JP2002119992A - Sewage treatment method by covering surface of water of anaerobic tank with sheet - Google Patents

Sewage treatment method by covering surface of water of anaerobic tank with sheet

Info

Publication number
JP2002119992A
JP2002119992A JP2000312815A JP2000312815A JP2002119992A JP 2002119992 A JP2002119992 A JP 2002119992A JP 2000312815 A JP2000312815 A JP 2000312815A JP 2000312815 A JP2000312815 A JP 2000312815A JP 2002119992 A JP2002119992 A JP 2002119992A
Authority
JP
Japan
Prior art keywords
anaerobic
sheet
sludge
tank
sewage
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.)
Pending
Application number
JP2000312815A
Other languages
Japanese (ja)
Inventor
Hiroaki Hashiguchi
裕昭 橋口
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.)
PURIO KK
Original Assignee
PURIO KK
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 PURIO KK filed Critical PURIO KK
Priority to JP2000312815A priority Critical patent/JP2002119992A/en
Publication of JP2002119992A publication Critical patent/JP2002119992A/en
Pending legal-status Critical Current

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Classifications

    • Y02W10/12

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for efficiently reducing highly concentrated organic sludge such as excretions, or the like, generated from a barn under an anaerobic atmosphere at a low cost. SOLUTION: The surface of the water of an anaerobic tank storing sewage is covered with an air impermeable sheet to hold the upper layer water area under the sheet to an anaerobic state to adjust the whole of sewage in the tank to an environment suitable for anaerobic microorganisms. By this constitution, the decomposition of sludge by the anaerobic microorganisms is performed highly efficiently and the decomposition gas of sludge by the microorganisms generated under the sheet is discharged or recovered.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明が属する技術分野】本発明は、住宅や畜舎などか
ら発生する糞尿などの高濃度有機汚水中の汚泥分を嫌気
的雰囲気下で効率良く減量化する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for efficiently reducing the amount of sludge in high-concentration organic sewage such as manure generated from a house or a livestock barn under an anaerobic atmosphere.

【0002】[0002]

【従来の技術】従来、汚水の微生物による処理方法とし
ては、エアレーションによる曝気(好気)処理によるも
のと、エアレーションを行わないで嫌気性雰囲気で処理
する嫌気処理と、曝気処理と嫌気処理を併用した方法が
行われている。通常、汚水のBOD濃度が5000〜7
000ppm以下の場合にはバクテリアなどの好気性微
生物による曝気処理(活性汚泥処理法)のみによる対応
ができるが、濃度がそれ以上に高い場合には分解効率が
悪くなり処理が困難となる。そこで、嫌気性雰囲気にし
て有機物分解細菌などの嫌気性微生物による処理を行う
ことになる。そして、より処理効率を高めるために、そ
の嫌気性処理した後にさらに曝気処理を行うことが多
い。
2. Description of the Related Art Conventionally, methods of treating wastewater by microorganisms include aeration (aerobic) treatment by aeration, anaerobic treatment in an anaerobic atmosphere without aeration, and a combination of aeration treatment and anaerobic treatment. The method has been done. Usually, the BOD concentration of sewage is 5,000 to 7,
If the concentration is less than 000 ppm, it can be dealt with only by aeration treatment with aerobic microorganisms such as bacteria (activated sludge treatment method). However, if the concentration is higher than this, the decomposition efficiency becomes poor and the treatment becomes difficult. Therefore, an anaerobic atmosphere is used to perform treatment with anaerobic microorganisms such as organic matter-decomposing bacteria. Then, in order to further increase the processing efficiency, an aeration process is often performed after the anaerobic process.

