JP4482717B1 - Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same - Google Patents

Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same Download PDF

Info

Publication number
JP4482717B1
JP4482717B1 JP2009159243A JP2009159243A JP4482717B1 JP 4482717 B1 JP4482717 B1 JP 4482717B1 JP 2009159243 A JP2009159243 A JP 2009159243A JP 2009159243 A JP2009159243 A JP 2009159243A JP 4482717 B1 JP4482717 B1 JP 4482717B1
Authority
JP
Japan
Prior art keywords
tank
water
separation
domestic wastewater
advanced
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.)
Active
Application number
JP2009159243A
Other languages
Japanese (ja)
Other versions
JP2011011175A (en
Inventor
龍男 白方
Original Assignee
龍男 白方
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 龍男 白方 filed Critical 龍男 白方
Priority to JP2009159243A priority Critical patent/JP4482717B1/en
Application granted granted Critical
Publication of JP4482717B1 publication Critical patent/JP4482717B1/en
Priority to CN2010102058263A priority patent/CN101941775B/en
Publication of JP2011011175A publication Critical patent/JP2011011175A/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Activated Sludge Processes (AREA)
  • Physical Water Treatments (AREA)

Abstract

【課題】生活排水を化学薬剤(凝集剤)を使用しないで安全且つ廉価に飲用に適するまで高度に浄化し、繰り返し再利用する生活排水高度浄化処理循環システム及び生活排水高度浄化処理循環方法を提供する。
【解決手段】複合有効微生物群を貯留し培養する複合有効微生物群培養槽10と、高度曝気槽30に流入する複合有効微生物群量を調整する処理水量調整槽20と、処理水量調整槽20から流入した汚水中の汚れを吸着分解処理する高度曝気槽30と、高度曝気槽30にて処理された汚水を固相と液相に分離する直列配置の第一分離沈殿槽40及び第二分離沈殿槽50と、第一分離沈殿槽40と第二分離沈殿槽50にて沈殿した汚泥を回収し貯留する汚泥貯留槽60と、最後尾の分離沈殿槽である第二分離沈殿槽50にて分離された液相である浄化水を滅菌処理する滅菌器70とから成る生活排水高度浄化処理循環システム及び生活排水高度浄化処理循環方法である。
【選択図】図1
[Problem] To provide a domestic wastewater advanced purification treatment circulation system and a domestic wastewater advanced purification treatment circulation method in which domestic wastewater is highly purified until it is suitable for drinking safely and inexpensively without using chemical agents (flocculating agents). To do.
SOLUTION: From a combined effective microorganism group culture tank 10 for storing and cultivating a combined effective microorganism group, a treated water amount adjusting tank 20 for adjusting a combined effective microorganism group amount flowing into an advanced aeration tank 30, and a treated water amount adjusting tank 20 An advanced aeration tank 30 that adsorbs and decomposes dirt in the wastewater that has flowed in, and a first separation precipitation tank 40 and a second separation precipitation that are arranged in series to separate the wastewater treated in the advanced aeration tank 30 into a solid phase and a liquid phase. Separation is performed in a tank 50, a sludge storage tank 60 that collects and stores sludge precipitated in the first separation and precipitation tank 40 and the second separation and precipitation tank 50, and a second separation and precipitation tank 50 that is the last separation and precipitation tank. This is a domestic wastewater advanced purification treatment circulation system and a domestic wastewater advanced purification treatment circulation method comprising a sterilizer 70 for sterilizing purified water in a liquid phase.
[Selection] Figure 1

Description

本発明は、生活排水を飲用に適するほどに高度に浄化処理し、再利用したのち、さらに高度に浄化処理して再利用することを繰り返し行うことができる生活排水高度浄化処理循環システム及びこれを利用した生活排水高度浄化処理循環方法に関するものである。   The present invention relates to a domestic wastewater advanced purification treatment circulation system capable of repeatedly purifying and reusing domestic wastewater so that it is suitable for drinking, and then further purifying and reusing it. It relates to the domestic wastewater advanced purification treatment circulation method.

従来、バクテリアなどの有効微生物を利用して排水を浄化処理する装置及び方法としては、産業排水及び工業排水を対象として、オゾン集積供給装置、オゾン反応沈殿槽、ろ過装置及び紫外線照射装置を設けた排水処理装置や水処理方法が提案されている(特許文献1)。また手洗いでの使用済みの排水や床排水や便器からの生活排水を浄化する装置及び方法としては、有効微生物着床用網状構造体と遠赤外線放射セラミック層により、有効微生物群を十分活動させることにより浄水化し、その浄水を再利用し得る排水処理再利用装置及び方法が提案されている(特許文献2)。   Conventionally, as an apparatus and method for purifying wastewater using effective microorganisms such as bacteria, an ozone accumulation supply device, an ozone reaction precipitation tank, a filtration device, and an ultraviolet irradiation device have been provided for industrial wastewater and industrial wastewater. A wastewater treatment apparatus and a water treatment method have been proposed (Patent Document 1). In addition, as an apparatus and method for purifying used wastewater, floor drainage, and domestic wastewater from toilet bowls, the active microorganism group should be fully activated by the net structure of effective microorganisms and the far infrared radiation ceramic layer. Has proposed a wastewater treatment reuse device and method that can purify water and reuse the purified water (Patent Document 2).

特開平9−174093号公報Japanese Patent Laid-Open No. 9-174093 特開平9−10784号公報Japanese Patent Laid-Open No. 9-10784

しかし、特許文献1において提案されている排水処理装置や水処理方法は、排水の浄化に主としてオゾンを使用するため装置が大掛かりであると共に高価であり、また装置のメンテナンスが頻繁に必要であるという課題があった。また特許文献2において提案されている排水処理再利用装置及び方法は、生活排水の浄化ではあるが、あくまで便器用あるいは洗浄用として再利用が可能なまでに浄化する程度に留まり、生活排水を飲用に適するまでに高度に浄化する装置や方法ではないという課題があった。   However, the wastewater treatment device and the water treatment method proposed in Patent Document 1 are large and expensive because ozone is mainly used for purification of wastewater, and the maintenance of the device is frequently required. There was a problem. In addition, the wastewater treatment reuse device and method proposed in Patent Document 2 is purification of domestic wastewater, but it is limited to the extent that it is purified until it can be reused for toilets or washing, and drinking domestic wastewater. There is a problem that it is not an apparatus or method for highly purifying until it is suitable.

本発明が解決しようとする課題は、大掛かりなオゾン集積供給装置を使用することなしに、生活排水を飲用に適するまでに高度に浄化し、浄化した水を再度生活水として再利用すると共に、その排水をさらに本発明によって高度に浄化して再利用するということを、繰り返し行うことができる生活排水高度浄化処理循環システム及びこれを利用した生活排水高度浄化処理循環方法を提供することにある。   The problem to be solved by the present invention is that the domestic wastewater is highly purified to be suitable for drinking without using a large-scale ozone accumulation and supply device, and the purified water is reused as domestic water again. It is another object of the present invention to provide a domestic wastewater advanced purification treatment circulation system capable of repeatedly purifying and reusing wastewater according to the present invention, and a domestic wastewater advanced purification treatment circulation method using the same.

請求項1記載の発明は、乳酸菌、酵母、光合成細菌を主体とする有用な微生物の共生体と、油分解微生物とから成る複合有効微生物群を貯留し培養する複合有効微生物群培養槽と、生活排水と複合有効微生物群培養槽中の複合有効微生物群と汚泥貯留槽中の汚泥とを混合して曝気し複合有効微生物群を増殖させると共に高度曝気槽に流入する複合有効微生物群量を調整する処理水量調整槽と、槽内中央部に接触材を浮遊状態に配設すると共に、散気管と逆洗管を90度の角度を持って配設し、散気管と逆洗管から同時に空気を排出して曝気することで、処理水量調整槽から流入した複合有効微生物群同士を衝突させて汚水中の汚れを吸着分解処理する高度曝気槽と、高度曝気槽にて処理された汚水を固相と液相に分離する直列配置の複数の分離沈殿槽と、複数の分離沈殿槽に沈殿した汚泥を回収して貯留する汚泥貯留槽と、最後尾の分離沈殿槽にて分離された液相である浄化水を滅菌処理する滅菌器とから成ることを特徴とする生活排水高度浄化処理循環システムを提供する。 The invention according to claim 1 is a compound effective microorganism group culture tank for storing and culturing a complex effective microorganism group consisting of microbial symbiosis mainly composed of lactic acid bacteria, yeast and photosynthetic bacteria, and oil-degrading microorganisms, The combined effective microorganism group in the waste water and the combined effective microorganism group culture tank and the sludge in the sludge storage tank are mixed and aerated to increase the combined effective microorganism group and adjust the amount of combined effective microorganism group flowing into the advanced aeration tank In addition to disposing a contact material in a floating state in the treated water amount adjustment tank and the central part of the tank, a diffuser pipe and a backwash pipe are arranged at an angle of 90 degrees, and air is simultaneously supplied from the diffuser pipe and the backwash pipe. By discharging and aeration, a complex aerobic microbial group that has flowed in from the treated water amount adjustment tank collides with each other to adsorb and decompose dirt in the sewage, and the sewage treated in the advanced aeration tank is solid-phased. And multiple components in series to separate into liquid phase It consists of a settling tank, a sludge storage tank that collects and stores sludge that has settled in a plurality of separate settling tanks, and a sterilizer that sterilizes purified water that is the liquid phase separated in the last settling tank Provide a domestic wastewater advanced purification treatment circulation system.

請求項2記載の発明は、請求項1記載の複合有効微生物群培養槽、処理水量調整槽、高度曝気槽、直列配置の複数の分離沈殿槽、及び汚泥貯留槽と、最後尾の分離沈殿槽にて分離された液相である浄化水を曝気することで有機物を分離する沈殿貯水槽と、沈殿貯水槽にて処理された浄化水を滅菌処理する滅菌器とから成ることを特徴とする生活排水高度浄化処理循環システムを提供する。   Invention of Claim 2 is the composite effective microorganism group culture tank of Claim 1, a treatment water amount adjustment tank, an advanced aeration tank, a plurality of separation and sedimentation tanks arranged in series, a sludge storage tank, and a rearmost separation and precipitation tank Living water characterized in that it comprises a precipitation reservoir that separates organic matter by aeration of purified water, which is a liquid phase separated in step 1, and a sterilizer that sterilizes purified water treated in the precipitation reservoir. Provide a wastewater advanced purification treatment circulation system.

