JP2010158610A - Facility for elimination treatment of human waste, purification tank, sewer, sludge, and food residue by microorganism - Google Patents

Facility for elimination treatment of human waste, purification tank, sewer, sludge, and food residue by microorganism Download PDF

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JP2010158610A
JP2010158610A JP2009001244A JP2009001244A JP2010158610A JP 2010158610 A JP2010158610 A JP 2010158610A JP 2009001244 A JP2009001244 A JP 2009001244A JP 2009001244 A JP2009001244 A JP 2009001244A JP 2010158610 A JP2010158610 A JP 2010158610A
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tank
digestion
sewage
decomposition
water
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JP4341857B1 (en
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Akiharu Moriwaki
昭治 森脇
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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
    • Y02W10/20Sludge processing
    • 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
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

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  • Biological Treatment Of Waste Water (AREA)
  • Processing Of Solid Wastes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Sludge (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a technology for an elimination treatment facility, a final treatment facility which eliminates waste, a large cost required for waste disposal in the time of serious financial conditions of cities, towns, and villages of the country, generated in the conventional wastewater treatment facility which is, after all, an intermediate treatment facility for performing solid-liquid separation using a coagulant, and dehydrating, drying, and burning precipitated sludge to mainly use the obtained ash for landfill or compost. <P>SOLUTION: The elimination treatment facility is a multi-tank and multistage treatment facility comprising nineteen tanks. When sewage, animal residues, organic sludge and the like are pretreated in a raw water tank and flow into a balancing tank, they are diluted with dilution water so as to sufficiently exhibit the decomposing power of bacteria according to a material to be treated, and when the diluted sewage flows into a decomposition tank, the process of solid-liquid separation, fermentation, decomposition, and digestion is repeatedly performed. A retention time in each decomposition tank is made long, thereby reducing the size of the facility and promoting the decomposition and digestion to perform elimination. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は屎尿、浄化槽、下水道、汚泥及び食品残渣の微生物による消滅処理する施設に関する。 The present invention relates to a facility for eradicating urine, septic tanks, sewers, sludge and food residues by microorganisms.

従来の汚水処理施設の処理方法は活性汚泥法であり、曝気作動を行い汚水中の好気性菌を活性化させる方法は大きな欠点があり、結果として余剰汚泥を生産することになっている。 The treatment method of the conventional sewage treatment facility is the activated sludge method, and the method of activating the aerobic bacteria in the sewage by performing the aeration operation has a major drawback, and as a result, excess sludge is produced.

汚水の個液分離を早める為に凝集剤を使用して、沈下した汚泥を引き抜きされ脱水して焼却後の灰を埋め立て処分するか、推肥化、メタン醗酵などで減量化が図られているが、完全に消滅させる事が出来ずにいる。 In order to expedite the separation of individual liquid wastewater, flocculants are used, and the settled sludge is drawn out and dewatered, and the incinerated ash is disposed of in landfills, or reduced by fertilization and methane fermentation. However, it is impossible to completely disappear.

上述した様に、汚泥を完全消滅させる事が出来ず、その処理の為に大量の石油を消費して、CO2を排出して温暖化の一助となり、廃棄すべきものに費用を使う無駄を解決する。 As mentioned above, sludge cannot be completely extinguished, a large amount of oil is consumed for its treatment, CO2 is emitted to help warming, and waste that spends money on what should be discarded is solved. .

本処理施設は従来の処理方法では解決出来なかった、余剰汚泥の完全消滅を実現する事を目的とするものである。 The purpose of this treatment facility is to realize the complete elimination of excess sludge, which could not be solved by conventional treatment methods.

