JP2005169240A - Sewage treating equipment - Google Patents

Sewage treating equipment Download PDF

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JP2005169240A
JP2005169240A JP2003412229A JP2003412229A JP2005169240A JP 2005169240 A JP2005169240 A JP 2005169240A JP 2003412229 A JP2003412229 A JP 2003412229A JP 2003412229 A JP2003412229 A JP 2003412229A JP 2005169240 A JP2005169240 A JP 2005169240A
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sludge
tank
sewage treatment
treatment facility
bacteria
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JP3854269B2 (en
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Ichiro Iiyama
一郎 飯山
Yoshikazu Kobayashi
由和 小林
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Miike Inc
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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
    • 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
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Activated Sludge Processes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide sewage treating equipment in which settled sludge produced in a settling tank of a sewage treating apparatus, particularly an activated sludge type sewage treating apparatus is treated and decomposed to form treated water and useful sludge the volume of which is reduced and the activated sludge in the activated sludge type sewage treating apparatus is activated. <P>SOLUTION: The sewage treating equipment in which the settled sludge accumulated in the settling tank of the sewage treating apparatus for decomposing organic materials in the sewage and discharging the treated water is treated comprises a collecting means for collecting the settled sludge from the settling tank, a superfine particle forming apparatus for forming the settled sludge collected by the collecting means into a sludge superfine particle, a fermentation tank for fermenting the sludge formed into the superfine particle by mixing fermentation bacteria with the sludge superfine particle and a separation tank for separating the fermented sludge superfine particle into the treated water and the fermented sludge. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、汚水処理設備に関し、特に、汚水処理装置の沈殿槽における止水部位において蓄積する沈殿汚泥を処理する汚水処理設備に関する。   The present invention relates to a sewage treatment facility, and more particularly, to a sewage treatment facility that treats precipitated sludge accumulated in a water stop portion of a settling tank of a sewage treatment apparatus.

飲食店業や食品加工工場などから排出される汚水は、多量の有機物を含むが、そのような汚水を処理するには、汚水処理装置により、排水と沈殿物に分離され、沈殿物は、汚泥の脱水ケーキを作り、再利用されるか、放棄され、処理水は、下水道や、特に、河川などに放流されている。近代的な汚水処理法には、排水中の有機物をバクテリアなどの微生物で分解して消滅を促進して、生化学的酸素要求量(BOD)と懸濁固形物(SS)が一定値以下に低下させた処理水として排出する活性汚泥式が知られている。   Sewage discharged from restaurants, food processing factories, etc. contains a large amount of organic matter, but in order to treat such wastewater, it is separated into wastewater and sediment by a wastewater treatment device. The dehydrated cake is made and reused or abandoned, and the treated water is discharged into sewers, especially rivers. In modern wastewater treatment methods, organic substances in wastewater are decomposed by microorganisms such as bacteria to promote disappearance, and biochemical oxygen demand (BOD) and suspended solids (SS) are below a certain value. An activated sludge type that is discharged as reduced treated water is known.

しかし、活性汚泥式汚水処理装置では、その分離槽ないし沈殿槽で、止水部位に汚泥が沈殿することが多く、これは別途収集されたとしても、このような有機物を含む汚泥は、再利用の際に汚泥の脱水ケーキを作ることが多かった。汚泥は、多くの微生物の細胞体が占め、細胞体は約70%前後の水分を含有しているので、脱水しても腐敗し易いものであり、結局は再利用されることなく焼却又は投棄されていた。   However, in activated sludge type sewage treatment equipment, sludge often settles at the water-stopping site in its separation tank or settling tank, and even if this is collected separately, sludge containing such organic matter is not reused. In many cases, a sludge dehydrated cake was made. Sludge is composed of many microbial cell bodies, and the cell bodies contain about 70% of water, so it is easy to rot even if dehydrated, and eventually incinerated or dumped without being reused. It had been.

汚水処理装置の沈殿槽に生じる沈殿汚泥は、供給源からの動物質や植物質の組織細胞などを多量に含み、これらと共に繁殖した微生物を含んでいる。例えば、ズーグレア等の細菌、ゾウリムシ等の繊毛虫類、ユレモやアオミドロやハネケイソウ等の藻類、ミドロムシ等の原生動物、ワムシや線虫等の後生動物等の細胞体などである。それら微生物は、水分に富んだ蛋白質、糖、脂質、アミノ酸を含む栄養価の高い細胞質や核酸を含んでいるので、沈殿物は腐敗し易い。   Sediment sludge generated in the sedimentation tank of the sewage treatment apparatus contains a large amount of moving substances, plant tissue cells, and the like from the source, and contains microorganisms propagated along with these. Examples include cell bodies such as bacteria such as zoo glare, ciliates such as Paramecium, algae such as uremo, blue-spotted moth, and diatom, protozoa such as euglena, and metazoans such as rotifer and nematode. These microorganisms contain highly nutritious cytoplasms and nucleic acids containing proteins, sugars, lipids, and amino acids rich in water, so that the precipitates are easily spoiled.

活性汚泥式の汚水処理装置の沈殿槽において生じる沈殿汚泥は短時間で腐敗が進んでウエルシュ菌等による硫化水素等の有害ガスを発生し、悪臭を放ち、新たに流入して来る活性汚泥にとって最悪の環境へと転化しつつあり、その活性を奪うことになる。   Sediment sludge generated in the sedimentation tank of activated sludge-type sewage treatment equipment is decayed in a short time, generating toxic gases such as hydrogen sulfide due to C. perfringens, etc. It is being transformed into a new environment and will take away its activity.

本発明は、汚水処理装置、特に、活性汚泥式汚水処理装置の沈殿槽において生じる沈殿汚泥を処理分解して、処理水と減容化して利用価値の高い汚泥に調製すると共に、活性汚泥式汚水処理装置の活性汚泥を活性化させる汚泥処理設備を提供するものである。   The present invention is a sewage treatment apparatus, in particular, the activated sludge sewage, which is prepared by processing and decomposing the precipitated sludge generated in the settling tank of the activated sludge sewage treatment apparatus to reduce the volume of the treated water to a highly useful sludge. The present invention provides a sludge treatment facility for activating activated sludge in a treatment apparatus.

本発明の汚水処理設備は、汚水処理装置の沈殿槽において生じる沈殿汚泥の大部分を占める微生物の細胞を粉砕して超微粒子化して、次いで、発酵菌によって発酵させ、多数の発酵菌を含んだ処理水と減容化して利用価値を高くした発酵汚泥とを造るのである。   The sewage treatment facility of the present invention pulverizes the cells of microorganisms occupying most of the precipitated sludge generated in the sedimentation tank of the sewage treatment apparatus, and then fermented with fermenting bacteria, and contained a large number of fermenting bacteria. This is to make treated water and fermented sludge whose volume is reduced to increase the utility value.

