JP2004122029A - Aeration treatment system for excretion water - Google Patents

Aeration treatment system for excretion water Download PDF

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Publication number
JP2004122029A
JP2004122029A JP2002291411A JP2002291411A JP2004122029A JP 2004122029 A JP2004122029 A JP 2004122029A JP 2002291411 A JP2002291411 A JP 2002291411A JP 2002291411 A JP2002291411 A JP 2002291411A JP 2004122029 A JP2004122029 A JP 2004122029A
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tank
tanks
pipe
treatment system
aeration
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Japanese (ja)
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Isamu Kobayashi
小林 勇
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IK SHOJI KK
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IK SHOJI KK
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    • 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

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  • Activated Sludge Processes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a highly efficient water treatment system which treats excretion water being a liquid, which is obtained from the excretion of stockbrceding animals or the like by a solid-liquid separation treatment, by the metabolic action of aerobic microorganisms, does not require a wide site and large-scaled civil engineering construction and obtains transparent water having no color and bubbles and almost free from turbidity. <P>SOLUTION: This excretion water treatment system constituted by connecting a plurality of tanks by piping and arranging an oxygen and/or ozone supply means and rotary blades in the piping, is characterized fundamentally by stirring excretion water obtained by the solid-liquid separation treatment of excretion with the rotary blades in a process for feeding excretion water through the piping under a pressure to enhance the aeration treatment effect. By arranging the rotary blades reverse in elevation in the stirring due to the rotary blades, a stirring direction is reversed to further enhance the aeration treatment effect. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、畜産動物等の糞尿から固液分離した液体としての屎尿水を好気性微生物の代謝作用で処理する曝気処理システムに関する。
【0002】
【従来の技術】
