JP2006088028A - Anaerobic biofiltration septic tank, sewage treatment system, and sewage treatment method - Google Patents

Anaerobic biofiltration septic tank, sewage treatment system, and sewage treatment method Download PDF

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JP2006088028A
JP2006088028A JP2004276216A JP2004276216A JP2006088028A JP 2006088028 A JP2006088028 A JP 2006088028A JP 2004276216 A JP2004276216 A JP 2004276216A JP 2004276216 A JP2004276216 A JP 2004276216A JP 2006088028 A JP2006088028 A JP 2006088028A
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anaerobic
sewage
septic tank
filter medium
bacteria
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Akio Yamahata
章夫 山端
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Yamaha Corp
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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

Abstract

<P>PROBLEM TO BE SOLVED: To effectively treat organic waste water by providing an anaerobic biofiltration septic tank which can increase the efficiency of anaerobic treatment, and obtain water quality sufficient to recycle the treated water. <P>SOLUTION: Sewage is made to flow into an aerobic regulating reservoir 10, and retained therein for 10-20 days to insolubilize/decompose organic matter. Black soil is spread all over the bottom of the regulating reservoir 10, and filter medium are circularly disposed on the central part. By feeding effective microorganisms (EM), the EM are fixed on the filter medium. The treated water of the regulating reservoir 10 is made to flow into the anaerobic biofiltration septic tank 12. The anaerobic biofiltration septic tank 12 is covered with a sheet, and its inside is kept in an anaerobic condition. The inside of the anaerobic biofiltration septic tank 12 is divided into many chambers, and each chamber is filled with the filter medium. The sewage flows vertically and horizontally in each chamber, and is brought into contact with the filter medium to be treated. The EM are also added to the anaerobic biofiltration septic tank 12 to be fixed on the filter medium. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、汚水を嫌気性微生物を利用して生物ろ過処理し、清澄な処理水を得る嫌気性生物ろ過浄化槽およびこれを用いた汚水処理システムに関する。   TECHNICAL FIELD The present invention relates to an anaerobic biological filtration septic tank in which sewage is subjected to biological filtration using anaerobic microorganisms to obtain clear treated water, and a sewage treatment system using the same.

従来より、家庭廃水や、畜産廃水など、各種の有機性廃水(汚水)処理に、微生物を利用する生物処理装置が利用されている。   2. Description of the Related Art Conventionally, biological treatment apparatuses using microorganisms have been used for various organic wastewater (sewage) treatment such as domestic wastewater and livestock wastewater.

例えば、家庭用の廃水処理装置としては、好気性生物を利用した浄化槽が広く利用されており、浮遊微生物を利用する活性汚泥法やろ材に付着した微生物を利用する浸漬ろ床法などが採用されている。一方、畜産廃水などの高濃度の有機性廃水(汚水)処理には、活性汚泥法が広く採用されている。   For example, septic tanks using aerobic organisms are widely used as household wastewater treatment equipment, and the activated sludge method using suspended microorganisms and the submerged filter bed method using microorganisms adhering to filter media are adopted. ing. On the other hand, the activated sludge method is widely used for the treatment of high-concentration organic wastewater (sewage) such as livestock wastewater.

しかし、これら好気性処理は、処理槽における好気性微生物の活性を維持するために、処理槽に酸素を供給する必要があり、ブロアなどからの空気を処理槽内に送り処理槽内を曝気する必要がある。そこで、送風のための電力を消費し、また汚泥の引抜きと処理コストが高くなるという問題がある。   However, in these aerobic treatments, in order to maintain the activity of the aerobic microorganisms in the treatment tank, it is necessary to supply oxygen to the treatment tank, and air from the blower or the like is sent into the treatment tank and aerated in the treatment tank. There is a need. Therefore, there is a problem that power for blowing air is consumed, and sludge extraction and processing costs increase.

これに対し、微生物を利用する処理として、嫌気性処理があり、これによれば汚水をそのままの状態においておくことで、処理が可能であり、エネルギーを必要としない。しかし、この嫌気性処理は、処理効率が悪く、処理時間が長く、かつ処理水の処理水質が比較的悪いという問題がある。   On the other hand, there is an anaerobic treatment as a treatment using microorganisms. According to this, the treatment can be performed by leaving the sewage as it is, and no energy is required. However, this anaerobic treatment has problems that treatment efficiency is poor, treatment time is long, and treated water quality is relatively poor.

なお、接触材を使用する嫌気性処理については、特許文献1などに記載がある。   In addition, there exists description in patent document 1 etc. about the anaerobic process which uses a contact material.

特開2002−45885号公報JP 2002-45885 A

本発明は、嫌気性処理の処理効率を上昇するとともに、処理水をリサイクルするのに十分な水質にできる嫌気性生物ろ過浄化槽を提供する。   The present invention provides an anaerobic biofiltration septic tank capable of increasing the treatment efficiency of anaerobic treatment and making the water quality sufficient to recycle treated water.

