WO2010119737A1 - Recirculation toilet based on complex fermentation method - Google Patents
Recirculation toilet based on complex fermentation method Download PDFInfo
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- WO2010119737A1 WO2010119737A1 PCT/JP2010/053827 JP2010053827W WO2010119737A1 WO 2010119737 A1 WO2010119737 A1 WO 2010119737A1 JP 2010053827 W JP2010053827 W JP 2010053827W WO 2010119737 A1 WO2010119737 A1 WO 2010119737A1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/005—Black water originating from toilets
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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
Definitions
- the present invention relates to a circulating toilet. More specifically, the present invention relates to a circulating toilet that is compact and does not generate bad odors using the technology of the complex fermentation method.
- Japanese Patent Application Laid-Open No. 11-131552 discloses a method in which microbial treatment is performed to separate excreta into solid and liquid, the solid is composted, and the liquid is purified and recycled.
- the method of using the urine storage tank generates a bad odor, which causes discomfort to the user.
- the manure transported here is both liquid and solid, and transportation costs are high.
- the purification facility using microorganisms has the disadvantage that the microorganisms become less effective when the temperature is lowered, and the purification efficiency deteriorates.
- the management of microorganisms is very delicate, and it may happen that microorganisms are not purified by unexpected events.
- the conventional treatment of urine with microorganisms has a drawback that the urine storage tank needs to be enlarged to some extent and cannot be made compact. Therefore, if it applies to a circulation type toilet, a processing tank will become huge.
- an object of the present invention is to provide a circulating toilet that has a limited private space and does not generate bad odor by microbial treatment, that is, a combined fermentation method .
- the present invention for solving the above-mentioned problems is a toilet seat, a fermenter and a fermenter / synthesizer tank for treating excrement from the toilet seat, and a fluid coming out of the fermenter / synthesizer tank into a fungus bed part and moisture, and the fungus bed It is a circulation type toilet by the combined fermentation method provided with the fermentation precipitation tank which returns a part to a fermenter, and the synthetic tank which carries out contact aeration of the water from the fermentation precipitation tank, and circulates as water for washing.
- the fermenter is disposed below the floor surface on which the toilet seat is disposed, and the fermentation synthesis tank, the fermentation precipitation tank, and the synthesis tank are disposed on the floor surface. is disposed (claim 1).
- the fermenter is a tank that mainly performs aerobic fermentation
- the fermentation synthesis tank is a tank that mainly performs both aerobic fermentation and anaerobic fermentation
- the fermentation In the settling tank anaerobic fermentation dominant fermentation and solid fermentation occurs at the bottom of the fermenter
- the synthesis tank is a tank that mainly performs anaerobic fermentation, and in each tank, the upstream side tank is the downstream side. Fermentation that increases the anaerobic degree as it moves to the tank is performed while continuously circulating (Claim 2).
- the fermenter is arranged in the horizontal direction of two or more toilet seats (Claim 3).
- the fermentation synthesis tank, the fermentation sedimentation tank, and the synthesis tank are configured to process excreta from two or more toilet seats (Claim 4).
- the synthesis tank can be disposed under the fermentation synthesis tank and the fermentation sedimentation tank (Claim 5).
- a microfilter can be provided in order to circulate and use the water from the synthesis tank as washing water (Claim 6).
- the excrement such as manure and paper is processed using the combined fermentation method, the excrement is effective without generating a bad odor outside. Can be processed. Moreover, it is possible to recirculate water by passing the water treated in the synthesis tank through, for example, a microfilter.
- the fermenter which is the first processing tank that receives the excrement from the toilet seat, is disposed directly below the toilet seat, the excrement can be processed effectively in a limited space.
- the treated water can be recirculated more safely.
- the circulation toilet of the present invention can be realized without performing foundation work. Therefore, for example, a temporary toilet or a mobile toilet can be realized.
- FIG. 1 is a diagram showing a first embodiment of the present invention. It is drawing which shows the concept of the complex fermentation method used by this invention. The top view which shows 2nd Embodiment of this invention. Drawing which shows 3rd Embodiment of this invention. The top view which shows 4th Embodiment of this invention.
- FIG. 1 is a drawing for explaining an embodiment of a circulating toilet of the present invention
- FIG. 2 is a drawing showing the concept of a combined fermentation method used in the present invention
- FIG. 3 is a second embodiment of the present invention.
- FIG. 4 is a plan view showing a third embodiment of the present invention
- FIG. 5 is a plan view showing a fourth embodiment of the present invention.
- the circulation type toilet according to the first embodiment of the present invention is a circulation type toilet that treats excrement based on the combined fermentation method and circulates and reuses the treated water as washing water. .
- complex fermentation used in the present specification refers to an organic / replacement / replacement based on the substrate and metabolism, causing the combined action of simple fermentation to re-fermentation, parallel re-fermentation, equilibrium re-fermentation, and solid fermentation.
- a chain circulation fermentation method that creates a biological information energy catalyst and creates its state. Such a chain-circulating fermentation leads all microorganisms to an effective ecosystem, generates an interlocking cycle of information and energy on the microorganisms, expresses the circulatory action of the microorganisms, and realizes coexistence, mutual prosperity, and symbiosis.
- the aerobic fermentation microorganisms start working.
- the fermentation microorganisms are yeast, lactic acid bacteria, etc., and physiologically active substances such as amino acids, vitamins, minerals, etc.
- make and suppress aerobic bacteria such as E. coli and filamentous fungi.
- lactic acid bacteria relay to facultative anaerobes, actinomycetes appear to make antibacterial substances, and anaerobic bacteria such as pathogenic bacteria and viruses are purified.
- nitrogen-fixing bacteria such as Azotobacter and rhizobia take in gas from the air and fix it.
- gas with photosynthetic bacteria, algae, and chemically synthesized bacteria immobilized. Is converted into useful substances and energy, such as photosynthesis.
- the organic sludge is converted (decomposed) into gas and water.
- the fermenter 2 which arrange
- a toilet that saves space within a range in which excrement (processing object) from the toilet and excrement (processing amount) of several to several tens of times per day are assumed in advance, For example, excrement in a portable toilet can be treated with a complex fermentation method in a space-saving manner. For this reason, in the circulating toilet of this embodiment, “fermentation synthesis tank 3”, “fermentation precipitation tank 4”, and “synthesis tank 5” are arranged immediately above “fermentation tank 2” as the first fermentation tank. Thus, the processed material and microorganisms are continuously circulated between these tanks.
- anaerobic degree is high as it transfers to "fermenter 2", “fermentation synthesis tank 3", “fermentation precipitation tank 4", “synthesis tank 5", and the downstream fermenter. Fermentation (complex fermentation in which anaerobic bacteria predominate over aerobic bacteria) occurs. Furthermore, the bacteria bed part from the fermentation sedimentation tank 4 is shifted to the fermentation tank 2, by circulating, to ensure the number of cells microorganism for performing fermentation treatment more than a predetermined number (e.g., 10 9 / cc or higher) Can do.
- a predetermined number e.g. 10 9 / cc or higher
- a fermenter 2 that is a first processing tank is disposed immediately below the toilet 1.