従来、畜舎から排出される糞尿等の畜舎汚水(以下、原水という。)は、原水槽に貯留して、そこからポンプにより糞尿固液分離装置に供給して糞等の固形分と液分に分離してそれぞれを処理する方法が採られている。これらの従来の振動篩方式及び傾斜スクリーン方式の固液分離システムは、ホッパー状の汚水受けの傾斜開口部に傾斜状の網目スクリーンを配置してなり、傾斜スクリーンの上部に糞尿をポンプにより供給して、網目スクリーンに沿って落下させることにより、液分はスクリーンの網目より落下しホッパー状の汚水受けから濾液槽に一旦ためてから、曝気槽等の次処理工程に送られる。一方、固形分はスクリーンに沿って流れてスクリーンの下端部から固形分収納ピッチに落下して堆積される。
【0003】
ところで、従来からこの種糞尿を取り扱う活性汚泥処理は大がかりな設備が必要となって、その設備に莫大な費用が掛かるばかりでなく、悪臭の強い汚泥が大量に生じて、その汚泥の処理にも煩わしい工程と多大の費用が必要となって、零細な畜産農家には負担が重く特に適していないという問題があった。この様な事情の中で、図5に示すような特許文献1(特開平11−33588号公報)の「豚その他の家畜の屎尿処理方法及び処理装置」が提案されている。この発明は、「(1) 豚その他の家畜の屎尿に固液分離処理を施して、屎尿中に含まれる固形物を除去し、(2) 前記固液分離によって分離された液体に光合成菌の存在下で一次曝気処理を施して屎尿中の有機物を分解し、ついで(3) このように一次曝気処理が施された液体に放射菌の存在下で更に二次曝気処理を施して屎尿中に残留している有機物を分解し、(4) 多孔質の珪酸カルシウムを濾材として、前記二次曝気処理で生じた前記液体中の燐酸分と窒素分を除去し、(5) 蘇生型の微生物を生成させる酵素がシラスに固定されているセラミックおよび磁鉄鉱を濾材として、前記濾過によって分離された水性液から不純物を除去して、この水性液を清水に変える、という工程からなる方法によって、前記屎尿を処理する。」ものである。その曝気処理の形態は、曝気槽内に水中ポンプ9、吸気管10及びディフュ−ザ−11が構成されており、水中ポンプ9が起動されると、その吐出水流が起こす吸引力(減圧)により液面上の吸気筒12から供給される空気が吸気管10を通じて吸引され、この空気によって形成された気液混合流15が超微細な気泡16を同伴して水中に噴出される。この一次曝気槽8では光合成菌(紅色土壌細菌)の存在下に一次曝気処理が施されて、その液体中に含まれている有機物が分解され、それによって屎尿に起因する臭気が軽減されるとともに、後の濾過工程で除去し易い形の燐酸分と窒素分を生ずる。しかしこのシステムにしても、図5に示されるように固液分離された屎尿水の処理において、一次曝気槽8、二次曝気槽18、第一の濾過槽23が収められている容器22、第二の濾過槽27を収納している容器26そして同一の槽で形成された貯留槽31と凝集沈殿槽32の設備を必要としている。これらの槽は従来の活性汚泥処理施設と比較すれば規模は小さくなっているとはいえ、それなりの広い用地を要すると共に、大きな穴を掘りコンクリート打ちによって槽を構築するといった大掛かりな土木工事を要するため、畜産農家にはやはり負担が相当に重いものである。
【0004】
【特許文献1】
特開平11−33588号公報
【0005】
【発明が解決しようとする課題】
本発明の課題は、畜産動物等の糞尿から固液分離した液体としての屎尿水を好気性微生物の代謝作用で処理する曝気処理システムであって、広い用地も大掛かりな土木工事も必要としない、小規模な設備で臭い、色及び泡が無く、濁りも殆ど無い透明な水を得る高効率の屎尿水処理システムを提供することにある。
【0006】
【課題を解決するための手段】
本発明の屎尿水処理システムは、複数の槽間を配管で連結すると共に、該配管には酸素及び/又はオゾンを供給する手段と、回転翼とが配備され、固体分離した屎尿水が該配管を圧送される過程で前記回転翼により撹拌され曝気処理効果を高めることを基本的特徴とする。その回転翼による撹拌を羽根の迎角が逆の回転翼をシリーズに配置することにより、撹拌方向を反転させて曝気処理効果を更に高めるようにした。また、複数の槽間を連結する配管は蛇行構造とすることにより、槽の配置を近くしたコンパクトな構造でも曝気処理工程を長く採ることができるようにし、曝気処理効果を更に高めるようにした。
そして、本発明の屎尿水処理システムは、上記のような構成で高効率の曝気処理効果を達成できたことにより、容量の小さな槽とそれを連結する配管とで構成できることとなり、複数の槽は土木工事を必要としない地上に設置された金属槽で実現できる。しかも広い用地を必要としないコンパクトな構造にできる。
また、本発明の屎尿水処理システムは、連続処理が可能であるように複数の槽を経由した屎尿水処理液は元の槽に戻され循環する形態をとると共に、最終槽から元の槽に戻される配管の移送液の一部を処理済み液として排出する手段を備えるようにした。そして、その処理済み液は高効率の曝気処理効果を達成できたことに加え、脱色処理工程を経て排水するようにしたことで、臭い、色及び泡が無く、濁りも殆ど無い透明な水を得ることができ一般下水道にそのまま排出することが可能となる。
【0007】
【発明の実施の形態】
