WO2023203787A1 - Recycling biological restroom - Google Patents

Recycling biological restroom Download PDF

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Publication number
WO2023203787A1
WO2023203787A1 PCT/JP2022/019213 JP2022019213W WO2023203787A1 WO 2023203787 A1 WO2023203787 A1 WO 2023203787A1 JP 2022019213 W JP2022019213 W JP 2022019213W WO 2023203787 A1 WO2023203787 A1 WO 2023203787A1
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Prior art keywords
fermentation
tank
water
bacteria
toilet
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PCT/JP2022/019213
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French (fr)
Japanese (ja)
Inventor
康豪 高嶋
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康豪 高嶋
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Priority to PCT/JP2022/019213 priority Critical patent/WO2023203787A1/en
Publication of WO2023203787A1 publication Critical patent/WO2023203787A1/en

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • EFIXED CONSTRUCTIONS
    • E03WATER SUPPLY; SEWERAGE
    • E03DWATER-CLOSETS OR URINALS WITH FLUSHING DEVICES; FLUSHING VALVES THEREFOR
    • E03D5/00Special constructions of flushing devices, e.g. closed flushing system
    • E03D5/016Special constructions of flushing devices, e.g. closed flushing system with recirculation of bowl-cleaning fluid

Definitions

  • the present invention relates to a recyclable bio-type toilet that can reliably decompose organic matter and human waste and make effective use of treated water.
  • bio-type toilets that utilize microorganisms are a type of toilet, and are also called ⁇ composting toilets'' or ⁇ composting toilets.'' Because they are not flushable, they have the advantage of being able to be installed in any location. There is. Additionally, since it does not require pumping work, it can be installed in areas that are inaccessible to human waste pumping vehicles. Since it does not cause excrement to flow away, it is attracting attention as a possible solution to the problem of excrement among mountain climbers, which has become a problem in recent years.
  • bio-type toilets There are two types of bio-type toilets: chip (sawdust) type and liquid treatment type using specific bacteria (microorganisms), which decompose excrement through the activity of aerobic microorganisms. It does not use water at all, or even if it does, it uses less water than flush toilets.
  • chip (sawdust) method mixes excrement with wood materials (sawdust, coconut fiber, peat moss, etc.) to achieve (1) decomposition by aerobic microorganisms, (2) Absorbs moisture and (3) reduces bad odors. Sawdust etc. are packed in the toilet tank, and the excreted excrement is stirred with the sawdust etc.
  • Non-patent document 1 Prior art documents Non-patent documents Non-patent document 1: NETIS (New Technology Information System) (Registration No. HK-040017) "Toilet that does not use water” In recycling toilets that use microorganisms, fermenting bacteria, yeast, lactic acid bacteria, heat-resistant soil bacteria, etc. are put into an aeration tank and fermented to reduce the volume of human waste, suppress bad odors, and recycle treated water. However, after 1 to 3 months, or even 6 months at most, antagonism occurs between naturally existing microorganisms such as airborne bacteria and fallen bacteria, and the introduced bacteria die, resulting in spoilage.
  • NETIS New Technology Information System
  • Patent document 1 uses two jet flush toilets and is used by 30 to 60 people a day.
  • a recycling toilet system that processes human waste and recycles water is placed below and behind the toilet 101, and can be transported by a 4-ton truck. Water is injected into a 27 m 3 fermentation liquefaction tank 102 through a blower 104 and an air pipe 105 while being aerated with a diffuser pipe 103 to fill it with water. 0.05% of the capacity of the fermentation liquefaction tank 102 was charged with molasses, aerated for 15 minutes, and EMBC (complex fermentation) solid bio was mixed at a weight ratio of 0.01% with respect to the amount of water.
  • EMBC complex fermentation
  • the MLSS fungal bed was introduced into the fermentation and liquefaction tank 102 so that the concentration was 500 ppm, and the mixture was aerated for 30 minutes. Sprinkle 0.1% of the volume of EMBC culture solution to provide strong aeration.