上記課題を解決する為の微生物 汚水、汚泥の消滅処理施設の方法は、原槽水(1)貯水槽(2)調整槽(3)分解槽(4)4槽、分解消化槽(8)4槽、消化槽(12)2槽、消化消滅槽(14)4槽の17槽とせせらぎ反応消滅槽(18)2槽の全槽で、19槽からなる多槽多段式構造であり、このシステムによる処理工程は個液分離→醗酵→分解→消化というプロセスにて行う。 Microorganisms to solve the above problems Wastewater and sludge extinguishing facility methods are: raw water (1) water storage tank (2) conditioning tank (3) decomposition tank (4) 4 tank, decomposition digestion tank (8) 4 This is a multi-stage multistage structure consisting of 19 tanks, consisting of 17 tanks, 2 tanks for digestion tank (12), 17 tanks for digestion extinction tank (14) and 2 tanks for muddle reaction extinction tank (18). The treatment process is performed by the process of individual liquid separation → fermentation → decomposition → digestion.

この地球上における最大、かつ最良の浄化施設は土であり、土は土壌菌の働きで機能している。当システムは土壌菌(中間菌)の機能を利用し、土壌の働きをコンパクトに集約した処理施設であり、悪臭や人畜への危険も全く無く、余剰汚泥も出ない最終処理であり、最も有効な処理方法である。 The largest and best purification facility on earth is soil, which functions as a function of soil fungi. This system uses the function of soil fungi (intermediate fungi), is a treatment facility that compactly integrates the work of soil, has no bad odor or danger to human livestock, and is the final treatment that does not generate excess sludge, the most effective It is a simple processing method.

菌床となる原料は杉材で、杉の菌床となる部分を特殊な方法で破砕して、腐敗部分を時間を掛けて取り除くと安定したセルロースが残る。このセルロースは微生物にとっては、大変住み心地の良い優れたバイオ材の杉チップが出来る。このチップの固有特性は、(イ)多孔質化の加工により有機物吸着機能を持っている。(ロ)微生物の増殖を促進する。(ハ)生分解を可能にする。(ニ)脱臭効果がある。(ホ)腐敗しない。(へ)自ら湿度を63%に調整する。 The raw material that becomes the fungus bed is cedar, and the portion that becomes the fungus bed of the cedar is crushed by a special method, and when the spoiled part is removed over time, a stable cellulose remains. This cellulose can be an excellent bio-cedar chip that is very comfortable for microorganisms to live in. The inherent characteristics of this chip are as follows: (a) It has an organic substance adsorption function due to the processing of making it porous. (B) Promote the growth of microorganisms. (C) Enable biodegradation. (D) Deodorizing effect. (E) Don't rot. (F) Adjust the humidity to 63%.

菌床となる原料は、ポリプロピレンで酵素を練り込んだ独特な形状の担体を、杉チップと同様に菌床として使用している。槽内に、詰められたこの担体に接触することで、担体に吸着している嫌気性、好気性、両性菌により分解と消化を行う。 As a raw material for the fungus bed, a carrier having a unique shape in which an enzyme is kneaded with polypropylene is used as the fungus bed as in the case of cedar chips. By contacting this carrier packed in the tank, it is decomposed and digested by anaerobic, aerobic and amphoteric bacteria adsorbed on the carrier.

菌床となる杉チップとポリプロピレン製の担体と中間菌を効果的に使い、酵素活性液供
給装置、細胞膜分解装置、醗酵菌培養装置を作動させて分解菌を安定、増殖させる。これ
らを調整する事で分解消化を行い、汚泥が消滅する。
Effective use of cedar chips, a polypropylene carrier and intermediate fungi as a fungus bed, and operation of an enzyme active solution supply device, a cell membrane decomposition device, and a fermentation bacteria culture device to stabilize and propagate the decomposed bacteria. By adjusting these, digestion is performed and sludge disappears.

上述したように、このシステムによる処理施設で汚泥が消滅するので、乾燥や焼却で石油を使わなくてもよい為、CO2を排出せず環境に良い。また、捨てる為に費用を使う無駄も省ける。 As mentioned above, since sludge disappears at the treatment facility using this system, it is not necessary to use oil for drying and incineration, so it is good for the environment without emitting CO2. It also saves money from wasting money.