- the term “arranged immediately below the toilet 1” used in the present invention means that it is disposed directly below a support member of the toilet such as a floor.
- a shape that is wide in the horizontal direction and shallow in the vertical direction generally means a range up to a full space that can be taken directly under an installation place such as a floor.
- the fermenter 2 disposed immediately below the toilet 1 is widely disposed horizontally below the floor, which is the installation surface of the toilet 1.
- the fermenter 2 is a fermenter configured to be wide in the horizontal direction and short in the vertical direction, and a plurality of aeration means 21 are provided at the bottom of the fermenter 2.
- the fermentation that occurs in the fermenter 2 of the present invention is mainly aerobic fermentation (for example, fermentation at a ratio of aerobic fermentation 9: anaerobic fermentation 1).
- the term “mainly aerobic fermentation” used in the present specification means aerobic / anaerobic combined fermentation in which aerobic fermentation is dominant, and means that some anaerobic fermentation occurs.
- the fermentation that occurs in the fermenter 2 of the present invention means an aerobic / anaerobic combined fermentation in which aerobic fermentation is dominant (fermentation in the combined fermentation shown in FIG. 2 (start)).
- the fermentation synthesis tank 3 for carrying out the primary process in the fermenter 2 (combined fermentation was started) and processing the processed material immediately above the fermenter 2;
- a fermentation sedimentation tank 4 and a synthesis tank 5 are arranged.
- Fermentation synthesis tank 3 is a second fermentation tank having aeration means 31 that is long in the vertical direction and narrow in width. In this fermentation synthesis tank 3, fermentation with anaerobic degree higher than that of fermentation tank 2 occurs. More specifically, in the fermentation synthesizer 3, combined fermentation occurs at a ratio of “both aerobic fermentation and anaerobic fermentation”, for example, aerobic bacteria 5: anaerobic bacteria 5.
- one fermentation synthesis tank 3 is arranged.
- the number of fermentation synthesis tanks 3 is not limited to one, and may be, for example, 2 to 3 (described later). 5).
- the fluid processed in the fermentation synthesis tank 3 is sent to a fermentation precipitation tank 4 arranged in parallel with the fermentation synthesis tank 3.
- the fermentation sedimentation tank 4 has a function of dividing the fluid sent from the fermentation synthesis tank 3 into a fungus bed part and moisture, and returning the fungus bed part to the fermentation tank 2 while sending moisture to the subsequent synthesis tank. .
- fermentation occurs at a higher anaerobic degree than the fermentation synthesis tank 3, and solid fermentation occurs at the bottom of the fermentation precipitation tank 4.
- solid fermentation refers to fermentation performed by microorganisms adhering directly to or penetrating solids without using water directly (Applied Microbiology, Sawao Murao, Motoo Arai). (See joint edition).
- the fungal bed portion returned from the fermentation settling tank 4 to the fermenter 2 has not yet been prepared by preparing a suitable fermentation environment in the fermenter 2 (increasing effective bacterial cells and suppressing oxidized bacteria) and circulating and performing fermentation. Circulate the processed product. By circulating treatment in this way, the microorganisms in the fermenter 2 have a higher concentration and the amount of enzyme increases (higher concentration of microorganism and higher concentration of enzyme in FIG. 2).
- the synthesis tank 5 is arranged in parallel with the fermentation precipitation tank 4 and has a function of processing the water sent from the fermentation precipitation tank 4 to optimize the water.
- the synthesis tank 5 is a tank for performing biocatalyst and enzyme catalyst treatment with photosynthetic microorganisms, algae, algae and the like. Crystals of physiologically active substances are obtained by the catalytic action of these photosynthetic bacteria and algae, and normal temperature superconductivity, which is an action between substances, is terminated. The function of bacteria is terminated in the synthesis tank 5 and the DNA of the bacteria is decomposed to convert the bases into original proteins and use them as crystals.
- the synthesis tank 5 further has an ion catalyst layer made of an organic energy medium and an inorganic medium (C ⁇ SiO 2, Ti, Fe, Al, Cu, Mg, Li, Be, B etc.). These ion catalyst tanks cause atom, ion level transition, displacement, and sublimation (disappearance). Moreover, the energy transfer by an organic protein crystal
- an organic energy medium and an inorganic medium C ⁇ SiO 2, Ti, Fe, Al, Cu, Mg, Li, Be, B etc.
- the water thus treated is sent to the washing tank 6 through a microfilter as desired.
- the fermentation synthesis tank 3, the fermentation precipitation tank 4, and the synthesis tank are arranged immediately above the fermentation tank 2, and are moved downstream while continuously circulating in a limited space.
- the fermentation is carried out with a high anaerobic degree, and the cells produced in the fermentation sedimentation tank 4 where the fermentation with a high anaerobic degree is carried out are returned to the fermenter 2.
- it has become possible to perform complex fermentation in a limited space in which fermentations with different anaerobic degrees are continuously performed while maintaining a predetermined number of cells or more.
- the circulating toilet shown in FIG. 3 is a combined fermentation method in which excreta from a plurality of toilet seats 1 are combined into a set of fermentation tank 2, fermentation synthesis tank 3, fermentation precipitation tank 4, and synthesis tank 5. It is a circulation type toilet to process by.
- a common fermenter 2 is disposed on the floors of the two toilet seats 1 and 1 (toilet room).
- the fermenter 3, the fermentation sedimentation tank 4, and the synthetic tank 5 are arrange
- the fermenter 2 the fermentation synthesis tank 3, the fermentation precipitation tank 4, and the synthesis tank 5 which are one set of complex fermentation systems are arranged efficiently, and the circulation type toilet by complex fermentation is saved more space Can be realized.
- the circulation toilet shown in FIG. 4 is an embodiment in which the synthesis tank 5 is disposed immediately above the fermentation tank 2 and the fermentation synthesis tank 3 and the fermentation precipitation tank 4 are provided on the synthesis tank 5.
- the fermenter 2 is disposed immediately below the toilet bowl 1, the synthesis tank 5 is provided thereon, and the fermenter 3 and the fermentation precipitation tank 4 are further provided on the synthesis tank 5, thereby saving more space. It becomes possible to embody a recycled toilet.
- the circulation type toilet shown in FIG. 5 has a wide range of fermentation tanks 2 immediately below a plurality of toilets 1, 1, 1 at the toilet installation location, and a set of fermentation synthesis tank 3 and fermentation settling tank behind the toilet room. 4 is an example in which a synthetic tank 5 is arranged to share an environment in which complex fermentation of excreta from a plurality of toilets 1, 1, 1 is performed.
- the synthesis tank 5 is widely arranged behind the plurality of toilet rooms via the floor, and the fermentation synthesis tanks 3 and 3 and the fermentation precipitation tank 4 are arranged thereon.
- the synthesis tank 5 has a relatively large installation area, a plurality of fermentation synthesis tanks 3 are provided. As described above, by providing a plurality of fermentation synthesis tanks 3, complex fermentation is caused more reliably and excrement can be processed more efficiently.