請求項3記載の発明は、請求項1記載の複合有効微生物群培養槽、処理水量調整槽、高度曝気槽、直列配置の複数の分離沈殿槽、及び汚泥貯留槽と、最後尾の分離沈殿槽にて分離された液相である浄化水を貯留する第一貯水槽と、第一貯水槽より流入する浄化水を曝気することで有機物を分離する沈殿貯水槽と、沈殿貯水槽にて分離処理された浄化水を貯留する第二貯水槽と、第二貯水槽の浄化水を滅菌処理する滅菌器とから成ることを特徴とする生活排水高度浄化処理循環システムを提供する。 Invention of Claim 3 is the composite effective microorganism group culture tank of Claim 1, a treatment water amount adjustment tank, an advanced aeration tank, a plurality of separation / precipitation tanks arranged in series, a sludge storage tank, and a separation / precipitation tank at the end Separation treatment in the first water storage tank for storing the purified water, which is the liquid phase separated in step 1, the precipitation water tank for separating the organic matter by aeration of the purified water flowing in from the first water storage tank, and the precipitation water storage tank There is provided a domestic wastewater advanced purification treatment circulation system comprising a second water storage tank for storing the purified water and a sterilizer for sterilizing the purified water in the second water storage tank.

請求項4記載の発明は、生活排水を請求項1乃至請求項3のいずれかに記載の生活排水高度浄化処理循環システムにより処理して生活水として再利用し、その生活排水を更に同一の請求項1乃至請求項3のいずれかに記載の生活排水高度浄化処理循環システムにより処理して浄化し生活水として繰り返し再利用することを特徴とする生活排水高度浄化処理循環方法を提供する。 Invention of Claim 4 processes domestic wastewater by the domestic wastewater advanced purification treatment circulation system in any one of Claims 1 thru | or 3, and recycles it as domestic water, and the domestic wastewater is further the same claim. A domestic wastewater advanced purification treatment circulation method characterized by being treated and purified by the domestic wastewater advanced purification treatment circulation system according to any one of Items 1 to 3 and repeatedly reused as domestic water.

本発明は、オゾン集積供給装置のような大掛かりな装置は使用せず、一般に入手可能な複合有効微生物群を培養して使用するため、極めて廉価であるという効果がある。また汚水を固相と液相に分離する際には硫酸アルミニウム等の化学薬剤(凝集剤)を一切使用しないため、生活排水を安全に飲用に適するまで浄化処理することができる効果がある。さらには、浄化された水は再び生活水として使用され生活排水となるが、当該生活排水は本発明によって繰り返し高度に浄化され生活水として使用することができる。  The present invention does not use a large-scale apparatus such as an ozone accumulation and supply apparatus, and has an effect that it is extremely inexpensive because a complex effective microorganism group that is generally available is cultured and used. In addition, when separating sewage into a solid phase and a liquid phase, since no chemical agent (flocculant) such as aluminum sulfate is used, there is an effect that the domestic waste water can be purified until it is safe for drinking. Furthermore, although the purified water is used again as domestic water and becomes domestic wastewater, the domestic wastewater can be repeatedly highly purified by the present invention and used as domestic water.

このように、本発明の生活排水高度浄化処理循環システム及びこれを利用した生活排水高度浄化処理循環方法によれば、限りある水を繰り返し浄化し、生活水として使用することができ、特に砂漠化等で水不足にある国や地域において利用価値が高く、また本発明の構成をユニット化し現場で組み立てられるようにすれば、地震、火災、戦争等での避難生活における生活水の確保に、極めて有効であるという効果がある。 As described above, according to the domestic wastewater advanced purification treatment circulation system of the present invention and the domestic wastewater advanced purification treatment circulation method using the same, it is possible to repeatedly purify limited water and use it as domestic water, especially desertification. It has high utility value in countries and regions where water is scarce due to the above, and if the composition of the present invention is unitized and assembled on site, it is extremely effective in securing living water in evacuation life due to earthquakes, fires, wars, etc. There is an effect that.

また複数の分離沈殿槽で分離沈殿した固相である汚泥は、有機肥料として畑や樹木の栽培に使用することができ、また滅菌処理する前の高度に浄化された水は池等に供給して魚の養殖に使用し、また水耕栽培用の水としても利用することができる効果がある。   In addition, sludge, which is a solid phase separated and settled in multiple separation and sedimentation tanks, can be used as organic fertilizer for cultivation of fields and trees, and highly purified water before sterilization is supplied to ponds. It can be used for fish culture and can also be used as water for hydroponics.

請求項1に係る発明の一実施例である生活排水高度浄化処理循環システムであって高度曝気槽の槽内中央部に浮遊状態に配設した接触材を省略した、全体状態図である。It is a domestic wastewater advanced purification treatment circulation system which is one embodiment of the invention according to claim 1, and is an overall state diagram in which a contact material arranged in a floating state in the central portion of the advanced aeration tank is omitted . 本発明に係る生活排水高度浄化処理循環システムを構成する高度曝気槽内に設けられた一組の散気管と逆洗管を示した状態斜視図である。It is a state perspective view showing a pair of diffuser tubes and backwash tubes provided in an advanced aeration tank constituting the domestic wastewater advanced purification treatment circulation system according to the present invention. 請求項3に係る発明の一実施例である生活排水高度浄化処理循環システムであって高度曝気槽の槽内中央部に浮遊状態に配設した接触材を省略した、全体状態図である。It is a domestic wastewater advanced purification treatment circulation system which is one embodiment of the invention according to claim 3, and is an overall state diagram in which a contact material arranged in a floating state in the central portion of the advanced aeration tank is omitted . 本発明に係る生活排水高度浄化処理循環システムを構成する高度曝気槽内の槽内中央部に浮遊状態に配設した接触材と、散気管と、逆洗管との関係を示す状態斜視図である。In the state perspective view which shows the relationship between the contact material arrange | positioned in the floating state in the center part in the tank in the advanced aeration tank which comprises the domestic waste water advanced purification treatment circulation system which concerns on this invention, a diffuser pipe, and a backwash pipe is there.

本発明に係る請求項1記載の生活排水高度浄化処理循環システムは、乳酸菌、酵母、光合成細菌を主体とする有用な微生物の共生体と、油分解微生物とから成る複合有効微生物群を貯留し培養する複合有効微生物群培養槽を備え、該複合有効微生物群培養槽に連接して、汚濁物が含まれた生活排水と、複合有効微生物群培養槽にて培養された複合有効微生物群と、汚泥貯留槽に貯留された汚泥を混合し曝気することで複合有効微生物群が汚水中の汚れを分解しながら増殖する処理水量調整槽が設けられている。   The living wastewater advanced purification treatment circulation system according to claim 1 according to the present invention stores and cultures a complex effective microorganism group consisting of symbiotic microorganisms mainly composed of lactic acid bacteria, yeast and photosynthetic bacteria, and oil-degrading microorganisms. A combined effective microorganism group culture tank, connected to the combined effective microorganism group culture tank, domestic wastewater containing contaminants, a combined effective microorganism group cultured in the combined effective microorganism group culture tank, and sludge A treated water amount adjusting tank is provided in which sludge stored in the storage tank is mixed and aerated to allow the composite effective microorganism group to grow while decomposing dirt in the wastewater.

ここで言う複合有効微生物群の中で、乳酸菌、酵母、光合成細菌を主体とする有用な微生物の共生体とは、例えば、一般に市販され入手可能な有効微生物であるEM・1(商品名、(有)サン興産業製)やEM・アーゼロン(商品名、日本ライフ株式会社製)等をいい、油分解微生物とは、例えば油分解微生物バクテリアGT1000−HC(商品名、米国バイオジェネシス社製)が含まれているスノムワイドN(商品名、(有)アセンティ製)を言う。   In the complex effective microorganism group mentioned here, the symbiosis of useful microorganisms mainly composed of lactic acid bacteria, yeast, and photosynthetic bacteria is, for example, EM · 1 (trade name, ( Yes) Sanko Sangyo Co., Ltd.) and EM / Arsenon (trade name, manufactured by Nippon Life Co., Ltd.) Snome Wide N (trade name, manufactured by Asenti) is included.

処理水量調整槽で増殖した複合有効微生物群は汚水と共に水中ポンプによって隣接した高度曝気槽内に送り込まれるが、高度曝気槽内に送り込まれる複合有効微生物群量がより多くなるように、例えば処理水量調整槽と高度曝気槽の縦長さと横長さが同一であれば処理水量調整槽の深さを高度曝気槽の深さより深くして処理水量調整槽の容量を高度曝気槽の容量より大きくし、より多くの複合有効微生物群を処理水量調整槽内で増殖させることが望ましい。   The complex effective microorganisms grown in the treated water amount adjustment tank are sent into the advanced aeration tank adjacent to the sewage by the submersible pump.For example, the amount of treated water is increased so that the combined effective microorganism group sent into the advanced aeration tank is increased. If the vertical and horizontal lengths of the adjustment tank and the advanced aeration tank are the same, the depth of the treated water volume adjustment tank is made deeper than the depth of the advanced aeration tank so that the capacity of the treated water volume adjustment tank is larger than the capacity of the advanced aeration tank. It is desirable to grow a large number of complex effective microorganisms in a treated water amount adjustment tank.

より多くの複合有効微生物群が高度曝気槽に送られることで、高度曝気槽内での汚水の汚れを吸着分解処理する能力が増加する。   By sending more complex effective microorganisms to the advanced aeration tank, the ability to adsorb and decompose sewage dirt in the advanced aeration tank increases.

また処理水量調整槽は、これに連設された高度曝気槽に流入する複合有効微生物群量を調整する役割も有し、処理水量調整槽中に設けた例えば水中ポンプの適宜な作動により、高度曝気槽に送り込む汚水の量を調整する。 The treated water amount adjusting tank also has a role of adjusting the amount of complex effective microorganisms flowing into the advanced aeration tank connected to the treated water amount, and the advanced water pump is appropriately operated by, for example, an appropriate operation of the submersible pump provided in the treated water amount adjusting tank. Adjust the amount of sewage sent to the aeration tank.