従来の曝気槽における空気の曝し方、すなわち屎尿水と空気との接触は、槽の底部に空気噴射口を配置して圧縮空気を噴出させるようにしたものが一般的である。この形態は空気の気泡が底部から屎尿水内をブクブクと上昇する過程で空気が接触する屎尿水に解け込み、好気性のバクテリアの活性を高めるのであるが、接触する屎尿水が広い槽内に流動自在の状態であるため、すべての屎尿水と空気を万遍なく接触させることが難しく、また接触状態を保つことも難しい。先の特許文献1に示された曝気処理形態は、前述したように曝気槽内に水中ポンプ9、吸気管10及びディフュ−ザ−11が構成されており(図5参照)、水中ポンプ9が起動されると、その吐出水流が起こす吸引力(減圧)により液面上の吸気筒12から供給される空気が吸気管10を通じて吸引され、この空気によって形成された気液混合流15が超微細な気泡16を同伴して水中に噴出されるというものであり、ディフュ−ザ−11内では気液混合流が超微細な気泡を同伴するものの、ここでも接触する屎尿水が広い槽内に噴出され、流動自在の状態となるため、すべての屎尿水と万遍なく接触させることが難しく、また接触状態を保つことも難しい。そこで、本発明では流動自在の槽内ではなく流動制約を受ける管内という領域で気液を混合すること、そして気体と混合された液体は元の槽に戻すこと無く次の槽に移送する形態を想到したものである。そうすることにより屎尿水と気体との接触は密にされ、曝気処理された屎尿水だけが次の槽に送られる。そして、接触させる気体としては空気でもよいがバクテリアに好まれる高純度の酸素を用いるようにすると、より効率化が図れる。また、気液混合のため管内に羽根のついた回転翼を配置し、屎尿水がポンプにより圧送されてくると該回転翼が回転させられ、渦流を生じ注入される酸素と撹拌させられるように構成した。この回転翼を配管内に複数個シリーズに配置し、羽根の向きが逆のものを1つおきに配備する。この構成を採ることにより、管内の屎尿水はこの回転翼を通過する毎に渦流が反転させられることとなり、気液混合がより促進させられる。
【0008】
本発明では複数の槽間を配管で連結する構成を採るようにしているが、曝気処理は従来のように槽内で行なうのでは無く配管内で行なうようにしているので、二つの槽を連結する配管の長さは長いほど曝気処理工程を長くすることができる。といって、二つの槽の距離を長くとるとシステムそのものの規模が大きくなってしまうため、本発明では管を蛇行配置して二つの槽を連結するようにした。
本発明の屎尿水処理システムは、流動制約を受ける管内という領域で気液を混合すること、接触させる気体としては酸素を用いるようにしたこと、気液混合のため管内に羽根のついた回転翼を配管内に複数個シリーズに配置し、羽根の向きが逆のものを1つおきに配備したこと、管を蛇行配置するなどの構成で高効率の曝気処理効果を達成できたことにより、従来の曝気槽設備に較べて格段に容量の小さな槽とそれを連結する配管とで同じ処理能力を持ったシステムを構成できることとなった。コンパクトな構造でシステムが実現できるため、複数の槽は土木工事を必要としない地上に設置された金属槽で実現でき、しかも広い用地を必要としない。
【0009】
【実施例1】
本発明の実施例を図1を参照しながら説明する。図の上段はパイプ式曝気システム実施例の平面図であり、下段は第1槽から第2槽への配管部分の側面図である。図から判るようにこの実施例は4槽を第1槽Tと第3槽T及び第2槽Tと第4槽Tがそれぞれ仕切り板Sで仕切られた隣接槽とし、第1槽Tから第4槽Tを順次配管で連結した構造となっている。各槽内には水中ポンプPが配設され、槽内屎尿水を連結された配管L,L,L,Lを通して次段の槽に圧送する。この実施例では5.5kwのポンプPを用い、配管L,L,L,Lには100mmφのステンレス管を、各槽もステンレス製のものを採用している。
【0010】
第1槽Tに固液分離された屎尿水が供給され、活性汚泥が混入される。吸気機構は図2の右下隅の部分拡大図に示すようにポンプPのすぐ下流部分の配管L(L)に吸気管Kが立てられており、圧送される屎尿水の流れによる負圧で該吸気管からガスを吸い込み配管内で気液混合させる。混合ガスは大気であってもよいが、この実施例ではバクテリアの活性を高めるため酸素ガスをボンベから供給するようにした。ボンベに替えて酸素発生装置を接続するようにしてもよい。配管L,L,L,Lは図1の下段に示すように次段の槽との間を二往復半するように蛇行させて移送する。その間図3に示すように迎角が逆となっている回転翼を交互に直列に5つ配置するようにした。これによって、屎尿水は該回転翼を通過する度に逆巻の渦流とされ、気液混合が促進される。最終段の第4槽からの配管Lでは酸素の他にオゾンを加えるようにし、屎尿水の脱色を行う。脱色手段にはオゾンの他炭を用いたり、特殊な土や薬品を使うことも可能である。この配管Lはバルブ2を介して第1槽Tに接続されると共にバルブ3を介して排出管Loにも接続されている。このバルブ2,3の開口を調節することにより第1槽Tに戻す処理済み屎尿水と排出管Loから排出させる処理済み屎尿水との割合が決められる。一般には80%〜90%が第1槽Tに戻され、供給される新たな屎尿水を希釈すると共に、次のサイクルで再度曝気処理が加えられる。
この実施例は各槽の幅寸法は1.2m×1.2mで高さ寸法も1.2mmとした。第1槽Tと第3槽T及び第2槽Tと第4槽T間の距離は6m余りとしたので、3m×9m程度の用地が有れば足り、地上設置が可能である。
【0011】
【実施例2】
本発明の異なる実施例を図4を参照しながら説明する。この実施例は基本的に先の実施例1のシステムを1ユニットとし、複数ユニットをシリーズに連結したもので、必要処理能力に応じて使い分けるものである。1ユニットは豚200頭規模の処理の目安であり、400頭規模であれば2ユニットが600頭規模であれば3ユニットが連設される。畜産農家の飼育規模に応じたユニット数を設置することができるし、最大飼育規模に合わせて設置しておき、飼育規模を小さくする時期には後段のユニットから必要ユニットのみを使用する形態も採れる。