【0003】また、畜舎から発生するBOD濃度が非常
に高い(20000ppm以上)糞尿などは、上記微生
物による処理の方法では時間がかかり過ぎるため、微生
物に拠らない方法を併用することが多い。その方法とし
ては、糞と尿を濾過スクリーンで固形分(糞)と液体分
(尿)とを分離し、通過した尿を中心とした液体につい
てはさらに水を加えて希釈し処理する方法(A方式)
と、凝集剤で固形分と液体分とを分離処理する方法(B
方式)とが行われている。
[0003] In addition, for manure and the like generated from cattle and having a very high BOD concentration (20,000 ppm or more), the method of treatment with the above microorganisms takes too much time, and therefore, a method not relying on microorganisms is often used in combination. As the method, a method is used in which a solid (feces) and a liquid (urine) are separated from feces and urine by a filtration screen, and the liquid mainly passing through the urine is further diluted by adding water to be treated (A). method)
And a method of separating a solid content and a liquid content with a coagulant (B
Method) has been performed.

【0004】上記A方式については、糞と尿とをスクリ
ーンで分離し、なおかつ発生する処理水にその水量の約
50%の水を加えてBOD濃度を約1500ppmまで
希釈してさらに曝気処理を行う方法であり、これには安
定した大量の水が必要となる難点がある。
In the above method A, feces and urine are separated by a screen, and about 50% of the amount of treated water is added to the generated treated water to dilute the BOD concentration to about 1500 ppm, followed by further aeration treatment. Method, which has the disadvantage of requiring a large amount of stable water.

【0005】また、上記B方式については、糞尿が混合
状態のままでスクリュープレスにかけて糞と尿を分離
し、分離した尿はBOD濃度が約15000ppmと高
いので、凝集剤を投入してスクリーンで凝集した固形分
をさらに分離してBOD濃度を約5000〜7000p
pm以下に下げ、その上でさらにその処理汚水を曝気処
理している。これに用いる凝集剤の費用は、例えば豚1
000頭の畜舎を参考にすると、1ヶ月毎に50万円程
かかっており、この負担は極めて大きい。しかも、凝集
剤の投入量が多いと、pH値が9近くにもなり、そうな
るとpH調整剤の投入も必要でありさらに維持費が嵩む
こととなる。
[0005] In the above-mentioned B method, feces and urine are separated by a screw press while the feces and urine are mixed, and the separated urine has a high BOD concentration of about 15000 ppm. The separated solid content is further separated to reduce the BOD concentration to about 5,000 to 7000 p.
pm or less, and then the treated wastewater is further aerated. The cost of the flocculant used for this is, for example,
Referring to the tent of 000 cattle, it costs about 500,000 yen per month, and this burden is extremely large. In addition, when the amount of the coagulant added is large, the pH value becomes close to 9, and in that case, it is necessary to add a pH adjuster, which further increases the maintenance cost.

【0006】このB方式は、一般的に普及しているもの
ではあるが、実施するための施設はスクリュープレスや
スクリーン装置など大掛かりな装置を備えなければなら
ず、その装置も設置後のメンテナンスを要し、その手間
やそのコストは養豚業者にとって大変な負担を強いるも
のであった。そして、分離除去される糞(有機固形分)
についての処分の方法は、肥料化し再利用することかが
好ましいが、凝集剤を含む糞はその薬利作用により堆肥
としては使用不適となることがある。そして、再利用で
きないそのような分離固形物は焼却などの処分費用もか
かってくる。
[0006] Although this B system is widely used, the facility for implementing it must be equipped with a large-scale device such as a screw press or a screen device, and the device also requires maintenance after installation. In essence, the labor and cost placed a heavy burden on pig farmers. And feces that are separated and removed (organic solids)
The method of disposal is preferably fertilization and reuse, but feces containing flocculants may be unsuitable for use as compost due to their medicinal properties. And such separated solids that cannot be reused also incur disposal costs such as incineration.

【0007】上記AB両方式のいずれにおいても、高額
な設備費用がかかり、また処理施設の場所も広面積が必
要であり、さらに電気代や薬品代などのランニングコス
トも大きく、これらの費用負担は養豚事業の経営にとっ
ては死活問題であった。このため、業者の中には、経費
削減のために、大量な汲み水で排出規制値の濃度まで薄
めるだけといった乱暴な処理方法も行われているのが実
態である。
[0007] In both of the above AB systems, high equipment costs are required, the location of the processing facility requires a large area, and running costs such as electricity and chemicals are large. It was a matter of life and death for the pig farming business. For this reason, some companies use a violent treatment method in which only a large amount of water is used to reduce the concentration to the emission regulation value in order to reduce costs.