  • a blower 104 and air piping 105 are passed through the first fermentation tank 106 of 0.65 m 3 installed so that the water overflowing from the fermentation liquefaction tank 102 enters the bottom through the advection pipe 116, and is aerated with the aeration pipe 103. Inject water and make it full.
  • Molasses was added at 0.05% of the capacity of the first fermenter 106, aerated for 15 minutes, and EMBC (complex fermentation) solid bio was mixed at a weight ratio of 0.01% to the amount of water. After aeration for a period of time, the MLSS fungal bed was introduced into the first fermenter 106 to a concentration of 300 ppm, and aerated for 30 minutes. Sprinkle 0.1% of the volume of EMBC culture solution to provide strong aeration.
  • a blower 104 and air piping 105 are passed through a blower 104 and an air pipe 105 to a second fermentation tank 107 of 0.65 m 3 installed so that water that overflows from the first fermentation tank 106 enters the bottom through a convection pipe 116, and aeration is performed with an aeration pipe 103. Inject water and make it full. Molasses is added in an amount of 0.05% of the capacity of the second fermenter 107 and aerated for 1 hour, and the MLSS bacterial bed is added to the second fermenter 107 to a concentration of 100 ppm, and aerated for 30 minutes. Sprinkle 0.1% of the volume of EMBC culture solution to provide strong aeration.
  • a blower 104 and air piping 105 are passed through a blower 104 and air piping 105 to a 0.38 m 3 solid fermentation tank 109 installed so that the water overflowing from the second fermentation tank 107 enters through the material catalyst tank 108 , and the water is aerated with an aeration pipe 103 . Fill it with water and fill it with water. Sprinkle 0.1% of the volume of EMBC culture solution to provide slight aeration. The water pumped up from the solid fermentation tank 109 by the pump 110 is injected into the first fermentation and synthesis tank 112 installed through the transfer pipe 111 through the blower 104 and the air pipe 105 while being aerated by the aeration pipe 103. and fill it with water.
  • the MLSS bacterial bed was introduced into the first fermentation synthesis tank 112 to a concentration of 1000 ppm, and aerated for 30 minutes. Sprinkle 0.1% of the volume of EMBC culture solution and aerate it, and adjust the amount of air so that the DO is 8.0 to 8.5.
  • a second fermentation and synthesis tank 113 is installed so that water that overflows the first fermentation and synthesis tank 112 enters the bottom through the advection pipe 116, and a third fermentation and synthesis tank is similarly installed next to the second fermentation and synthesis tank 113.
  • 114 are prepared in the same manner as the first fermentation synthesis tank 112.
  • Water is injected from the third fermentation/synthesis tank 114 through an advection pipe 117 into a settling tank 115 installed so that the water enters at the same level as the water level of the settling tank 115 when the water is full, thereby filling the settling tank 115 with water.
  • a water storage tank 119 installed to collect water overflowing from the settling tank 115, and a water supply tank in the toilet 101 (to drain water and air at high pressure and flush human waste from the toilet bowl into the first fermentation and liquefaction tank) Prepare the tank by filling it with water in the same way as the sedimentation tank 115 and spraying the EMBC culture solution. After all this preparation is completed, maintain aeration and leave it for 72 hours before using it as a regular toilet.
  • the fermentation liquefaction tank 102 is medium, the first fermentation tank 106 is high, the second fermentation tank 107 is medium, the solid fermentation tank 109 is low, the first fermentation and synthesis tank 112 is high, and the aeration is high.
  • the second fermentation synthesis tank 113 is the middle one, and the third fermentation synthesis tank 114 is the middle one.
  • 0.02% of the capacity of the fermentation liquefaction tank 102 is filled with EMBC culture solution from the toilet drain in the morning and evening.
  • Anaerobic fermentation and solid fermentation are caused, degrading bacteria and degrading enzymes are made to exist, and complex fermentation and fermentation synthesis are caused in the first fermentation and synthesis tank 112, second fermentation and synthesis tank 113, and third fermentation and synthesis tank 114, and precipitation is carried out.