【0012】
【発明の効果】
本発明の屎尿水処理システムは、複数の槽間を配管で連結すると共に、該配管には酸素及び/又はオゾンを供給する手段と、回転翼とが配備され、固体分離した屎尿水が流動制限を受けている該配管を圧送される過程で前記回転翼により撹拌される形態を取っているので、気液混合が効率よく行なわれると共に、処理された屎尿水は未処理の屎尿水と混合されること無く次段の槽に移送されるので確実で高い曝気処理効果を奏する。
また、本発明では回転翼による撹拌を羽根の迎角が逆の回転翼をシリーズに配置することにより撹拌方向が反転させられるので、気液混合が効率よく行なわれ、更に高い曝気処理効果を奏する。複数の槽間を連結する配管は蛇行構造とすることにより、槽の配置を近くしたコンパクトな構造でも曝気処理工程を長く採ることができるようにし、曝気処理効果を更に高めることが可能となる。
そして、本発明の屎尿水処理システムは、上記のような構成で高効率の曝気処理効果を達成できたことにより、容量の小さな槽とそれを連結する配管とで構成できることとなり、複数の槽は土木工事を必要としない地上に設置された金属槽で実現できる。しかも広い用地を必要としないコンパクトな構造として実現できる。
また、本発明の屎尿水処理システムは、複数の槽を経由した屎尿水処理液は元の槽に戻され循環する形態をとると共に、最終槽から元の槽に戻される配管の移送液の一部を処理済み液として排出する手段を備えるようにしたことにより、数十日というような長期間のバッチ処理では無く連続処理が可能となった。そして、その処理済み液は高効率の曝気処理効果を達成できたことに加え、脱色処理工程を経て排水するようにしたことで、臭い、色及び泡を無くし、濁りも殆ど無い透明な水を得ることができ一般下水道にそのまま排出することが可能となる。
【図面の簡単な説明】
【図1】本発明の1実施例を示す図であり、上段が平面図で下段が第1槽から第2槽への配管部分の側面図である。
【図2】本発明の1実施例の槽構造を示す断面図である。
【図3】実施例において配管内に回転翼を設置した形態を示す透過斜視図である。
【図4】本発明のパイプ式曝気システムの設計における規模に応じた対応を説明する例である。
【図5】従来の曝気システムを説明する図である。
【符号の説明】
,T,T,T 第1槽乃至第4槽  B 右巻き回転翼
,L,L,L 配管        B 左巻き回転翼
P 水中ポンプ
,B,B バルブ
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an aeration treatment system for treating human wastewater as a liquid which is separated into solid and liquid from manure of livestock animals and the like by the metabolic action of aerobic microorganisms.
[0002]
[Prior art]
Conventionally, livestock sewage (hereinafter, referred to as raw water) such as manure discharged from a livestock house is stored in a raw water tank, and then supplied to a manure solid-liquid separation device by a pump to be converted into solids and liquids such as feces. The method of separating and treating each is adopted. These conventional vibrating sieve type and inclined screen type solid-liquid separation systems are configured such that an inclined mesh screen is arranged at an inclined opening of a hopper-shaped wastewater receiver, and manure is supplied to the upper part of the inclined screen by a pump. Then, by dropping along the mesh screen, the liquid component falls from the mesh of the screen and is temporarily stored in a filtrate tank from a hopper-like wastewater receiver, and then sent to the next processing step such as an aeration tank. On the other hand, the solids flow along the screen, fall from the lower end of the screen to the solids storage pitch, and are deposited.