このために、本発明の沈殿汚泥の処理設備は、沈殿槽内の止水部位ないし死角部位に蓄積した沈殿汚泥を処理するために、沈殿槽の止水部位から沈殿汚泥を集める収集手段と、収集した沈殿汚泥を汚泥超微粒子に超微粒子化する超微粒子化装置と、汚泥超微粒子に発酵菌を混合して槽内で汚泥超微粒子を発酵させる発酵菌槽と、発酵した汚泥超微粒子を分離槽において処理水と発酵汚泥とに分離する分離槽と、から成るものである。   For this purpose, the sedimentation sludge treatment facility of the present invention has a collecting means for collecting the sedimentation sludge from the water stop part of the precipitation tank in order to treat the sedimentation sludge accumulated in the water stop part or blind spot part in the precipitation tank, Separates the collected sludge into ultrafine particles into ultrafine sludge, a fermenter that mixes fermented bacteria with the ultrafine sludge and ferments the ultrafine sludge in the tank, and fermented ultrafine sludge And a separation tank that separates the treated water and the fermentation sludge in the tank.

本発明の沈殿汚泥の処理設備は、汚水処理装置の沈殿槽における流れに淀みが生じ易い四隅等の止水部位に蓄積する沈殿汚泥を収集手段によって水と共に超微粒子化装置に収集して、超微粒化装置によりきわめて微細な粒子に分化し、汚泥を成す動植物や微生物の組織や細胞を微細化し拡散し且つ表面積を拡大する。発酵菌槽は、分解した有機物を槽内に混合した発酵菌により短時間で大量に分解させ、汚泥の有機物を残部無機分へと転化させ、次いで、分離槽で発酵菌に富んだ処理水と、発酵菌の増殖過程で大幅に減容化された無機汚泥とに分離する。   The sedimentation sludge treatment facility of the present invention collects sedimentation sludge that accumulates in water-stopping sites such as the four corners where the stagnation of the flow in the sedimentation tank of the sewage treatment apparatus is likely to occur together with water in the ultrafine particle device, It is differentiated into extremely fine particles by the atomization device, and the tissues and cells of animals and plants and microorganisms that form sludge are refined and diffused, and the surface area is increased. The fermenting fungus tank decomposes the decomposed organic matter in a large amount in a short time with the fermenting fungus mixed in the tank, converts the sludge organic matter into the remaining inorganic content, and then the treated water rich in fermenting fungi in the separation tank It is separated into inorganic sludge that has been greatly reduced in volume during the growth of fermenting bacteria.

さらに、本発明においては、汚水処理装置の沈殿槽から、沈殿汚泥を上記処理設備を通じて定常的に又は日定期的に除去して、汚水処理装置、特に、活性汚泥式汚水処理装置における活性汚泥の活性を維持して、汚泥の分解速度とその効率を高めることができる。   Furthermore, in the present invention, the settled sludge is removed from the settling tank of the sewage treatment apparatus regularly or regularly through the treatment facility, and the activated sludge in the sewage treatment apparatus, particularly the activated sludge type sewage treatment apparatus, is removed. The activity can be maintained, and the degradation rate and efficiency of sludge can be increased.

汚水処理装置は、例えば、飲食店厨房や食品加工所、集合住宅の等から排出され、有機物を多量に含む産業的ないし生活的な汚水ないし排水を処理するもので、汚水中の有機物を分解して、その処理水を排出可能にするものである。特に、活性汚泥式汚水処理装置が含まれ、河川等に排出できるように排水基準を満たすように処理している。このような汚水処理装置は、汚水を分解槽ないし曝気槽に導いて汚水中の動植物や細菌の組織や細胞などの有機物を、バクテリアなどの細菌その他の微生物の働きで分解して、生化学的酸素要求量と懸濁固形物量を一定基準以下に低下させた処理水として排出するものである。   Sewage treatment equipment treats industrial or domestic wastewater or wastewater containing a large amount of organic matter discharged from restaurant kitchens, food processing plants, apartment houses, etc., and decomposes organic matter in wastewater. Thus, the treated water can be discharged. In particular, an activated sludge sewage treatment device is included, and the wastewater standard is satisfied so that it can be discharged into a river or the like. Such a sewage treatment device guides sewage to a decomposition tank or an aeration tank, decomposes organic matter such as animals and plants and bacterial tissues and cells in the sewage by the action of bacteria and other microorganisms, and biochemical It is discharged as treated water in which the oxygen demand and the amount of suspended solids are reduced below a certain standard.

汚水処理装置には、処理水から、有機物を分離するための沈殿槽を含んでおり、沈殿槽中の止水域中には汚泥が沈殿し、本発明は、このような沈殿汚泥を処理するものである。ここで、沈殿槽の語は、汚水処理装置に含まれて、槽内に液流の滞留部位を生じて有機物汚泥の沈殿物を生じやすい処理槽を広く含み、曝気槽、分解槽、沈殿槽を含んでいる。   The sewage treatment apparatus includes a settling tank for separating organic substances from the treated water, and sludge is precipitated in the water stop area of the settling tank, and the present invention treats such precipitated sludge. It is. Here, the term “sedimentation tank” includes a processing tank that is included in a sewage treatment apparatus and that tends to generate a liquid flow retention site in the tank to easily cause sedimentation of organic sludge. An aeration tank, a decomposition tank, and a sedimentation tank Is included.

本発明の処理設備は、沈殿汚泥を超微粒子化装置に移送するための汚泥収集手段を含むが、収集手段の一例は、吸引装置とこの吸引装置に接続して、その吸引口が、槽内に、特に、止水部位に位置づけ可能な可撓性又は固定の配管とから成るものがある。このような配管には、フレキシブルホース又は固定パイプが利用でき、吸引装置には、これらの配管に接続したポンプがあり、ポンプは、さらに、超微粒子化装置に配管接続することができる。   The treatment facility of the present invention includes a sludge collecting means for transferring the precipitated sludge to the ultrafine particle forming apparatus. An example of the collecting means is connected to the suction apparatus and the suction apparatus, and the suction port is in the tank. In particular, there are some which consist of flexible or fixed piping which can be positioned at the water stop. A flexible hose or a fixed pipe can be used for such piping, and the suction device has a pump connected to these piping. The pump can be further connected to an ultrafine particle generator.

