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 PDFInfo
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- 244000005700 microbiome Species 0.000 title claims description 9
- 239000010802 sludge Substances 0.000 title abstract description 14
- 230000008030 elimination Effects 0.000 title abstract description 6
- 238000003379 elimination reaction Methods 0.000 title abstract description 6
- 239000010794 food waste Substances 0.000 title description 2
- 238000000746 purification Methods 0.000 title description 2
- 239000010800 human waste Substances 0.000 title 1
- 230000029087 digestion Effects 0.000 claims abstract description 45
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 33
- 239000010865 sewage Substances 0.000 claims abstract description 26
- 241000894006 Bacteria Species 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 13
- 238000000855 fermentation Methods 0.000 claims abstract description 9
- 230000004151 fermentation Effects 0.000 claims abstract description 9
- 238000000926 separation method Methods 0.000 claims abstract description 6
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- 239000012895 dilution Substances 0.000 claims abstract description 5
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- 241000218645 Cedrus Species 0.000 claims description 20
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- 241000233866 Fungi Species 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 claims description 12
- 238000005192 partition Methods 0.000 claims description 10
- 239000003657 drainage water Substances 0.000 claims description 9
- 102000004190 Enzymes Human genes 0.000 claims description 7
- 108090000790 Enzymes Proteins 0.000 claims description 7
- 239000004743 Polypropylene Substances 0.000 claims description 6
- -1 polypropylene Polymers 0.000 claims description 6
- 229920001155 polypropylene Polymers 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 230000000694 effects Effects 0.000 claims description 5
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- 241001148471 unidentified anaerobic bacterium Species 0.000 claims description 2
- 229910000831 Steel Inorganic materials 0.000 claims 1
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/78—Recycling 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
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)
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
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
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.
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
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)
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).
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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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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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