本発明は、汚水を受け入れ、嫌気性細菌を担持したろ材を利用して生物処理を行う嫌気性生物ろ過浄化槽であって、仕切り壁によって仕切られた複数の細長い処理室が形成された処理槽を有し、各処理室には、一端側上部と、他端側下部に流通口が設けられ、一方の流通口から流入した汚水が他方の流通口から流出し、これによって、複数の処理室内に汚水が順次流通し、各処理室には、周囲壁から離隔して、上端まで水没し、嫌気性微生物を担持する多孔質のろ材が浸漬配置されており、汚水が前記ろ材と接触しながら、各処理室内を流通することで、汚水を嫌気性生物処理することを特徴とする。   The present invention is an anaerobic biological filtration and purification tank that accepts sewage and performs biological treatment using a filter medium carrying anaerobic bacteria, wherein the treatment tank is formed with a plurality of elongated treatment chambers partitioned by a partition wall. Each processing chamber has a circulation port at one upper end and a lower end at the other end, and the sewage flowing from one circulation port flows out from the other circulation port, and thereby into a plurality of processing chambers. Sewage flows in sequence, each processing chamber is separated from the surrounding wall, submerged to the upper end, a porous filter medium carrying anaerobic microorganisms is immersed, and while the sewage is in contact with the filter medium, It is characterized by anaerobic biological treatment of sewage by circulating in each treatment chamber.

また、前記ろ材は、多孔質の石塊と、スポンジ状材の両方を含むことが好適である。   The filter medium preferably includes both a porous stone block and a sponge-like material.

また、前記一端側上部に設けられた流通口は、越流せきとして機能することが好適である。   Moreover, it is preferable that the circulation port provided in the upper part on the one end side functions as an overflow cough.

また、前記嫌気性微生物として、EM菌が利用されることが好適である。   Moreover, it is preferable that EM bacteria are used as the anaerobic microorganism.

また、本発明は、上記嫌気性生物ろ過浄化槽を用いた汚水処理システムであって、前記嫌気性生物ろ過浄化槽の前段に汚水を一端貯留する調整池を設け、この調整池に所定期間滞留させた汚水を前記嫌気性生物ろ過浄化槽に流入させることを特徴とする。   Further, the present invention is a sewage treatment system using the anaerobic biological filtration septic tank, wherein an adjustment pond for storing sewage at one end is provided in the previous stage of the anaerobic biological filtration septic tank, and the sewage is retained in the adjustment pond for a predetermined period of time. It is characterized by flowing sewage into the anaerobic biological filtration septic tank.

また、前記調整池は、土中に穴を掘り、汚水が地中に浸透しない構造に形成されることが好適である。   The adjustment pond is preferably formed in a structure in which a hole is dug in the soil and sewage does not penetrate into the ground.

また、前記調整池の底部には、所定量の土壌を敷き詰めることが好適である。   Moreover, it is preferable to spread a predetermined amount of soil on the bottom of the adjustment pond.

また、前記調整池には、細菌を担持するろ材が浸漬配置されていることが好適である。   Further, it is preferable that a filter medium carrying bacteria is immersed in the adjustment pond.

また、本発明は、汚水を受け入れ、嫌気性細菌を担持したろ材を利用して生物処理を行う汚水処理方法であって、汚水処理の開始に際し、EM菌を前記ろ材に予め担持させ、その後、EM菌を添加しつつ汚水を流入し、前記ろ材に担持されたEM菌を利用して汚水の嫌気処理を行うことを特徴とする。   Further, the present invention is a sewage treatment method for accepting sewage and performing biological treatment using a filter medium supporting anaerobic bacteria, and at the start of sewage treatment, EM bacteria are previously supported on the filter medium, The waste water flows in while adding EM bacteria, and the EM bacteria carried on the filter medium are used to perform anaerobic treatment of the sewage.

このように、処理室内に汚水を流し流れ、汚水とろ材の接触が図られる。そこで、ろ材に担持された嫌気性微生物によって汚水中の有機物が効果的に処理される。さらに、処理室は、汚水が上部から流入した場合には下部から流出し、また下部から流入した場合には、上部から流出するように構成されている。そこで、汚水とろ材との接触が効率的に行われ、効果的な処理を行うことができる。   In this way, sewage flows and flows through the processing chamber, and contact between the sewage and the filter medium is achieved. Therefore, the organic matter in the sewage is effectively treated by the anaerobic microorganisms supported on the filter medium. Furthermore, the processing chamber is configured to flow out from the lower part when sewage flows from the upper part, and to flow out from the upper part when flowing from the lower part. Therefore, the contact between the sewage and the filter medium is efficiently performed, and an effective treatment can be performed.

また、予めろ材にEM菌を担持させてから汚水処理を行うことで、当初より、効果的な処理を行うことができる。   Moreover, effective treatment can be performed from the beginning by carrying out sewage treatment after carrying EM bacteria on the filter medium in advance.