収集手段は、人力による場合と異なり、汚水処理装置の沈殿槽の止水部位にフレキシブルホース又はパイプの吸引口を接続しているので、設備の運転を止めずに適宜沈殿汚泥を収集して、超微粒子化装置に移送することができるようになる。   Collecting means, unlike the case by human power, because the suction port of the flexible hose or pipe is connected to the water stop part of the sedimentation tank of the sewage treatment device, collect the precipitated sludge as appropriate without stopping the operation of the equipment, It can be transferred to an ultrafine particle device.

収集された沈殿汚泥は、多量の水に動植物の細胞組織や微生物細胞など有機物を分散しているが、超微粒子化装置は、沈殿汚泥中これら有機物を細胞寸法以下の超微粒子に微粒化する。   The collected precipitated sludge disperses organic matter such as animal and plant cell tissues and microbial cells in a large amount of water, but the ultrafine particle device atomizes these organic matter into ultrafine particles having a size smaller than the cell size in the precipitated sludge.

このための超微粒子化装置には、これら細胞に対して高速水流を利用して、その剪断、破壊、分解などの作用により、動植物や微生物の組織や細胞をさらに破壊して、超微細化するものが利用可能である。   For this purpose, the ultrafine particle device uses ultra high-speed water flow to these cells to further destroy the tissues and cells of animals and plants and microorganisms by the action of shearing, destruction, decomposition, etc. Things are available.

このような超微粒子化装置には、高速水流の衝撃力、水流速度差による剪断力、又は気泡破裂即ちキャビテーションにより生じる超音波による分解、のいずれか1つ又は2つ以上の作用を利用することができる。   For such an ultrafine particle device, one or more of the impact force of high-speed water flow, shear force due to difference in water flow velocity, or ultrasonic decomposition caused by bubble rupture or cavitation should be used. Can do.

超微粒子化装置の一つの態様は、同心状に配置した内筒および外筒とこれらの間の環状流路とからなる容器中と、環状流路に沿って高速水流を形成する水噴射ノズルと、内筒壁に形成して内筒内部から沈殿汚泥水を該高速水流中にほぼ直角方向に吐出するスロットと、内筒内部と連通した汚泥供給口と、環状流路に連通する汚泥微細化粒子排出口と、から成っている。   One aspect of the ultrafine particle forming apparatus includes a container composed of an inner cylinder and an outer cylinder arranged concentrically and an annular channel between them, and a water jet nozzle that forms a high-speed water flow along the annular channel. , A slot that is formed on the inner cylinder wall and discharges the precipitated sludge water from the inside of the inner cylinder into the high-speed water flow in a substantially perpendicular direction, a sludge supply port that communicates with the inside of the inner cylinder, and sludge refinement that communicates with the annular channel It consists of a particle outlet.

環状流路内は、水噴射ノズルから噴射された水により高速水流が循環しており、内筒壁に形成したスロットからは、粉砕すべき沈殿汚泥の有機物を含むスラリとして環状流路内に吐出されるので、汚泥中有機物粒子が高速水流で剪断、破壊、分解を受けて、単一細胞の大きさ程度に、ないしそれより微細に分解することができる。   Inside the annular channel, a high-speed water stream is circulated by the water jetted from the water jet nozzle. From the slot formed in the inner cylinder wall, the slurry is discharged into the annular channel as a slurry containing organic matter of precipitated sludge to be crushed. Therefore, the organic particles in the sludge can be decomposed to the size of a single cell or finer by being sheared, broken, and decomposed by a high-speed water flow.

発酵菌槽は、超微粒子化装置からの汚泥超微粒子を、槽内で発酵菌を混合して発酵させるもので、汚泥超微粒子を含む液を受容する受容槽を有し、液を槽内に一定時間滞留するように設計され、好ましくは、液を攪拌混合する攪拌装置と発酵適温に保持する適温調整装置を適宜備えて、均一な発酵分解を促進することが好ましい。   The fermenting fungus tank is a fertilizer that mixes fermenting bacteria in the tank with the sludge ultrafine particles from the ultrafine particle generator, and has a receiving tank that accepts the liquid containing the sludge ultrafine particles. It is designed to stay for a certain period of time, and preferably it is suitably equipped with a stirrer that stirs and mixes the liquid and a suitable temperature adjustment device that maintains a suitable temperature for fermentation to promote uniform fermentation decomposition.

発酵菌槽で、微細化汚泥の発酵に用いる発酵菌は、動植物の組織や微生物細胞など微細化粒子物を微生物学的に分解させる商業的に入手可能な細菌や菌類を広く使用することができる。このような菌類には、例えば、ラクトバチルス類も酵母類、ビフィズス類が挙げられる。   Fermentative bacteria used for fermenting refined sludge in fermenting fungi tanks can be widely used commercially available bacteria and fungi that microbiologically decompose fine particles such as animal and plant tissues and microbial cells . Such fungi include, for example, lactobacilli as well as yeasts and bifidos.

発酵菌を混合する別の形態は、自然界から菌の付着した植物又は土壌を採取し、この試料から、培養装置によって培養して得られた菌も利用することができる。このような発酵用に利用可能な菌類には、乳酸菌類、例えば、ラクトバチルス類も酵母類、ビフィズス類などの菌種が利用できる。発酵菌として、例えば、乳酸菌は、汚水処理装置の周辺での植物や土壌から採取しても良い。   As another form of mixing the fermenting bacteria, it is also possible to use bacteria obtained by collecting a plant or soil to which bacteria are attached from the natural world and culturing them from this sample using a culture apparatus. As fungi that can be used for such fermentation, lactic acid bacteria, for example, Lactobacillus can also be used, such as yeasts and bifido species. As fermentative bacteria, for example, lactic acid bacteria may be collected from plants or soil around the sewage treatment apparatus.

採取した発酵菌を含む試料は、資料中に含む多数の雑菌からいくつかの有用な発酵性菌株を培養する必要があるが、このためには、例えば、紫外線照射による雑菌死滅と紫外線利用菌類の拡大培養法が利用できる。   For the sample containing the collected fermentative bacteria, it is necessary to cultivate some useful fermentative strains from a large number of miscellaneous bacteria included in the data. Expansion culture methods can be used.