- the fermentation synthesis tank 3 and the fermentation precipitation tank 4 are provided on the synthesis tank 5.
- the circulating toilet of the present invention has the fermenter 2, the fermenting synthesis tank 3, the fermenting settling tank 4 and the synthesizing tank 5 in a predetermined arrangement, so that the combined fermentation method is ensured in a limited space. It becomes possible to process the excrement by.
- the toilet bowl is disposed on the floor and the fermenter 2 is disposed below the floor.
- the foundation of the circulating toilet is assembled in a form covering the fermenter 2, and the top
- Such disaster toilets and emergency toilets can be easily installed without complicated foundation work because each part is configured as a unit.
- an operation-type circulation toilet can be realized by providing a unitized fermenter, fermentation synthesis tank, fermentation sedimentation tank, and synthesis tank.
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- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Biodiversity & Conservation Biology (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Non-Flushing Toilets (AREA)
- Sanitary Device For Flush Toilet (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
本発明は循環式トイレに関する。より詳しく述べると、複合発酵法の技術を用いたコンパクトでなおかつ悪臭が発生しない循環式トイレに関する。 The present invention relates to a circulating toilet. More specifically, the present invention relates to a circulating toilet that is compact and does not generate bad odors using the technology of the complex fermentation method.
下水道設備の普及していない地域の住居、公園、河川敷、山小屋等にトイレを設置した場合、通常その排泄物を屎尿収容槽に溜めて、屎尿がある程度の量になるとバキュームカー等で回収して浄化設備を有している場所に移送しここで処理していた。 When toilets are installed in houses, parks, riverbeds, mountain huts, etc. where sewerage facilities are not widespread, the excrement is usually collected in a urine storage tank, and when the amount of urine reaches a certain level, it can be collected with a vacuum car, etc. It was transferred to a place with purification equipment and processed there.
特開平11-131552号公報は、微生物処理を行い、排泄物の固体と液体とに分離し、固体はコンポスト化し、液体は浄化処理を行ってリサイクルする方法を開示している。 Japanese Patent Application Laid-Open No. 11-131552 discloses a method in which microbial treatment is performed to separate excreta into solid and liquid, the solid is composted, and the liquid is purified and recycled.
しかしながら、従来の屎尿の微生物処理方法において、屎尿収容槽を利用する方法は、悪臭が発生し、これを使用する者に不快感を与える。ここで運搬する屎尿は液体と固体の両者であり、運送費も高い。微生物による浄化設備は、微生物は温度が低くなると働きが鈍くなり、浄化効率が悪くなるという欠点がある。微生物の管理は非常に微妙であり、予期せぬ出来事により微生物が浄化しないことも生じる恐れがある。 However, in the conventional method for treating urine microorganisms, the method of using the urine storage tank generates a bad odor, which causes discomfort to the user. The manure transported here is both liquid and solid, and transportation costs are high. The purification facility using microorganisms has the disadvantage that the microorganisms become less effective when the temperature is lowered, and the purification efficiency deteriorates. The management of microorganisms is very delicate, and it may happen that microorganisms are not purified by unexpected events.
また、従来の屎尿の微生物処理では、屎尿収容槽をある程度大きくする必要があり、コンパクトにはならないという欠点があった。そのため、循環式トイレに適用すると、処理槽が巨大化してしまう。 Also, the conventional treatment of urine with microorganisms has a drawback that the urine storage tank needs to be enlarged to some extent and cannot be made compact. Therefore, if it applies to a circulation type toilet, a processing tank will become huge.
従って、本発明の課題は、微生物処理すなわち複合発酵法による、限られた専有スペースで、かつ悪臭の発生がない循環式トイレを提供することである。 Accordingly, an object of the present invention is to provide a circulating toilet that has a limited private space and does not generate bad odor by microbial treatment, that is, a combined fermentation method .
上記課題を解決する本発明は、便座と、前記便座からの排泄物を処理するための発酵槽と発酵合成槽と、前記発酵合成槽から出た流体を菌床部分と水分に分け前記菌床部分を発酵槽に戻す発酵沈殿槽と、前記発酵沈殿槽からの水分を接触曝気して水洗用の水として循環する合成槽と、を備えた複合発酵法による循環式トイレである。 The present invention for solving the above-mentioned problems is a toilet seat, a fermenter and a fermenter / synthesizer tank for treating excrement from the toilet seat, and a fluid coming out of the fermenter / synthesizer tank into a fungus bed part and moisture, and the fungus bed It is a circulation type toilet by the combined fermentation method provided with the fermentation precipitation tank which returns a part to a fermenter, and the synthetic tank which carries out contact aeration of the water from the fermentation precipitation tank, and circulates as water for washing.
本発明の複合発酵法による循環式トイレにおいて、前記発酵槽は、前記便座が配置された床面の下に配置され、前記発酵合成槽と前記発酵沈殿槽と合成槽は、前記床面の上に配置されている(請求項1)。 In the circulating toilet according to the combined fermentation method of the present invention, the fermenter is disposed below the floor surface on which the toilet seat is disposed, and the fermentation synthesis tank, the fermentation precipitation tank, and the synthesis tank are disposed on the floor surface. is disposed (claim 1).
本発明の複合発酵法による循環式トイレにおいて、前記発酵槽は、主として好気発酵を行う槽であり、前記発酵合成槽は、主として好気発酵と嫌気発酵の両方を行う槽であり、前記発酵沈殿槽では、嫌気発酵優位の発酵と、前記発酵槽の底部で固形発酵が生じ、前記合成槽は、主として嫌気発酵を行う槽であり、そして前記各槽において、上流側の槽から下流側の槽に移行するに従って嫌気度が高くなる発酵を連続して循環しながら行っている(請求項2)。 In the circulating toilet according to the combined fermentation method of the present invention, the fermenter is a tank that mainly performs aerobic fermentation, and the fermentation synthesis tank is a tank that mainly performs both aerobic fermentation and anaerobic fermentation, and the fermentation In the settling tank, anaerobic fermentation dominant fermentation and solid fermentation occurs at the bottom of the fermenter, and the synthesis tank is a tank that mainly performs anaerobic fermentation, and in each tank, the upstream side tank is the downstream side. Fermentation that increases the anaerobic degree as it moves to the tank is performed while continuously circulating (Claim 2).
本発明の好ましい実施形態によると、前記発酵槽は、2以上の便座の水平方向に渡って配置されている(請求項3)。 According to a preferred embodiment of the present invention, the fermenter is arranged in the horizontal direction of two or more toilet seats (Claim 3).
本発明の更に好ましい実施形態によると、前記発酵合成槽と、前記発酵沈殿槽と、前記合成槽は、2以上の便座からの排泄物を処理するように構成されている(請求項4)。 According to a further preferred embodiment of the present invention, the fermentation synthesis tank, the fermentation sedimentation tank, and the synthesis tank are configured to process excreta from two or more toilet seats (Claim 4).
また、本発明の循環式トイレにおいて、前記発酵合成槽と前記発酵沈殿槽の下に前記合成槽を配置することができる(請求項5)。 Further, in the circulation type toilet of the present invention, the synthesis tank can be disposed under the fermentation synthesis tank and the fermentation sedimentation tank (Claim 5).