以下、本発明の実施形態について、図面に基づいて説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は、処理システム全体の概略構成図である。畜産廃水などの有機性汚水(原水)は、まず調整池10に導入され、ここに所定期間、例えば10〜20日程度滞留される。調整池10内において、滞留調整された調整水は、ポンプPによって、嫌気多層生物ろ過浄化槽12に導入され、ここで嫌気性微生物によって、有機物が分解処理される。嫌気性生物ろ過浄化槽12の処理水は、ポンプPによって、貯水池14に導入され、ここに貯留される。そして、貯水池14内の処理水は、適宜散水、洗浄水などにリサイクルされる。   FIG. 1 is a schematic configuration diagram of the entire processing system. Organic sewage (raw water) such as livestock wastewater is first introduced into the regulating pond 10 and retained therein for a predetermined period, for example, about 10 to 20 days. In the adjustment pond 10, the adjusted adjustment water is introduced into the anaerobic multilayer biological filtration clarification tank 12 by the pump P, where organic substances are decomposed by the anaerobic microorganisms. The treated water in the anaerobic biological filtration septic tank 12 is introduced into the reservoir 14 by the pump P and stored therein. Then, the treated water in the reservoir 14 is appropriately recycled to sprinkling water, washing water and the like.

調整池10は、図2に示すような構成を有しており、地中に掘った窪みに遮水シートを配設し、防水して形成されている。また、この調整池10は、屋外にそのまま(雨ざらしの状態で)設置され、内部は好気的状態が維持される。   The adjustment pond 10 has a configuration as shown in FIG. 2 and is formed to be waterproof by disposing a water shielding sheet in a recess dug in the ground. Further, the adjustment pond 10 is installed outdoors (in a rainy condition), and the inside is maintained in an aerobic state.

この調整池10は、深さ2m前後であり、その底部には、黒土が厚さ50cm程度収容されている。この黒土には、土壌菌が含まれており、この土壌菌が後述するEM菌と相乗的に働き、汚水中の有機物の可溶化分解を促進する。   The adjustment pond 10 has a depth of about 2 m, and black soil is accommodated in a thickness of about 50 cm at the bottom thereof. This black soil contains soil fungi, and this soil fungus works synergistically with EM fungi described later to promote solubilization and decomposition of organic matter in the wastewater.

また、この黒土の上には、ろ材20が円環状(例えば、半径2.5m程度)に配置されている。また、調整池10は、長さ5m、幅15m、深さ2.3m程度とする。   Further, the filter medium 20 is arranged in an annular shape (for example, a radius of about 2.5 m) on the black soil. In addition, the adjustment pond 10 has a length of 5 m, a width of 15 m, and a depth of about 2.3 m.

ここで、ろ材20について、図3(A)の平面図、図3(B)の正面図に基づいて説明する。このように、ろ材20は、多数のユニットからなっており、1つのユニットは、多数の軽石が充填された中央部分20aとそれの両側に配置されたポリウレタンが充填された周辺部20bからなっている。そして、これらがプラスチックコンテナ20cに収容されている。プラスチックコンテナ20cは、上部が開放で、底部にはプラスチックの底がある。また、周辺部は、メッシュになっており、汚水が内部の軽石、ポリウレタンなどと接触する。また、軽石は、プラスチック製の網材などで包んでおくことが好適である。また、ろ材20には、浮遊しないように重しを入れておく。   Here, the filter medium 20 will be described based on the plan view of FIG. 3A and the front view of FIG. Thus, the filter medium 20 is composed of a large number of units, and one unit is composed of a central portion 20a filled with a large number of pumice stones and a peripheral portion 20b filled with polyurethane disposed on both sides thereof. Yes. And these are accommodated in the plastic container 20c. The plastic container 20c is open at the top and has a plastic bottom at the bottom. In addition, the peripheral part is a mesh, and the sewage comes into contact with the internal pumice, polyurethane, and the like. Moreover, it is preferable that the pumice be wrapped with a plastic netting material. Further, a weight is put on the filter medium 20 so as not to float.

1つのユニットは、その外形として、長さ650mm×幅340mm×高さ270mm程度の大きさであり、両側のポリウレタンの各充填部、真ん中の軽石充填部の長さは、各々200mm程度になっている。また、軽石は、その径が40mm程度のものが好適である。   One unit has a size of about 650 mm long × 340 mm wide × 270 mm high as its outer shape, and the lengths of the polyurethane filling portions on both sides and the pumice filling portion in the middle are about 200 mm each. Yes. In addition, the pumice preferably has a diameter of about 40 mm.

さらに、調整池10には、スプリンクラーSが設けられており、調整池10内の汚水(調整水)表面に処理水などを散水することで、調整池10の表面に浮遊するスカムなどの浮遊固形物を沈殿させる。   Further, the adjustment pond 10 is provided with a sprinkler S, and floating water such as scum floating on the surface of the adjustment pond 10 by spraying treated water or the like on the surface of the sewage (adjustment water) in the adjustment pond 10. Precipitates.