高度曝気槽内では、汚水が高度曝気槽内に複数本設置された散気管から排出される空気によって曝気されるとともに、散気管の上方に近設し、散気管と90度の角度を持って配設された複数本の逆洗管からも同時に空気を勢いよく排出することで、汚水が高度曝気槽内でぶつかりあい、その結果、汚水中の有効微生物同士が高度曝気槽内で勢いよく衝突する。この衝突の際、有効微生物の一部はその細胞壁が壊れ、その中にある細胞質が浸出すると考えられる。浸出した細胞質はコロイド状で粘性、弾性を有するため、当該細胞質に汚水中の汚れが効率よく吸着されるものと判断される。 In the advanced aeration tank, sewage is aerated by the air discharged from the diffuser pipes installed in the advanced aeration tank, and is placed close to the upper part of the diffuser pipe so that it has an angle of 90 degrees with the diffuser pipe. By simultaneously exhausting air from multiple installed backwash pipes simultaneously, the sewage collides in the advanced aeration tank, and as a result, effective microorganisms in the sewage collide with each other in the advanced aeration tank. To do. During this collision, some of the effective microorganisms are thought to break their cell walls and leach out their cytoplasm. Since the leached cytoplasm is colloidal and has viscosity and elasticity, it is judged that dirt in the sewage is efficiently adsorbed to the cytoplasm.

高度曝気槽にて処理された汚水は、汚れが有効微生物の細胞質を略中心として高度に凝集した状態と成っていると考えられ、当該汚水はその状態で、高度曝気槽に連設された分離沈殿槽に送り込まれる。分離沈殿槽では、有効微生物の細胞質に効率よく吸着した汚れが高度に凝集した状態にあると考えられるため、該凝集物の単位当たりの重量が大きく、このため自重による沈殿速度も比較的早くなり、効率良く分離沈殿槽内の底部に沈殿する。また、これらと分離した液相である浄化水が上方に滞留する。   The sewage treated in the advanced aeration tank is considered to be in a state in which the dirt is highly agglomerated mainly with the cytoplasm of the effective microorganisms, and the sewage is separated in this state continuously connected to the advanced aeration tank. It is sent to the settling tank. In the separation / sedimentation tank, it is considered that the dirt efficiently adsorbed to the cytoplasm of the effective microorganisms is in a highly aggregated state, so the weight per unit of the aggregate is large, and the sedimentation rate due to its own weight is also relatively fast. Precipitates efficiently at the bottom of the separation and precipitation tank. Moreover, the purified water which is a liquid phase separated from these stays upward.

分離沈殿槽は少なくとも2個直列配置で連接されていて、高度曝気槽に連設した第一分離沈殿槽では、有効微生物の細胞質に吸着した汚れが一部分解途中にあるため、分解時に発生したガスによって、上記凝集状態にある汚れの一部は上方に持ち上げられ浮遊することがある。上方に浮遊した凝集物は通常スカムと呼称されているが、当該スカムは連接している第二分離沈殿槽に流入しないように処理されるように成っている。 At least two separate sedimentation tanks are connected in series, and in the first separate sedimentation tank connected to the advanced aeration tank, the dirt adsorbed on the cytoplasm of the active microorganisms is partly in the process of decomposition. Accordingly, a part of the dirt in the aggregated state may be lifted upward and floated. The agglomerates floating above are usually called scum, but the scum is treated so as not to flow into the second separation and sedimentation tank connected thereto.

該処理は、まず固相である汚泥をエアーリフトによって吸い上げることによって汚泥貯留槽に送り、第一分離沈殿槽内の水位を下げる。その後、第一分離沈殿槽内に設けられた散気管から空気を排出し曝気する。該曝気によって、スカムに吸着したガスが払い除かれて、該スカムは第一分離沈殿槽の底部に沈殿し液相と分離する。このような処理により第二分離沈殿槽にはスカムが流入しない。 In the treatment, first, sludge as a solid phase is sucked up by an air lift and sent to a sludge storage tank to lower the water level in the first separation and precipitation tank. Thereafter, air is discharged from the air diffuser provided in the first separation / sedimentation tank and aerated. The gas adsorbed on the scum is removed by the aeration, and the scum is precipitated at the bottom of the first separation / precipitation tank and separated from the liquid phase. By such treatment, scum does not flow into the second separation / sedimentation tank.

一方、第一分離沈殿槽や第二分離沈殿槽である複数の分離沈殿槽内の内壁は例えばポリエチレンテレフタレート(PET)樹脂のように表面が平滑な仕上げとなっていることが望ましく、十分に表面が平滑である場合は汚水中の凝集状態にある汚れが内壁面に付着することが無く、より高速で固相と液相の分離が行われる。 On the other hand, the inner walls of the plurality of separation / precipitation tanks, which are the first separation / precipitation tank, desirably have a smooth finish like, for example, polyethylene terephthalate (PET) resin. When is smooth, dirt in the coagulated state in the sewage does not adhere to the inner wall surface, and the solid phase and the liquid phase are separated at a higher speed.

次に、第一分離沈殿槽で分離された液相は越流堰を越えて第二分離沈殿槽に送り込まれ、第一分離沈殿槽で分離沈殿された固相である汚泥は、エアーリフトによって吸い上げられることにより回収され、汚泥貯留槽に送り込まれるように成っている。 Next, the liquid phase separated in the first separation / sedimentation tank passes over the overflow weir and is sent to the second separation / sedimentation tank, and the sludge, which is the solid phase separated and settled in the first separation / sedimentation tank, is removed by an air lift. It is collected by being sucked up and sent to a sludge storage tank.

第二分離沈殿槽では流入してくる液相である水は、高度に浄化されているため、上記第一分離沈殿槽のように、スカムが発生することがなく、したがって第二分離沈殿槽内には、原則として空気を排出して曝気を行う散気管を設ける必要はない。しかし、より高度に浄化する目的で散気管を設けてもよく、さらにはより多くの数の分離沈殿槽を直列に連設しても良い。   In the second separation / sedimentation tank, the water, which is the liquid phase that flows in, is highly purified, so that no scum is generated as in the first separation / settlement tank. In principle, it is not necessary to provide an air diffuser that discharges air and performs aeration. However, a diffuser tube may be provided for the purpose of purifying to a higher degree, and a larger number of separation and sedimentation tanks may be connected in series.

第二分離沈殿槽で分離された水は高度に浄化されていて、当該浄化水は最後尾となる第二分離沈殿槽に連設された滅菌器で塩素や紫外線等を利用して細菌等が滅菌処理され、生活水として再利用される。   The water separated in the second separation / sedimentation tank is highly purified, and the purified water is sterilized in the second separation / sedimentation tank, which is the last one. Sterilized and reused as domestic water.

また第二分離沈殿槽で分離された水の一部は前記複合有効微生物群培養槽内に滅菌器を通さずに供給され、複合有効微生物群の培養に利用される。   A part of the water separated in the second separation / precipitation tank is supplied to the complex effective microorganism group culture tank without passing through the sterilizer, and used for culturing the complex effective microorganism group.

次に本発明に係る請求項2記載の生活排水高度浄化処理循環システムは、上記請求項1記載の生活排水高度浄化処理循環システムにおいて、直列配置の複数の分離沈殿槽のうち最後尾の分離沈殿槽に連接して沈殿貯水槽が設けられていて、該沈殿貯水槽では最後尾の分離沈殿槽にて分離された液相である浄化水を、沈殿貯水槽内に設けられた散気管及び逆洗管から排出される空気によって同時に曝気し、万が一にも含まれる微量の有機物を分離する。   Next, the domestic wastewater advanced purification treatment circulation system according to claim 2 according to the present invention is the domestic wastewater advanced purification treatment circulation system according to claim 1, wherein the last separation precipitation in a plurality of serially arranged separation sedimentation tanks. A sedimentation tank is provided in connection with the tank, and in the sedimentation tank, purified water, which is a liquid phase separated in the last separated sedimentation tank, is supplied to the diffuser pipe and the reverse provided in the sedimentation tank. At the same time, it is aerated by the air exhausted from the washing tube to separate a trace amount of organic matter.

有機物が分離された後の浄化水は、滅菌器に送られて滅菌処理され、生活水として再利用される。また沈殿貯水槽で分離された浄化水の一部は前記複合有効微生物群培養槽内に滅菌器を通さずに供給され、複合有効微生物群の培養に利用される。 The purified water from which the organic matter has been separated is sent to a sterilizer, sterilized, and reused as domestic water. Further, a part of the purified water separated in the precipitation water tank is supplied to the complex effective microorganism group culture tank without passing through the sterilizer and used for culturing the complex effective microorganism group.

また本発明に係る請求項3記載の生活排水高度浄化処理循環システムは、上記請求項1記載の生活排水高度浄化処理循環システムにおいて、直列配置の複数の分離沈殿槽のうち、最後尾の分離沈殿槽に連接して第一貯水槽を設け、最後尾の分離沈殿槽にて分離された浄化水を一時貯留する。第一貯水槽には沈殿貯水槽が連設されていて、第一貯水槽より流入する浄化水は、沈殿貯水槽内に設けられた散気管及び逆洗管から排出される空気によって同時に曝気され、万が一にも含まれる微量の有機物を分離する。   Moreover, the domestic wastewater advanced purification treatment circulation system of Claim 3 which concerns on this invention is the domestic wastewater advanced purification treatment circulation system of Claim 1 in the separation separation precipitation of the last among several separated sedimentation tanks arranged in series. A first water storage tank is provided in connection with the tank, and the purified water separated in the last separation and precipitation tank is temporarily stored. A settling tank is connected to the first tank, and the purified water flowing from the first tank is simultaneously aerated by the air discharged from the air diffuser and backwash pipe provided in the set tank. In the unlikely event that a trace amount of organic matter is separated.

沈殿貯水槽には第二貯水槽が連設されていて、沈殿貯水槽から排出される高度に浄化された水は一時的に該第二貯水槽に貯留する。第二貯水槽から排出される浄化水は滅菌器を通して生活水として再利用される。また第二貯水槽から排出される浄化水の一部は複合有効微生物群培養槽内に滅菌器を通さずに供給され、複合有効微生物群の培養に利用される。   A second water tank is connected to the precipitation water tank, and highly purified water discharged from the precipitation water tank is temporarily stored in the second water tank. The purified water discharged from the second water tank is reused as domestic water through a sterilizer. A part of the purified water discharged from the second water storage tank is supplied to the complex effective microorganism group culture tank without passing through the sterilizer, and is used for culturing the complex effective microorganism group.