植物又は土壌とともに採取した乳酸菌その他の発酵菌は、別体の培養装置を用いて別途培養することができる。培養装置は、微粒化部と培養槽とを備えるものが好ましく、微粒化部は、高速水流の衝撃力、大きな水流速度差による剪断力、又は気泡崩壊、即ち、キャビテーションを利用して、適当な培養用有機材料を微粒化する。培養槽は、微粒化された有機物材料を培養基材として発酵菌を培養する。この培養装置では、有機材料の細胞膜も微粒化部で粉砕され細胞内物質が培養液中に分散され、固形分は、表面積を大幅に拡大しているので、培養槽において発酵菌を大量に培養することができる。   Lactic acid bacteria and other fermentative bacteria collected together with plants or soil can be separately cultured using a separate culture apparatus. The culture apparatus is preferably provided with a micronization part and a culture tank, and the micronization part can be suitably used by utilizing the impact force of a high-speed water flow, the shearing force due to a large water flow velocity difference, or bubble collapse, that is, cavitation. Atomize organic material for culture. The culture tank cultivates the fermenting bacteria using the atomized organic material as a culture substrate. In this culture device, the cell membrane of organic material is also pulverized in the atomization part, the intracellular substances are dispersed in the culture solution, and the solid content greatly expands the surface area. can do.

尤も、微粒化部は、上記の沈殿汚泥を微粒化する超微粒子化装置が兼ねるようにして、超微粒子化装置からの汚泥微細化粒子の一部を培養槽に供給して、発酵菌の培養に利用するのが好ましい。   However, the atomization unit supplies the culture tank with a part of the sludge fine particles from the ultra fine particle device so that the ultra fine particle device that atomizes the precipitated sludge also serves as the culture medium for fermentation bacteria. It is preferable to use it.

分離槽は、発酵菌槽で発酵させた汚泥超微粒子を処理水と発酵汚泥とに分離するものであるが、適当な沈殿槽や濾過槽で固液分離を行う。   The separation tank separates the sludge ultrafine particles fermented in the fermentation bacteria tank into treated water and fermentation sludge, and performs solid-liquid separation in an appropriate precipitation tank or filtration tank.

本発明の処理設備は、さらに、分離槽において分離された発酵汚泥を、急速発酵分解汚泥処理機を用いて処理する工程を含むのが好ましい。急速発酵分解汚泥処理機では、回転撹拌を受けて残存有機物は発酵菌によって効率的に水や炭酸ガスと無機分とに分解される。   The treatment facility of the present invention preferably further includes a step of treating the fermented sludge separated in the separation tank using a rapid fermentation decomposition sludge treatment machine. In the rapid fermentation and decomposition sludge treatment machine, the remaining organic matter is efficiently decomposed into water, carbon dioxide and inorganic components by the fermenting bacteria after receiving rotational agitation.

処理設備は、さらに、分離槽において分離された処理水を汚水処理装置の沈殿槽に供給して循環する配管を含んでもよい。処理水は超微粒子化された沈殿汚泥の有機物により大量に増殖した発酵菌を含んでいるので、汚水処理装置の沈殿槽では、汚水の活性汚泥処理に活用することができる。この沈殿槽は、上述のように、汚水処理装置の曝気槽、分解槽又は沈殿槽を含んでいる。   The treatment facility may further include a pipe that circulates by supplying the treated water separated in the separation tank to the settling tank of the sewage treatment apparatus. Since the treated water contains fermenting bacteria grown in large quantities by the organic matter of the precipitated sludge that has been made into ultrafine particles, it can be used for the activated sludge treatment of the sewage in the settling tank of the sewage treatment apparatus. As described above, the sedimentation tank includes an aeration tank, a decomposition tank, or a sedimentation tank of the sewage treatment apparatus.

以上の説明により、本発明の処理設備によって得られた無機汚泥は、大部分が無機分であり、腐敗せずに、土地改良にも利用できる。   From the above description, the inorganic sludge obtained by the treatment facility of the present invention is mostly inorganic and can be used for land improvement without being spoiled.

他方、本発明の処理設備によって得られた処理水は、前述のように、活性汚泥式汚水処理装置の、特に、沈殿槽に戻して混合して発酵菌を供給することもでき、活性汚泥を活性化させて生化学的酸素要求量(BOD)と懸濁固形物(SS)を短時間で一定値以下に低下させることができる。処理設備によって得られた上記処理水は、汚水処理装置を通じて、清浄化した水として、河川等に放出することができる。   On the other hand, the treated water obtained by the treatment facility of the present invention, as described above, can be supplied to the activated sludge type sewage treatment apparatus, in particular, returned to the sedimentation tank and mixed to supply the fermentation bacteria. It can be activated to reduce biochemical oxygen demand (BOD) and suspended solids (SS) below a certain value in a short time. The treated water obtained by the treatment facility can be discharged to a river or the like as purified water through a sewage treatment apparatus.

また、処理設備によって得られた上記の処理水は、例えば、一時保管中の残飯や廃棄食品に散布混合することもでき、これにより、保管中の悪臭の発生を抑制できる。処理水は、畜産の分野では家畜の糞尿に混合してもよく、養分に富んで悪臭の少ない堆肥化を促進できる。処理水は、さらに湖沼河川の浄化や土地改良にも活用できる。   Moreover, said treated water obtained by the processing equipment can also be sprayed and mixed with, for example, leftover food during temporary storage or waste food, thereby suppressing the generation of malodor during storage. Treated water may be mixed with livestock manure in the field of livestock production, and can promote composting that is rich in nutrients and has less offensive odor. The treated water can also be used for purification of lakes and rivers and land improvement.

本発明の汚水処理設備においては、発酵菌槽に添加する発酵菌には、例えば、乳酸菌と共生関係を有するある種の光合成菌類を混合することもできる。   In the sewage treatment facility of the present invention, for example, certain photosynthetic fungi having a symbiotic relationship with lactic acid bacteria can be mixed with the fermenting bacteria added to the fermenting bacteria tank.

光合成菌類は、発酵菌槽において太陽光を受けて光合成を行い、発酵菌は増殖力を高め、互いに、必要とする共生物質を供給して培養を早めることが期待できる。光合成菌類のある菌種の中には、腐敗により発生する悪臭物質を栄養源として摂取するものもある。本発明においては、このような光合成菌類には、入手可能なものとして、紅色非硫黄細菌群(Rhodospirillaceac科)など(例えば、ジーラント社の「ジーラ発酵菌群」として市販)
が利用できる。
It is expected that the photosynthetic fungi receive sunlight in the fermenting fungus tank and perform photosynthesis, and the fermenting fungi can increase the growth ability and supply the necessary symbiotic substances to accelerate the culture. Some species of photosynthetic fungi ingest malodorous substances generated by spoilage as nutrient sources. In the present invention, such photosynthetic fungi include, for example, red non-sulfur bacteria group (Rhodospirillaceac family) and the like (for example, commercially available as “Zilla fermenting bacteria group” of Geeland)
Is available.

