. is introduced. By these biotreatments, aerobic / anaerobic Fusarium genus is suppressed, and the generated bases are proteinized to form crystals. The first processing chamber 18 is provided with a water conduit 27 connected to the circulation pipe 13 extending from the second storage tank 6, and the inner end of the water conduit 27 faces the lower portion of the first processing chamber 18.
[0016]
  Demonstrates purification using mineralsThe mineral processing tank 21 is silicaMedium 28, carbon catalyst layer 29 and material touchMedium 30 and is contained in the treated water biotreated in the first and second treatment chambers 18 and 19.Nitrogen (N), physiologically active substance, protein crystalIs eliminated by an inorganic medium (C.SiO2, Ti, Fe, Al, Cu, Mg, Li, Be, etc). In particular,In the silica catalyst 28, fixed nitrogen, physiologically active substance, and protein crystal (enzyme-bonded crystal) contained in the treated water are ions (C · SiO) that are inorganic catalyst bodies. 2 ) Is adsorbed by carbon ions (C). In the carbon catalyst 29, all remaining hydrogen groups (H + ) Is adsorbed on carbon (C), which is an inorganic catalyst body contained in the carbon catalyst 29. Further, all the catalytic actions are completed at the material catalyst 30.
[0017]
  A return pipe 31 for returning treated water from the mineral treatment tank 21 to the first treatment chamber 18 is disposed between the first treatment chamber 18 and the mineral treatment tank 21. This return pipe 31 returns the treated water from the mineral treatment tank 21 to the first treatment chamber 18 to make up for the shortage of biotreatment of the treated water in the mineral treatment tank 21 and performs each purification by recombination fermentation and catalytic treatment again. Is for doing.
[0018]
  The treated water storage tank 22 is provided with a drainage mechanism for sending the treated water subjected to the catalyst treatment in the mineral treatment tank 21 from the apparatus main body 9a to the filter member 9b. This drainage mechanism is composed of a motor 32 and a suction pipe 33 with its tip facing the lower part of the treated water storage tank 22, and this suction pipe 33 is connected to a connecting pipe 34 connected to the filter member 9b. is there.
[0019]
  4 and 5, reference numeral 35 is an overflow pipe provided on the upper part of the treated water reservoir 22 for discharging treated water to the outside when the water level rises too much, and reference numeral 36 is the first and second microorganisms. It is an opening provided in the upper part of the treatment tanks 18 and 19 and the mineral treatment tank 21.
[0020]
  Next, the process of treating rainwater with the water purifier 1 will be described. First, rainwater in the second storage tank 6 is poured into the adjustment tank 9c, and after a predetermined time has passed since the enzyme solution was introduced, the water to be treated is gradually allowed to flow into the first treatment chamber 18 from the water conduit 27 and the air. A predetermined switching valve is operated from the discharge portions 18a, 18b, 19a, 19b to discharge air. In the first treatment chamber 18, the fermentation system preferred microorganism group treatment with aerobic fungi lactic acid bacteria, yeast, etc., the aerobic fungus and anaerobic fungus lactic acid bacteria, actinomycetes fermentation and fermentation synthesis microorganism group treatment, By fermenting and synthesizing microorganism groups with anaerobic fungi, oxidation, deterioration, decay prevention by antioxidant action, physiology of amino acids, sugars, vitamins, minerals, etc.ActivityProduction of substances, inhibition of E. coli, bacteria, general bacteria, production of antibiotics such as Streptomyces penicillium, sterilization of viruses, pathogens and rickettcher, and growth inhibition. In the first and second processing chambers 18 and 19, the photosynthetic bacteria, algae, and photosynthetic microorganisms that are present and expressed on the nonwoven fabrics 26a and 26b generate carbon dioxide gas and nitrogen gas by the light of a light source (not shown). Incorporate and perform energy replacement and exchange such as photosynthesis. In other words, this biotreatment and energy replacement and exchange cut off almost complete oxidation, deterioration, and decay of treated water, extinguish aerobic and anaerobic Fusarium, and lead all harmful effects of microorganisms to effective action . In other words, the biotreatment enables the coexistence, mutual prosperity, and symbiosis of each bacterium, and draws out the effective action of microorganisms to cut off oxidation, deterioration, and decay.