また本発明に係る請求項4記載の生活排水高度浄化処理循環方法は、生活排水を請求項1乃至請求項3のいずれかに記載の生活排水高度浄化処理循環システムにより処理することにより浄化して生活水として再利用し、その汚濁物を含んだ生活排水をさらに同一の請求項1乃至請求項3のいずれかに記載の生活排水高度浄化処理循環システムにより処理して浄化し生活水として繰り返し再利用するように成っている。 According to a fourth aspect of the present invention, there is provided a domestic wastewater advanced purification treatment and circulation method which purifies the domestic wastewater by treating it with the domestic wastewater advanced purification treatment circulation system according to any one of the first to third aspects. Recycled as domestic water, the domestic wastewater containing the pollutant is further treated and purified by the same domestic wastewater advanced purification treatment circulation system according to any one of claims 1 to 3, and reused as domestic water repeatedly. It is made to use.

以下図1乃至図4に基づき詳細に説明する。   This will be described in detail below with reference to FIGS.

図1は請求項1に係る発明の一実施例である生活排水高度浄化処理循環システムであって高度曝気槽の槽内中央部に浮遊状態に配設した接触材を省略した、全体状態図である。槽内中央部に接触材を浮遊状態に配設した高度曝気槽の一実施例は図4に示している。1は人々が生活をする家屋であって、台所、風呂、洗面所、便所などからの排水をすべて回収し、回収された該生活排水は図1において処理水量調整槽20の左端上部に流れ込むように排水回収管2が家屋1と処理水量調整槽20に連設されている。 FIG. 1 is a diagram showing an entire state diagram of a domestic wastewater advanced purification treatment circulation system which is an embodiment of the invention according to claim 1, omitting a contact material arranged in a floating state in the central portion of the advanced aeration tank . is there. FIG. 4 shows an embodiment of an advanced aeration tank in which a contact material is placed in a floating state in the center of the tank. 1 is a house where people live and collects all wastewater from kitchens, baths, toilets, toilets, etc., and the collected domestic wastewater flows into the upper left end of the treated water amount adjustment tank 20 in FIG. In addition, a drainage collecting pipe 2 is connected to the house 1 and the treated water amount adjusting tank 20.

処理水量調整槽20の左端上部には排水回収管2のほかに、生活排水中の汚濁物を分解するための複合有効微生物群を投入する複合有効微生物群投入管11が連設されると共に、汚水を処理した後の汚泥を貯留する汚泥貯留槽60中の汚泥を再度分解処理するために、該汚泥の一部が流下する汚泥流下管61が連設されている。   In addition to the drainage recovery pipe 2, a combined effective microorganism group input pipe 11 for introducing a composite effective microorganism group for decomposing pollutants in domestic wastewater is connected to the upper left end of the treated water amount adjustment tank 20. In order to decompose again the sludge in the sludge storage tank 60 that stores the sludge after treating the sludge, a sludge down pipe 61 through which a part of the sludge flows down is connected.

複合有効微生物群投入管11の他端は前記複合有効微生物群を貯留し培養する複合有効微生物群培養槽10の底部に連設され、複合有効微生物群培養槽10の上部には浄化水投入管59が連設されている。浄化水投入管59からは後述の第二分離沈殿槽50にて分離された浄化水が流入するように成っている。 The other end of the composite effective microorganism group input tube 11 is connected to the bottom of the composite effective microorganism group culture tank 10 for storing and culturing the composite effective microorganism group, and a purified water input pipe is disposed above the composite effective microorganism group culture tank 10. 59 is continuously provided. The purified water separated in the second separation / precipitation tank 50 described later flows from the purified water supply pipe 59.

また、複合有効微生物群培養槽10内には、散気エアー管12が配設されていて、浄化水投入管5から流下した浄化水中で複合有効微生物群が効率よく培養されるように、適宜送気ポンプ13から送られる空気が、散気エアー管12の先端にT字状に固着された散気管12a、12bから空気泡となって排出され曝気されるように成している。 The composite Valid microbial culture tank 10, as the air diffuser air pipe 12 have been disposed, the composite effective microorganisms can be efficiently cultured in purifying water flowing down from the purified water feeding pipe 5 9, The air supplied from the air supply pump 13 is discharged as air bubbles from the air diffusion pipes 12a and 12b fixed in a T-shape to the tip of the air diffusion pipe 12, and aerated.

複合有効微生物群は、EM・1(商品名、(有)サン興産業製)とスノムワイドN(商品名、(有)アセンティ製)の混合物であり、複合有効微生物群培養槽10には、水100リットルに対してEM・1を500ccとスノムワイドNを500g投入し、さらには破砕した野菜屑と天ぷら油等の植物性廃油を各々500g投入して約3日間曝気し培養した複合有効微生物群を貯留している。当該複合有効微生物群は、処理する生活排水の量にもよるが月に1回程度、新たに培養することで十分な量を確保することができる。   The complex effective microorganism group is a mixture of EM · 1 (trade name, manufactured by Sanko Sangyo) and SNOMWIDE N (trade name, manufactured by Asenti), and the complex effective microorganism group culture tank 10 contains water. 100 liters of 500 ml of EM · 1 and 500 g of SNOMWIDE N were added, and 500 g of vegetable waste oil such as crushed vegetable waste and tempura oil was added, and a complex effective microorganism group which was aerated and cultured for about 3 days. Reserved. The complex effective microorganism group can ensure a sufficient amount by newly culturing about once a month depending on the amount of domestic wastewater to be treated.

一方、前記処理水量調整槽20内には複数本の散気エアー管21が上方から下方に向かって配設されていて、散気エアー管21の上部は水平送気管22と連設され、水平送気管22は空気を送り込む送気ポンプ23と連設している。散気エアー管21の先端にはT字状に散気管21a、21bが固着され、送気ポンプ23から送られる空気は水平送気管22及び散気エアー管21を通って散気管21a、21bから空気泡となって排出し、処理水量調整槽20中の汚水を曝気するように成している。 Meanwhile, the volume of treated water regulation tank a plurality of the 20 diffuser air pipe 21 have been arranged as they go downward, the upper portion of the diffuser air pipe 21 is provided continuously with the horizontal flue 22, the horizontal The air supply pipe 22 is connected to an air supply pump 23 for supplying air. Diffuser air pipe 21 of the pipe 21a diffuser in a T-shape the tip, 21b are fixed, the air sent from the air pump 23 pipe 21a diffusing through the horizontal flue 22 and diffuser air pipe 21, from 21b The air bubbles are discharged and the sewage in the treated water amount adjusting tank 20 is aerated.

処理水量調整槽20中の汚水は図1において左から右へと徐々に流下移動するように成っていて、該処理水量調整槽20の右端には、処理水量調整槽20中の汚水を高度曝気槽30内に送り込む汚水送流管24が連設され、汚水送流管24の入口端部は処理水量調整槽20内の汚水中に埋設するように配置されると共に、その先端部には水中ポンプ25が固着されている。また汚水送流管24の他端は高度曝気槽30の左端に連設され、前記水中ポンプ25の駆動により送られる汚水が高度曝気槽30内に流入するよう成っている。   The sewage in the treated water amount adjusting tank 20 gradually flows down from the left to the right in FIG. 1, and the sewage in the treated water amount adjusting tank 20 is highly aerated at the right end of the treated water amount adjusting tank 20. A sewage flow pipe 24 to be fed into the tank 30 is continuously provided, and an inlet end of the sewage flow pipe 24 is disposed so as to be buried in the sewage in the treated water amount adjusting tank 20, and a water flow is provided at the tip of the sewage flow pipe 24. The pump 25 is fixed. The other end of the sewage flow pipe 24 is connected to the left end of the advanced aeration tank 30 so that the sewage sent by driving the submersible pump 25 flows into the advanced aeration tank 30.

処理水量調整槽20内では複合有効微生物群が汚水と混合されながら曝気されるため、汚水中の汚れは複合有効微生物群によって分解されながら、複合有効微生物群は逆に増殖する状態と成っている。複合有効微生物群が含まれた汚水は汚水送流管24によって高度曝気槽30に送られるが、高度曝気槽30に送られる複合有効微生物群の量はより多いほうが好ましく、そのため図1においては処理水量調整槽20の容量は高度曝気槽30の容量より大きくなるように処理水量調整槽20の深さが高度曝気槽30の深さより深く成っている。   Since the composite effective microorganism group is aerated in the treated water amount adjusting tank 20 while being mixed with the sewage, the composite effective microorganism group grows in reverse while the dirt in the sewage is decomposed by the composite effective microorganism group. . The sewage containing the complex effective microorganism group is sent to the advanced aeration tank 30 by the sewage flow pipe 24, but it is preferable that the amount of the complex effective microorganism group sent to the advanced aeration tank 30 is larger. The depth of the treated water amount adjusting tank 20 is deeper than the depth of the advanced aeration tank 30 so that the capacity of the water amount adjusting tank 20 is larger than the capacity of the advanced aeration tank 30.

また水中ポンプ25にはフロートスイッチ(図示せず)が連設されていて、処理水量調整槽20中の水量が規定以上になった際に自動的にフロートスイッチが作動して水中ポンプ25が駆動し、処理水量調整槽20内の汚水が高度曝気槽30内に汚水送流管24を通して流下するように成っている。   In addition, a float switch (not shown) is connected to the submersible pump 25. When the amount of water in the treated water amount adjusting tank 20 exceeds a specified level, the float switch is automatically activated to drive the submersible pump 25. The sewage in the treated water amount adjustment tank 20 flows down into the advanced aeration tank 30 through the sewage flow pipe 24.

高度曝気槽30内には図2に示すように先端部にT字状に散気管31a、31bが固着された散気エアー管31と、同じく先端部に逆洗管32a、32bが固着された逆洗エアー管32が、その散気管31a、31bと逆洗管32a、32bにおいて90度の角度を持ってクロスするように設けられ、図2に示す散気エアー管31と逆洗エアー管32をそれぞれ2本(合計4本)を一組として、図1の実施例では2組が高度曝気槽30内に配設されている。なお散気エアー管31と逆洗エアー管32の配設本数は、曝気処理する汚水量に応じて増減させることができる。 In the advanced aeration tank 30, as shown in FIG. 2, a diffused air pipe 31 having T-shaped diffused pipes 31a and 31b fixed to the tip part and backwashing pipes 32a and 32b fixed to the tip part are also provided. backwash air pipe 32, the aeration tube 31a, 31b and the backwash tube 32a, at an angle of 90 degrees in the 32b provided so as to cross, diffuser air pipe 31 and the backwash air tube 32 shown in FIG. 2 In the embodiment shown in FIG. 1, two sets are arranged in the advanced aeration tank 30. The number of the diffused air pipes 31 and the backwash air pipes 32 can be increased or decreased according to the amount of sewage to be aerated.