なお、光合成菌類は、アミノ酸やミネラルやビタミン等の優れた栄養分に富んでいて菌体自身が有機肥料としても有用であるが、ある種の光合成菌は、腐敗汚泥に会うと硫酸還元菌が発生させる硫化水素を栄養源として積極的に摂取することも知られている。ある種の光合成菌は、有毒アミンであるプトレシンやカタベリン、また発癌催奇性のジメチルニトロサミンも好んで基質として摂取して分解除去することが知られている。   Photosynthetic fungi are rich in amino acids, minerals, vitamins, and other excellent nutrients, and the cells themselves are useful as organic fertilizers, but certain photosynthetic bacteria generate sulfate-reducing bacteria when they encounter septic sludge. It is also known to actively take in hydrogen sulfide as a nutrient source. It is known that certain types of photosynthetic bacteria prefer to take toxic amines putrescine and cataverine and carcinogenic teratogenic dimethylnitrosamine as a substrate and decompose and remove them.

また、光合成菌類は、緑農地に還元すると作物の根が嫌う有害物質を分解除去し、根の呼吸や栄養代謝系を守り、窒素固定も行って作物の増収をもたらす働きをすることが期待できる。   In addition, when photosynthetic fungi are reduced to green farmland, they can decompose and remove harmful substances that the roots of crops dislike, protect root respiration and nutrient metabolism systems, and also perform nitrogen fixation to increase the yield of crops. .

本発明の沈殿汚泥の処理設備の実施例を、図1を参照して説明する。この実施例の沈殿槽11は、高層ビルに入居している多数の飲食店厨房からの汚泥排水W1を処理する設備であるが、沈殿槽11内の止水部位11aあるいは死角部位においては、汚泥Dが沈殿し、汚泥Dは、時には、硫化水素を発生する程腐敗し、悪臭を発していた。   An embodiment of the treatment facility for precipitated sludge according to the present invention will be described with reference to FIG. The sedimentation tank 11 of this embodiment is a facility for treating sludge drainage W1 from a large number of restaurant kitchens occupying a high-rise building, but in the water stop part 11a or blind spot part in the precipitation tank 11, sludge is used. D settled, and the sludge D sometimes rotted to generate hydrogen sulfide and gave off a bad odor.

その沈殿汚泥Dを処理するために、沈殿槽11における止水部位11aにパイプ12aを固定し、吸引装置としてポンプ12により、スラリー状の沈殿汚泥Dを吸引して、超微粒子化装置20に移送する。微粒子化装置20は、汚泥Dの有機物、即ち細菌や原生動物等の細胞を破壊し、細胞質をミクロンレベルまで微粒化する。   In order to treat the precipitated sludge D, the pipe 12a is fixed to the water stop part 11a in the settling tank 11, and the slurry-like precipitated sludge D is sucked by the pump 12 as a suction device and transferred to the ultrafine particle device 20. To do. The micronizer 20 destroys the organic matter of the sludge D, that is, cells such as bacteria and protozoa, and micronizes the cytoplasm to the micron level.

超微粒子化装置20の一例は、図2に示すように、中空円筒容器21を天板21aと底板21bと外筒21cとから形成し、内部に内筒22aを同心状に設けて外側の環状流路23aと内腔室23bとを形成している。外筒21cの底板21bの近くに水噴出ノズル24の吐出口24aを、環状流路内にその接線方向に向けて取り付け、高圧ポンプPから供給される水流によって環状流路23a内に循環する高速水流Fを発生させる。環状流路内の高速水流は、十分な微細化させるために、平均流速8m/s以上、好ましくは、平均10〜30m/sの速度にして、著しい乱流を形成している。   As shown in FIG. 2, an example of the ultrafine particle device 20 includes a hollow cylindrical container 21 formed of a top plate 21a, a bottom plate 21b, and an outer cylinder 21c, and an inner cylinder 22a provided concentrically inside, and an outer annular shape. A flow path 23a and a lumen chamber 23b are formed. A discharge port 24a of a water jet nozzle 24 is attached in the annular flow path in the tangential direction near the bottom plate 21b of the outer cylinder 21c, and is circulated in the annular flow path 23a by the water flow supplied from the high pressure pump P. A water stream F is generated. The high-speed water flow in the annular channel forms a significant turbulent flow at an average flow rate of 8 m / s or more, preferably an average speed of 10 to 30 m / s in order to sufficiently reduce the size.

内筒22aには縦長のスロット25aを複数形成し、スラリー供給管12aを内筒内部63bに開口するように天板21aに取り付けある。微粒化すべき沈殿汚泥はスラリーSとしてスロット25aから吐出させ、上記高速の水流Fに対して略直角に衝突させる。   A plurality of vertically long slots 25a are formed in the inner cylinder 22a, and the slurry supply pipe 12a is attached to the top plate 21a so as to open to the inner cylinder interior 63b. The precipitated sludge to be atomized is discharged as a slurry S from the slot 25a and collides with the high-speed water flow F substantially at a right angle.

スロット25aからスラリーが吐出した環状流路の混合領域Aでは、スラリーS中の有機物を衝撃による圧縮や、高速水流Fによる剪断、キャビテーションなどによって、また高速水流Fと内筒22aの外面や外筒21cの内面に沿った低速水流との大きな速度差による剪断などのよって、有機物粒子は、おおよそ1〜10μmまで微粒化される。水噴出ノズル24からの噴出水流に気泡を混入する気泡発生器を水噴出ノズル24に付設してもよい。   In the mixing region A of the annular flow path from which the slurry is discharged from the slot 25a, the organic matter in the slurry S is compressed by impact, sheared by the high-speed water flow F, cavitation, etc., and the outer surface of the inner cylinder 22a and the outer cylinder The organic particles are atomized to approximately 1 to 10 μm by shearing due to a large speed difference from the low-speed water flow along the inner surface of 21c. A bubble generator that mixes bubbles in the water flow ejected from the water ejection nozzle 24 may be attached to the water ejection nozzle 24.

超微粒子化装置20で微粒化された有機物を含む高速水流Fは、環状流路から、大部分を排出管29で発酵菌槽30に供給する。その水流Fの一部分は、排出管29から配管34を通して、培養装置35に供給する。   Most of the high-speed water flow F containing the organic matter atomized by the ultrafine particle device 20 is supplied to the fermenting bacteria tank 30 through the discharge pipe 29 from the annular channel. A part of the water flow F is supplied from the discharge pipe 29 to the culture apparatus 35 through the pipe 34.