[0021]
  Subsequently, the water to be treated is transferred from the water channel 24 a to the second processing chamber 19 from the water channel 24 a of the first processing chamber 18, and the bioprocessing similar to the case of the first processing chamber 18 is performed in the second processing chamber 19. Energy replacement and exchange by photosynthesis is performed.
[0022]
  Subsequently, from the second treatment chamber 19, treated water passes through the water channel 24b and is subjected to mineral treatment.Tank21. This mineral processingTank 2In 1, the material touchMedium 30And carbon touchMedium 29 and silica touchMedium 28Are inorganic catalyst bodies (C · SiO2, Ti, Fe, Al, Cu, Mg, Li, Be, etc.Of fixed nitrogen, bioactive substances, protein crystalsDo disappear.
[0023]
  Next, mineral processingTankFrom 21, treated water (potable water) flows from the water channel 24 c into the treated water storage tank 22. This treated water is further filtered by a filter member 9b in which a pump is driven by a motor 32, the treated water is pumped by a suction pipe 33, and bamboo charcoal for a catalyst, SWA material, and a microfilter are laminated (not shown). Then, it is sent to drinking water use place 13 as potable water. The treated water is continuously introduced into the first treatment chamber 18.
[0024]
  In addition, sewage (sewage) after being used at the water use place 11 passes through the water pipe 13.Second water purification device 10Sent to. In addition, when an unnecessary substance is still present in the treated water in the mineral treatment tank 21 obtained as described above, it is returned to the first treatment chamber 18 by the return pipe 31 and again biotreated and mineralized.UsedIt is possible to perform a catalyst treatment.
[0025]
  As shown in FIG.1 and FIG.10, the 2nd water purifier 10 adjusts so that the flow volume of the sewage sent into this tank main body 10a and this apparatus main body 10a may be processed effectively by the apparatus main body 10a. First flow rate adjustment tank 10b and second flow rate adjustmentTank10c. The same enzyme solution as that used in the first water purifier 9 described above is periodically charged into the first flow rate adjusting tank 10b.
[0026]
  As shown in FIGS. 10 to 16, the inside of the apparatus main body 10 a is partitioned by walls 37, 38, 39, 40, 41, so that a first microorganism treatment tank 42, a second microorganism treatment tank 43, a third microorganism treatment tank 44, It divides into the 4th microorganism treatment tank 45, the 5th microorganism treatment tank 46, and the mineral treatment tank 47, and air discharge part 42a, 43a, 44a, 45a, each lower part of each said 1st-5th microorganism treatment tank 42-46. 46 a, an air discharge part 46 b is also arranged on both sides of the fifth microorganism treatment tank 46, and an air discharge part 47 a is arranged below the mineral treatment tank 47. On the partition walls 37, 38, 39, the first microbial treatment tank 42 to the second microbial treatment tank 43, the second microbial treatment tank 43 to the third microbial treatment tank 44, and the third microbial treatment tank 44 to the second microbial treatment tank 44. A water channel 48 a for transferring the treated water to each of the four microorganism treatment tanks 45 is provided. Into the second to fourth microbial treatment tanks 43 to 45 on the outlet sides of the respective water channels 48a, the treated water transferred through the respective water channels 48a is guided to the lower portions of the second to fourth microbial treatment tanks 43 to 45. A guide tube 49 having a semicircular cross section is provided. Further, an opening 50 is provided in the upper part of the apparatus main body 10a so as to correspond to each of the tanks for maintenance management of each internal member.
[0027]
  As clearly shown in FIG. 12, the air discharge portions 42a, 43a, 44a, 45a, and 47a are supplied by the first air pipe 51a, and the air discharge portions 46a and 46b are supplied by the second air pipe 51b. It is configured to receive air supply from a device (not shown).
[0028]
  As clearly shown in FIG. 10, the first microorganism treatment tank 42 is preliminarily filled with a bed for aerobic fungi lactic acid bacteria and yeast to preferentially grow, and the partition 52 separates the interior into two parts. The processing chamber 53a is divided into two processing chambers 53a and 53b that communicate with each other at the lower portion, and sewage water to be treated is introduced into the lower portion of the end-side processing chamber 53a from the outside into the processing chamber 53a on the end portion side of the apparatus body 10a. A water conduit 54 is provided. The water conduit 54 is connected to the second flow rate adjusting tank 10c by a connecting pipe 55 (see FIG. 1).