散気エアー管31と逆洗エアー管32の上部端部は水平送気管33と連設され、水平送気管33は空気を送り込む送気ポンプ34と連設している。送気ポンプ34から送り込まれる空気は水平送気管33、散気エアー管31、逆洗エアー管32を通って散気管31a、31b、逆洗管32a、32bから空気泡となって同時に排出し、高度曝気槽30内の汚水を曝気する。ここで散気エアー管31の散気管31a、31bは逆洗エアー管32の逆洗管32a、32bに対して90度の角度を持って配設されているため、曝気される汚水は高度曝気槽30内で激しくぶつかり合う状態と成る。このため汚水中に含まれる有効微生物は、前述のように互いに勢いよく衝突し、衝突した有効微生物の一部はその細胞壁が壊れ、その中にある細胞質が浸出するものと考えられる。浸出した細胞質はコロイド状で粘性、弾性を有するため、当該細胞質に排水中の汚れが効率よく吸着されるものと判断される。 The upper ends of the diffused air pipe 31 and the backwash air pipe 32 are connected to a horizontal air supply pipe 33, and the horizontal air supply pipe 33 is connected to an air supply pump 34 for feeding air. Air fed from the air pump 34 is discharged simultaneously become air bubbles from the horizontal flue 33, diffuser air tube 31, the backwash air tube 32 through to diffusion pipe 31a, 31b, the backwash tube 32a, 32b, The sewage in the advanced aeration tank 30 is aerated. Here diffusing pipe 31a of diffuser air tube 31, because 31b is disposed at an angle of 90 degrees with respect to the backwash tube 32a, 32b of the backwash air pipe 32, sewage altitude aeration is aerated It will be in the state which collides violently in the tank 30. FIG. For this reason, it is considered that the effective microorganisms contained in the sewage collide vigorously with each other as described above, and some of the collided effective microorganisms break the cell wall, and the cytoplasm contained therein is leached. Since the leached cytoplasm is colloidal and has viscosity and elasticity, it is judged that dirt in the waste water is efficiently adsorbed to the cytoplasm.

高度曝気槽30には、曝気水送流管35が連設されていて、前記水中ポンプ25の駆動により処理水量調整槽20内の汚水が高度曝気槽30内に送り込まれて、該高度曝気槽30内の水量が一定以上となると、自然に、隣接されている第一分離沈殿槽40内に設けられた下部が開放された円筒形状である第一縦流入管41内の略上部に流入するように成っている。   The advanced aeration tank 30 is connected with an aeration water flow pipe 35, and the sewage in the treated water amount adjusting tank 20 is sent into the advanced aeration tank 30 by driving the submersible pump 25. When the amount of water in the tank 30 exceeds a certain level, the water naturally flows into a substantially upper part of the first vertical inflow pipe 41 having a cylindrical shape with an open lower part provided in the adjacent first separation and precipitation tank 40. It ’s like that.

第一縦流入管41内に流入する汚水は、高度曝気槽30にて高度に曝気処理された結果、汚れが有効微生物の細胞質を略中心として高度に凝集した状態と成っていると考えられるため、該凝集した汚れは第一縦流入管41内で緩やかな流下により第一分離沈殿槽40の底部に沈殿する。   Since the sewage flowing into the first vertical inflow pipe 41 is highly aerated in the advanced aeration tank 30, it is considered that the dirt is highly agglomerated mainly with the cytoplasm of effective microorganisms as a center. The agglomerated dirt settles down at the bottom of the first separation / sedimentation tank 40 by gentle flow in the first vertical inflow pipe 41.

第一縦流入管41の下端部は、高度曝気槽30にて高度に曝気処理された汚水が第一縦流入管41内の上部に流入する際、すでに第一分離沈殿槽40の底部に沈殿している固相である沈殿物を舞い上がらせることがないように、第一沈殿分離槽40の底面より上方に配設されている。 The lower end of the first vertical inflow pipe 41 has already settled at the bottom of the first separation / precipitation tank 40 when the sewage that has been highly aerated in the advanced aeration tank 30 flows into the upper part of the first vertical inflow pipe 41. It is disposed above the bottom surface of the first precipitation separation tank 40 so that the precipitate, which is the solid phase, does not rise.

このように第一分離沈殿槽40の底面には、汚れが凝集した沈殿物が滞留し、一方、第一分離沈殿槽40の上部には汚れと分離した浄化水が滞留する。 As described above, the sediment in which dirt is agglomerated stays on the bottom surface of the first separation / precipitation tank 40, while the purified water separated from the dirt stays in the upper part of the first separation / precipitation tank 40.

滞留した浄化水は順次越流堰42を越え、分離浄化水送流管43を通って、第一分離沈殿槽40に対して直列配置されている第二分離沈殿槽50内に設けられ下部が開放された円筒形状である第二縦流入管51内の略上部に流入する。第二縦流入管51内に流入する浄化水は浄化されているため、ほとんど凝集した汚れを含まないが、第二縦流入管51内を緩やかに流下することにより、微量含まれることがあるかもしれない凝集した汚れが第二分離沈殿槽50の底部に沈殿し、第二分離沈殿槽50の上部には高度に浄化された浄化水が滞留する。   The retained purified water sequentially passes over the overflow weir 42, passes through the separated purified water feed pipe 43, and is provided in a second separation / precipitation tank 50 arranged in series with respect to the first separation / precipitation tank 40. It flows into the substantially upper part in the second vertical inflow pipe 51 having an open cylindrical shape. Since the purified water flowing into the second vertical inflow pipe 51 is purified, it hardly contains agglomerated dirt, but it may be contained in a small amount by gently flowing down in the second vertical inflow pipe 51. The agglomerated dirt that cannot be settled at the bottom of the second separation and precipitation tank 50, and highly purified purified water stays at the top of the second separation and precipitation tank 50.

なお、第二分離沈殿槽50内に設けられた第二縦流入管51の下端部は、前記第一縦流入管41と同様に、第一分離沈殿槽40にて汚れと分離された浄化水が第二縦流入管51内の上部に流入する際、万が一にも第二分離沈殿槽50の底部に沈殿している固相である沈殿物を舞い上がらせることがないように、第二沈殿分離槽50の底面より上方に配設されている。   In addition, the lower end part of the 2nd vertical inflow pipe 51 provided in the 2nd separation / precipitation tank 50 is the purified water separated from the dirt in the 1st separation / precipitation tank 40 similarly to the said 1st vertical inflow pipe 41. When the liquid flows into the upper part of the second vertical inflow pipe 51, the second sedimentation separation is performed so that the sediment that is the solid phase precipitated at the bottom of the second separation / precipitation tank 50 should not be allowed to rise. The tank 50 is disposed above the bottom surface.

第一分離沈殿槽40内にはスカム散気エアー管44が上下に配設されていて、スカム散気エアー管44の下部先端には散気管44a、44bがT字状に固着されている。スカム散気エアー管44の上部は送気ポンプ45と連設されていて、第一分離沈殿槽40の上部に前記スカムが浮遊した場合に、送気ポンプ45から空気を送り込み、散気管44a、44bから空気泡を排出し曝気することで、浮遊しているスカムに付着したガスを払い除くように成っている。 The first separating settling tank 40 by scum diffuser air pipe 44 are disposed vertically, trachea 44a diffusing the lower tip of the scum diffuser air tube 44, 44b is secured in a T-shape. The upper part of the scum aeration air pipe 44 is connected to the air supply pump 45. When the scum floats on the upper part of the first separation sedimentation tank 40, air is supplied from the air supply pump 45, and the air diffusion pipe 44a, By discharging air bubbles from 44b and aeration, the gas adhering to the floating scum is removed.

図1においては、第二分離沈殿槽50内にも、スカム散気エアー管54が上下に配設されていて、万が一にも第二分離沈殿槽50内にスカムが浮遊した際には、スカム散気エアー管54の下部先端にT字状に固着されたスカム散気管54a、54bより、送気ポンプ55から送り込まれた空気が排出され空気泡となって曝気されるように成っている。 In FIG. 1, the scum diffuser air pipe 54 is also provided in the second separation / sedimentation tank 50, so that if the scum floats in the second separation / sedimentation tank 50, From the scum diffuser tubes 54a and 54b fixed in a T-shape to the lower end of the diffuser air tube 54, the air sent from the air supply pump 55 is discharged and aerated as air bubbles.

第一縦流入管41及び第二縦流入管51の中央部にはエアーリフト46、56が設けられていて、それぞれ第一分離沈殿槽40の底部に沈殿した汚泥又は第二分離沈殿槽50の底部に沈殿した汚泥を吸い上げ、汚泥回収管47、57を通って汚泥貯留槽回収管62を経て、汚泥貯留槽60内に回収されるように成っている。   Air lifts 46 and 56 are provided at the central portions of the first vertical inflow pipe 41 and the second vertical inflow pipe 51, respectively, and sludge settled at the bottom of the first separation / precipitation tank 40 or the second separation / precipitation tank 50. The sludge settled on the bottom is sucked up, passed through the sludge collection pipes 47 and 57, and then collected in the sludge storage tank 60 through the sludge storage tank collection pipe 62.

第二分離沈殿槽50の上部に滞留している高度に浄化された浄化水は、順次越流堰52を超え、高度浄化水送流管58を流下して滅菌器70で塩素により滅菌され、生活水として家屋1内で再利用されるように成っている。滅菌器70は塩素による滅菌のほか、紫外線照射によって滅菌するもの、またはこれらを併用したものであっても良い。なお高度浄化水送流管58の滅菌器70の手前位置(図1においては滅菌器70の右側)には着脱自在のスクリーンを内蔵したスクリーンボックスが設けられ(図示せず)、高度浄化水送流管58内を流下する浄化水中の浮遊ゴミを該スクリーンにて除去するように成している。このため滅菌器70には浮遊ゴミは流入しない。 The highly purified purified water staying in the upper part of the second separation / precipitation tank 50 sequentially passes the overflow weir 52, flows down the highly purified water feed pipe 58, and is sterilized with chlorine in the sterilizer 70, It is designed to be reused in the house 1 as living water. The sterilizer 70 may be sterilized by irradiating with ultraviolet rays in addition to sterilization by chlorine, or a combination of these. A screen box (not shown) with a detachable screen is provided at a position of the advanced purified water feed pipe 58 in front of the sterilizer 70 (on the right side of the sterilizer 70 in FIG. 1). The screen is used to remove floating dust in the purified water flowing down in the flow pipe 58. For this reason, floating dust does not flow into the sterilizer 70.