また、本発明の循環式トイレにおいて、合成槽からの水を水洗用の水として循環利用するに当たってマイクロフィルタを設けることができる(請求項6)。 Further, in the circulation type toilet of the present invention, a microfilter can be provided in order to circulate and use the water from the synthesis tank as washing water (Claim 6).
また、発酵槽を土台として、その上に他の構成要件を配置することも本発明の範囲内である(請求項7)。 It is also within the scope of the present invention to place other components on the fermenter as a foundation (claim 7).
請求項1および請求項2に記載の循環式トイレによると、複合発酵法を使用して屎尿や紙などの排泄物を処理しているので、悪臭を外部に発生すること無しに排泄物を有効に処理することが可能である。しかも、合成槽で処理した水を、例えばマイクロフィルタなどに通過させることによって水を再循環させることが可能である。 According to the circulation type toilet according to claim 1 and claim 2, since the excrement such as manure and paper is processed using the combined fermentation method, the excrement is effective without generating a bad odor outside. Can be processed. Moreover, it is possible to recirculate water by passing the water treated in the synthesis tank through, for example, a microfilter.
さらに、便座からの排泄物を受ける第一の処理槽である発酵槽を便座と水平方向直下に配置したので、限られたスペースで有効に排泄物を処理できる構成となった。 Furthermore, since the fermenter, which is the first processing tank that receives the excrement from the toilet seat, is disposed directly below the toilet seat, the excrement can be processed effectively in a limited space.
請求項3および請求項4に記載の循環式トイレによると、更に2以上の便座からの排泄物を1つの複合発酵ユニット(発酵槽、発酵合成槽、合成槽)で処理することが可能となるので、更に省スペースで循環式トイレを実現可能となる。 According to the circulation type toilet according to claim 3 and claim 4, it becomes possible to further treat excreta from two or more toilet seats in one complex fermentation unit (fermentor, fermentation synthesis tank, synthesis tank). Therefore, it becomes possible to realize a recirculating toilet with further space saving.
請求項5に記載の循環式トイレによると、前記発酵合成槽と前記発酵沈殿槽の下に前記合成槽を配置することによって、更に省スペース化を図ることができる。 According to the circulation type toilet according to claim 5, further space saving can be achieved by arranging the synthesis tank below the fermentation synthesis tank and the fermentation sedimentation tank.
請求項6に記載の循環式トイレによると、合成槽で処理した水から不純物を除去するためのマクロフィルタが設けられているので、処理水をより安全に再循環させることができる。 According to the circulation type toilet according to claim 6, since the macro filter for removing impurities from the water treated in the synthesis tank is provided, the treated water can be recirculated more safely.
請求項7に記載の循環式トイレによると、発酵槽を土台と一体化したので、基礎工事を行わないで本発明の循環式トイレを具現化できる。そのため、例えば、仮設トイレ、移動式のトイレなどを具現化できる。 According to the circulation toilet according to claim 7, since the fermenter is integrated with the base, the circulation toilet of the present invention can be realized without performing foundation work. Therefore, for example, a temporary toilet or a mobile toilet can be realized.
以下、本発明の実施の形態を添付図面に基づいて説明する。図1は本発明の循環式トイレの実施形態を説明するための図面であり、図2は本発明で使用する複合発酵法の概念を
示す図面であり、図3は、本発明の第2実施形態を示す平面図であり、図4は、本発明の
第3実施形態を示す図面であり、そして図5は、本発明の第4実施形態を示す平面図であ
る。
Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. FIG. 1 is a drawing for explaining an embodiment of a circulating toilet of the present invention, FIG. 2 is a drawing showing the concept of a combined fermentation method used in the present invention, and FIG. 3 is a second embodiment of the present invention. FIG. 4 is a plan view showing a third embodiment of the present invention, and FIG. 5 is a plan view showing a fourth embodiment of the present invention.
(第1実施形態)
図1に示す通り本発明の第1実施形態に係る循環式トイレは、複合発酵法に基づいて排泄物を処理し、処理した水を水洗用の水として循環再利用する循環型のトイレである。
(First embodiment)
As shown in FIG. 1, the circulation type toilet according to the first embodiment of the present invention is a circulation type toilet that treats excrement based on the combined fermentation method and circulates and reuses the treated water as washing water. .
なお、本明細書で使用する用語「複合発酵法」とは、単発酵から復発酵、並行復発酵、平衡復発酵、固形発酵の連動と作用を引き起こし、基質と代謝から置換と交換という有機・生物的情報エネルギー触媒を生み出し、その状態を創り上げる連鎖循環式発酵法を言う。このような連鎖循環式発酵によりすべての微生物を有効な生態系へ導き、その微生物の情報とエネルギーの連動サイクルを生じ、微生物の循環作用を発現し、共存・共栄・共生を実現している。 The term “complex fermentation” used in the present specification refers to an organic / replacement / replacement based on the substrate and metabolism, causing the combined action of simple fermentation to re-fermentation, parallel re-fermentation, equilibrium re-fermentation, and solid fermentation. A chain circulation fermentation method that creates a biological information energy catalyst and creates its state. Such a chain-circulating fermentation leads all microorganisms to an effective ecosystem, generates an interlocking cycle of information and energy on the microorganisms, expresses the circulatory action of the microorganisms, and realizes coexistence, mutual prosperity, and symbiosis.
より具体的には、図2に示す通り、まず好気発酵微生物が働き出すことから始まるが、ここで発酵微生物とは酵母、乳酸菌類等であり、アミノ酸、ビタミン、ミネラル等の生理活性物質を作り、大腸菌、糸状菌等の好気性雑菌を浄菌、抑制する。次に乳酸菌が通性嫌気性菌類へとリレーし、放線菌類が現れて抗菌性物質を作り、病原性細菌、ウィルス等の嫌気性雑菌を浄菌する。この2つの浄菌作用が連動すると、アゾトバクター、根粒菌等の窒素固定菌が、空気中より気体を取りこんで固定する働きをし、最後に光合成細菌、藻類、化学合成細菌が固定化された気体を取りこんで光合成等、有用な物質やエネルギーへの変換が行われる。このサイクルが継続されることによって、有機性の汚泥はガスや水に変換(分解)されることになる。 More specifically, as shown in FIG. 2, first, the aerobic fermentation microorganisms start working. Here, the fermentation microorganisms are yeast, lactic acid bacteria, etc., and physiologically active substances such as amino acids, vitamins, minerals, etc. Make and suppress aerobic bacteria such as E. coli and filamentous fungi. Next, lactic acid bacteria relay to facultative anaerobes, actinomycetes appear to make antibacterial substances, and anaerobic bacteria such as pathogenic bacteria and viruses are purified. When these two bactericidal actions are linked, nitrogen-fixing bacteria such as Azotobacter and rhizobia take in gas from the air and fix it. Finally, gas with photosynthetic bacteria, algae, and chemically synthesized bacteria immobilized. Is converted into useful substances and energy, such as photosynthesis. By continuing this cycle, the organic sludge is converted (decomposed) into gas and water.