[0029]
  In addition, the second and third microorganism treatment tanks 43 and 44 are loaded with a bed for preferentially producing the aerobic and anaerobic lactic acid bacteria, actinomycetes, azotobacter, amylobacter, and root-knot fungus. ing.
[0030]
  As clearly shown in FIG. 2 and FIG. 11, the fourth microorganism treatment tank 45 is loaded with a fungus bed for preferentially growing the anaerobic fungi, and treated water is disposed on the side wall thereof. Precipitation for precipitating various fungi contained inTank 56 is provided with a treated water outlet hole 57 that is connected to 6.
[0031]
  As clearly shown in FIG. 15, the fifth microbial treatment tank 46 suspends a plurality of non-woven fabrics 58 that are the same as those used in the microbial treatment tank 20 in the first water purification tank 9 at predetermined intervals, and has sidewalls thereof. Is provided with a water receiving port 59 connected to the settling tank 56. The outlet end of the water receiving port 59 opens at the lower part of the fifth microorganism treatment tank 46.
[0032]
  The mineral processing tank 47 is silicaMedium 62, Carbon touchMedium 61. Material touchMedium 60And is contained in the treated water biotreated in the fifth microorganism treatment tank 46Fixed nitrogen, bioactive substance, protein crystalIs eliminated by an inorganic medium (C.SiO2, Ti, Fe, Al, Cu, Mg, Li, Be, etc). Specifically, silicaMedium 62InFixed nitrogen, physiologically active substance,Protein crystals are C · SiO2By colliding withPlus ionTurned intoButAdsorbed on carbon (C), MaCarbon touchMedium 6In 1The restAll hydrogen groups (H +) retained are adsorbed on carbon (C),In the medium 60,All disappearanceCatalysis is over. 10 to 12, reference numeral 63 denotes an overflow pipe.
[0033]
  Next, the process of obtaining purified water with the second water purification apparatus 10 will be described. First, when sewage is gradually introduced into the treatment chamber 53a of the first microorganism treatment tank 42 through the first and second flow rate adjustment tanks 10b and 10c, the second microorganism treatment tank is passed from the first microorganism treatment tank 42 through the water channel 48a. It flows into the lower part of 43 and is further transferred to the third and fourth microorganism treatment tanks 44 and 45. From the fourth microorganism treatment tank 44, treated water enters the precipitation tank 56 through the treated water outlet hole 57, and enters the lower part of the fifth microorganism treatment tank 46 from the water receiving port 59 through the precipitation tank 56. Moreover, it is transferred from the fifth microorganism treatment tank 46 to the lower part of the mineral treatment tank 47 through the water channel 48b.
[0034]
  And in the 1st microorganism treatment tank 42, air is supplied and the fermentation system priority microorganisms process by the aerobic fungi lactic acid bacteria and yeast advances, oxidation by an antioxidant action, deterioration, suppression of decay, and solid matter Liquefaction is performed.
[0035]
  In the second microbial treatment tank 43, the aerobic and anaerobic lactic acid bacteria, fermentation with actinomycetes, and fermentation-synthetic microorganism group treatment proceed, and the biosynthesis in which the fermentation-synthetic microorganism group mainly with anaerobic fungi progresses simultaneously. By processing, amino acids, sugars, vitamins, minerals, etc.Physiological activity ofProduction of material takes place.
[0036]
  In the third microorganism treatment tank 44, the fermentative and synthetic microorganism group treatment proceeds, and sterilization and growth inhibition of aerobic bacteria and anaerobic bacteria, viruses, pathogens, and rickettcher are performed.
[0037]
  In the fourth microorganism treatment tank 45, anaerobic fungi mainly exist in the treated water, and the synthetic system preferential microorganism group treatment is performed, which is sent to the settling tank 56 to precipitate various fungi. The precipitated fungus is returned to the first microbial treatment tank where it begins to act again. The treated water that has flowed from the sedimentation tank 56 into the fifth microorganism treatment tank 46 is substantially free of fungi.