【0008】また、マンション、アパート、レストラ
ン、パチンコ店、オフィスビルなどから発生する屎尿の
処理には、汚水中の浮遊物を分離し、同時に分離したス
カムや沈殿物を貯留する50〜500人規模の沈殿分離
槽を備えた沈殿分離方式が採られている。沈殿分離方式
は、糞尿が水で薄められるのでBOD濃度は500pp
m程度になるが、規模が大きいほど悪臭がひどくなり、
1年に数回汲み取りしなければならないために高い維持
費を要する。さらに500人規模になると、沈殿分離槽
は約180m3の大きさとなり、また、そこから発生す
るスカムと汚泥を分けて汲み取ることが難しく、汲み取
り費用も多額となっていた。
[0008] In the treatment of human waste generated from condominiums, apartments, restaurants, pachinko parlors, office buildings, etc., 50 to 500 persons are required to separate suspended matters in sewage and simultaneously store the separated scum and sediment. The sedimentation separation system provided with the sedimentation separation tank is adopted. In the sedimentation separation method, since the manure is diluted with water, the BOD concentration is 500 pp.
m, but the larger the scale, the worse the odor becomes,
High maintenance costs due to having to pump several times a year. Further, when the scale becomes 500 people, the size of the sedimentation separation tank becomes about 180 m 3 , and it is difficult to separate and extract the scum and sludge generated therefrom, and the pumping cost is large.

【0009】[0009]

【発明が解決しようとする課題】本発明は、上記実情に
鑑みてなされたもので、住宅や畜舎などから発生する糞
尿など高濃度の有機汚泥を嫌気的雰囲気下において低コ
ストで効率良く減量化する方法を提供するものである
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above circumstances, and has been proposed to efficiently reduce high-concentration organic sludge such as manure generated from a house or a livestock barn at low cost under an anaerobic atmosphere. Provide a way to

【0010】[0010]

【課題を解決するための手段】上記課題を解決するため
に、本発明は、汚水を入れた嫌気槽の水面を不通気性シ
ートで被覆してシート下の上層水域を嫌気状態に保持す
ることで、槽内汚水全体を嫌気性微生物の適環境に整え
て嫌気性微生物による汚泥分の分解を高効率に処理する
とともに、そのシート下に発生する微生物による汚泥分
解ガスを大気中に放出するか又は回収することを特徴と
するシートによる嫌気槽水面被覆汚水処理法である。
In order to solve the above problems, the present invention is to cover the water surface of an anaerobic tank containing sewage with an impermeable sheet and to maintain an upper water area under the sheet in an anaerobic state. In order to treat sludge decomposed by anaerobic microorganisms with high efficiency by adjusting the entire sewage in the tank to an appropriate environment for anaerobic microorganisms, and to release sludge decomposition gas by microorganisms generated under the sheet into the atmosphere Or an anaerobic tank water surface covering sewage treatment method using a sheet characterized by being recovered.

【0011】また、上記構成において、前記嫌気槽の汚
水中に微生物活性材を投入し汚泥分の分解を促進させる
ことを特徴とするものである。
[0011] In the above structure, a microorganism-activating agent is added to the sewage in the anaerobic tank to promote the decomposition of sludge.

【0012】さらに、上記構成において、前記微生物活
性材に、曝気槽で得られた上澄液を用いるものである。
Further, in the above configuration, a supernatant obtained in an aeration tank is used as the microorganism active material.

【0013】[0013]

【発明の実施の形態】本発明の実施の形態を図の実施例
に基づいて以下説明する
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings.