また、ろ材20には、EM菌が定着しやすいものを採用することが好適である。ここで、EM菌とは、自然環境に有用な微生物群のことを言い、Effective(有用)とMicroorganisms(微生物)の頭文字をとった略称である。EM菌は様々な微生物からなり、大別すると光合成細菌群、乳酸菌群、酵母群、放線菌群、糸状菌群等がある。それぞれの菌には特性があり、水質汚染による強い酸化状態を防ぐ菌や他の有用微生物が増殖するための栄養を作り出す菌、有害なメタンガスや硫化水素等を基質として、糖やアミノ酸を生成する菌、乳酸を生成することにより有害な微生物の腐敗分解を抑制する菌等が複合培養されおり、有用な微生物が単独で働くよりも極めて大きな効果を有する。   Moreover, it is suitable to employ | adopt the filter medium 20 as what a EM microbe tends to fix. Here, EM fungus refers to a group of microorganisms that are useful in the natural environment, and is an abbreviation that stands for Effective (useful) and Microorganisms (microorganisms). EM bacteria are composed of various microorganisms, and roughly classified into groups of photosynthetic bacteria, lactic acid bacteria, yeast, actinomycetes, and filamentous fungi. Each bacterium has its own characteristics, and it produces sugars and amino acids using bacteria that prevent the strong oxidative state due to water pollution and other nutrients that produce useful microorganisms for growth and harmful methane gas and hydrogen sulfide as substrates. Bacteria and bacteria that suppress the spoilage decomposition of harmful microorganisms by producing lactic acid are complex-cultured, and have a much greater effect than useful microorganisms work alone.

このEM菌は、処理の各段階で適量注入することが好適である。なお、注入量が多すぎると、処理水BOD値が高くなる。   It is preferable to inject an appropriate amount of this EM fungus at each stage of the treatment. In addition, when there is too much injection amount, the treated water BOD value will become high.

調整池10においては、汚水量に対し、0.03%程度のEM菌を注入することが好適であり、これによってろ材20にEM菌が担持される。そして、上述した黒土中の土壌菌と、EM菌の相乗効果によって、有機物の好気的な可溶化、分解が進む。なお、調整池10において、土壌菌を利用せず、EM菌のみを利用すると、分解に時間がかかり、滞留時間を長くしなければ、十分な処理が行えない。   In the adjustment pond 10, it is preferable to inject about 0.03% of EM bacteria with respect to the amount of sewage, whereby the EM bacteria are supported on the filter medium 20. And the aerobic solubilization and decomposition | disassembly of organic substance progress by the synergistic effect of the soil microbe in the black soil mentioned above, and EM microbe. In addition, in the adjustment pond 10, when soil bacteria are not used but only EM bacteria are used, decomposition takes time, and sufficient treatment cannot be performed unless the residence time is increased.

このようにして、調整池10において、好気性処理が行われ、有機物が分解される。処理を行う場合には、土中に流入予定量より大きめの穴を掘り、遮水シートを敷く。そして、この調整池10の底に流入汚水予定量の約20%に当たる黒土を敷き詰める。   In this manner, the aerobic treatment is performed in the adjustment pond 10 to decompose the organic matter. When processing, dig a hole larger than the expected inflow volume in the soil and lay a water-impervious sheet. Then, black soil corresponding to about 20% of the planned amount of inflow sewage is spread over the bottom of the adjustment pond 10.

次に、黒土の上に、ろ材20を円環状に設置する。この設置は上述の通りである。このように、調整池10にろ材20を設置した後、流入汚水予定量の9%の水を入れ、EM菌を0.03%注入し、このEM菌をろ材20に定着させ、汚水を流入する。   Next, the filter medium 20 is installed in an annular shape on the black soil. This installation is as described above. Thus, after the filter medium 20 is installed in the adjustment pond 10, 9% of the expected amount of inflow sewage is added, 0.03% of EM bacteria is injected, the EM bacteria are fixed on the filter medium 20, and the sewage flows in. To do.

そして、10〜20日程度停留させておくことによって、土壌菌と、EM菌による相乗効果により、流入汚水中の有機物が可溶化、分解される。そして、この調整池10において、臭気が弱くなった段階で、ポンプPを駆動して、調整水を嫌気性生物ろ過浄化槽12に供給する。   Then, by retaining for about 10 to 20 days, the organic matter in the influent sewage is solubilized and decomposed by the synergistic effect of the soil bacteria and the EM bacteria. In the adjustment pond 10, when the odor becomes weak, the pump P is driven to supply adjustment water to the anaerobic biological filtration septic tank 12.