この処理施設は地域の事情、事業形態に応じた処理施設の設置が可能であり、建設費用も安価であり、維持管理が簡単であり、経済的である。 This treatment facility can be installed according to the local circumstances and business form, has a low construction cost, is easy to maintain and is economical.

以下、本発明の実施の形態を図示される(1)〜(21)に基づいて説明する。尚、以下に述べる実施形態は本発明を具体化した一例であり、本発明の技術的範囲を限定するものではない。 Hereinafter, embodiments of the present invention will be described based on (1) to (21) shown in the drawings. The embodiment described below is an example embodying the present invention, and does not limit the technical scope of the present invention.

本発明の微生物による、汚水、汚泥の消滅処理施設の構成は、(1)原水槽(2)貯水槽(3)調整槽(4)分解槽4槽(8)分解消化槽4槽(12)消化槽2槽(14)消化消滅槽4槽(18)せせらぎ反応消滅槽2槽の計19槽と、排水集水槽2槽から成り立つ施設である。 The structure of the sewage and sludge elimination treatment facility by the microorganism of the present invention is as follows: (1) Raw water tank (2) Water storage tank (3) Adjustment tank (4) Decomposition tank 4 tank (8) Decomposition digestion tank 4 tank (12) Digestion tank 2 tank (14) Digestion extinction tank 4 tank (18) Seseragi reaction extinction tank 2 tanks total 19 tanks and drainage water collecting tank 2 tanks.

図示(1)原水層では、処理対象物を貯留する槽であり、投入時に夾雑物を除去する為に
ドラムスクリーンを設け、酵素活性液供給装置を設置して制御された一定時に一定量の活性液が槽内に投入され、バッキレーターにて汚水を撹拌して処理対象物を粉砕し、大量の酸素を供給して脱臭と腐敗防止の前処理を行い、制御により一定時に一定量が、水中ポンプの作動にて(3)調整槽に送水される。
(1) The raw water layer is a tank for storing the object to be treated. A drum screen is provided to remove impurities at the time of charging, and a certain amount of activity is controlled at a fixed time by installing an enzyme activity liquid supply device. The liquid is put into the tank, the sewage is stirred with a buckler to pulverize the object to be treated, and a large amount of oxygen is supplied to perform pre-treatment for deodorization and anti-corruption. Water is sent to the adjustment tank by the pump operation (3).

図示(2)は、貯水槽であり、この槽では(21)排水集水槽より最終処理水を中水として受け入れ、希釈水として(3)調整槽に制御により一定時に一定量が、設置された水中ポンプで送水される。 In the figure, (2) is a water storage tank. In this tank, the final treated water is received as middle water from the (21) drainage water collection tank, and (3) a fixed amount is installed in the adjustment tank at a fixed time as control. Water is pumped with a submersible pump.

図示(3)調整槽では、(1)原水槽より送水されて来た汚水を、微生物が分解処理しやすく適正な濃度になる様に、(2)貯水槽より制御にて一定時に一定量の希釈水が送水されて来て調整される槽であり、槽内の底面中央に設置された散気管により、エアレーションにて大量の酸素を供給、撹拌し設置されているイオンコントロール装置を稼動し、溶存酸素値LFT+999に調整し、また、細胞膜分解装置を稼動して微生物による分解消化に適正な粒子に調整され、制御により一定時に一定量の汚水が、設置された水中ポンプで(4)分解槽に送られる。 (3) In the adjustment tank shown in the figure, (1) The sewage sent from the raw water tank is controlled by the water tank so that the microorganisms are easily decomposed and have an appropriate concentration. Dilution water is sent to the tank and adjusted, and a large amount of oxygen is supplied and agitated by an aeration tube installed in the center of the bottom of the tank. The dissolved oxygen level is adjusted to LFT + 999, and the cell membrane digester is operated to adjust the particles to be suitable for digestion by microorganisms. By control, a certain amount of sewage is fixed at a fixed time with an installed submersible pump (4) Decomposition tank Sent to.