[0038]
  In the fifth microorganism treatment tank 46, photosynthetic bacteria, algae, and photosynthetic microorganisms that are present and expressed on the nonwoven fabrics 26a and 26b take in carbon dioxide gas and nitrogen gas by light from a light source (not shown) and perform photosynthesis and the like. Perform energy replacement and exchange. In other words, this biotreatment and energy replacement and exchange cut off almost complete oxidation, deterioration, and decay of treated water, extinguish aerobic and anaerobic Fusarium, and lead all harmful effects of microorganisms to effective action . In other words, the biotreatment enables the coexistence, mutual prosperity, and symbiosis of each bacterium, and draws out the effective action of microorganisms to cut off oxidation, deterioration, and decay.
[0039]
  Subsequently, the treated water in the fifth microorganism treatment tank 46 passes through the water channel 48b and is subjected to the mineral treatment.TankWhen entering 47, as in the case of the mineral processing tank 21 of the first water purifier 9, the laminated material touches are used.Medium 60, Carbon touchMedium 61. Silica touchMedium 62Are inorganic catalyst bodies (C · SiO 2, Ti, Fe, Al, Cu, Mg, Li, Be B etc)Depending on the ion catalyst used,Dissolve fixed nitrogen (N), physiologically active substances, and protein crystals.
[0040]
  That is, the material touchMedium 60Then,in frontThe effect | action which purifies the treated water processed with the microbe processing tank 45 more is exhibited. The carbon touchMedium 61 is proteinqualityAll remaining hydrogen groups (H+) Carbon catalyst61It is made to adsorb | suck to carbon (C) which is an inorganic catalyst body contained in. Silica touchMedium 62In the treated waterFixedNitrogen, bioactive substances, proteinsqualityThe crystal is a silica catalyst62Ions (C · SiO) that are inorganic catalyst bodies contained in2)Plus ionAdsorbed to carbon ion (C)The
[0041]
  The middle water thus obtained is sent to the circulation pipe 13 (see FIG. 1) to the third storage tank 7 (see FIG. 1) of the water supply device 8 to be used again as toilet water or the like.
[0042]
  The circulation type water supply / drainage facility by the water supply / drainage facility 1 configured as described above includes the second storage tank 6 and the third storage tank 8 through the rainwater receiving tank 3, the first storage tank 4, and the filtration layer 5 that receive middle water in the water supply device 8. Middle water is stored in the storage tank 7, the middle water of the third storage tank 7 is sent to a use place 11 such as a toilet and used, and sewage after use is purified into middle water by the second water purification device 10. While returning to the third storage tank 7, the middle water of the second storage tank 6 is purified into clean water by the first water supply device 9, and sent to the water use place 12 such as a kitchen for use. The sewage after use is sent to the second water purification device 10 for purification together with the sewage discharged from the middle water use place 11 and returned to the third storage tank 7.
[0043]
  In addition, this invention is not limited to the said embodiment at all, For example, instead of rain water, river water and lake water may be sufficient as middle water.
[0044]
【The invention's effect】
  As described above, according to the present invention described in claim 1, drinking water or the like is obtained using the middle water such as rain water or river water, and the sewage after using the water or the middle water has a bad smell. In addition to ensuring that domestic water can be secured without relying entirely on public water and sewage facilities and purification equipment, water and sewage equipment Costs can be reduced, and in addition, there is no environmental problem even if the drainage of the sewage water is discharged into the river.In addition, effective bioprocessing can be performed.There is an effect.
[Brief description of the drawings]
FIG. 1 is a schematic view of a circulation type water supply and drainage facility.
FIG. 2 is a plan view of a facility provided with water supply / drainage equipment.
FIG. 3 is a front view of a facility where water supply / drainage facilities are provided.
FIG. 4 is a longitudinal front view of the main body of the first water purifier.
FIG. 5 is a cross-sectional plan view of the device main body in the first water purifier.
FIG. 6 is a cross-sectional plan view showing an air supply mechanism of the apparatus main body in the first water purifier.
7 is a cross-sectional view taken along line AA in FIG.
8 is a sectional view taken along line BB in FIG.