表1乃至表3に滅菌器70で滅菌された水の水質検査結果を示す。該水質検査は、(株)ミズラボ(計量証明事業登録 東京都第1290号)で行ったものである。 Tables 1 to 3 show the water quality test results of the water sterilized by the sterilizer 70. The water quality test was conducted at Mizu Lab Co., Ltd. (registered for measurement certification business, Tokyo No. 1290).

表1は平成15年度厚生労働省令101号水質基準に関する省令による検査方法による15項目の検査結果を、表2は全窒素、全りん、及びアンモニア性窒素の検査結果を、表3は5項目の検査結果を示しており、例えばBODは1と成っていて飲用に適するほどに高度に浄化されている。 Table 1 shows the inspection results of 15 items according to the inspection method according to the Ministerial Ordinance No. 101 of the Ministry of Health, Labor and Welfare No. 101 of Water Quality Standard, Table 2 shows the inspection results of total nitrogen, total phosphorus, and ammonia nitrogen, and Table 3 shows the five items The test results are shown. For example, BOD is 1 and it is highly purified so as to be suitable for drinking.

Figure 0004482717
Figure 0004482717

Figure 0004482717
Figure 0004482717

Figure 0004482717
Figure 0004482717

越流堰52を超えた高度に浄化された浄化水の一部は滅菌器70を通さずに浄化水投入管59を通って複合有効微生物群培養槽10に送られ再利用される。なお滅菌器70を通過した浄化水を家屋1内に安定して供給するため滅菌器70に連設して、該浄化水を一時的に貯留する貯留水槽を設けることができ、貯留水槽の容量を超える量の浄化水は排水回収管2に直接流下させるように形成することもできる。   A part of the highly purified purified water exceeding the overflow weir 52 passes through the purified water input pipe 59 without passing through the sterilizer 70 and is sent to the complex effective microorganism group culture tank 10 for reuse. In addition, in order to stably supply the purified water that has passed through the sterilizer 70 to the house 1, it is possible to provide a storage tank that is connected to the sterilizer 70 and temporarily stores the purified water. It is also possible to form the purified water in an amount exceeding that directly in the drainage recovery pipe 2.

汚泥貯留槽60内には散気エアー管63が上下方向に配設されていて、その先端にはT字状に散気管63a、63bが固着され、散気エアー管63の上部は送気ポンプ64に連設されている。 Diffuser air pipe 63 to the sludge storage tank 60 is not disposed in the vertical direction, the trachea 63a diffusing in a T-shape at its distal end, 63 b is fixed, the upper portion of the diffuser air pipe 63 air pump 64 is continuously provided.

汚泥貯留槽60内に貯留されている汚泥は、徐々に固化していくため、適宜空気ポンプ64より空気を送り、散気エアー管63の散気管63a、63bより空気泡を排出し曝気することで汚泥を軟化させ、汚泥流下管61から処理水量調整槽20に該汚泥が流下可能に成している。 Since the sludge stored in the sludge storage tank 60 is gradually solidified, air is appropriately sent from the air pump 64, and air bubbles are discharged from the air diffusion pipes 63a and 63b of the air diffusion air pipe 63 and aerated. Thus, the sludge is softened so that the sludge can flow from the sludge flow down pipe 61 to the treated water amount adjusting tank 20.

なお、上記実施例1に係る生活排水高度浄化処理循環システムによって生活排水を繰り返し再利用した結果、浄化処理するための水量が不足する場合は、生活排水と共に河川や池等の水や雨水を排水回収管2を介して補給するように形成することができる。 In addition, as a result of repeated reuse of domestic wastewater by the domestic wastewater advanced purification treatment circulation system according to the first embodiment, when the amount of water for purification treatment is insufficient, water and rainwater such as rivers and ponds are drained together with domestic wastewater. It can be configured to replenish via the collection tube 2.

次に実施例2について説明する。図3は請求項3に係る発明の一実施例である生活排水高度浄化処理循環システムであって高度曝気槽の槽内中央部に浮遊状態に配設した接触材を省略した、全体状態図である。家屋1、複合有効微生物群培養槽10、処理水量調整槽20、高度曝気槽30、第一分離沈殿槽40、第二分離沈殿槽50、汚泥貯留槽60、滅菌器70の構成は前記実施例1と同様であるため説明を省略し、ここでは第二沈殿分離槽50に連設した第一貯水槽80と、これに連設した沈殿貯水槽90及びこれに連設した第二貯水槽85の構成について説明する。 Next, Example 2 will be described. FIG. 3 is a diagram showing an entire state diagram of a domestic wastewater advanced purification treatment circulation system which is an embodiment of the invention according to claim 3, omitting a contact material arranged in a floating state in the central portion of the advanced aeration tank . is there. The configuration of the house 1, the combined effective microorganism group culture tank 10, the treated water amount adjustment tank 20, the advanced aeration tank 30, the first separation / precipitation tank 40, the second separation / precipitation tank 50, the sludge storage tank 60, and the sterilizer 70 are the same as those in the above embodiment. 1, the description is omitted. Here, a first water storage tank 80 connected to the second precipitation separation tank 50, a precipitation water storage tank 90 connected to the first water storage tank 90, and a second water storage tank 85 connected to the first water storage tank 85. The configuration of will be described.

第二沈殿分離槽50内の越流堰52を超えて流下する高度に浄化された浄化水は、第一貯留水配送管81を通って第一貯水槽80内の中央部に設けられ下部が開放された円筒形状である第一貯水槽縦流入管82内の略上部に流入する。   The highly purified purified water flowing down over the overflow weir 52 in the second sedimentation separation tank 50 is provided in the central part of the first water storage tank 80 through the first stored water delivery pipe 81 and the lower part is It flows into the substantially upper part in the first water tank vertical inflow pipe 82 having an open cylindrical shape.

第一貯水槽80内に貯留された浄化水は、エアーリフト83によって吸い込まれて、沈殿貯水槽配水管84を通り、該沈殿貯水槽配水管84が連設されている沈殿貯水槽90に投入されるように成っている。なお本実施例ではエアーリフト83により送水しているが、これに替えて水中ポンプにより送水してもよい。   The purified water stored in the first water storage tank 80 is sucked in by the air lift 83, passes through the precipitation water tank distribution pipe 84, and is input to the precipitation water storage tank 90 connected to the precipitation water storage tank distribution pipe 84. It is made to be. In the present embodiment, water is supplied by the air lift 83, but water may be supplied by a submersible pump instead.

沈殿貯水槽90内は浄化水が図3において左から右へと順次流下可能なように、4枚の開放隔壁91a、91b、91c、91dで仕切られている。沈殿貯水槽配水管84より流下する浄化水は、まず第一室92に入る。第一室92、第二室93、第三室94には、図2で示すような散気エアー管96及び逆洗エアー管97が配設されていて、散気エアー管96の先端には散気管がT字状に固着され、逆洗エアー管97の先端には逆洗管がT字状に固着され、他端は水平送気管99に連設されている。水平送気管99には送気ポンプ100が連設されていて、浄化水の状態により送気ポンプ100から空気が送られて、散気管及び逆洗管から同時に空気泡を排出して曝気処理が可能なように成している。 The settling tank 90 is partitioned by four open partition walls 91a, 91b, 91c, 91d so that purified water can flow sequentially from left to right in FIG. Purified water flowing down from the settling tank distribution pipe 84 first enters the first chamber 92. First chamber 92, second chamber 93, the third chamber 94, have been diffuser air pipe 96 and the backwash air pipe 97 is arranged as shown in Figure 2, the tip of the diffuser air tube 96 A diffuser tube is fixed in a T shape, a backwash tube is fixed in a T shape at the tip of the backwash air tube 97, and the other end is connected to a horizontal air supply tube 99. The horizontal flue 99 air pump 100 is being continuously provided, and air is sent from the air pump 100 depending on the state of the clarified water, aeration and discharging air bubbles at the same time from the aeration tube and backwash tube It is made possible.

当該曝気処理により、第一室92、第二室93、第三室94内の浄化水に万が一にも含まれる有機物を分離することができる。   By the aeration treatment, the organic matter contained in the purified water in the first chamber 92, the second chamber 93, and the third chamber 94 can be separated.

第三室94より流下した浄化水は第四室95の上部に移動するように成っていて、第四室95には活性炭若しくはこれに準ずるろ材で作製されたろ過材98が配設されている。第四室95の上部の浄化水は該ろ過材98を透過して第四室95の下部に移動する。その際浄化水はろ過材98によってさらに浄化される。ろ過材98を通過した浄化水は開放隔壁91dの下部を通過して第二貯留水配送管86を通って第二貯水槽85内に流下する。   The purified water flowing down from the third chamber 94 is moved to the upper part of the fourth chamber 95, and the fourth chamber 95 is provided with a filter medium 98 made of activated carbon or a filter medium equivalent thereto. . The purified water in the upper part of the fourth chamber 95 passes through the filter medium 98 and moves to the lower part of the fourth chamber 95. At that time, the purified water is further purified by the filter medium 98. The purified water that has passed through the filter medium 98 passes through the lower portion of the open partition wall 91d and flows down into the second water storage tank 85 through the second reserved water delivery pipe 86.

第二貯水槽85内の中央部には、下部が開放された円筒形状である第二貯水槽縦流入管87が縦状に設けられていて、その中心位置にはエアーリフト88が配設されている。第二貯留水配水管86を通って第二貯水槽85内に貯留された浄化水は、該エアーリフト88によって吸い上げられ、高度浄化水送流管58内を流下して滅菌器70を通って滅菌され、生活水として家屋1内で再利用されるように成っている。滅菌器70は塩素による滅菌のほか、紫外線照射によって滅菌するもの、またはこれらを併用したものであっても良い。なお本実施例ではエアーリフト88により送水しているが、これに替えて水中ポンプにより送水してもよい。   In the center of the second water tank 85, a second water tank vertical inflow pipe 87 having a cylindrical shape with an open bottom is provided in a vertical shape, and an air lift 88 is disposed at the center. ing. The purified water stored in the second water storage tank 85 through the second stored water distribution pipe 86 is sucked up by the air lift 88, flows down in the advanced purified water flow pipe 58, and passes through the sterilizer 70. It is sterilized and reused in the house 1 as domestic water. The sterilizer 70 may be sterilized by irradiating with ultraviolet rays in addition to sterilization by chlorine, or a combination of these. In this embodiment, water is supplied by the air lift 88, but water may be supplied by a submersible pump instead.