図示(4)分解槽では槽内の壁面の両側に仕切壁を設置し、壁面と仕切壁の間に太さがランダムなバイオネットパイプ(ポリプロピレン製のネットに酵素を練り込んだパイプ)を充填させ、仕切壁の下部には底面より25cmの高さまで穴があり、仕切壁と仕切壁の間の底部に散気管が設置されており、菌床となる杉チップを槽内容積の3〜5%入れてあり、醗酵菌培養装置が設置され、(21)排水集水槽よりエアーリフトにて処理水が培養装置に送水される事で菌の増加と活動の安定を図る。(3)調整槽より汚水が(4)分解槽に流入してくると散気管より噴出する超微細な気泡のエアーリフト作用により、静かに撹拌され槽内を浮遊している杉チップを汚水が通過する時、個液分離が行われ同時に液体に含まれる汚濁物質は杉チップに吸収され効率的に醗酵、分解が始まる。処理水は壁面側に設置されている仕切壁の下部から上部にバイオネットパイプの詰められた層を通過して、順次この働きを繰り返し、(4)〜(8)の分解消化槽へと流出して行く。 (4) In the decomposition tank, partition walls are installed on both sides of the wall surface in the tank, and a bionet pipe with a random thickness between the wall surface and the partition wall (a pipe made by kneading enzymes in a polypropylene net) is filled. There is a hole in the lower part of the partition wall up to a height of 25 cm from the bottom, and an aeration tube is installed at the bottom between the partition wall and the cedar chip that becomes the fungus bed is 3-5 of the internal volume of the tank The fermentation bacteria culture device is installed, and (21) The treated water is sent from the drainage water collection tank to the culture device by an air lift to increase the number of bacteria and stabilize the activity. (3) Sewage from the adjustment tank (4) When the sewage flows into the decomposition tank, the sewage is suspended by the cedar chips that are gently agitated and suspended in the tank by the air lift action of the ultrafine bubbles ejected from the diffuser. When passing, individual liquid separation is performed, and at the same time, the pollutant contained in the liquid is absorbed by the cedar chips and efficiently fermented and decomposed. The treated water passes through the layer filled with the bayonet pipe from the lower part to the upper part of the partition wall installed on the wall surface, and repeats this function in sequence, and then flows out into the digestion and digestion tanks of (4) to (8). Go.

図示(8)分解消化槽では底面より25cmの位置に15cm角の穴の開いた棚板を設けてその上にポリプロピレン製の独特な形状の担体をネット袋に詰め込んで、槽内にぎっしりと詰めてあり槽内中央にエアーリフトの装置を設けてあり(7)分解槽より流入して来た汚水は、上部有孔管からシャワー状態となって槽内四方に落水する。エアーリフトの作用で、強制的に槽内下部から上部に循環させて汚水が担体と接触する事により、担体に付着する分解菌によって分解消化を行い、順次この働きを繰り返しながら(8)〜(12)の消化槽へと流出して行く。 (8) In the digestion and digestion tank, a shelf board with a 15 cm square hole is provided at a position 25 cm from the bottom, and a unique shaped carrier made of polypropylene is packed in a net bag on the shelf, and the tank is packed tightly. An air lift device is provided in the center of the tank. (7) The sewage flowing in from the decomposition tank falls into a shower state from the upper perforated pipe and falls into the tank. By the action of the air lift, the sewage is forced to circulate from the lower part to the upper part in the tank, and the sewage comes into contact with the carrier. It flows out to the digestion tank of 12).