上記微粒過程では、半径1mmの球状の有機体は、比表面積が計算上0.00120m2/gであるとして、これが、半径0.0001mmの球状に均一粒径に微細化されたと仮定すると、その比表面積は計算上12.0m/gと非常に大きくなる。このような微小で多数の超微細化粒子の群には、全体として、多数の発酵菌が表面に付着することができて、発酵菌槽30や培養槽35において発酵菌を効率的に大量に培養することができる。 In the fine particle process, assuming that the spherical organic substance having a radius of 1 mm is calculated to have a specific surface area of 0.00120 m 2 / g, it is refined into a spherical particle having a radius of 0.0001 mm and a uniform particle diameter. The surface area is very large at 12.0 m 2 / g in calculation. In such a group of minute and many ultrafine particles, a large number of fermentation bacteria can adhere to the surface as a whole, and the fermentation bacteria can be efficiently produced in a large amount in the fermentation bacteria tank 30 and the culture tank 35. It can be cultured.

図1に戻って、この例は、発酵菌として乳酸菌を使用し、乳酸菌は、汚水処理装置の設置場所近くの植物や土壌から採取され、培養装置の培養槽35によって大量に培養してから利用する。   Returning to FIG. 1, this example uses lactic acid bacteria as fermentation bacteria, and the lactic acid bacteria are collected from plants and soil near the place where the sewage treatment apparatus is installed, and are used after being cultured in large quantities in the culture tank 35 of the culture apparatus. To do.

この実施例では、採取された土壌を原料として培養槽35に入れて、糖蜜の糖分とミネラル分とを添加した拡大培養法により、乳酸菌として、主として、ラクトバチルス類を培養している。   In this embodiment, the Lactobacillus is mainly cultured as a lactic acid bacterium by an expansion culture method using the collected soil as a raw material in a culture tank 35 and adding the sugar content and mineral content of molasses.

この実施例は、培養に際して、上記の超微粒子化装置20から、微細化された汚泥超微粒子を含む栄養液流 82の一部を配管34を介して、培養槽35に適時供給し、上記発酵菌を培養させて常時大量の発酵菌を保管しておく。培養装置は、培養槽35と、超微粒化部と、から成るが、この例は、その超微粒化部として上記超微粒子化装置20を利用して、微粒化された有機物を培養基材として、培養槽35に供給し、発酵菌を大量に培養している。   In this embodiment, during culturing, a part of the nutrient solution stream 82 containing the refined sludge ultrafine particles is supplied from the ultrafine particle device 20 to the culture tank 35 through the pipe 34 in a timely manner. A large amount of fermented bacteria are always stored by culturing the bacteria. The culture apparatus includes a culture tank 35 and an ultrafine atomization unit. In this example, the ultrafine particle generation apparatus 20 is used as the ultrafine atomization part, and the atomized organic matter is used as a culture substrate. , And supplied to the culture tank 35 to culture a large amount of fermentation bacteria.

発酵菌槽30は、この例では、前部槽30aと後部槽30bとの2槽構造で、両部の中間を、仕切り板38により適当に区画され、仕切り板38には、貫通路ないし溢流路のような水路を設けて両部が連通され、前部槽30aと後部槽30bの内部には、回転刃根37を槽内に配置した攪拌器を用いて、槽内の液を攪拌している。   In this example, the fermenting fungus tank 30 has a two-tank structure of a front tank 30a and a rear tank 30b, and the middle of both parts is appropriately partitioned by a partition plate 38, and the partition plate 38 has a through passage or overflow. A water channel such as a flow path is provided so that both parts communicate with each other. Inside the front tank 30a and the rear tank 30b, the liquid in the tank is stirred using a stirrer in which a rotary blade root 37 is disposed in the tank. ing.

この例は、前部槽30aに上記超微粒子化装置20により微粒化した汚泥超微粒子を含む栄養液流82として配管29を通して供給する。同時に、培養槽35からは、配管36を通じて、乳酸菌を含む培養液を供給して、汚泥超微粒子と発酵菌培養液とを撹拌機37によって混合曝気し、汚泥超微粒子を発酵分解させる。発酵菌は、前部槽30aに供給された上記の超微粒子化の汚泥有機質を同時に栄養源として効率的に摂取して、増殖する。   In this example, the nutrient solution flow 82 containing the sludge ultrafine particles atomized by the ultrafine atomizer 20 is supplied to the front tank 30a through the pipe 29. At the same time, a culture solution containing lactic acid bacteria is supplied from the culture tank 35 through the pipe 36, and the sludge ultrafine particles and the fermentation bacteria culture solution are mixed and aerated by the stirrer 37 to fermentatively decompose the sludge ultrafine particles. The fermenting bacteria efficiently ingest the above-mentioned ultrafine particle sludge organic matter supplied to the front tank 30a as a nutrient source and proliferate.

その際、乳酸菌と共生関係を取る光合成菌を選んで発酵菌槽に添加することもなされ、昼間は発酵菌槽を太陽光で照射状態にすることにより、光合成菌が増殖し、発酵菌にさらに活力を与え、排水中の有機物の分解を促進させることができる。   At that time, photosynthetic bacteria having a symbiotic relationship with lactic acid bacteria can be selected and added to the fermenting fungus tank, and by daylighting the fermenting fungus tank with sunlight, the photosynthetic bacteria can grow and further Gives vitality and promotes the decomposition of organic matter in the waste water.

発酵菌槽では、前部槽30aから後部槽30bに移動する水流により発酵菌と汚泥超微粒子との懸濁液を後部槽30bに移すが、後部槽30bには、この例は、上記汚水処理装置の沈殿槽11から、その上澄み排水83を、配管19を介して、供給している。後部槽30bでは、発酵菌により排水83を撹拌機37の攪拌下で、混合曝気しながら活性汚泥処理させる。   In the fermenting fungus tank, the suspension of the fermenting bacteria and the sludge ultrafine particles is transferred to the rear tank 30b by the water flow moving from the front tank 30a to the rear tank 30b. The supernatant drainage 83 is supplied from the settling tank 11 of the apparatus through the pipe 19. In the rear tank 30b, the activated sludge is treated by fermenting bacteria with the activated sludge while being mixed and aerated under the stirring of the stirrer 37.