次に、嫌気性生物ろ過浄化槽12は、図4に示すような構成を有している。なお、この嫌気性生物ろ過浄化槽12の上部には、暗シートを固定して上方を覆ってある。そして、槽内部は嫌気的状態に維持される。鉄筋コンクリートの槽体30の入り口側には、3つの嫌気ろ床槽32a、32b、32cが仕切り壁によって仕切り形成されている。嫌気ろ床槽32aには、調整水が上部より流入し、越流水が隣接する嫌気ろ床槽32bに流入する。この越流部には、越流部を覆って、下方に伸びるカバー34aが設けられており、嫌気ろ床槽32a内の調整水は、カバーの下方からカバー内を上昇して越流部から嫌気ろ床槽32bに流入する。従って、調整水は、嫌気ろ床槽32b上部に流入する。嫌気ろ床槽32bにも同様に越流部およびカバー34bが設けられ、嫌気ろ床槽32b内の調整水がカバー34b内部を上昇して嫌気ろ床槽32cに流入する。嫌気ろ床槽32cも同様の構成を有しており、カバー34c内を上昇した調整水は越流部から嫌気処理部40に流入する。   Next, the anaerobic biological filtration septic tank 12 has a configuration as shown in FIG. In addition, a dark sheet is fixed to the upper part of the anaerobic biological filtration purification tank 12 to cover the upper part. And the inside of a tank is maintained in an anaerobic state. Three anaerobic filter floor tanks 32a, 32b, and 32c are formed on the entrance side of the reinforced concrete tank body 30 by partition walls. The adjustment water flows into the anaerobic filter bed tank 32a from the top, and the overflow water flows into the adjacent anaerobic filter bed tank 32b. The overflow part is provided with a cover 34a that covers the overflow part and extends downward, and the adjustment water in the anaerobic filter floor tank 32a rises from the lower part of the cover to the overflow part. It flows into the anaerobic filter floor tank 32b. Therefore, the adjustment water flows into the upper part of the anaerobic filter floor tank 32b. Similarly, the overflow portion and the cover 34b are provided in the anaerobic filter bed tank 32b, and the adjustment water in the anaerobic filter bed tank 32b rises inside the cover 34b and flows into the anaerobic filter bed tank 32c. The anaerobic filter floor tank 32c has the same configuration, and the adjusted water that has risen in the cover 34c flows into the anaerobic treatment section 40 from the overflow section.

嫌気処理部40は、仕切り壁によって6つの細長い直方体形状の接触室42a〜42fに仕切られている。各接触室42a〜42fには、ろ材44a〜44fがそれぞれ収容されている。このろ材44a〜44fは、接触室42a〜42fの内部空間より所定量だけ小さい直方体形状であり、接触室42a〜42f内の底面上に上方および周囲に空間を形成して設置されている。   The anaerobic treatment unit 40 is partitioned into six elongated rectangular parallelepiped contact chambers 42a to 42f by a partition wall. In each of the contact chambers 42a to 42f, filter media 44a to 44f are accommodated, respectively. The filter media 44a to 44f have a rectangular parallelepiped shape that is smaller than the internal space of the contact chambers 42a to 42f by a predetermined amount, and are installed on the bottom surfaces in the contact chambers 42a to 42f with spaces above and around it.

そして、嫌気ろ床槽32cからの調整水は、6つの接触室42a〜42fを順番に通過する。すなわち、嫌気ろ床槽32cからの流入水は接触室42aの一端上部から流入され、接触室42aの他端底部に設けられた開口から接触室42bに流入する。接触室42aの流出水は接触室42bの底部から流入され、接触室42bの他端上部越流部から接触室42cに流入する。そして、接触室42cは、上部から流入、下部から流出、接触室42dは、底部から流入、上部から流出、接触室42eは上部から流入、下部から流出、接触室42fは、底部から流入、上部から流出となる。なお、被処理水は、接触室42a〜42f内を上下だけでなく左右にも流れ、これによってろ材44との十分な接触が行われる。   And the adjustment water from the anaerobic filter floor tank 32c passes the six contact chambers 42a-42f in order. That is, the inflow water from the anaerobic filter floor tank 32c flows from the upper end of the contact chamber 42a, and flows into the contact chamber 42b from the opening provided at the bottom of the other end of the contact chamber 42a. The outflow water of the contact chamber 42a flows from the bottom of the contact chamber 42b and flows into the contact chamber 42c from the overflow portion at the other end of the contact chamber 42b. The contact chamber 42c flows in from the top, flows out from the bottom, the contact chamber 42d flows in from the bottom, flows out from the top, the contact chamber 42e flows in from the top, flows out from the bottom, and the contact chamber 42f flows in from the bottom. Outflow. The water to be treated flows not only vertically but also horizontally in the contact chambers 42a to 42f, whereby sufficient contact with the filter medium 44 is performed.

このように、嫌気性生物ろ過浄化槽12においては、接触室42内を被処理水がろ材44に沿って流れる。これによって、被処理水は、ろ材44内部に適宜入り込み、ろ材44に担持された微生物と接触する。そこで、被処理水中の有機物は、ろ材44に担持された微生物によって、分解される。嫌気性微生物はその増殖速度が遅いが、ろ材44内に保持されることによって、接触室42内に高濃度に維持することができる。このため、各接触室42において効果的な処理を行うことができ、被処理水中の有機物を効果的に分解除去することができる。   As described above, in the anaerobic biological filtration septic tank 12, the water to be treated flows along the filter medium 44 in the contact chamber 42. Thus, the water to be treated appropriately enters the inside of the filter medium 44 and comes into contact with microorganisms carried on the filter medium 44. Therefore, the organic matter in the water to be treated is decomposed by the microorganisms supported on the filter medium 44. Anaerobic microorganisms have a slow growth rate, but can be maintained in the contact chamber 42 at a high concentration by being held in the filter medium 44. For this reason, an effective process can be performed in each contact chamber 42, and organic substances in the water to be treated can be effectively decomposed and removed.