[0003]
By the way, conventionally, activated sludge treatment that treats this kind of manure requires a large-scale facility, which not only costs enormous costs, but also generates a large amount of strongly odorous sludge. A cumbersome process and enormous cost are required, and there is a problem that the burden is heavy for a small-scale livestock farming farmer and is not particularly suitable. Under such circumstances, a "method and apparatus for treating human waste of pigs and other livestock" of Patent Document 1 (Japanese Patent Laid-Open No. 11-33588) as shown in FIG. 5 has been proposed. The present invention provides "(1) a solid-liquid separation treatment for human waste of pigs and other livestock to remove solid substances contained in the human waste, and (2) a photosynthetic bacterium is added to the liquid separated by the solid-liquid separation. The primary aeration treatment is performed in the presence to decompose the organic matter in the human waste, and then (3) the liquid subjected to the primary aeration treatment is further subjected to the secondary aeration treatment in the presence of the radioactive bacterium to produce the waste in the human waste. The remaining organic matter is decomposed, and (4) the phosphoric acid and nitrogen components in the liquid generated by the secondary aeration treatment are removed using porous calcium silicate as a filter material, and (5) resuscitation-type microorganisms are removed. Removing the impurities from the aqueous liquid separated by the filtration using the ceramic and magnetite in which the enzyme to be produced is fixed to shirasu as a filter medium, and converting the aqueous liquid into fresh water, the method comprising the steps of: Process. " A. In the form of the aeration process, a submersible pump 9, an intake pipe 10, and a diffuser 11 are configured in an aeration tank, and when the submersible pump 9 is started, the suction force (decompression) generated by the discharge water flow. Air supplied from an intake pipe 12 above the liquid surface is sucked through an intake pipe 10, and a gas-liquid mixed flow 15 formed by the air is ejected into water with superfine bubbles 16. In this primary aeration tank 8, primary aeration treatment is performed in the presence of photosynthetic bacteria (red soil bacteria) to decompose organic substances contained in the liquid, thereby reducing the odor caused by human waste. In the subsequent filtration step, phosphoric acid and nitrogen are easily removed. However, even in this system, as shown in FIG. 5, in the treatment of the human waste water separated into solid and liquid, the container 22 containing the primary aeration tank 8, the secondary aeration tank 18, and the first filtration tank 23, A container 26 accommodating the second filtration tank 27, and a storage tank 31 and a coagulation sedimentation tank 32 formed of the same tank are required. Although these tanks are smaller in size than conventional activated sludge treatment facilities, they require a certain amount of land and require large-scale civil works such as digging large holes and constructing tanks by concrete casting. Therefore, the burden on livestock farmers is still considerable.
[0004]
[Patent Document 1]
JP-A-11-33588 [0005]
[Problems to be solved by the invention]
An object of the present invention is an aeration treatment system for treating human wastewater as a liquid which is separated into solid and liquid from manure of livestock animals or the like by the metabolic action of aerobic microorganisms, and does not require a large site or large-scale civil engineering work. It is an object of the present invention to provide a high-efficiency human wastewater treatment system that can obtain transparent water with little odor, color, and bubble, and almost no turbidity with a small-scale facility.
[0006]
[Means for Solving the Problems]
In the human wastewater treatment system of the present invention, a plurality of tanks are connected by a pipe, and a means for supplying oxygen and / or ozone and a rotating blade are provided in the pipe, and the human wastewater separated into solids is provided in the pipe. The basic feature is that the agitator is agitated by the rotating blades in the process of being pumped to enhance the aeration treatment effect. The stirring by the rotating blades is arranged in a series of rotating blades having the opposite angles of attack of the blades, thereby reversing the stirring direction to further enhance the aeration treatment effect. Further, the piping connecting the plurality of tanks has a meandering structure, so that the aeration process can be performed for a long time even in a compact structure in which the arrangement of the tanks is close, and the effect of the aeration process is further enhanced.
Then, the human wastewater treatment system of the present invention can achieve a high-efficiency aeration treatment effect with the above-described configuration, and thus can be configured with a small-capacity tank and a pipe connecting the tank, and a plurality of tanks are provided. This can be achieved with a metal tank installed on the ground that does not require civil engineering. Moreover, a compact structure that does not require a large area can be achieved.