発酵菌槽30からの排液は、配管により固液分離槽40に移し、そこで発酵菌を含む処理水84と、無機分を主成分とする発酵汚泥92とに分離する。処理水84は、排水基準を満たしていることを条件に、配水管42を通じて河川に放流する。   The effluent from the fermenting fungus tank 30 is transferred to a solid-liquid separation tank 40 by piping, where it is separated into treated water 84 containing the fermenting fungus and fermented sludge 92 containing an inorganic component as a main component. The treated water 84 is discharged into the river through the water distribution pipe 42 on condition that the drainage standard is satisfied.

また、発酵汚泥93を回転ドラム式の急速発酵分解汚泥処理機50に移送して、残存有機物を発酵菌によって炭酸ガスと水にさらに分解処理し無機分が残る。   Further, the fermented sludge 93 is transferred to a rotary drum type rapid fermentation and decomposition sludge treatment machine 50, and the remaining organic matter is further decomposed into carbon dioxide gas and water by the fermenting bacteria, leaving an inorganic content.

回転ドラム式の急速発酵分解汚泥処理機50は、図1と図3に示すように、両端部に静止端壁56a、56bを備えて、横長の円筒体の回転ドラム53を含み、回転ドラムは、固定支台51上に、ドラム外周に、前部と中間部と後部とに設けたリング52を、それぞれ、左右一対の支持ローラ521によって支持して、ドラム中間部のリング歯車54aに噛み合うピニオン54bを介して減速機付きモータ55によって定速で回転駆動する。   As shown in FIG. 1 and FIG. 3, the rotary drum type rapid fermentation decomposition sludge treatment machine 50 includes stationary end walls 56a and 56b at both ends, and includes a horizontally long cylindrical rotary drum 53. The ring 52 provided on the outer periphery of the drum on the fixed abutment 51 and on the front, the middle and the rear is supported by a pair of left and right support rollers 521 and meshes with the ring gear 54a in the middle of the drum. It is rotationally driven at a constant speed by a motor 55 with a speed reducer via 54b.

回転ドラム53の内周壁面には、螺旋体58が取り付けられて、回転方向に応じて被処理物の発酵菌汚泥91を一方の静止端壁56a側から他方の静止端壁57a側へ移動させる。   A spiral body 58 is attached to the inner peripheral wall surface of the rotating drum 53, and the fermented bacteria sludge 91 to be processed is moved from one stationary end wall 56a side to the other stationary end wall 57a side in accordance with the rotation direction.

当該一方の静止端壁56aには、下部に、はスクリューコンベヤ56bを介して被処理物の発酵菌汚泥93をドラム内部に供給する供給口を設けて、分離槽の底部に接続されている。端壁56aの中間部には、木材チップに発酵菌を混合したジーラ材を供給する供給器56cを設けている。静止端壁56aの上部には、排気管56dを設けて、発酵菌汚泥93の残存有機物分解で発生する炭酸ガス排出する。   The one stationary end wall 56a is provided with a supply port for supplying fermented bacteria sludge 93 to be processed into the drum through the screw conveyor 56b, and is connected to the bottom of the separation tank. In the middle part of the end wall 56a, a supply device 56c is provided for supplying a gelatin material in which fermented bacteria are mixed with wood chips. An exhaust pipe 56d is provided at the upper part of the stationary end wall 56a to discharge the carbon dioxide gas generated by the decomposition of the remaining organic matter of the fermentation bacteria sludge 93.

当該他方側の静止端壁57aは、その下部に出口57bを設けて、発酵済みの汚泥94を排出する。   The stationary end wall 57a on the other side is provided with an outlet 57b at a lower portion thereof, and the fertilized sludge 94 is discharged.

この装置の使用に際しては、分離槽30底部からの発酵菌汚泥92をスクリューコンベヤ56bを介してドラム53内部に供給して、端壁56aの中間部からは木材チップに発酵菌を混合したジーラ材を補給器56cを通してドラム内部に補給される。ドラムを回転させることにより、ジーラ材と発酵菌汚泥93とをドラム内を他方側に輸送しながら混合し発酵させる。上部からは、発酵菌汚泥93の残存有機物分解で発生する炭酸ガスを排気管56dを介して排出している。   When using this apparatus, the fermented bacteria sludge 92 from the bottom of the separation tank 30 is supplied into the drum 53 via the screw conveyor 56b, and from the middle part of the end wall 56a, the gillar material in which the fermented bacteria are mixed with the wood chips. Is supplied into the drum through the replenisher 56c. By rotating the drum, the Zilla material and the fermented bacteria sludge 93 are mixed and fermented while being transported to the other side in the drum. From the upper part, the carbon dioxide gas generated by the decomposition of the remaining organic matter of the fermentation bacteria sludge 93 is discharged through the exhaust pipe 56d.

ドラム53内では、有機物がほぼ完全に分解処理されて、無機物化した残滓94は、出口57bからは、排出される。ジーラ材補給器56cには、発酵菌を補給するために分離槽40から処理水92が適宜供給される。   In the drum 53, the organic substance is almost completely decomposed, and the residue 94 converted to an inorganic substance is discharged from the outlet 57b. The treated water 92 is appropriately supplied from the separation tank 40 to the jilla material replenisher 56c in order to replenish fermented bacteria.

この例は、さらに、分離槽40において分離された処理水92の一部は、活性汚泥式汚水処理装置の沈殿槽11に配管45を通して、循環することができ、超微粒子化された沈殿汚泥の有機物を摂取して大量に増殖した発酵菌によって沈殿槽11から発酵菌槽30にかけての活性汚泥処理に再度活用している。   Further, in this example, a part of the treated water 92 separated in the separation tank 40 can be circulated through the pipe 45 to the settling tank 11 of the activated sludge type sewage treatment apparatus. It is used again for the activated sludge treatment from the sedimentation tank 11 to the fermentation bacteria tank 30 by the fermenting bacteria that ingested organic matter and proliferated in large quantities.

本発明の実施例に係る沈殿汚泥の処理設備の工程図。The process figure of the processing equipment of the precipitation sludge which concerns on the Example of this invention. 本発明の実施例に係る沈殿汚泥の処理設備に使用する超微粒子化装置の部分切り欠き横断面図(A)と部分切り欠き縦断面図(B)。The partial notch cross-sectional view (A) and partial notch longitudinal cross-sectional view (B) of the ultrafine-particle-ized apparatus used for the processing equipment of the precipitation sludge which concerns on the Example of this invention. 本発明の実施例に係る沈殿汚泥の処理設備に使用する回転ドラム式の急速発酵分解汚泥処理機の立面図。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an elevational view of a rotary drum type rapid fermentation decomposition sludge treatment machine used in a sedimentation sludge treatment facility according to an embodiment of the present invention.