【0014】本発明は、図1に示すように、汚水を入れ
た嫌気槽1の水面を酸素遮断する不通気性シート2で被
覆し、その不通気性シート下の汚水上層水域を嫌気状態
に保持する。すると、槽内に流れている汚水全体が嫌気
性微生物の適環境に整えられて嫌気性微生物による汚泥
分の分解が高められる。
According to the present invention, as shown in FIG. 1, the water surface of an anaerobic tank 1 containing sewage is covered with an impermeable sheet 2 for blocking oxygen, and the upper water area of the sewage below the impermeable sheet is made anaerobic. Hold. Then, the entire sewage flowing in the tank is adjusted to an appropriate environment for anaerobic microorganisms, and the decomposition of sludge by anaerobic microorganisms is enhanced.

【0015】移送管には空気の侵入を防ぐためキャップ
を被せる。また、このキャップで蓋することによって悪
臭の放出を防ぐことができる。また、不通気性シート2
下に発生する微生物による汚泥分解ガスを大気中に放出
するか又は回収する。
The transfer tube is covered with a cap to prevent air from entering. Further, by covering with this cap, emission of offensive odor can be prevented. In addition, impermeable sheet 2
Release or recover the sludge decomposed gas from the microorganisms generated below into the atmosphere.

【0016】また、嫌気槽の汚水中に微生物活性栄養粉
又は微生物活性栄養液などの微生物活性材を投入し、汚
泥分の分解を促進させることができる。
[0016] In addition, a microbial active material such as a microbial active nutrient powder or a microbial active nutrient solution can be introduced into the sewage of the anaerobic tank to promote the decomposition of sludge.

【0017】さらに、前記微生物活性材は、曝気槽で得
られた上澄液が使用できる。この上澄液は、豊富な栄養
素を含み、また汚泥分解の触媒的な作用をする酵素が含
まれていて、嫌気と好気併用施設では、この上澄液は同
じ処理施設内で得られるものなので、簡単且つ豊富に供
給使用できる利点がある。
Further, as the above-mentioned microorganism active material, a supernatant obtained in an aeration tank can be used. The supernatant contains abundant nutrients and contains enzymes that catalyze sludge degradation. In a combined anaerobic and aerobic facility, the supernatant is obtained in the same treatment facility. Therefore, there is an advantage that it can be easily and abundantly supplied and used.

【0018】[0018]

【作用】これまでの嫌気槽は、図2に示すように、汚水
の水面部分に酸素があるために汚水上層部の嫌気性細菌
の活動が抑制され、また水面に浮遊物質が皮膜上に集合
しさらにはその表面が乾燥して厚い層を成す所謂「スカ
ム」が発生していた。このカスムは時間とともに増加し
てくので槽の容量と通路確保のため何度も繰り返し除去
しなければならなかった。
[Function] As shown in Fig. 2, the conventional anaerobic tank suppresses the activity of anaerobic bacteria in the upper part of the sewage due to the presence of oxygen in the water surface of the sewage. Further, so-called "scum" in which the surface is dried to form a thick layer has occurred. Since the amount of the gas increased with time, it had to be removed many times to secure the capacity and passage of the tank.

【0019】本発明は、図1に示すように、汚水を入れ
た嫌気槽1の水面を不通気性シート2で被覆するものな
ので、嫌気槽1内の汚水部分F内に、その上の空間部分
Sにある酸素が供給されなくなる。また、水面を不通気
性シート2で覆うことにより、水の水面からの蒸発がな
くなり、汚水の気化冷却を防ぐとともに、シート素材が
備えた断熱性により保温効果が生じ、比較的高い温度域
で活発化する嫌気性細菌にとって汚水が適温な環境とな
る。このため不通気性シート2下に嫌気性雰囲気を好む
微生物が活発に増殖し、汚泥分が速やかに分解される。
そして、この水面には、空気接触面がないために、これ
までの嫌気槽につきものカスムは全く発生できなくな
る。
In the present invention, as shown in FIG. 1, the water surface of an anaerobic tank 1 containing sewage is covered with an impermeable sheet 2, so that a sewage portion F in the anaerobic tank 1 has a space above it. The oxygen in the portion S is not supplied. In addition, by covering the water surface with the air-impermeable sheet 2, the water is prevented from evaporating from the water surface, preventing the evaporative cooling of the sewage, and the heat insulating effect provided by the sheet material produces a heat retaining effect. Sewage provides a suitable temperature environment for activating anaerobic bacteria. For this reason, microorganisms that prefer an anaerobic atmosphere under the air-impermeable sheet 2 actively proliferate, and sludge components are rapidly decomposed.
Then, since there is no air contact surface on this water surface, no dregs can be generated at all with the conventional anaerobic tank.