なお、この嫌気性生物ろ過浄化槽12のろ材44についても、上述と同様のろ材を利用することができる。なお、嫌気性生物ろ過浄化槽12におけるろ材44の方が高さが高くなっている。例えば、このろ材44は、幅650mm、長さ4.3m、高さ1.35mである。   In addition, about the filter medium 44 of this anaerobic biological filtration purification tank 12, the filter medium similar to the above can be utilized. In addition, the height of the filter medium 44 in the anaerobic biological filtration septic tank 12 is higher. For example, the filter medium 44 has a width of 650 mm, a length of 4.3 m, and a height of 1.35 m.

嫌気性生物ろ過浄化槽12は、上述のようにRC構造で製作され、各接触室42にろ材44が配置される。そして、浄化処理の開始前に各接触室42a〜42fには、満水状態にして各室容量の0.004%程度のEM菌を添加し、ろ材44にEM菌を担持させる。その後、調整池10において、10〜20日間調整した汚水を嫌気性生物ろ過浄化槽12に15〜20m3/日で流入する。このとき嫌気性生物ろ過浄化槽12への流入水に対しては、EM菌を200倍の水に混合した水溶液を、0.004%程度添加する。このようにして、3日間の運転の場合で、45〜60m3の汚水が浄化される。 The anaerobic biological filtration clarification tank 12 is manufactured with an RC structure as described above, and a filter medium 44 is disposed in each contact chamber 42. Then, before the start of the purification treatment, the contact chambers 42 a to 42 f are filled with EM bacteria of about 0.004% of the volume of each chamber, and the filter medium 44 carries the EM bacteria. Then, in the adjustment pond 10, the sewage adjusted for 10 to 20 days flows into the anaerobic biological filtration septic tank 12 at 15 to 20 m 3 / day. At this time, about 0.004% of the aqueous solution which mixed EM bacteria with 200 times the water is added with respect to the inflow water to the anaerobic biological filtration purification tank 12. In this way, 45 to 60 m 3 of sewage is purified in the case of operation for 3 days.

そして、接触室42fの流出水は、処理水槽50を通過した後、木炭収容室52を通過し、さらに調整室54から処理水として流出する。 また、木炭は、径φ=4〜8cm、長さ10cm〜20cm程度のものが採用され、また木炭収容室52には上部から流入し、下部から流出するようになっている。   The effluent water from the contact chamber 42f passes through the treated water tank 50, then passes through the charcoal storage chamber 52, and further flows out from the adjustment chamber 54 as treated water. Further, charcoal having a diameter of φ = 4 to 8 cm and a length of about 10 cm to 20 cm is adopted, and flows into the charcoal storage chamber 52 from the upper part and flows out from the lower part.

また、2回目移行の処理についても、適当量のEM菌を添加して処理を行う。まず、調整池10に汚水流入後、汚水量の0.03%のEM菌を添加し、流入調整水に対しては、EM菌を200倍の水に混合した水溶液を0.004%程度添加する。さらに、嫌気性生物ろ過浄化槽12には、各室容量の0.004%程度のEM菌を添加する。このように、EM菌を所定量添加することで、好適な処理を継続することができる。   Moreover, also about the process of 2nd transfer, an appropriate amount EM microbe is added and processed. First, after the sewage flows into the adjustment pond 10, 0.03% of EM bacteria of the amount of sewage is added, and about 0.004% of an aqueous solution obtained by mixing EM bacteria with 200 times the water is added to the inflow adjustment water. To do. Furthermore, about 0.004% of EM bacteria of each chamber capacity are added to the anaerobic biological filtration septic tank 12. Thus, a suitable process can be continued by adding a predetermined amount of EM bacteria.

さらに、汚水を定常的に受け入れる場合は、調整池10の容量を流入汚水の10〜20日分の容量とし、この調整池10で調整して処理を行う。この場合のEM菌の添加量も上述の回分式の場合と同等とする。   Furthermore, when receiving sewage regularly, the capacity | capacitance of the adjustment pond 10 is made into the capacity | capacitance for 10 to 20 days of inflow sewage, and it adjusts in this adjustment pond 10 and processes. In this case, the amount of EM bacteria added is also the same as in the batch type described above.