9 is a cross-sectional view taken along line CC of FIG.
FIG. 10 is a front view showing a main part of the second water purifier in a longitudinal manner.
FIG. 11 is a cross-sectional plan view of the apparatus main body in the second water purification apparatus.
FIG. 12 is a cross-sectional plan view showing an air supply mechanism of the main body device in the second water purifier.
13 is a cross-sectional view taken along line AA in FIG.
14 is a sectional view taken along line BB in FIG.
15 is a cross-sectional view taken along line CC in FIG.
16 is a sectional view taken along line DD of FIG.
[Explanation of symbols]
1 Water supply and drainage equipment
2 facilities
3 Middle water receiving tank
4 1st storage tank
5 Filtration tank
6 Second storage tank
7 third storage tank
8 Water supply device
9 1st water purifier
9a Device body
9b Filter member
9c Adjustment tank
10 Second water purifier
10a Device body
10b First flow rate adjustment tank
10c Second flow rate adjustment tank
11 Middle water use place
12 Water use place
13 Circulation pipe
14 Sat, turf layer
16 Silica layer
15 Sandwashing layer
17 Water conveyance pipe
18 First treatment chamber
19 Second processing chamber
20 Microbial treatment tank
21 Mineral processing tank
22 treated water storage tank
23 partition wall
24a, 24b, 24c
25a First air pipe
25b Second air pipe
26a, 26b non-woven fabric
27 Water conduit
28 Silica touchMedium
29 carbon touchMedium
30 Material touchMedium
31 Return pipe
32 motor
33 Suction pipe
34 Connecting pipes
35 Overflow pipe
36 opening
37, 38, 39, 40, 41 Partition wall
42 First microorganism treatment tank
43 Second microorganism treatment tank
44 3rd microorganism treatment tank
45 4th microorganism treatment tank
46 5th microorganism treatment tank
47 Mineral processing tank
42a, 43a, 44a, 45a, 46a, 46b, 47a Air discharge part
48a, 48b waterway
49 Guide tube
50 openings
51a First air pipe
51b Second air pipe
52 Bulkhead
53a, 53b processing chamber
54 Water conduit
55 continuous pipes
56 Sedimentation tank
57 Garbage outlet
58 Nonwoven fabric
59 Treated water outlet
60Material catalyst
61 Carbon catalyst
62Silica catalyst
63 Overflow pipe

Claims (1)

雨水などの中水を濾過した後に、二つの貯留槽に貯留し、必要に応じて前記各貯留槽から各別に供給しうる水供給装置と、前記一方の貯留槽から供給された中水を複合発酵により浄化して飲用可能な上水を得るための第1浄水装置と、前記他方の貯留槽の前記中水及び前記第1浄水装置からの上水をそれぞれ使用した後の下水を複合発酵により浄化して中水を得るための第2浄水装置とを備えた給排水設備を用いた循環型給排水設備であって、前記他方の貯留槽から送られた中水をトイレなどの中水使用場所に移送するとともに、この中水使用場所から送られた下水を第2浄水装置で順次浄化して前記他方の貯留槽に移送する一方、前記一方の貯留槽から送られた中水を第1浄水装置で浄化して飲用水となし、厨房などの上水使用場所に移送するとともに、この上水使用場所で出た下水を第2浄水装置に順次供給して浄化したうえ、前記他方の貯留槽に移送するように構成し、前記第1浄水装置及び第2浄水装置の装置本体には、所定の微生物を育成するとともに、エアーを送り込むようになした微生物処理槽と、シリカ触媒、カーボン触媒及びマテリアル触媒の鉱物触媒を積層してなる鉱物処理槽とを設け、前記微生物処理槽にて、あらかじめ水と、松、笹、梅、イチジク、桃、柿などの葉から抽出した抽出液と、オカラと、糖蜜とからなる原液から酵素を抽出してなる発酵を誘導するための酵素液を投入した被処理水を、槽内の微生物によりバイオ処理を行った後に、前記鉱物処理槽において、バイオ処理によって生成された固定窒素、生理活性物質、タンパク質結晶を消失させるように構成したことを特徴とする循環型給排水設備。 After filtering the middle water such as rainwater, it is stored in two storage tanks and combined with the water supply device that can be supplied separately from each of the storage tanks as needed, and the middle water supplied from the one storage tank Combined fermentation of sewage after using the first water purification device for obtaining drinking water purified by fermentation and the intermediate water of the other storage tank and the water from the first water purification device respectively A circulation type water supply / drainage facility using a water supply / drainage facility provided with a second water purification device for purifying and obtaining intermediate water, wherein the intermediate water sent from the other storage tank is used as a place for using intermediate water such as a toilet While