図示(12)消化槽では、底面より25cmの所に15cm角の析目に穴のある棚板を設置して、担体層と杉チップ層の二層になっており、その容積は担体層3に対して杉チップ層1の割合であり、担体も杉チップもネット袋に詰められている。(11)分解消化槽より流入して来た処理水は上部の有孔管からシャワー状態となって槽内の四方に落水する。槽中央に設置されているエアーリフトにて処理水を循環させて杉チップに付着する中間菌(両性菌)と担体に付着する分解菌により消化を促進させる(13)消化槽より(14)消化消滅槽に流出して行く。 In the illustrated (12) digester, a shelf board with holes of 15 cm squares is installed at a location 25 cm from the bottom, and it has two layers, a carrier layer and a cedar chip layer, the volume of which is the carrier layer 3 The ratio of the cedar chip layer 1 to the carrier, and the carrier and cedar chips are packed in a net bag. (11) The treated water that has flowed in from the digestive digestion tank enters a shower state from the upper perforated pipe and falls in all directions in the tank. Circulating treated water with an air lift installed in the center of the tank to promote digestion by intermediate bacteria (amphoteric bacteria) adhering to the cedar chip and degrading bacteria adhering to the carrier (13) From the digestion tank (14) Digestion It flows out into the extinguishing tank.

図示(14)消化消滅槽では、(12)(13)消化槽と槽内の構造も働きも同じであるが、担体と杉チップとの容積率は1対1の割合であり、エアーリフトの働きによって槽内の処理水を強制的に循環させる事で、中間菌(好気性、嫌気性、両性菌)の増殖を促し、有機物の消化消滅が促進する。この工程を繰り返しながら(14)〜(17)と順次流通して(20)排水集水槽に流出して水中ポンプの作動にて(18)(19)せせらぎ反応消滅槽に排出される。 The (14) digestion extinction tank shown in the figure has the same structure and function as the (12) (13) digestion tank, but the volume ratio of the carrier and the cedar chip is a one-to-one ratio. By forcibly circulating the treated water in the tank by working, it promotes the growth of intermediate bacteria (aerobic, anaerobic, amphoteric) and promotes the digestion and extinction of organic matter. While repeating this step, (14) to (17) are circulated in sequence, (20) are discharged into the drainage water collection tank, and are discharged into the (18) (19) turbulence reaction extinction tank by the operation of the submersible pump.

図示(18)せせらぎ反応消滅槽では槽内には菌床となる杉チップがぎっしりと敷き詰めてあり、流入して来た処理水は、この槽でBOD、COD、SS、窒素、リン等の数値が減少され、好気性菌、嫌気性菌、中間菌の大量発生により、残留処理物を消滅させる槽であり、この槽は(18)せせらぎ反応消滅槽と(19)せせらぎ反応消滅槽とは10日間を目処にして交互使用する事で、消滅作業を促進させる最終処理の槽であり、処理水は無色透明な水となって(21)排水集水槽に流出する。 (18) In the murmuring reaction extinction tank, the cedar chips that become the fungus bed are packed in the tank, and the treated water that has flowed in is a numerical value such as BOD, COD, SS, nitrogen, phosphorus, etc. Is a tank that extinguishes the residual treatment product due to a large amount of aerobic bacteria, anaerobic bacteria, and intermediate bacteria. These tanks are (18) murmur reaction extinction tank and (19) murmur reaction extinction tank. It is a tank for final treatment that promotes extinction work by alternately using it for the day, and the treated water becomes colorless and transparent water (21) and flows into the drainage water collection tank.

図示(21)排水集水槽では、中水として(2)貯水槽に水中ポンプに返送され希釈水となって再利用される。また、一部の処理水は(4)分解槽に設置されている醗酵菌培養装置に返送され、菌の補充と活動を安定させる。余剰水については、イオンコントロール装置を使って液肥として利用できる。また、放流しても良い。放流水のBOD数値は3〜5である。 In the illustrated (21) drainage water collection tank, as intermediate water, (2) the water tank is returned to the submersible pump and reused as dilution water. In addition, part of the treated water is returned to (4) the fermentation bacteria culture device installed in the decomposition tank to stabilize the replenishment and activity of the bacteria. Excess water can be used as liquid fertilizer using an ion control device. Moreover, you may discharge. The BOD value of discharged water is 3-5.