本発明においては、トイレという限られたスペースでこれらの複合発酵を実現するために図1に示すような便器1から水や紙などとともに排泄される屎尿を所定条件で配置された「発酵槽2」、「発酵合成槽3」、「発酵沈殿槽4」、「合成槽5」により、所定の菌体数を維持しつつ異なる嫌気度で連続して発酵させることに特徴がある。 In this invention, in order to implement | achieve these combined fermentation in the limited space called a toilet, the fermenter 2 which arrange | positioned the manure excreted with water, paper, etc. from the toilet bowl 1 as shown in FIG. ”,“ Fermentation synthesis tank 3 ”,“ fermentation sedimentation tank 4 ”, and“ synthesis tank 5 ”are characterized in that they are continuously fermented at different anaerobic degrees while maintaining a predetermined number of cells.
すなわち、本発明においては、トイレからの排泄物(処理対象物)と一日の処理量が数回から数十回の排泄物(処理量)が予め想定された範囲内で省スペースのトイレ、例えばポータブル型トイレにおける排泄物を省スペースでなおかつ確実に複合発酵法により処理可能としている。このために、本実施形態の循環式トイレでは、最初の発酵槽である「発酵槽2」の直上に、「発酵合成槽3」、「発酵沈殿槽4」、「合成槽5」を配置して、これらの槽間に処理物および微生物を絶えず循環させている。 That is, in the present invention, a toilet that saves space within a range in which excrement (processing object) from the toilet and excrement (processing amount) of several to several tens of times per day are assumed in advance, For example, excrement in a portable toilet can be treated with a complex fermentation method in a space-saving manner. For this reason, in the circulating toilet of this embodiment, “fermentation synthesis tank 3”, “fermentation precipitation tank 4”, and “synthesis tank 5” are arranged immediately above “fermentation tank 2” as the first fermentation tank. Thus, the processed material and microorganisms are continuously circulated between these tanks.
なお、本発明において、後述する通り、「発酵槽2」、「発酵合成槽3」、「発酵沈殿槽4」、「合成槽5」と下流側の発酵槽に移行するに従って、嫌気度が高い発酵(嫌気性菌が好気性菌と比較して優位に作用する複合発酵)が生じる。さらに、発酵沈殿槽4からの菌床部分を発酵槽2に移行させ、循環することにより、発酵処理を行う菌体微生物数を所定数以上(例えば、109個/cc以上)に確保することができる。 In addition, in this invention, as it mentions later, anaerobic degree is high as it transfers to "fermenter 2", "fermentation synthesis tank 3", "fermentation precipitation tank 4", "synthesis tank 5", and the downstream fermenter. Fermentation (complex fermentation in which anaerobic bacteria predominate over aerobic bacteria) occurs. Furthermore, the bacteria bed part from the fermentation sedimentation tank 4 is shifted to the fermentation tank 2, by circulating, to ensure the number of cells microorganism for performing fermentation treatment more than a predetermined number (e.g., 10 9 / cc or higher) Can do.
そのために、図1に示すように便器1の直下に第1の処理槽である発酵槽2を配置した。なお、本発明において使用する用語「便器1の直下に配置」とは、床などの便器の支持部材を介して真下に配置されることを意味する。 Therefore, as shown in FIG. 1, a fermenter 2 that is a first processing tank is disposed immediately below the toilet 1. Note that the term “arranged immediately below the toilet 1” used in the present invention means that it is disposed directly below a support member of the toilet such as a floor.
また、水平方向に広く、垂直方向に浅い形状とは、一般には床などの設置場所の真下に
おいて取れるスペース一杯までの範囲を言う。
Further, a shape that is wide in the horizontal direction and shallow in the vertical direction generally means a range up to a full space that can be taken directly under an installation place such as a floor.
本実施形態において便器1の直下に配置される発酵槽2は、便器1の設置面である床下に、前記床面と水平に幅広く配置されている。 In this embodiment, the fermenter 2 disposed immediately below the toilet 1 is widely disposed horizontally below the floor, which is the installation surface of the toilet 1.
発酵槽2は、水平方向に広く垂直方向に短く構成された発酵槽であり、発酵槽2の底部には、複数の曝気手段21が設けられている。 The fermenter 2 is a fermenter configured to be wide in the horizontal direction and short in the vertical direction, and a plurality of aeration means 21 are provided at the bottom of the fermenter 2.
このように構成された発酵槽2に便器1から水や紙類とともに屎尿が流されると、曝気条件下で主として好気発酵が生じる。 When the urine is flowed from the toilet 1 together with water and paper to the fermenter 2 configured in this way, mainly aerobic fermentation occurs under aerated conditions.
本発明の発酵槽2で生じる発酵は、主として好気発酵(例えば、好気発酵9:嫌気発酵1の割合での発酵)である。なお本明細書で使用する用語「主として好気発酵」とは、好気発酵が優位である好気/嫌気複合発酵を意味し、若干の嫌気発酵が生じていることを意味する。換言すると、本発明の発酵槽2で生じる発酵は、好気性発酵が優位な好気/嫌気複合発酵を意味する(図2に示す複合発酵における発酵(の開始))。 The fermentation that occurs in the fermenter 2 of the present invention is mainly aerobic fermentation (for example, fermentation at a ratio of aerobic fermentation 9: anaerobic fermentation 1). The term “mainly aerobic fermentation” used in the present specification means aerobic / anaerobic combined fermentation in which aerobic fermentation is dominant, and means that some anaerobic fermentation occurs. In other words, the fermentation that occurs in the fermenter 2 of the present invention means an aerobic / anaerobic combined fermentation in which aerobic fermentation is dominant (fermentation in the combined fermentation shown in FIG. 2 (start)).
また図1に示す通り、本実施形態において、発酵槽2の直上には、発酵槽2で一次処理された(複合発酵がスタートされた)、処理物を連続処理するための発酵合成槽3、発酵沈殿槽4、合成槽5が配置されている。 Moreover, as shown in FIG. 1, in this embodiment, the fermentation synthesis tank 3 for carrying out the primary process in the fermenter 2 (combined fermentation was started) and processing the processed material immediately above the fermenter 2; A fermentation sedimentation tank 4 and a synthesis tank 5 are arranged.
発酵合成槽3は、縦方向に長く幅が狭い曝気手段31を有する第2の発酵槽であり、この発酵合成槽3では、発酵槽2よりも高い嫌気度の発酵が生じる。より、具体的には、発酵合成槽3において、「好気発酵と嫌気発酵の両方」、例えば好気性菌5:嫌気性菌5の割合で複合発酵が生じる。 Fermentation synthesis tank 3 is a second fermentation tank having aeration means 31 that is long in the vertical direction and narrow in width. In this fermentation synthesis tank 3, fermentation with anaerobic degree higher than that of fermentation tank 2 occurs. More specifically, in the fermentation synthesizer 3, combined fermentation occurs at a ratio of “both aerobic fermentation and anaerobic fermentation”, for example, aerobic bacteria 5: anaerobic bacteria 5.