transporting, the second water purifier sequentially purifies the sewage sent from the place where the middle water is used and transfers it to the other storage tank , while the middle water sent from the one storage tank is the first water purification apparatus. Purified with water, no drinking water, transferred to drinking water use place such as kitchen Rutotomoni, after which the sewage leaving this clean water use place sequentially supplied to purify the second water purification device, and configured to transfer the storage tank of the other, of the first water purification device and the second water purification device The apparatus main body is provided with a microorganism treatment tank in which predetermined microorganisms are grown and air is fed, and a mineral treatment tank in which a mineral catalyst of a silica catalyst, a carbon catalyst and a material catalyst is laminated, and the microorganism In order to induce fermentation in the treatment tank by extracting the enzyme from the stock solution consisting of water, extracts from leaves such as pine, bamboo shoots, plums, figs, peaches and strawberries, okara and molasses. The treated water charged with the enzyme solution was bioprocessed with microorganisms in the tank, and then the fixed nitrogen, bioactive substance, and protein crystals generated by the bioprocess were lost in the mineral processing tank. Recycling-plumbing characterized by being configured to so that.
JP2002019385A 2002-01-29 2002-01-29 Circulation type water supply and drainage equipment Expired - Fee Related JP4178440B2 (en)

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JP2003211183A (en) * 2002-01-29 2003-07-29 Yasutoshi Takashima Water cleaning apparatus for rainwater or the like
JP2003211182A (en) * 2002-01-29 2003-07-29 Yasutoshi Takashima Sewage cleaning apparatus
JP2006043558A (en) * 2004-08-03 2006-02-16 Nihon Choriki Method of using water resource for school lunch, and system therefor
JP2007326016A (en) * 2006-06-07 2007-12-20 Yusei Kenkyu Kikinkai Biological waste water treatment method
JP4482717B1 (en) * 2009-07-03 2010-06-16 龍男 白方 Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same
JP7582883B2 (en) * 2021-03-09 2024-11-13 康豪 高嶋 Treatment method for domestic wastewater and toilet wastewater
WO2023175806A1 (en) * 2022-03-16 2023-09-21 中国電力株式会社 Water circulation/purification system

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JPH0550079A (en) * 1991-08-23 1993-03-02 Hitachi Chem Co Ltd Method for accelerating function of septic tank
JPH06238288A (en) * 1993-02-18 1994-08-30 Hitachi Chem Co Ltd Reclaimed water device
JP3567011B2 (en) * 1995-02-27 2004-09-15 株式会社住本科学研究所 Circulation system and water storage tank
JPH09174072A (en) * 1995-10-26 1997-07-08 Inax Corp Reclaimed water treatment apparatus
JP3261033B2 (en) * 1996-03-01 2002-02-25 淳一 岩村 Water purification treatment equipment
JPH10309187A (en) * 1996-03-07 1998-11-24 Yasutoshi Takashima Combined fermentation for making all aerobic microorganism and anaerobic microorganism coexist, prosper and symbiotically live, leading to effective action of fermentation-decomposition-synthesis and producing ecosystem of fermentation and synthesis
JPH1034175A (en) * 1996-07-19 1998-02-10 Toyo Bio Reactor Kk Sewage purifying tank
JPH1054067A (en) * 1996-08-08 1998-02-24 Chuo Setsubi Kogyo Kk Circulation type flush toilet
JPH10118671A (en) * 1996-10-22 1998-05-12 Yasutoshi Takashima Automatic cleaning of waste solution and waste water by composite fermentation method and apparatus therefore
JP2000117240A (en) * 1998-10-14 2000-04-25 Inax Corp Supplying device for reuse of waste water

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