第二貯水槽85内の浄化水の一部は滅菌器70を通さずに浄化水投入管59を通って複合有効微生物群培養槽10に送られ再利用される。なお滅菌器70を通過した浄化水を家屋1内に安定して供給するため滅菌器70に連設して、該浄化水を一時的に貯留する貯留水槽を設けることもでき、貯留水槽の容量を超える量の浄化水は排水回収管2に直接流下させるように形成することができることは実施例1と同様である。   A portion of the purified water in the second water storage tank 85 is sent to the combined effective microorganism group culture tank 10 through the purified water input pipe 59 without passing through the sterilizer 70 and reused. In addition, in order to supply the purified water that has passed through the sterilizer 70 to the house 1 in a stable manner, it is possible to provide a storage tank that is connected to the sterilizer 70 and temporarily stores the purified water. It is the same as in Example 1 that the amount of purified water exceeding 1 can be formed to flow directly down to the drainage recovery pipe 2.

加えて、上記実施例2に係る生活排水高度浄化処理循環システムによって生活排水を繰り返し再利用した結果、浄化処理するための水量が不足する場合は、生活排水と共に河川や池等の水や雨水を排水回収管2を介して補給するように形成することができることも上記実施例1と同様である。 In addition, if the amount of water for purification treatment is insufficient as a result of repeated reuse of domestic wastewater by the domestic wastewater advanced purification treatment circulation system according to the second embodiment, water and rainwater such as rivers and ponds are collected together with domestic wastewater. It can be formed so as to be replenished through the drainage collecting pipe 2 as in the first embodiment.

次に図4について説明する。図4は上記実施例1及び実施例2における高度曝気槽30の槽内を示している。 Next, FIG. 4 will be described. FIG. 4 shows the inside of the advanced aeration tank 30 in the first embodiment and the second embodiment.

図4における高度曝気槽30の中央部を挟むように網状体36a36bがそれぞれ左右に張設されていて、その中央部には多数のプラスチック製の接触材37が浮遊状態に配設されている。接触材37は種々の形状とすることができるが、該接触材37は網状体36a36bの一つの升目よりも大きく形成され、このため網状体36aの上方には通過することが無く、また網状体36bの下方にも通過することが無い。 Reticulated bodies 36a and 36b are stretched to the left and right so as to sandwich the central portion of the advanced aeration tank 30 in FIG. 4, and a large number of plastic contact materials 37 are arranged in a floating state in the central portion. Yes. The contact material 37 can have various shapes, but the contact material 37 is formed larger than one mesh of the mesh bodies 36a and 36b , and therefore does not pass above the mesh body 36a. There is no passage below the mesh 36b .

散気エアー31、逆洗エアー32の先端部には図2と同様に散気管31a31b逆洗管32a、32bがそれぞれT字状に固着されていて、送気ポンプ34から送られる空気は水平送気管33を経て散気エアー31、逆洗エアー32に達し、それぞれの散気管31a、31b逆洗管32a、32bから空気泡となって同時に排出され、高度曝気槽30内の汚水は勢いよくかき混ぜられ曝気されるように成している。 Diffuser air tube 31, the backwash air tube 32 of the distal end portion 2 similarly to diffuser tubes 31a, 31b, and backwash tube 32a, 32b has been fixed in a T-shape, respectively, feeding from the air pump 34 The air that is generated reaches the diffused air pipe 31 and the backwash air pipe 32 through the horizontal air pipe 33 and is simultaneously discharged as air bubbles from the respective diffuser pipes 31a and 31b and the backwash pipes 32a and 32b. The sewage in 30 is vigorously stirred and aerated.

高度曝気槽30内の汚水がかき混ぜられると接触材37同士も衝突し、汚水中に存在する有効微生物も接触材37との衝突によって、死滅する機会が増加すると考えられる。死滅した有効微生物量が増加すると、上述のように汚水中の汚れが、有効微生物の壊れた細胞壁から浸出する細胞質により多く吸着し、より高度に凝集すると思われる。 When the sewage in the advanced aeration tank 30 is agitated, the contact materials 37 also collide with each other, and the effective microorganisms present in the sewage are thought to increase the chance of being killed by the collision with the contact material 37 . As the amount of effective microorganisms killed increases, as described above, dirt in the sewage is more adsorbed to the cytoplasm leached from the broken cell walls of the effective microorganisms and seems to aggregate more highly.

なお、実施例2において沈殿貯水槽90の底部には、沈殿貯水槽90内の底部に汚れが沈殿した場合に備えて、該沈殿物を回収する沈殿回収管(図示せず)を回収バルブ(図示せず)を介して連設し、該沈殿回収管の他端を前記汚泥貯留槽回収管62に連設して、沈殿貯水槽90内の沈殿物を、回収バルブを開放することによって汚泥貯留槽60に回収する如く構成することもできる。   In Example 2, a sediment recovery pipe (not shown) for recovering the sediment is provided at the bottom of the sedimentation reservoir 90 in the case where dirt is deposited on the bottom of the sedimentation reservoir 90. (Not shown), the other end of the sediment collection pipe is connected to the sludge storage tank collection pipe 62, and the sediment in the sediment storage tank 90 is sludged by opening the collection valve. It can also comprise so that it may collect | recover in the storage tank 60. FIG.

1 家屋
2 排水回収管
10 複合有効微生物群培養槽
11 複合有効微生物群投入管
12 散気エアー
12a、12b 散気管
13 送気ポンプ
20 処理水量調整槽
21 散気エアー
21a、21b 散気管
22 水平送気管
23 送気ポンプ
24 汚水送流管
25 水中ポンプ
30 高度曝気槽
31 散気エアー
31a、31b 散気管
32 逆洗エアー
32a、32b 逆洗管
33 水平送気管
34 送気ポンプ
35 曝気水送流管
36a、36b 網状体
37 接触材
40 第一分離沈殿槽
41 第一縦流入管
42 越流堰
43 分離浄化水送流管
44 スカム散気エアー
44a、44b スカム散気管
45 送気ポンプ
46 エアーリフト
47 汚泥回収管
50 第二分離沈殿槽
51 第二縦流入管
52 越流堰
54 スカム散気エアー
54a、54b スカム散気管
55 送気ポンプ
56 エアーリフト
57 汚泥回収管
58 高度浄化水送流管
59 浄化水投入管
60 汚泥貯留槽
61 汚泥流下管
62 汚泥貯留槽回収管
63 散気エアー
63a、63b 散気管
64 送気ポンプ
70 滅菌器
80 第一貯水槽
81 第一貯留水配送管
82 第一貯水槽縦流入管
83 エアーリフト
84 沈殿貯水槽配水管
85 第二貯水槽
86 第二貯留水配送管
87 第二貯水槽縦流入管
88 エアーリフト
90 沈殿貯水槽
91a、91b、91c、91d 開放隔壁
92 第一室
93 第二室
94 第三室
95 第四室
96 散気エアー
97 逆洗エアー
98 ろ過材
99 水平送気管
100 送気ポンプ
DESCRIPTION OF SYMBOLS 1 House 2 Wastewater collection pipe 10 Combined effective microorganism group culture tank 11 Combined effective microorganism group input pipe 12 Aeration air pipe 12a, 12b Aeration pipe 13 Air supply pump 20 Treated water amount adjustment tank 21 Aeration air pipe 21a, 21b Aeration pipe 22 horizontal air pipes 23 air pump 24 sewage feed flow tube 25 submerged pump 30 high aeration tank 31 diffuser air tube 31a, 31b diffusion pipe 32 back washing air tube 32a, 32b backwash tube 33 horizontal feed pipe 34 the air supply pump 35 aeration Water flow pipe
36a, 36b network
37 Contact material 40 First separation / precipitation tank 41 First longitudinal inflow pipe 42 Overflow weir 43 Separated purified water supply pipe 44 Scum diffused air pipe 44a, 44b Scum diffused pipe 45 Air supply pump 46 Air lift 47 Sludge collection pipe 50 Second separation sedimentation tank 51 Second longitudinal inflow pipe 52 Overflow weir 54 Scum diffused air pipe 54a, 54b Scum diffused pipe 55 Air feed pump 56 Air lift 57 Sludge recovery pipe 58 Advanced purified water feed pipe 59 Purified water input pipe 60 sludge storage tank 61 sludge flow down pipe 62 sludge storage tank recovery pipe 63 aeration air pipe 63a, 63b aeration pipe 64 air pump 70 sterilizer 80 first water tank 81 first water storage delivery pipe 82 first water tank vertical inflow Pipe 83 Airlift 84 Precipitation reservoir distribution pipe 85 Second reservoir 86 Second reservoir delivery pipe 87 Second reservoir longitudinal inflow pipe 88 Airlift 90 Precipitation reservoir 91a, 91b, 91 c, 91d Open partition 92 First chamber 93 Second chamber 94 Third chamber 95 Fourth chamber 96 Aeration air pipe 97 Backwash air pipe 98 Filter material 99 Horizontal air supply pipe 100 Air supply pump

Claims (4)