なお、図1に示す実施形態において、1つの発酵合成槽3を配置したが、発酵合成槽3の数は1つの限定されるものではなく、例えば2ないし3であってもよい(後述の図5参照)。 In the embodiment shown in FIG. 1, one fermentation synthesis tank 3 is arranged. However, the number of fermentation synthesis tanks 3 is not limited to one, and may be, for example, 2 to 3 (described later). 5).
次いで、発酵合成槽3で処理された流体は、発酵合成槽3に並列に配置された発酵沈殿槽4に送られる。 Next, the fluid processed in the fermentation synthesis tank 3 is sent to a fermentation precipitation tank 4 arranged in parallel with the fermentation synthesis tank 3.
発酵沈殿槽4は、発酵合成槽3から送られた流体を菌床部分と水分に分け、そして菌床部分を発酵槽2に戻し、一方水分を後段の合成槽に送る機能を有している。なお、発酵沈殿槽4では、発酵合成槽3よりも高い嫌気度で発酵(嫌気発酵が優位な発酵)が生じており、そして発酵沈殿槽4の底部においては、固形発酵が生じている。なお、本明細書で使用する用語「固形発酵」とは、水を直接使用せず固形物に直接微生物が付着または内部に侵入して行う発酵を意味する(応用微生物学、村尾澤夫、荒井基夫 共編参照)。 The fermentation sedimentation tank 4 has a function of dividing the fluid sent from the fermentation synthesis tank 3 into a fungus bed part and moisture, and returning the fungus bed part to the fermentation tank 2 while sending moisture to the subsequent synthesis tank. . In the fermentation sedimentation tank 4, fermentation (fermentation in which anaerobic fermentation is superior) occurs at a higher anaerobic degree than the fermentation synthesis tank 3, and solid fermentation occurs at the bottom of the fermentation precipitation tank 4. As used herein, the term “solid fermentation” refers to fermentation performed by microorganisms adhering directly to or penetrating solids without using water directly (Applied Microbiology, Sawao Murao, Motoo Arai). (See joint edition).
発酵沈殿槽4から発酵槽2に戻された菌床部分は、発酵槽2において好適な発酵環境を整えるとともに(有効菌体の増加と酸化細菌の抑制)、循環して発酵を行うことにより未処理の処理物を循環処理する。このように循環処理することによって、発酵槽2における微生物は、より高濃度となり、酵素量が増加する(図2における微生物の高濃度化および酵素の高濃度化)。 The fungal bed portion returned from the fermentation settling tank 4 to the fermenter 2 has not yet been prepared by preparing a suitable fermentation environment in the fermenter 2 (increasing effective bacterial cells and suppressing oxidized bacteria) and circulating and performing fermentation. Circulate the processed product. By circulating treatment in this way, the microorganisms in the fermenter 2 have a higher concentration and the amount of enzyme increases (higher concentration of microorganism and higher concentration of enzyme in FIG. 2).
また、合成槽5は、発酵沈殿槽4に並列に配置され、発酵沈殿槽4から送られてきた水分を処理して水を最適化する機能を有ししている。 Further, the synthesis tank 5 is arranged in parallel with the fermentation precipitation tank 4 and has a function of processing the water sent from the fermentation precipitation tank 4 to optimize the water.
合成槽5は、光合成系微生物群、藻類、藻菌類等による生物触媒及び酵素触媒処理を行うための槽である。これら光合成細菌や藻菌類の触媒作用により生理活性物質の結晶体を獲得し、物質間の作用である常温超伝導を終了さる。合成槽5にて細菌類の働きを終了させると共に、細菌類のDNAを分解させ、塩基類を元のタンパク化させ結晶体として作用に用いる。 The synthesis tank 5 is a tank for performing biocatalyst and enzyme catalyst treatment with photosynthetic microorganisms, algae, algae and the like. Crystals of physiologically active substances are obtained by the catalytic action of these photosynthetic bacteria and algae, and normal temperature superconductivity, which is an action between substances, is terminated. The function of bacteria is terminated in the synthesis tank 5 and the DNA of the bacteria is decomposed to convert the bases into original proteins and use them as crystals.
また、合成槽5は、さらに有機性エネルギー培地と無機性媒体(C・SiO2、Ti、Fe、Al、Cu、Mg、Li、Be、B etc.)によるイオン触媒層を有している。これらのイオン触媒槽により、原子、イオンレベルの転移、変位、昇華(消失)を生じさせる。また、有機性タンパク結晶によるエネルギー転移も同時に行われ、発酵沈殿槽4から送られてきた水分を水洗用の水として最適化する。 The synthesis tank 5 further has an ion catalyst layer made of an organic energy medium and an inorganic medium (C · SiO 2, Ti, Fe, Al, Cu, Mg, Li, Be, B etc.). These ion catalyst tanks cause atom, ion level transition, displacement, and sublimation (disappearance). Moreover, the energy transfer by an organic protein crystal | crystallization is also performed simultaneously, and the water | moisture content sent from the fermentation precipitation tank 4 is optimized as water for washing.
このようにして、処理された水は、所望によりマイクロフィルタを介して水洗タンク6へと送られる。 The water thus treated is sent to the washing tank 6 through a microfilter as desired.
第1実施形態に係る循環式トイレにおいて、発酵槽2の直上に、発酵合成槽3、発酵沈殿槽4および合成槽を配置し、限られた空間内で連続的になおかつ循環しながら下流に移行するに従って嫌気度の高い発酵を行い、嫌気度の高い発酵が行われている発酵沈殿槽4で生じた菌体を発酵槽2に戻す構成を有している。そのため、所定以上の菌体数を維持しつつ嫌気度の異なる発酵を連続して行う複合発酵を、限られたスペース内で行うことが可能となった。 In the circulation type toilet according to the first embodiment, the fermentation synthesis tank 3, the fermentation precipitation tank 4, and the synthesis tank are arranged immediately above the fermentation tank 2, and are moved downstream while continuously circulating in a limited space. Thus, the fermentation is carried out with a high anaerobic degree, and the cells produced in the fermentation sedimentation tank 4 where the fermentation with a high anaerobic degree is carried out are returned to the fermenter 2. For this reason, it has become possible to perform complex fermentation in a limited space in which fermentations with different anaerobic degrees are continuously performed while maintaining a predetermined number of cells or more.
このようにして、複合発酵を有効に実施することが可能であるので、紙類とともに水洗された屎尿を無臭で処理することが可能となる。しかも、処理後の水を水洗用の水として水洗タンク6に戻すことにより循環再利用することが可能となる。 In this way, since complex fermentation can be carried out effectively, it becomes possible to treat urine washed with paper together with water without odor. Moreover, the recycled water can be reused by returning the treated water to the washing tank 6 as washing water.
そのため、一度水を水洗タンク6に注入しておけば、緊急用トイレ、災害用のトイレ、
イベント用のトイレなど種々の場面でも有効に活用できる省スペースのトイレを実現でき
る。
Therefore, once water is poured into the washing tank 6, emergency toilets, disaster toilets,
A space-saving toilet that can be used effectively in various situations such as a toilet for an event can be realized.