【0020】またそのシート2下には嫌気性細菌の活動
により発生するメタン、硫化水素などの悪臭を放つガス
が溜まるが、そのガスの容積の拡大とともにその部分の
シートが膨らんでいき、やがて周辺の隙間から大気中に
放出される。なお、メタン、硫化水素などの生成ガスは
燃料等に使用できる有用な資源でもあり、これを積極的
に回収することもできる。例えば、不通気性シート2下
にガス回収用のパイプの吸入口を臨ませてタンクなどの
容器に回収できるようにすれば良い。
Under the sheet 2, gas emitting odors such as methane and hydrogen sulfide generated by the activity of anaerobic bacteria accumulates, and the sheet in that portion expands as the volume of the gas expands, and the surrounding area eventually becomes large. Is released into the atmosphere through the gap. Note that generated gas such as methane and hydrogen sulfide is a useful resource that can be used as fuel and the like, and can be actively collected. For example, the suction port of the gas recovery pipe may be exposed under the impermeable sheet 2 so that the gas can be recovered in a container such as a tank.

【0021】前記嫌気槽については、地面を掘って作る
溜池方式と、地下に埋設する水槽方式などがあるが、溜
池方式ではその上にシートを被せれば良く、図3に示す
ように、雨水の浸入を防ぐためにさらにシート屋根3な
どを設けて溜池上を覆えるようにすると良い。また水槽
方式では、タンク内に袋状のシートを内蔵させ、水量の
変化に合わせてその袋を膨張と収縮させる方法などが可
能である。
The anaerobic tank is classified into a basin type in which the ground is dug and a tank type in which it is buried underground. In the basin type, a sheet may be placed thereon, and as shown in FIG. It is preferable to provide a sheet roof 3 or the like so as to cover the reservoir. In the water tank system, a method in which a bag-like sheet is incorporated in the tank and the bag is expanded and contracted in accordance with a change in the amount of water is possible.

【0022】[0022]

【実験例1】A養豚場の既存の屋外処理施設で実験を行
った。このA養豚場は約1000頭の豚を飼育してお
り、図3に示されているように、直径7m深さ3mの底
面と側面に防水処理を施した8個の池(1000m3×
8=8000m3)と5つの曝気層4(合計70m3)と
から成る設備があった。この養豚場では平均4.5m3
/日程度の糞尿が発生する。先ず、その既存の施設にお
いて流入する糞尿を検査したら下記のようであった。
[Experimental Example 1] An experiment was conducted in an existing outdoor treatment facility at a pig farm. This pig farm breeds about 1000 pigs, and as shown in FIG. 3, 8 ponds (1000 m 3 ×
8 = 8000 m 3 ) and five aeration layers 4 (70 m 3 in total). This pig farm averages 4.5m 3
Manure per day. First, it was as follows when the manure flowing into the existing facility was examined.

【0023】<流入糞尿> BOD 21500mg/l CODMn 7780mg/l SS 2350mg/l<Inflowing manure> BOD 21500 mg / l CODMn 7780 mg / l SS 2350 mg / l

【0024】そして、最後の8番目の池から曝気層4に
流れ込む汚水の検査結果は次のようであった。
The inspection results of sewage flowing into the aeration layer 4 from the last eighth pond were as follows.