乳酸菌、酵母、光合成細菌を主体とする有用な微生物の共生体と、油分解微生物とから成る複合有効微生物群を貯留し培養する複合有効微生物群培養槽と
生活排水と複合有効微生物群培養槽中の複合有効微生物群と汚泥貯留槽中の汚泥とを混合して曝気し複合有効微生物群を増殖させると共に高度曝気槽に流入する複合有効微生物群量を調整する処理水量調整槽と、
槽内中央部に接触材を浮遊状態に配設すると共に、散気管と逆洗管を90度の角度を持って配設し、散気管と逆洗管から同時に空気を排出して曝気することで、処理水量調整槽から流入した複合有効微生物群同士を衝突させて汚水中の汚れを吸着分解処理する高度曝気槽と、
高度曝気槽にて処理された汚水を固相と液相に分離する直列配置の複数の分離沈殿槽と、
複数の分離沈殿槽に沈殿した汚泥を回収して貯留する汚泥貯留槽と、
最後尾の分離沈殿槽にて分離された液相である浄化水を滅菌処理する滅菌器とから成ることを特徴とする生活排水高度浄化処理循環システム。
In a combined effective microorganism group culture tank that stores and cultivates a complex effective microorganism group consisting of lactic acid bacteria, yeast, photosynthetic bacteria, and other useful microorganisms, and oil-degrading microorganisms. A treatment water amount adjustment tank that adjusts the amount of combined effective microorganism group flowing into the advanced aeration tank while aeration by mixing the combined effective microorganism group of sludge and sludge in the sludge storage tank and amplifying the combined effective microorganism group,
Arrange the contact material in a floating state in the center of the tank, and arrange the diffuser tube and backwash tube at an angle of 90 degrees, and discharge air from the diffuser tube and backwash tube at the same time for aeration . Then, an advanced aeration tank that causes the combined effective microorganisms flowing from the treated water amount adjustment tank to collide with each other to adsorb and decompose dirt in the sewage,
A plurality of separation and sedimentation tanks arranged in series to separate sewage treated in an advanced aeration tank into a solid phase and a liquid phase;
A sludge storage tank that collects and stores sludge precipitated in a plurality of separate settling tanks;
A domestic wastewater advanced purification treatment circulation system comprising a sterilizer for sterilizing purified water which is a liquid phase separated in a separation and precipitation tank at the tail end.
請求項1記載の複合有効微生物群培養槽、処理水量調整槽、高度曝気槽、直列配置の複数の分離沈殿槽、及び汚泥貯留槽と、
最後尾の分離沈殿槽にて分離された液相である浄化水を曝気することで有機物を分離する沈殿貯水槽と、
沈殿貯水槽にて処理された浄化水を滅菌処理する滅菌器とから成ることを特徴とする生活排水高度浄化処理循環システム。
The combined effective microorganism group culture tank according to claim 1, a treated water amount adjustment tank, an advanced aeration tank, a plurality of separation and sedimentation tanks arranged in series, and a sludge storage tank,
A precipitation reservoir for separating organic matter by aeration of purified water, which is a liquid phase separated in the last separation and sedimentation tank;
A domestic wastewater advanced purification treatment circulation system comprising a sterilizer for sterilizing purified water treated in a settling tank.
請求項1記載の複合有効微生物群培養槽、処理水量調整槽、高度曝気槽、直列配置の複数の分離沈殿槽、及び汚泥貯留槽と、
最後尾の分離沈殿槽にて分離された液相である浄化水を貯留する第一貯水槽と、
第一貯水槽より流入する浄化水を曝気することで有機物を分離する沈殿貯水槽と、
沈殿貯水槽にて分離処理された浄化水を貯留する第二貯水槽と、
第二貯水槽の浄化水を滅菌処理する滅菌器とから成ることを特徴とする生活排水高度浄化処理循環システム。
The combined effective microorganism group culture tank according to claim 1, a treated water amount adjustment tank, an advanced aeration tank, a plurality of serially arranged sedimentation tanks, and a sludge storage tank,
A first water storage tank for storing purified water that is a liquid phase separated in the last separation and sedimentation tank;
A precipitation reservoir that separates organic matter by aeration of purified water flowing from the first reservoir;
A second water storage tank for storing purified water separated in the precipitation water storage tank;
A domestic wastewater advanced purification treatment circulation system comprising a sterilizer for sterilizing the purified water in the second water tank.
生活排水を請求項1乃至請求項3のいずれかに記載の生活排水高度浄化処理循環システムにより処理して生活水として再利用し、その生活排水を更に同一の請求項1乃至請求項3のいずれかに記載の生活排水高度浄化処理循環システムにより処理して浄化し生活水として繰り返し再利用することを特徴とする生活排水高度浄化処理循環方法。
The domestic wastewater is processed by the domestic wastewater advanced purification treatment circulation system according to any one of claims 1 to 3 and reused as domestic water, and the domestic wastewater is further the same as any one of claims 1 to 3. A domestic wastewater advanced purification treatment circulation system characterized in that it is treated and purified by the domestic wastewater advanced purification treatment circulation system and repeatedly reused as domestic water.
JP2009159243A 2009-07-03 2009-07-03 Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same Active JP4482717B1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2009159243A JP4482717B1 (en) 2009-07-03 2009-07-03 Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same
CN2010102058263A CN101941775B (en) 2009-07-03 2010-06-22 Recycle system and method for highly purifying and processing domestic wastewater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009159243A JP4482717B1 (en) 2009-07-03 2009-07-03 Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same

Publications (2)

Publication Number Publication Date
JP4482717B1 true JP4482717B1 (en) 2010-06-16
JP2011011175A JP2011011175A (en) 2011-01-20

Family

ID=42351830

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009159243A Active JP4482717B1 (en) 2009-07-03 2009-07-03 Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same

Country Status (2)

Country Link
JP (1) JP4482717B1 (en)
CN (1) CN101941775B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113044994A (en) * 2021-03-29 2021-06-29 福州碧瑞源生物科技有限公司 Method for treating rare earth production tail water by utilizing waste mine pit based on photosynthetic microorganisms

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102120662A (en) * 2011-01-07 2011-07-13 张宪宗 Detachable and mobile universal sewage treater
JP4826975B1 (en) * 2011-03-15 2011-11-30 株式会社 宮田エンジニアリング Rainwater infiltration circulation storage tank.
KR101272267B1 (en) 2012-07-19 2013-06-13 (주)우진 Method and apparatus for reducing sludge using complex microbe
CN105371053B (en) * 2015-12-10 2017-09-15 重庆山岱科技有限责任公司 Caravan sewer purification mechanism
CN105540866B (en) * 2015-12-10 2018-01-09 重庆山岱科技有限责任公司 Caravan sewer purification method
CN105399280B (en) * 2015-12-17 2018-07-17 李秋芬 A kind of sewage disposal system
KR101779762B1 (en) 2016-02-01 2017-09-19 전주대학교 산학협력단 Useful microbial fermentation and amplification equipment for water treatment
CN110709370A (en) * 2017-02-28 2020-01-17 德莱特有限公司 Systems, methods, and apparatus for improving the quality of wastewater effluents and biosolids

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03267199A (en) * 1990-03-14 1991-11-28 Taisei Corp Method and facility for in-vessel deodorizing waste water treatment
JPH0910784A (en) * 1995-06-27 1997-01-14 Tochigi Denshi Kogyo Kk Method and apparatus for treating and reutilizing waste water
JPH09174093A (en) * 1995-12-21 1997-07-08 Toshio Uematsu Drainage treatment and apparatus therefor
JPH1157762A (en) * 1997-08-19 1999-03-02 Nippon Soda Co Ltd Aerobic treating method of sewage
JP2003211174A (en) * 2002-01-29 2003-07-29 Yasutoshi Takashima Circulation-type water supplying and draining equipment
JP2004154712A (en) * 2002-11-07 2004-06-03 Aoki Denki Kogyo Kk Method of disposing garbage

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61197093A (en) * 1985-02-25 1986-09-01 Idemitsu Petrochem Co Ltd Treatment of waste water
CN1224580C (en) * 2001-02-21 2005-10-26 广西必佳微生物工程有限责任公司 Composite microbe process for treating high-concentration organic sewage
AU2002338128A1 (en) * 2002-09-27 2004-04-19 Shanghai Gi Biotechnology Engineering Co., Ltd. A method of processing organic wastewater
CN101050423A (en) * 2007-03-19 2007-10-10 上海真美科技发展有限公司 Composite preparation microbiological, and preparation method
CN101544445B (en) * 2009-04-30 2012-12-05 华南理工大学 A method for restoring microorganism ecology of paper making waste water and a device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03267199A (en) * 1990-03-14 1991-11-28 Taisei Corp Method and facility for in-vessel deodorizing waste water treatment
JPH0910784A (en) * 1995-06-27 1997-01-14 Tochigi Denshi Kogyo Kk Method and apparatus for treating and reutilizing waste water
JPH09174093A (en) * 1995-12-21 1997-07-08 Toshio Uematsu Drainage treatment and apparatus therefor
JPH1157762A (en) * 1997-08-19 1999-03-02 Nippon Soda Co Ltd Aerobic treating method of sewage
JP2003211174A (en) * 2002-01-29 2003-07-29 Yasutoshi Takashima Circulation-type water supplying and draining equipment
JP2004154712A (en) * 2002-11-07 2004-06-03 Aoki Denki Kogyo Kk Method of disposing garbage

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113044994A (en) * 2021-03-29 2021-06-29 福州碧瑞源生物科技有限公司 Method for treating rare earth production tail water by utilizing waste mine pit based on photosynthetic microorganisms

Also Published As

Publication number Publication date
CN101941775B (en) 2012-10-10
CN101941775A (en) 2011-01-12
JP2011011175A (en) 2011-01-20

Similar Documents

Publication Publication Date Title
JP4482717B1 (en) Domestic wastewater advanced purification treatment circulation system and domestic wastewater advanced purification treatment circulation method using the same
KR0175229B1 (en) Apparatus and method for waste water treatment using granular sludge
KR101303525B1 (en) A livestock wastewater treatment system using constructed wetlands
US11407660B2 (en) System and method for remediation of wastewater including aerobic and electrocoagulation treatment
KR101226547B1 (en) Sewage treatment system for marine use
CN213112948U (en) Integrated circulating culture system
KR102170601B1 (en) Advanced sewage and wastewater separation membrane device using low temperature plasma
CN106430847A (en) Intensive swine wastewater treating equipment
CN214060278U (en) Mariculture tail water discharging device
CN107963786A (en) A kind of sewage water treatment method and system
CN107055884A (en) A kind of nitrogen phosphorus waste water separating and treating apparatus
CN107043196A (en) A kind of batch production high-density aquiculture system
KR20210091951A (en) Automatic Sedimentation Circulation Breeding Tank for Bioflock aquafarm.
CN210287055U (en) Domestic sewage integrated treatment device
CN107555600A (en) A kind of sewage disposal system
CN103011528B (en) Comprehensive sewage treatment system and method
JP2006289153A (en) Method of cleaning sewage and apparatus thereof
CN210538263U (en) High-efficient filtration clean system of water is bred to sturgeon
CN205676326U (en) A kind of integrated sewage disposal intermediate filtered bioreactor
CN1077553C (en) Facilities for treating waste water on large scale
CN115974305B (en) Integrated membrane method water treatment system and treatment method
CN208327714U (en) Rural domestic sewage treatment integrated apparatus
CN107162197A (en) Three rank O/A decentralized type sewages handle integrated apparatus and method
CN1074752C (en) Improved effective tank for purification of water for cattle drinking in which
CN112794529A (en) Combined sewage treatment process

Legal Events

Date Code Title Description
TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100305

R150 Certificate of patent or registration of utility model

Ref document number: 4482717

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130402

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130402

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20160402

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250