(第2から第4実施形態)
次に、図3から図6に基づいて本発明の第2から第4実施形態に係る循環式トイレについて説明する。
(Second to fourth embodiments)
Next, a circulation type toilet according to second to fourth embodiments of the present invention will be described with reference to FIGS.
なお、図3から図6に示す第2から第4実施形態において、図1に示す第1実施形態と同一の部材については同一符号を附しその説明を省略する。 In addition, in 2nd-4th embodiment shown in FIGS. 3-6, the same code | symbol is attached | subjected about the same member as 1st Embodiment shown in FIG. 1, and the description is abbreviate | omitted.
図3に示す循環式トイレは、図1に示す実施形態において、複数の便座1からの排泄物を一組の発酵槽2、発酵合成槽3、発酵沈殿槽4及び合成槽5により複合発酵法により処理する循環式トイレである。 In the embodiment shown in FIG. 1, the circulating toilet shown in FIG. 3 is a combined fermentation method in which excreta from a plurality of toilet seats 1 are combined into a set of fermentation tank 2, fermentation synthesis tank 3, fermentation precipitation tank 4, and synthesis tank 5. It is a circulation type toilet to process by.
図3に示す通り、本実施形態では二つの便座1、1(トイレルーム)の床面に共用の発酵槽2を配置している。 As shown in FIG. 3, in this embodiment, a common fermenter 2 is disposed on the floors of the two toilet seats 1 and 1 (toilet room).
そして、トイレルームとトイレルームとの間に発酵槽3、発酵沈殿槽4、合成槽5を配置している。 And the fermenter 3, the fermentation sedimentation tank 4, and the synthetic tank 5 are arrange | positioned between the toilet rooms.
このように構成することによって、1組の複合発酵システムである発酵槽2、発酵合成槽3、発酵沈殿槽4及び合成槽5を効率的に配置し、より省スペースで複合発酵による循環式トイレの実現が可能となる。 By comprising in this way, the fermenter 2, the fermentation synthesis tank 3, the fermentation precipitation tank 4, and the synthesis tank 5 which are one set of complex fermentation systems are arranged efficiently, and the circulation type toilet by complex fermentation is saved more space Can be realized.
図4に示す循環式トイレは、合成槽5を発酵槽2の直上に配置し、合成槽5の上に発酵合成槽3と発酵沈殿槽4を設けた実施形態である。 The circulation toilet shown in FIG. 4 is an embodiment in which the synthesis tank 5 is disposed immediately above the fermentation tank 2 and the fermentation synthesis tank 3 and the fermentation precipitation tank 4 are provided on the synthesis tank 5.
このように、他の槽(合成槽5)を介して発酵槽3、発酵沈殿槽4を設けることも本発明の範囲内である。 Thus, it is also within the scope of the present invention to provide the fermentation tank 3 and the fermentation precipitation tank 4 via other tanks (synthesis tank 5).
図4に示す通り、発酵槽2を便器1の直下に配置し、その上に合成槽5を設け、更に合成槽5の上に発酵槽3、発酵沈殿槽4を設けることにより、より省スペース化した循環式トイレを具現化することが可能となる。 As shown in FIG. 4, the fermenter 2 is disposed immediately below the toilet bowl 1, the synthesis tank 5 is provided thereon, and the fermenter 3 and the fermentation precipitation tank 4 are further provided on the synthesis tank 5, thereby saving more space. It becomes possible to embody a recycled toilet.
また、図5に示す循環式トイレは、トイレ設置場所の複数の便器1、1、1の直下に幅広く発酵槽2を配置し、トイレルームの後方に一組の発酵合成槽3、発酵沈殿槽4、合成槽5を配置して、複数の便器1、1、1からの排泄物の複合発酵を実施する環境を共用した例である。 In addition, the circulation type toilet shown in FIG. 5 has a wide range of fermentation tanks 2 immediately below a plurality of toilets 1, 1, 1 at the toilet installation location, and a set of fermentation synthesis tank 3 and fermentation settling tank behind the toilet room. 4 is an example in which a synthetic tank 5 is arranged to share an environment in which complex fermentation of excreta from a plurality of toilets 1, 1, 1 is performed.
図5に示す実施形態では、床を介して複数のトイレルームの後方に幅広く合成槽5を配置し、その上に発酵合成槽3、3、発酵沈殿槽4を配置している。 In the embodiment shown in FIG. 5, the synthesis tank 5 is widely arranged behind the plurality of toilet rooms via the floor, and the fermentation synthesis tanks 3 and 3 and the fermentation precipitation tank 4 are arranged thereon.
そのため、合成槽5の比較的大きい設置面積を有するので、発酵合成槽3を複数設けている。このように、発酵合成槽3を複数設けることにより、より確実に複合発酵が惹起し、より効率的に排泄物を処理可能となる。 Therefore, since the synthesis tank 5 has a relatively large installation area, a plurality of fermentation synthesis tanks 3 are provided. As described above, by providing a plurality of fermentation synthesis tanks 3, complex fermentation is caused more reliably and excrement can be processed more efficiently.
なお、図5に示す実施形態では、合成槽5の上に発酵合成槽3と発酵沈殿槽4とを設けたが、図1に示す通り、発酵合成槽3、発酵沈殿槽4、合成槽5を並立することも本発明の範囲内である。 In the embodiment shown in FIG. 5, the fermentation synthesis tank 3 and the fermentation precipitation tank 4 are provided on the synthesis tank 5. However, as shown in FIG. 1, the fermentation synthesis tank 3, the fermentation precipitation tank 4, and the synthesis tank 5. It is also within the scope of the present invention to juxtapose.
このように、複数の便座(トイレルーム)に対して、一組の発酵槽2、発酵合成槽3、発酵沈殿槽4、合成槽5を共用することにより、より一層省スペース化を図ることが可能となる。 In this way, by sharing a set of fermentation tank 2, fermentation synthesis tank 3, fermentation precipitation tank 4, and synthesis tank 5 for a plurality of toilet seats (toilet rooms), further space saving can be achieved. It becomes possible.
以上説明した通り、本発明の循環式トイレは、所定の配置で発酵槽2、発酵合成槽3、発酵沈殿槽4および合成槽5を配置したので、限られたスペース内で確実に複合発酵法による排泄物を処理することが可能となる。 As described above, the circulating toilet of the present invention has the fermenter 2, the fermenting synthesis tank 3, the fermenting settling tank 4 and the synthesizing tank 5 in a predetermined arrangement, so that the combined fermentation method is ensured in a limited space. It becomes possible to process the excrement by.
以上、本発明の実施の形態を添付図面に基づいて説明したが、本発明はこれらの実施形態に限定されるものではない。 As mentioned above, although embodiment of this invention was described based on the accompanying drawing, this invention is not limited to these embodiment.