本発明の実施形態を示す処理施設の平面図The top view of the processing facility which shows embodiment of this invention 分解槽の構成を示す図1におけるA−A線断面図AA line sectional view in Drawing 1 showing composition of a decomposition tank 分解消化槽の構成を示す図1におけるB−B線断面図BB sectional view in FIG. 1 showing the structure of the digestion digester 消化消滅槽の構成を示す図1におけるC−C線断面図CC sectional view in FIG. 1 showing the configuration of the digestion extinguishing tank

1 原水層
2 貯水槽
3 調整槽
4 分解槽A
5 分解槽B
6 分解槽C
7 分解槽D
8 分解消化槽A
9 分解消化槽B
・ 分解消化槽C
11 分解消化槽D
12 消化槽A
・ 消化槽B
14 消化消滅槽A
15 消化消滅槽B
16 消化消滅槽C
17 消化消滅槽D
18 せせらぎ反応消滅槽A
19 せせらぎ反応消滅槽B
20 排水集水槽A
21 排水集水槽B
1 Raw water layer 2 Reservoir 3 Adjustment tank 4 Decomposition tank A
5 Decomposition tank B
6 Decomposition tank C
7 Decomposition tank D
8 Decomposition digester A
9 Decomposition digester B
・ Decomposition digester C
11 Decomposition digester D
12 Digestion tank A
・ Digestion tank B
14 Digestion tank A
15 Digestion extinguishing tank B
16 Digestion tank C
17 Digestion tank D
18 Lazy reaction extinction tank A
19 Seseragi reaction extinction tank B
20 Drainage tank A
21 Drainage tank B

Claims (7)