また、図4には、図示を省略したが、図1に示すように、処理水槽50には、ポンプPが設けられており、嫌気処理部40内の水の一部を調整池10または嫌気ろ床槽32aに返送できるようになっている。例えば、処理水槽50の処理水を流入水がない時に循環水として、調整池10に汚泥を返送する。また、処理水のBOD値をさらに低くする必要がある場合には、嫌気ろ床槽32に処理水を返送して再処理する。   Although not shown in FIG. 4, as shown in FIG. 1, the treated water tank 50 is provided with a pump P, and a part of the water in the anaerobic treatment unit 40 is supplied to the adjustment pond 10 or anaerobic. It can return to the filter bed tank 32a. For example, the treated water in the treated water tank 50 is returned to the adjustment pond 10 as circulating water when there is no inflow water. Further, when it is necessary to further lower the BOD value of the treated water, the treated water is returned to the anaerobic filter bed tank 32 and reprocessed.

嫌気性生物ろ過浄化槽12の処理水が流入貯留される貯水池14は、基本的に調整池10と同様に遮水シートによって形成されている。   The reservoir 14 into which treated water from the anaerobic biological filtration clarification tank 12 is stored is basically formed of a water shielding sheet in the same manner as the regulating pond 10.

畜産廃水について、上述の実施形態に記載した汚水処理システムを利用して、処理実験を行った。   About livestock wastewater, the treatment experiment was done using the sewage treatment system described in the above-mentioned embodiment.

原水は、BOD2,030mg/L、大腸菌140万個/cm3であった。この原水を処理し、BOD15〜30mg/L、大腸菌0個/cm3の浄化槽処理水が得られた。また、汚泥の沈殿は確認されていない。 The raw water was BOD 2,030 mg / L and 1.4 million E. coli / cm 3 . This raw water was treated to obtain septic tank treated water having a BOD of 15 to 30 mg / L and 0 E. coli / cm 3 . In addition, no sludge precipitation has been confirmed.

このように、本実施形態による汚水処理システムによれば、非常に清澄な処理水を得ることができる。   Thus, according to the sewage treatment system by this embodiment, very clear treated water can be obtained.

特に、本実施形態では、調整池10において、好気性処理を行い、その後嫌気性生物ろ過浄化槽12により嫌気性の処理を行う。一般的には、嫌気性処理を行った後、好気性処理を行っているが、これとは順序が反対である。しかし、この反対の順序で処理することによって、上述のような好適な汚水処理が行われる。   In particular, in this embodiment, an aerobic process is performed in the adjustment pond 10 and then an anaerobic process is performed by the anaerobic biological filtration septic tank 12. In general, anaerobic treatment is performed after anaerobic treatment, but the order is opposite. However, by treating in the reverse order, the above-described suitable sewage treatment is performed.

汚水処理システムの全体構成を示す図である。It is a figure which shows the whole structure of a sewage treatment system. 調整池の構成を示す図である。It is a figure which shows the structure of an adjustment pond. ろ材の構成を示す図である。It is a figure which shows the structure of a filter medium. 嫌気性生物ろ過浄化槽の構成を示す図である。It is a figure which shows the structure of an anaerobic biological filtration septic tank.

符号の説明Explanation of symbols

10 調整池、12 嫌気性生物ろ過浄化槽、14 貯水池、20 ろ材、30 槽体、 32 嫌気ろ床槽、34 カバー、40 嫌気処理部、42 接触室、44 ろ材、50 処理水槽、52 木炭収容室、54 調整室。   DESCRIPTION OF SYMBOLS 10 Adjustment pond, 12 Anaerobic biological filtration purification tank, 14 Reservoir, 20 Filter medium, 30 Tank body, 32 Anaerobic filter floor tank, 34 Cover, 40 Anaerobic treatment part, 42 Contact room, 44 Filter medium, 50 Treated water tank, 52 Charcoal storage room 54 Adjustment room.

Claims (9)