【0025】<曝気層へ流入汚水> BOD 6800mg/l CODMn 3900mg/l SS 340mg/l<Sewage flowing into the aeration layer> BOD 6800 mg / l CODMn 3900 mg / l SS 340 mg / l

【0026】次に、その施設において、8個の池全部に
ビニールシート2を覆って実験した。そして、その結
果、そのビニールシート2の下にはこれまでの嫌気槽1
につきものカスムが全く発生していなかった。また、シ
ートで覆った結果、外観の見苦しさが解消され、特に悪
臭が解消された。従来この設備では約6ヶ月間かかっ
て、BODを約7300ppmまで処理していたが、本
実験では約2ヶ月間で同程度のBOD値まで処理するこ
とができた。つまり時間的に今までより1/3の短時間
の処理が可能となり、このことは即ち、処理槽の容積は
1/3の大きさで処理可能であることを意味している。
Next, at that facility, an experiment was conducted in which all eight ponds were covered with a vinyl sheet 2. And as a result, the anaerobic tank 1 so far under the vinyl sheet 2
There was no dregs at all. In addition, as a result of covering with the sheet, unsightly appearance was eliminated, and particularly, offensive odor was eliminated. Conventionally, it took about 6 months to process BOD to about 7300 ppm in this facility, but in this experiment, it was possible to process to about the same BOD value in about 2 months. In other words, the processing can be performed in a shorter time of 1/3 than before, which means that the processing tank can be processed with a volume of 1/3.

【0027】そしてさらに、最終曝気層4にできる上澄
液を返送パイプ5で8個の池に投入したら、約1ヶ月間
で従来の場合と同程度のBOD値まで処理することがで
きた。このことは、時間的に今までより1/6の短時間
の処理が可能となり、このことは即ち、処理槽の容積を
1/6の大きさに大幅に縮小することが可能であること
を表している。
Further, when the supernatant liquid formed in the final aeration layer 4 was put into eight ponds by the return pipe 5, it was possible to treat the BOD value to about the same level as the conventional case in about one month. This means that processing can be performed in a shorter time of 1/6 than before, which means that the volume of the processing tank can be greatly reduced to 1/6. Represents.

【0028】さらに、汚水中に液体、粉体又はペレット
状の微生物活性栄養物などの微生物活性材を投入した
ら、上記上澄液を入れた場合と同様に、汚泥分の分解が
促進され、大きな処理効果が得られた。これに用いる微
生物活性材は、ゼロワン(株式会社プリオの商標名)、
ゼロツウ(株式会社プリオの商標名)などがあり、また
現在では有機物、無機物などの配合物が各種提供されて
おり、それら市販のものを使用することができる。
Further, when a microbial activator such as a liquid, powder or pellet-form microbial active nutrient is put into the wastewater, the decomposition of the sludge is promoted as in the case of the above-mentioned supernatant, and the large amount of the sludge is promoted. A processing effect was obtained. The microbial active materials used for this are Zero One (trade name of Prio Co., Ltd.),
Zeroto (trade name of Prio Co., Ltd.), etc., and at present, various compounds such as organic substances and inorganic substances are provided, and commercially available ones can be used.

【0029】[0029]

【実験例2】Bレストランの既存の地下処理施設で実験
を行った。このBレストランは約100人用の地下貯留
施設がある。そして、この槽内の汚水のBOD濃度は約
500ppm程度であった。ここでは、汚水が満杯にな
る前に定期的(1ヶ月に1回)に汲み出す方式を採って
いる。非常に悪臭がひどく、汚物の減量化が進まず、そ
の沈殿汚泥を汲み取るのに年間約100万円の費用がか
かっていた。
[Experimental Example 2] An experiment was conducted at an existing underground treatment facility at Restaurant B. This B restaurant has an underground storage facility for about 100 people. And the BOD concentration of the sewage in this tank was about 500 ppm. Here, a method is adopted in which sewage is pumped out regularly (once a month) before it becomes full. The odor was very bad, the amount of waste was not reduced, and it took about one million yen a year to pump the sludge.