符号の説明Explanation of symbols

11:沈殿槽
11a:止水部位
12:収集手段(吸引装置)
12a:パイプ
20:超微粒子装置
30:発酵菌槽
35:培養槽
40:分離槽
50:急速発酵分解汚泥処理機
9:沈殿汚泥
93:発酵菌汚泥
83:排水
84:処理水
11: Precipitation tank 11a: Water stop part 12: Collecting means (suction device)
12a: Pipe 20: Ultrafine particle device 30: Fermentation bacteria tank 35: Culture tank 40: Separation tank 50: Rapid fermentation decomposition sludge treatment machine 9: Precipitation sludge 93: Fermentation bacteria sludge 83: Waste water 84: Treated water

Claims (8)

汚水中の有機物を分解処理して処理水を排出する汚水処理装置の沈殿槽内に蓄積した沈殿汚泥を処理する汚水処理設備であって、
上記の沈殿槽から沈殿汚泥を収集する収集手段と、
該収集手段により収集した沈殿汚泥を汚泥超微粒子に超微粒子化する超微粒子化装置と、
汚泥超微粒子に発酵菌を混合して、汚泥超微粒子を発酵させる発酵菌槽と、
発酵した汚泥超微粒子を処理水と発酵汚泥とに分離する分離槽と、
から成る汚水処理設備。
A sewage treatment facility for treating precipitated sludge accumulated in a settling tank of a sewage treatment apparatus that decomposes organic matter in sewage and discharges treated water,
A collecting means for collecting the precipitated sludge from the settling tank,
An ultrafine particle forming apparatus for making the precipitated sludge collected by the collecting means into ultrafine sludge particles;
A fermenting fungus tank in which fermented bacteria are mixed with sludge ultrafine particles to ferment the sludge ultrafine particles;
A separation tank for separating fermented sludge ultrafine particles into treated water and fermented sludge;
Sewage treatment facility consisting of.
汚水処理装置が、汚水中の有機物を微生物の働きで分解して生化学的酸素要求量と懸濁固形物量を一定基準以下に低下させた処理水として排出するための活性汚泥式汚水処理装置である請求項1に記載の汚水処理設備。   Sewage treatment equipment is an activated sludge sewage treatment equipment that decomposes organic matter in sewage by the action of microorganisms and discharges it as treated water with reduced biochemical oxygen demand and suspended solids below a certain standard. The sewage treatment facility according to claim 1. 収集手段が、吸引装置とこの吸引装置に接続して先端部が沈殿槽内の沈殿部位に位置づけ可能な可撓性若しくは固定の配管とから成る請求項1又は2記載の汚水処理設備。   The sewage treatment facility according to claim 1 or 2, wherein the collecting means comprises a suction device and a flexible or fixed pipe which is connected to the suction device and whose tip can be positioned at a sedimentation site in the sedimentation tank. 超微粒子化装置が、高速水流の衝撃力、水流速度差による剪断力又は気泡破裂の超音波によって有機物を微粒化する請求項1ないし3いずれかに記載の汚水処理設備。   The sewage treatment facility according to any one of claims 1 to 3, wherein the microparticulater atomizes the organic matter by an impact force of a high-speed water flow, a shearing force due to a difference in water flow velocity, or an ultrasonic wave of bubble burst. 発酵菌が、植物又は土壌から採取され培養装置によって培養して得られた乳酸菌である請求項1ないし4いずれかに記載の汚水処理設備。   The sewage treatment facility according to any one of claims 1 to 4, wherein the fermentative bacterium is a lactic acid bacterium obtained from a plant or soil and cultured by a culture apparatus. 培養装置が、高速水流の衝撃力と大きな水流速度差による剪断力と気泡破裂の超音波によって有機物を微粒化する微粒化部と、微粒化された有機物を培養基材として発酵菌を培養する培養槽と、から成る請求項5に記載の汚水処理設備。   Cultivation equipment cultivates fermenting bacteria using the atomized organic material as the culture substrate, and the atomization part that atomizes the organic material by the shearing force due to the impact force of the high-speed water flow and the large water flow velocity difference and the ultrasonic wave of bubble burst The sewage treatment facility according to claim 5, comprising a tank. 上記の処理設備が、分離槽において分離された発酵汚泥を処理する回転ドラム式の急速発酵分解汚泥処理機を含む請求項1ないし6いずれかに記載の汚水処理設備。   The sewage treatment facility according to any one of claims 1 to 6, wherein the treatment facility includes a rotary drum type rapid fermentation decomposition sludge treatment machine for treating the fermentation sludge separated in the separation tank. 分離槽において分離された処理水を汚水処理装置の沈殿槽に循環する配管を含む請求項1ないし7いずれかに記載の汚水処理設備。
The sewage treatment facility according to any one of claims 1 to 7, further comprising a pipe for circulating the treated water separated in the separation tank to the settling tank of the sewage treatment apparatus.
JP2003412229A 2003-12-10 2003-12-10 Sewage treatment equipment Expired - Fee Related JP3854269B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006167622A (en) * 2004-12-16 2006-06-29 Miike Iron Works Co Ltd Method and device for decomposing organic substance with microorganism
WO2011132267A1 (en) * 2010-04-20 2011-10-27 Katayose Shigeru Sludge treatment method
CN103350097A (en) * 2013-06-25 2013-10-16 重庆欣彦生物技术有限公司 Ecological comprehensive treatment system of waste
KR20180057361A (en) * 2016-11-22 2018-05-30 (주)우정티알비서울사무소 High efficiency apparatus for removing algae

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Publication number Priority date Publication date Assignee Title
EP2311968A1 (en) 2009-10-14 2011-04-20 PURAC Biochem BV Fermentation process at reduced pressure

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006167622A (en) * 2004-12-16 2006-06-29 Miike Iron Works Co Ltd Method and device for decomposing organic substance with microorganism
JP4585302B2 (en) * 2004-12-16 2010-11-24 株式会社御池鐵工所 Method and apparatus for decomposing organic matter by microorganisms
WO2011132267A1 (en) * 2010-04-20 2011-10-27 Katayose Shigeru Sludge treatment method
CN103350097A (en) * 2013-06-25 2013-10-16 重庆欣彦生物技术有限公司 Ecological comprehensive treatment system of waste
KR20180057361A (en) * 2016-11-22 2018-05-30 (주)우정티알비서울사무소 High efficiency apparatus for removing algae
KR101948590B1 (en) * 2016-11-22 2019-02-15 (주)우정티알비서울사무소 High efficiency apparatus for removing algae

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