原水槽(1)に酵素活性液供給装置を設置し、酵素活性液を制御によって定時に定量を槽内に入れ、水中バッキレーターにて大量の酸素を供給し、カッターポンプで有機物を粉砕し脱臭、腐敗防止の前処理を行い、制御により定時に定量を調節槽(3)に流出する処理方法。 An enzyme active solution supply device is installed in the raw water tank (1), and a fixed amount of the enzyme active liquid is put into the tank at a fixed time by control, a large amount of oxygen is supplied with an underwater crater, and organic substances are crushed and deodorized with a cutter pump. The processing method which performs the pre-processing of anti-corruption and flows out fixed quantity to a control tank (3) at regular time by control. 調整槽(3)に細胞膜分解装置を設置し、有機物を微細化して分解能力を促進させる処置を施し、イオンコントロール装置し、槽内の溶存酸素値を安定させ、原水槽(3)から送られてきた汚水を微生物が処理しやすいBOD値に貯水槽(2)より制御にて、定時に定量の送水されて来た希釈水にて調整され、制御にて定時に定量の汚水をポンプにて、第一分解槽(4)に送水される処理方法。 A cell membrane degrading device is installed in the adjustment tank (3), the organic substance is refined to improve the decomposition ability, an ion control apparatus is used, the dissolved oxygen value in the tank is stabilized, and sent from the raw water tank (3). The sewage water is adjusted to a BOD value that is easy for microorganisms to treat, and is adjusted with dilution water that has been sent in a fixed amount at a fixed time by control from the water storage tank (2). The processing method with which water is sent to the first decomposition tank (4). 分解槽(4)〜分解槽(7)では、槽内の中心部に散気管を設置し、壁面の両サイドに仕切りを設置し、その両サイドの仕切壁と壁面の間に太さがランダムなバイオネットパイプ(ポリプロピレン製のネットに分解酵素を練り込めたパイプ)が充填されてあり、仕切壁の下部には底面より、高さ25cm部分はランダムに穴が開けられており、仕切壁と仕切壁の間には、菌床となる杉チップ(醗酵腐蝕土)を槽内容器の3〜5%を入れてあり、散気管より噴出する超微細な気泡のエアーリフト作用により静かに撹拌され、槽内を浮遊している杉チップを汚水が通過する時個液分離が行われ、同時に液体に含まれる汚濁物質は、杉チップに吸収されて水分63%前後の条件下で効率的に醗酵が始まり、そしてこの時、多量の極小微生物が発生する。この極小微生物は、中間菌と呼ばれる菌であり、従来の汚水処理に仕様されていた好気性菌でも嫌気性菌でもない両性菌である。この中間菌が当システムの分解菌であり、こうして分解された汚水は設置されている両側の仕切壁の下部の有孔部から充填されてあるバイオネットパイプ部を上部に通過して分解槽(4)から分解槽(7)に順次流出流入して行く処理方法、分解槽(4)に醗酵菌培養装置が設置されてあり、排水集水層(21)より定時に定量の処理水を培養装置に返送する事で醗酵菌の活動を安定させる処理方法。 In the decomposition tank (4) to the decomposition tank (7), an aeration tube is installed in the center of the tank, partitions are installed on both sides of the wall surface, and the thickness is randomly between the partition wall and the wall surface on both sides. A bayonet pipe (a pipe made of polypropylene netted with a degrading enzyme) is filled, and the bottom of the partition wall is randomly perforated at a height of 25 cm from the bottom. Between the partition walls, 3-5% of the cedar chip (fermented and corroded soil) that becomes the fungus bed is put in the tank, and it is gently agitated by the air-lifting action of the superfine bubbles ejected from the air diffuser. When the sewage passes through the cedar chips floating in the tank, individual liquid separation is performed, and at the same time, the pollutants contained in the liquid are absorbed into the cedar chips and efficiently fermented under conditions of about 63% moisture. Begins, and at this time, a lot of microbes are generated . This micro-microorganism is a bacterium called an intermediate bacterium, and is an amphoteric bacterium that is neither an aerobic bacterium nor an anaerobic bacterium that has been specified for conventional sewage treatment. This intermediate bacterium is a decomposing bacterium of this system, and the sewage thus decomposed passes through the bayonet pipe part filled from the perforated part of the lower part of the partition walls on both sides to the upper part, and the decomposition tank ( 4) A treatment method that sequentially flows into and out of the decomposition tank (7), and a fermentation bacteria culture device is installed in the decomposition tank (4), and a fixed amount of treated water is cultured from the drainage water collection layer (21) at a fixed time. A processing method that stabilizes the activity of fermenting bacteria by returning it to the device. 分解消化槽(8)〜分解消化槽(11)では分解槽(7)より分解消化槽(8)に流入して来た汚水は、上部の有孔管よりシャワー状態となって四方に落水する。この槽には底面より25cmの所に有孔の棚板が設置してあり、その上に醗酵菌を練り込んだポリプロピレン製の独特な形状の担体をネット袋に入れ、ぎっしりと詰められており、エアーリフトの作動により槽内の汚水を底面より、上部に循環させながら分解消化を繰り返し、定時に定量が消化槽(12)に流入して行く処理方法。 