【0030】その施設において、図1に示すように、水
面全面にビニールシート2を覆い、移送管には空気の侵
入を防ぐためキャップ6を被せて実験した。その結果、
そのビニールシート2の下にはこれまでの嫌気槽1につ
きものカスムが全く発生せず、悪臭も解消された。そし
て、そのビニールシート2を被せたまま1ヶ月後に検査
すると、汚泥分が分解されてBOD濃度がビニールシー
ト2を被う前は500ppm程度あったのが約300p
pm程度に低下していた。また、槽内の沈殿汚泥の量も
減少していた。
At the facility, as shown in FIG. 1, an experiment was conducted by covering the entire surface of the water with a vinyl sheet 2 and covering the transfer pipe with a cap 6 to prevent air from entering. as a result,
Under the vinyl sheet 2, no humming of the conventional anaerobic tank 1 occurred, and the odor was eliminated. When the inspection is performed one month later with the vinyl sheet 2 covered, the sludge is decomposed and the BOD concentration is about 500 ppm before the vinyl sheet 2 is covered.
pm. The amount of settled sludge in the tank also decreased.

【0031】[0031]

【発明の効果】本発明は以上のようであり、上記実験結
果にも示されるように、嫌気槽1の水面から酸素が侵入
するのを遮断する不通気性シート2で被覆することによ
って、そのシート下の酸素の供給が絶たれ、嫌気槽1内
の汚水上層部分での嫌気性微生物の増殖と汚泥分を分解
とが促進され、汚泥分の処理効率を大幅に向上させるこ
とができるようになった。
The present invention is as described above. As shown in the above experimental results, the anaerobic tank 1 is covered with an air-impermeable sheet 2 for blocking oxygen from entering from the water surface. The supply of oxygen under the sheet is cut off, the growth of anaerobic microorganisms in the upper part of the sewage in the anaerobic tank 1 and the decomposition of sludge are promoted, and the treatment efficiency of sludge can be greatly improved. became.

【0032】そして、嫌気槽1内水面に対して空気接触
がなくなったために、これまでの嫌気槽につきもののカ
スムは全く発生できなくなり、また悪臭の解消が可能に
なった。
Since there was no air contact with the water surface in the anaerobic tank 1, no fogging, which had been associated with the conventional anaerobic tank, could be generated, and the odor could be eliminated.

【0033】また、効率良く処理されるために、これま
で行われていたような濃度を薄めるための取水は不要と
なり、さらに設備稼動にかかる電気代などの節約もでき
るようになった。さらに、沈殿分離される余剰汚泥の量
も大幅に減量化され、且つ凝集剤などの添加がないの
で、その余剰汚泥の堆肥化も積極的に推進でき、排出物
の最終処理の負担も大幅に改善することができるように
なった。
In addition, since the water is efficiently treated, the water intake for reducing the concentration, which has been performed so far, is not required, and the electricity cost for operating the equipment can be saved. In addition, the amount of excess sludge settled and separated is greatly reduced, and there is no addition of a coagulant. Therefore, composting of the excess sludge can be actively promoted, and the burden of final treatment of discharged materials is greatly increased. Can be improved.

【0034】また、マンションなどの住居での屎尿処理
では、これまでは1年に数回汲み取りしなければならな
かったが、本発明では沈殿汚泥の量も大幅に減量化され
るので、汲み取り回数が数年に1回となり維持費が大幅
に削減できるようになった。さらに、畜産業者の経営に
とっては、糞尿処理に伴うコストの大幅な削減が可能と
なり、畜産業者の経営改善に益すること大きいものがあ
る。
[0034] In the case of human waste treatment in dwellings such as condominiums, so far it has been necessary to pump several times a year, but in the present invention, the amount of settled sludge is greatly reduced. Once every few years, maintenance costs can be greatly reduced. Furthermore, for the management of the livestock industry, there is a significant advantage that the cost associated with the treatment of manure can be significantly reduced and the management of the livestock industry can be improved.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の模式的な(イ)が平面図、(ロ)が縦
断側面図。
FIG. 1 is a schematic plan view of the present invention, and FIG.