Further, the human wastewater treatment system of the present invention takes a form in which the human wastewater treatment liquid passed through a plurality of tanks is returned to the original tank and circulated so that continuous processing is possible, and the final tank is returned to the original tank. Means are provided for discharging a part of the transfer liquid in the returned pipe as a processed liquid. And, in addition to being able to achieve the high-efficiency aeration treatment effect, the treated liquid is drained through the decolorization treatment process, so that there is no odor, no color, no bubbles, and almost no turbidity. And it can be discharged to the general sewer as it is.
[0007]
BEST MODE FOR CARRYING OUT THE INVENTION
A conventional method of exposing air in an aeration tank, that is, contact between human wastewater and air, is generally a method in which an air injection port is arranged at the bottom of the tank to eject compressed air. In this form, air bubbles dissolve into the wastewater that comes into contact with air in the process of rising from the bottom and into the wastewater, and increase the activity of aerobic bacteria. Since it is in a free-flowing state, it is difficult to make all the wastewater and air uniformly contact, and it is also difficult to maintain the contact state. In the aeration processing mode described in Patent Document 1, as described above, the submersible pump 9, the suction pipe 10, and the diffuser 11 are configured in the aeration tank (see FIG. 5). When activated, the air supplied from the intake cylinder 12 on the liquid surface is sucked through the intake pipe 10 by the suction force (decompression) caused by the discharge water flow, and the gas-liquid mixed flow 15 formed by this air is superfine. The gas-liquid mixed flow is accompanied by ultra-fine bubbles in the diffuser 11, but also contacts the human wastewater into a wide tank. In addition, since it is in a free flowing state, it is difficult to make uniform contact with all human wastewater, and it is also difficult to maintain the contact state. Therefore, in the present invention, a form in which gas-liquid is mixed not in a free-flowing tank but in a pipe, which is subject to flow restriction, and the liquid mixed with the gas is transferred to the next tank without returning to the original tank. That is what I imagined. By doing so, the contact between the wastewater and the gas is made dense, and only the aerated wastewater is sent to the next tank. As the gas to be contacted, air may be used, but if high-purity oxygen, which is preferred by bacteria, is used, efficiency can be further improved. In addition, a rotating blade with a blade is arranged in the tube for gas-liquid mixing, and when the waste water is pumped by a pump, the rotating blade is rotated to generate a vortex and to be stirred with injected oxygen. Configured. A plurality of the rotor blades are arranged in series in the pipe, and the blades having the opposite direction of the blade are provided every other one. By adopting this configuration, the vortex of the human wastewater in the pipe is reversed every time it passes through the rotary wing, and the gas-liquid mixing is further promoted.
[0008]
In the present invention, a configuration is adopted in which a plurality of tanks are connected by piping. However, since the aeration treatment is performed not in the tank as in the conventional case but in the pipe, the two tanks are connected. The longer the length of the piping, the longer the aeration process. However, if the distance between the two tanks is increased, the scale of the system itself becomes large. Therefore, in the present invention, the two tanks are connected by meandering the tubes.
The human wastewater treatment system of the present invention is characterized in that gas-liquid is mixed in an area of a pipe subject to flow restriction, oxygen is used as a gas to be brought into contact, and a rotary blade having a blade in the pipe for gas-liquid mixing. In a series of multiple pipes in a pipe, and every other pipe with the opposite direction of the blades was installed. It is now possible to construct a system with the same processing capacity by using a tank with much smaller capacity than the aeration tank equipment and the piping connecting it. Since the system can be realized with a compact structure, the plurality of tanks can be realized by metal tanks installed on the ground which do not require civil engineering work, and do not require a large site.
[0009]
Embodiment 1
An embodiment of the present invention will be described with reference to FIG. The upper part of the figure is a plan view of the embodiment of the pipe type aeration system, and the lower part is a side view of a pipe portion from the first tank to the second tank. This embodiment, as seen from the figure a 4 tank first tank T 1 and the third tank T 3 and the second tank T 2 and the adjacent tank fourth tank T 4 were each partitioned by the partition plate S, the first and it has a structure connected by the tank T 1 sequentially piping fourth tank T 4. A submersible pump P is provided in each tank, and pumps the wastewater in the tank through the connected pipes L 1 , L 2 , L 3 , and L 4 to the next tank. In this embodiment, a 5.5 kW pump P is used, a 100 mmφ stainless steel pipe is used for the pipes L 1 , L 2 , L 3 , and L 4 , and each tank is made of stainless steel.