In the digestive digester (8) to the digestive digester (11), the sewage that has flowed into the digestive digester (8) from the digester (7) enters a shower state from the upper perforated pipe and falls in all directions. . This tank has a perforated shelf at 25cm from the bottom, and is packed tightly into a net bag with a unique carrier made of polypropylene kneaded with fermentation bacteria on it. The treatment method in which the digestion is repeated while circulating the sewage in the tank from the bottom to the top by the operation of the air lift, and the fixed amount flows into the digestion tank (12) at regular times. 消化槽(12)〜消化槽(13)では分解消化槽(11)より流入して来た汚水は、上部の有孔気管より消化槽(12)の四方にシャワー状態となって落水する。この消化槽では二層構造になっており、担体容積槽3に対して杉チップ容積槽1の割合である、底面より25cmの位置に有孔の棚板が設置され醗酵菌を練り込んだポリプロピレン製の独特な形状の担体をネット袋に入れた状態で積み込まれ、その上に有孔の棚板が設けられ、ネットに詰めた杉チップを積み込んであり容積比3対1である槽内の汚水をエアーリフトの作動により底面より上部に循環しながら強制的に分解処理を繰り返し定時に定量が消化消滅槽(14)に流入して行く処理方法。 In the digestion tank (12) to the digestion tank (13), the sewage that has flowed in from the decomposition digestion tank (11) falls from the upper perforated trachea into a shower state in four directions of the digestion tank (12). This digestion tank has a two-layer structure, and is a ratio of the cedar chip volume tank 1 to the carrier volume tank 3, a perforated shelf board placed at a position 25 cm from the bottom and kneaded with fermentation bacteria A unique shaped carrier made of steel is loaded in a net bag, a perforated shelf board is provided on it, cedar chips packed in the net are loaded, and the volume ratio is 3: 1 A treatment method in which sewage is forced to repeat the decomposition process while circulating the sewage from the bottom to the upper part by the operation of the air lift, and the fixed amount flows into the digestion extinguishing tank (14) at a fixed time. 消化消滅槽(14)〜消化消滅槽(17)では消化槽(13)より流入して来たら汚水は上部の有孔管より消化消滅槽(14)の四方にシャワー状態となって落水する。この消化消滅槽でも二層構造になっており棚板の下部には担体層上部には杉チップ層となり、そ
の容積率は1対1の割合となって、槽内の汚水をエアーリフトの作動にて、底面より上部に循環しながら有機物を消化消滅して第一せせらぎ反応消滅槽(18)(19)に流入して行く処理方法。
In the digestion extinction tank (14) to the digestion extinction tank (17), the sewage flows into the digestion extinction tank (14) in the four directions of the digestion extinction tank (14) and falls from the upper perforated pipe. This digestion extinguishing tank also has a two-layer structure. The bottom of the shelf is a cedar chip layer above the carrier layer, the volume ratio is 1: 1, and the sewage in the tank is operated by an air lift. Then, the organic substance is digested and extinguished while circulating from the bottom to the upper part, and flows into the first stagnation reaction extinction tank (18) (19).
消化消滅槽(17)より第一排水集水槽(20)に流入した汚水は、水中ポンプの作動にて第一せせらぎ反応槽(18)第二せせらぎ反応槽(19)に送られる第一せせらぎ反応槽(18)と第二せせらぎ反応槽(19)は、10日間毎に交互に流入される、槽の底面には、焼成炭含浸した通気性嫌気性菌のバイオブロックを敷き詰め、その上に杉チップを敷き詰め、ミネラルストーンがその上に敷き詰められた最終処理槽であり、無色透明の処理済み水となって第二排水集水槽に流出するBOD値は3〜2である。この排水は中水として希釈水に使用する為、水中ポンプの作動にて貯水槽に返送され、また余剰水は放流するかイオンコントロール装置内を通して液肥に利用する処理方法。 The sewage flowing into the first drainage water collecting tank (20) from the digestion extinguishing tank (17) is sent to the first murmuring reaction tank (18) and the second murmuring reaction tank (19) by the operation of the submersible pump. The tank (18) and the second murmuring reaction tank (19) flow alternately every 10 days. The bottom of the tank is laid with a bioblock of anaerobic anaerobic bacteria impregnated with calcined charcoal, and a cedar on top of it. A final treatment tank in which chips are spread and mineral stones are spread thereon, and the BOD value that flows into the second drainage water collection tank as colorless and transparent treated water is 3 to 2. Since this wastewater is used as dilution water for diluting water, it is returned to the water tank by the operation of the submersible pump, and the surplus water is discharged or used for liquid fertilizer through the ion control device.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5116888B1 (en) * 2012-04-17 2013-01-09 誠二 高松 Non-water-supplying circulating flush toilet system and container toilet containing this system
CN105110481A (en) * 2015-07-02 2015-12-02 武汉水之蓝环保生物科技发展有限公司 Microorganism breeding device and microorganism breeding system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5116888B1 (en) * 2012-04-17 2013-01-09 誠二 高松 Non-water-supplying circulating flush toilet system and container toilet containing this system
CN105110481A (en) * 2015-07-02 2015-12-02 武汉水之蓝环保生物科技发展有限公司 Microorganism breeding device and microorganism breeding system

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