【図2】従来の方法の模式的な(イ)が平面図、(ロ)
が縦断側面図。
FIG. 2 is a plan view schematically showing a conventional method (A) and (B).
Is a longitudinal side view.

【図3】実験施設の模式的な(イ)が平面図、(ロ)が
縦断側面図。
FIGS. 3A and 3B are schematic plan views of the experimental facility, and FIGS.

【符号の説明】[Explanation of symbols]

1 嫌気槽 2 不通気性シート 3 屋根 4 曝気槽 5 返送パイプ 6 キャップ F 内の汚水部分 S 内上の空間部分 DESCRIPTION OF SYMBOLS 1 Anaerobic tank 2 Impermeable sheet 3 Roof 4 Aeration tank 5 Return pipe 6 Cap F Waste water part in S S Space part in S

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 汚水を入れた嫌気槽の水面を不通気性シ
ートで被覆してシート下の上層水域を嫌気状態に保持す
ることで、槽内汚水全体を嫌気性微生物の適環境に整え
て嫌気性微生物による汚泥分の分解を高効率に処理する
とともに、そのシート下に発生する微生物による汚泥分
解ガスを大気中に放出するか又は回収することを特徴と
するシートによる嫌気槽水面被覆汚水処理法。
1. An anaerobic tank filled with sewage is covered with an impermeable sheet to maintain an upper anaerobic area under the sheet in an anaerobic state, so that the entire sewage in the tank is adjusted to an appropriate environment for anaerobic microorganisms. An anaerobic tank water-surface-covered sewage treatment using sheets, which efficiently treats decomposition of sludge by anaerobic microorganisms and releases or collects sludge decomposition gas generated by microorganisms under the sheet into the atmosphere. Law.
【請求項2】 嫌気槽の汚水中に微生物活性材を投入し
汚泥分の分解を促進させることを特徴とする請求項1記
載のシートによる嫌気槽水面被覆汚水処理法。
2. The anaerobic tank water surface covering sewage treatment method according to claim 1, wherein a microbial activator is introduced into the anaerobic tank sewage to promote the decomposition of sludge.
【請求項3】 微生物活性材が、曝気槽で得られた上澄
液である請求項2記載のシートによる嫌気槽水面被覆汚
水処理法。
3. The method according to claim 2, wherein the microbial activator is a supernatant obtained in an aeration tank.
JP2000312815A 2000-10-13 2000-10-13 Sewage treatment method by covering surface of water of anaerobic tank with sheet Pending JP2002119992A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000312815A JP2002119992A (en) 2000-10-13 2000-10-13 Sewage treatment method by covering surface of water of anaerobic tank with sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000312815A JP2002119992A (en) 2000-10-13 2000-10-13 Sewage treatment method by covering surface of water of anaerobic tank with sheet

Publications (1)

Publication Number Publication Date
JP2002119992A true JP2002119992A (en) 2002-04-23

Family

ID=18792331

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000312815A Pending JP2002119992A (en) 2000-10-13 2000-10-13 Sewage treatment method by covering surface of water of anaerobic tank with sheet

Country Status (1)

Country Link
JP (1) JP2002119992A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008105017A (en) * 2006-09-29 2008-05-08 Dowa Holdings Co Ltd Method and apparatus for purifying water to be treated
JP2011000386A (en) * 2009-06-22 2011-01-06 Yoshinori Moronaga Bio-toilet
KR200484654Y1 (en) * 2017-07-12 2017-11-06 주식회사 정원플랜트 High efficiency precipitation tank

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008105017A (en) * 2006-09-29 2008-05-08 Dowa Holdings Co Ltd Method and apparatus for purifying water to be treated
JP2011000386A (en) * 2009-06-22 2011-01-06 Yoshinori Moronaga Bio-toilet
KR200484654Y1 (en) * 2017-07-12 2017-11-06 주식회사 정원플랜트 High efficiency precipitation tank

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