[0010]
Raw sewage water which is solid-liquid separation in the first tank T 1 is supplied, the activated sludge is mixed. As shown in the enlarged view of the lower right corner in FIG. 2, the intake mechanism has an intake pipe K provided in a pipe L 1 (L 3 ) immediately downstream of the pump P, and a negative pressure caused by the flow of the excreted waste water. Then, gas is sucked from the intake pipe and gas-liquid mixed in the pipe. The mixed gas may be air, but in this example, oxygen gas was supplied from a cylinder to increase the activity of bacteria. An oxygen generator may be connected instead of the cylinder. The pipes L 1 , L 2 , L 3 , L 4 meander and transfer so as to make two-and-a-half reciprocations with the next tank as shown in the lower part of FIG. In the meantime, as shown in FIG. 3, five rotors having opposite angles of attack were alternately arranged in series. As a result, each time the waste water passes through the rotary wing, it becomes a reverse vortex, which promotes gas-liquid mixing. To apply a ozone in addition to the pipe L 4 in oxygen from the fourth tank in the final stage, performs bleaching of human waste water. As the decoloring means, it is possible to use charcoal other than ozone, or to use special soil or chemicals. The pipe L 4 are also connected to the discharge pipe Lo through the valve 3 is connected to the first tank T 1 through a valve 2. Ratio of the treated sewage water to discharge from the discharge pipe Lo and treated sewage water to return to the first tank T 1 is determined by adjusting the opening of the valve 2. Generally 80% to 90% is returned to the first tank T 1 is in, along with diluting the new raw sewage water supplied again aeration in the next cycle is added.
In this embodiment, each tank had a width of 1.2 m × 1.2 m and a height of 1.2 mm. Since the first tank T 1 and the third tank T 3 and the second tank T 2 the distance between the fourth tank T 4 was more than 6 m, sufficient if there is land of about 3m × 9m, can Ground is there.
[0011]
Embodiment 2
A different embodiment of the present invention will be described with reference to FIG. In this embodiment, the system of the first embodiment is basically one unit, and a plurality of units are connected in series, and are selectively used according to the required processing capacity. One unit is a standard for the processing of 200 pigs, and 2 units for 400 pigs and 3 units for 600 pigs. The number of units can be set according to the breeding scale of a livestock farmer, or it can be installed according to the maximum breeding scale, and when the breeding scale is reduced, it is possible to use only the necessary units from the later units. .
[0012]
【The invention's effect】
In the human wastewater treatment system of the present invention, a plurality of tanks are connected by pipes, and the pipes are provided with a means for supplying oxygen and / or ozone, and a rotary blade, and the wastewater separated from solids is flow-limited. In the process of being pressure-fed through the receiving pipe, the rotary blade is agitated by the rotating blades, so that gas-liquid mixing is efficiently performed, and the treated wastewater is mixed with untreated wastewater. Since it is transferred to the next tank without any trouble, a reliable and high aeration effect can be obtained.
In addition, in the present invention, the stirring direction is reversed by arranging the rotating blades having the opposite angle of attack of the blades in series in the stirring by the rotating blades, so that the gas-liquid mixing is performed efficiently, and a higher aeration effect is achieved. . The piping connecting the plurality of tanks has a meandering structure, so that the aeration process can be performed for a long time even with a compact structure in which the arrangement of the tanks is close, and the aeration treatment effect can be further enhanced.
Then, the human wastewater treatment system of the present invention can achieve a high-efficiency aeration treatment effect with the above-described configuration, and thus can be configured with a small-capacity tank and a pipe connecting the tank, and a plurality of tanks are provided. This can be achieved with a metal tank installed on the ground that does not require civil engineering. Moreover, it can be realized as a compact structure that does not require a large area.