汚水を受け入れ、嫌気性細菌を担持したろ材を利用して生物処理を行う嫌気性生物ろ過浄化槽であって、
仕切り壁によって仕切られた複数の細長い処理室が形成された処理槽を有し、
各処理室には、一端側上部と、他端側下部に流通口が設けられ、一方の流通口から流入した汚水が他方の流通口から流出し、
これによって、複数の処理室内に汚水が順次流通し、
各処理室には、周囲壁から離隔して、上端まで水没し、嫌気性微生物を担持する多孔質のろ材が浸漬配置されており、
汚水が前記ろ材と接触しながら、各処理室内を流通することで、汚水を嫌気性生物処理することを特徴とする嫌気性生物ろ過浄化槽。
An anaerobic biological filtration septic tank that accepts sewage and performs biological treatment using a filter medium carrying anaerobic bacteria,
A treatment tank having a plurality of elongated treatment chambers partitioned by a partition wall;
Each treatment chamber is provided with a circulation port at one upper end and a lower end at the other end, and sewage flowing from one circulation port flows out from the other circulation port,
As a result, the sewage sequentially flows through the plurality of processing chambers,
In each processing chamber, a porous filter medium carrying anaerobic microorganisms is immersed and arranged so as to be submerged to the upper end, separated from the surrounding wall.
An anaerobic biological filtration septic tank, wherein the sewage is anaerobically treated by flowing through each processing chamber while the sewage is in contact with the filter medium.
請求項1に記載の嫌気性生物ろ過浄化槽において、
前記ろ材は、多孔質の石塊と、スポンジ状材の両方を含むことを特徴とする嫌気性生物ろ過浄化槽。
In the anaerobic biological filtration septic tank according to claim 1,
The anaerobic biological filtration septic tank, wherein the filter medium includes both a porous stone block and a sponge-like material.
請求項1または2に記載の嫌気性生物ろ過浄化槽において、
前記一端側上部に設けられた流通口は、越流せきとして機能することを特徴とする嫌気性生物ろ過浄化槽。
In the anaerobic biological filtration septic tank according to claim 1 or 2,
An anaerobic biological filtration septic tank characterized in that a circulation port provided at the upper end of the one end functions as an overflow cough.
請求項1〜3のいずれか1つに記載の嫌気性生物ろ過浄化槽において、
前記嫌気性微生物として、EM菌が利用されることを特徴とする嫌気性生物ろ過浄化槽。
In the anaerobic biological filtration septic tank according to any one of claims 1 to 3,
An anaerobic biological filtration septic tank using EM bacteria as the anaerobic microorganism.
請求項1〜4のいずれか1つに記載の嫌気性生物ろ過浄化槽を用いた汚水処理システムであって、
前記嫌気性生物ろ過浄化槽の前段に汚水を一端貯留する調整池を設け、この調整池に所定期間滞留させた汚水を前記嫌気性生物ろ過浄化槽に流入させることを特徴とする汚水処理システム。
A sewage treatment system using the anaerobic biological filtration septic tank according to any one of claims 1 to 4,
A sewage treatment system characterized in that an adjustment pond for storing sewage at one end is provided in the previous stage of the anaerobic biofiltration septic tank, and the sewage retained in the adjustment pond for a predetermined period is caused to flow into the anaerobic biofiltration septic tank.
請求項5に記載のシステムにおいて、
前記調整池は、土中に穴を掘り、汚水が地中に浸透しない構造に形成されることを特徴とする汚水処理システム。
The system of claim 5, wherein
The sewage treatment system is characterized in that the adjustment pond is formed in a structure in which a hole is dug in the soil and sewage does not penetrate into the ground.
請求項5または6に記載のシステムにおいて、
前記調整池の底部には、所定量の土壌を敷き詰めることを特徴とする汚水処理システム。
The system according to claim 5 or 6,
A sewage treatment system, wherein a predetermined amount of soil is spread on the bottom of the adjustment pond.
請求項5〜7のいずれか1つに記載のシステムにおいて、
前記調整池には、細菌を担持するろ材が浸漬配置されていることを特徴とする汚水処理システム。
In the system according to any one of claims 5 to 7,
A sewage treatment system, wherein a filter medium carrying bacteria is immersed in the adjustment pond.
汚水を受け入れ、嫌気性細菌を担持したろ材を利用して生物処理を行う汚水処理方法であって、
汚水処理の開始に際し、EM菌を前記ろ材に予め担持させ、
その後、EM菌を添加しつつ汚水を流入し、前記ろ材に担持されたEM菌を利用して汚水の嫌気処理を行うことを特徴とする汚水処理方法。
A sewage treatment method for accepting sewage and performing biological treatment using a filter medium supporting anaerobic bacteria,
At the start of sewage treatment, EM bacteria are preloaded on the filter medium,
Then, sewage is introduced while adding EM bacteria, and the sewage is anaerobically treated using the EM bacteria supported on the filter medium.
JP2004276216A 2004-09-22 2004-09-22 Anaerobic biofiltration septic tank, sewage treatment system, and sewage treatment method Pending JP2006088028A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5308570B1 (en) * 2012-10-12 2013-10-09 昭司 野口 Method for urination treatment of livestock animals
CN103449672A (en) * 2013-09-05 2013-12-18 湖北特微生物环保有限公司 Treatment method and recycling method of livestock and poultry breeding wastewater and biogas slurry
CN107651808A (en) * 2016-07-26 2018-02-02 樊志金 A kind of sewage-treatment plant based on PASG technologies
CN108609801A (en) * 2018-05-02 2018-10-02 江苏大彭环保科技有限公司 A kind for the treatment of process of aquaculture wastewater

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5308570B1 (en) * 2012-10-12 2013-10-09 昭司 野口 Method for urination treatment of livestock animals
CN103449672A (en) * 2013-09-05 2013-12-18 湖北特微生物环保有限公司 Treatment method and recycling method of livestock and poultry breeding wastewater and biogas slurry
CN107651808A (en) * 2016-07-26 2018-02-02 樊志金 A kind of sewage-treatment plant based on PASG technologies
CN108609801A (en) * 2018-05-02 2018-10-02 江苏大彭环保科技有限公司 A kind for the treatment of process of aquaculture wastewater

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