例えば、上記の実施の形態では、床上に便器を配置し、床下に発酵槽2を配置したが、床以外に、例えば、発酵槽2を覆う形で、循環式トイレの土台を組み、その上に、便器1を有するトイレルームと、他の処理槽を配置することも本発明の範囲内である。 For example, in the above embodiment, the toilet bowl is disposed on the floor and the fermenter 2 is disposed below the floor. However, in addition to the floor, for example, the foundation of the circulating toilet is assembled in a form covering the fermenter 2, and the top In addition, it is also within the scope of the present invention to arrange a toilet room having the toilet 1 and other treatment tanks.
このように、発酵槽を取り囲む状態で土台を作り、その上に便器1を有するトイレルームと、他の処理槽を配置することにより、省スペースで新たに水を加えない災害用の簡易トイレやイベント用等の仮設トイレを実現することが可能である。 In this way, by making a foundation in a state surrounding the fermentation tank, and placing a toilet room having the toilet 1 and another treatment tank thereon, a simple toilet for disasters that does not add water in a space-saving manner, It is possible to realize a temporary toilet for events.
このような災害用トイレや緊急用トイレは、各パーツをユニットとして構成しているために複雑な基礎工事を行わないでも、容易に設置可能である。 Such disaster toilets and emergency toilets can be easily installed without complicated foundation work because each part is configured as a unit.
特に、図4に示す循環式トイレにおいて、ユニット化された発酵槽、発酵合成槽、発酵沈殿槽、合成槽を設けることにより、稼動式の循環式トイレを具現化できる。 In particular, in the circulation toilet shown in FIG. 4, an operation-type circulation toilet can be realized by providing a unitized fermenter, fermentation synthesis tank, fermentation sedimentation tank, and synthesis tank.
1 便座
2 発酵槽
3 発酵合成槽
4 発酵沈殿槽
5 合成槽
6 水洗タンク
21 曝気手段
31 曝気手段
DESCRIPTION OF SYMBOLS 1 Toilet seat 2 Fermenter 3 Fermentation synthesis tank 4 Fermentation precipitation tank 5 Synthesis tank 6 Flush tank 21 Aeration means 31 Aeration means
Claims (7)
前記便座からの排泄物を処理するための発酵槽と発酵合成槽と、
前記発酵合成槽から出た流体を菌床部分と水分に分け前記菌床部分を発酵槽に戻す発酵沈殿槽と、
前記発酵沈殿槽からの水分を接触曝気して水洗用の水として循環する合成槽と、
を備えた複合発酵法による循環式トイレであって、
前記発酵槽は、前記便座が配置された床面の下に配置され、
前記発酵合成槽と前記発酵沈殿槽と合成槽は、前記床面の上に配置されていることを特徴とする複合発酵法による循環式トイレ。 Toilet seat and
A fermenter and a fermenter for processing excreta from the toilet seat;
A fermentation settling tank that divides the fluid from the fermentation synthesis tank into a fungus bed part and moisture and returns the fungus bed part to the fermenter;
A synthesis tank that circulates as water for washing by contact aeration of water from the fermentation settling tank;
A circulating toilet with a combined fermentation method,
The fermenter is disposed under the floor surface on which the toilet seat is disposed,
The fertilization synthesis tank, the fermentation precipitation tank, and the synthesis tank are arranged on the floor surface, and is a circulation type toilet by a combined fermentation method.
前記発酵合成槽は、主として好気発酵と嫌気発酵の両方を行う槽であり、
前記発酵沈殿槽では、嫌気発酵優位の発酵と、前記発酵槽の底部で固形発酵が生じ、
前記合成槽は、主として嫌気発酵を行う槽であり、そして
前記各槽において、上流側の槽から下流側の槽に移行するに従って嫌気度が高くなる発酵を連続して循環しながら行うことを特徴とする請求項1に記載の複合発酵法による循環式トイレ。 The fermenter is a tank that mainly performs aerobic fermentation,
The fermentation synthesis tank is a tank that mainly performs both aerobic fermentation and anaerobic fermentation,
In the fermentation settling tank, anaerobic fermentation dominant fermentation and solid fermentation occurs at the bottom of the fermentation tank,
The synthesis tank is a tank that mainly performs anaerobic fermentation, and in each tank, fermentation is performed while continuously anaerobically increasing as it moves from an upstream tank to a downstream tank. The circulation type toilet by the combined fermentation method according to claim 1.
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| JP2009-099489 | 2009-04-16 | ||
| JP2009099489A JP2010248792A (en) | 2009-04-16 | 2009-04-16 | Circulating toilet based on compound fermentation method |
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| WO2010119737A1 true WO2010119737A1 (en) | 2010-10-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| PCT/JP2010/053827 Ceased WO2010119737A1 (en) | 2009-04-16 | 2010-03-09 | Recirculation toilet based on complex fermentation method |
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| WO (1) | WO2010119737A1 (en) |
Cited By (6)
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| CN108505773A (en) * | 2018-06-13 | 2018-09-07 | 洛阳理工学院 | A kind of odorless public dry pail latrine in cities and towns |
| CN109678293A (en) * | 2018-12-27 | 2019-04-26 | 宜兴艾科森生态环卫设备有限公司 | A kind of ecology material balance lavatory and its operation method |
| CN110240281A (en) * | 2019-06-28 | 2019-09-17 | 湖北茂源水生态资源开发有限公司 | A kind of restorative procedure of water body in lake |
| CN111852084A (en) * | 2020-07-23 | 2020-10-30 | 张家口奥博环境科技有限公司 | Biodegradable intelligent ecological public toilet |
| CN112456657A (en) * | 2021-01-19 | 2021-03-09 | 惠州市济圣环保科技有限公司 | Sewage treatment method for circulating water ecological toilet |
| JP2022087970A (en) * | 2020-12-02 | 2022-06-14 | 康豪 高嶋 | Recycling biological toilet |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| JPWO2012060165A1 (en) | 2010-11-05 | 2014-05-12 | Necカシオモバイルコミュニケーションズ株式会社 | Mobile communication terminal |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108505773A (en) * | 2018-06-13 | 2018-09-07 | 洛阳理工学院 | A kind of odorless public dry pail latrine in cities and towns |
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| CN109678293A (en) * | 2018-12-27 | 2019-04-26 | 宜兴艾科森生态环卫设备有限公司 | A kind of ecology material balance lavatory and its operation method |
| CN109678293B (en) * | 2018-12-27 | 2022-03-29 | 宜兴艾科森生态环卫设备有限公司 | Ecological material balance toilet and operation method thereof |
| CN110240281A (en) * | 2019-06-28 | 2019-09-17 | 湖北茂源水生态资源开发有限公司 | A kind of restorative procedure of water body in lake |
| CN111852084A (en) * | 2020-07-23 | 2020-10-30 | 张家口奥博环境科技有限公司 | Biodegradable intelligent ecological public toilet |
| JP2022087970A (en) * | 2020-12-02 | 2022-06-14 | 康豪 高嶋 | Recycling biological toilet |
| JP7258836B2 (en) | 2020-12-02 | 2023-04-17 | 康豪 高嶋 | Recycled bio-toilet |
| CN112456657A (en) * | 2021-01-19 | 2021-03-09 | 惠州市济圣环保科技有限公司 | Sewage treatment method for circulating water ecological toilet |
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| JP2010248792A (en) | 2010-11-04 |
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