Further, in the human wastewater treatment system of the present invention, the human wastewater treatment liquid passed through the plurality of tanks is returned to the original tank and circulated, and one of the pipe transfer liquids returned from the final tank to the original tank. By providing a means for discharging the part as a processed liquid, continuous processing can be performed instead of long-term batch processing such as several tens of days. And, in addition to being able to achieve the high-efficiency aeration treatment effect, the treated liquid is drained through a decolorization treatment step, eliminating odors, colors and bubbles, and clear water with almost no turbidity. And it can be discharged to the general sewer as it is.
[Brief description of the drawings]
FIG. 1 is a view showing one embodiment of the present invention, in which an upper part is a plan view and a lower part is a side view of a pipe portion from a first tank to a second tank.
FIG. 2 is a sectional view showing a tank structure according to one embodiment of the present invention.
FIG. 3 is a transparent perspective view showing a form in which a rotor is installed in a pipe in the embodiment.
FIG. 4 is an example for explaining a measure according to a scale in designing a pipe-type aeration system of the present invention.
FIG. 5 is a diagram illustrating a conventional aeration system.
[Explanation of symbols]
T 1 , T 2 , T 3 , T 4 First to fourth tanks BR Right-handed rotary blades L 1 , L 2 , L 3 , L 4 piping B L Left-handed rotary blades P Submersible pumps B 1 , B 2 , B 3 valve

Claims (6)

複数の槽間をポンプを介して配管で連結すると共に、該配管には酸素及び/又はオゾンを供給する手段と、回転翼とが配備され、固体分離した屎尿水が該配管を圧送される過程で前記回転翼により撹拌され曝気処理効果を高めたことを特徴とする屎尿水処理システム。A process in which a plurality of tanks are connected by a pipe via a pump, and a means for supplying oxygen and / or ozone and a rotating blade are provided in the pipe, and a process in which human waste water separated into solids is pumped through the pipe. The wastewater treatment system according to any one of claims 1 to 3, wherein the agitating effect is enhanced by the rotating blades to enhance an aeration treatment effect. 羽根の迎角が逆の回転翼を交互にシリーズに配置し、撹拌方向を反転させて曝気処理効果を高めたことを特徴とする請求項1に記載の屎尿水処理システム。2. The human waste water treatment system according to claim 1, wherein the rotating blades having the opposite attack angles of the blades are alternately arranged in series, and the stirring direction is reversed to enhance the aeration treatment effect. 複数の槽間を連結する配管は蛇行構造とすることにより、槽の配置が近くても槽間の曝気処理工程を長く採るようにした請求項1又は2に記載の屎尿水処理システム。The wastewater treatment system according to claim 1 or 2, wherein the piping connecting the plurality of tanks has a meandering structure so that the aeration process between the tanks is long even when the arrangement of the tanks is close. 複数の槽は地上に設置できる金属槽で形成したものである請求項1乃至3のいずれかに記載の屎尿水処理システム。The human wastewater treatment system according to any one of claims 1 to 3, wherein the plurality of tanks are formed by metal tanks that can be installed on the ground. 複数の槽を経由した糞尿処理液は元の槽に戻され循環する形態をとると共に、最終槽から元の槽に戻される配管の移送液の一部を処理済み液として排出する手段を前記配管に備えた請求項1乃至4のいずれかに記載の屎尿水処理システム。The manure treatment liquid passing through the plurality of tanks is returned to the original tank and takes a form to circulate, and the pipe is provided with means for discharging a part of the transfer liquid of the pipe returned from the final tank to the original tank as a treated liquid. The human wastewater treatment system according to any one of claims 1 to 4, wherein 処理済み液は脱色処理工程を経て排水するようにした請求項1乃至5のいずれかに記載の屎尿水処理システム。The wastewater treatment system according to any one of claims 1 to 5, wherein the treated liquid is drained through a decolorizing treatment step.
JP2002291411A 2002-10-03 2002-10-03 Aeration treatment system for excretion water Pending JP2004122029A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106746458A (en) * 2016-12-26 2017-05-31 广东象博生态科技有限公司 A kind of fecal pollution processing system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106746458A (en) * 2016-12-26 2017-05-31 广东象博生态科技有限公司 A kind of fecal pollution processing system
CN106746458B (en) * 2016-12-26 2023-03-31 广东象博生态科技有限公司 Excrement treatment system

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