  • Anaerobic fermentation and solid fermentation are caused in the tank 115, and decomposition bacteria and decomposition enzymes are allowed to proliferate to decompose and eliminate human waste into water, carbon, and gas, and the treated water is recycled by simply replenishing the loss of water. Does not generate sludge.
  • the EMBC solid bio is a material consisting of 90% by weight of rice bran, 5% by weight of water, 2.5% by weight of rice husk, and 2.5% by weight of straw, and an enzyme released by microorganisms in a complex fermentation state is added to the material by 3% of the total amount of the material.
  • the number of microorganisms (live bacteria) per 1 cc increased from 10 7 to 10 8 to 10 9 by adding and mixing % by weight, humidifying, and turning the material upside down several times to mix in microorganisms from the air.
  • the number of viable bacteria increases dramatically to 10 20 ⁇ 10 30 , resulting in a high density of microorganisms, and after being left in this state for a while, it is dried and crushed.
  • the EMBC enzyme solution is a stock solution consisting of 90% by weight of water, 6% by weight of extracts extracted from pine, bamboo, plum, fig, chestnut, peach, and persimmon leaves, 3% by weight of okara, and 1% by weight of molasses, and air.
  • microorganisms are mixed in from inside and the number of microorganisms (live bacteria) per cc increases from 10 7 to 10 8 to 10 9 , the bacteria no longer die, and as a result, the number dramatically increases to 10 20 to 10 30 .
  • the enzyme solution is obtained by filtering the solution containing the antioxidant.
  • the MLSS fungal bed is made by treating human waste or domestic wastewater using a complex fermentation technology, causing anaerobic fermentation and solid fermentation in a sedimentation tank, etc., and microorganisms in a state of complex fermentation attach to the MLSS, and the anaerobic fungi It is allowed to take root (implantation) and is further colonized (bed) by anaerobic fungi.
  • sawdust The amount of sawdust in the chip (sawdust) type of bio-based toilets varies depending on the processing capacity, but the amount of sawdust required is approximately 0.01 m 3 x the number of times the toilet is processed per day.
  • the lifespan of sawdust is about 6 months under conditions of use commensurate with its processing capacity, but its lifespan is significantly reduced when it is used in a manner that exceeds its processing capacity.
  • the amount that can be fermented and decomposed is very small. Therefore, if it is used continuously beyond its capacity, undecomposed sludge accumulates and a bad odor is generated, making it necessary to replace the bacterial bed. Even if it is done several times a year, it has to be done manually.
  • the treated water will be recycled and no sludge will be generated, but the details of the recycling, what kind of treated water is used, and how it will be used are not specified.
  • the purpose of the present invention is to provide a recyclable bio-type toilet that eliminates the disadvantages of the conventional example, reliably achieves the decomposition of organic matter and human waste, and allows effective use of treated water for flushing the toilet bowl. Our goal is to provide the following.
  • the present invention as set forth in claim 1 provides a method for inducing complex fermentation in a complex fermentation and liquefaction toilet tank that receives excrement and urine from a toilet bowl as a primary treatment. Extract extracted from leaves selected from chestnuts, peaches, and persimmons, okara, and molasses are added, and aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria are inoculated, and aerobic bacteria and anaerobic bacteria are added. It is possible to coexist, co-prosperate, and coexist with sexual bacteria through facultative anaerobic bacteria, to produce composite fermentation malt that is the supernatant liquid, and to prepare water for the composite fermentation malt and molasses for aerobic fermentation.
  • a complex fermentation liquefaction tank with a fermentation liquefaction tank that is a tank to which the complex fermentation culture solution is added, a fermentation tank in which complex fermentation is carried out, and an SS removal layer. It consists of a solid fermentation tank and a flow rate adjustment tank, and liquefies it by sending it to these sequentially.
  • a secondary treatment it is sequentially led to a combined septic tank, a synthesis tank, and a treated water tank, where it is purified by combined fermentation, and then processed from the treated water tank.
  • the gist of the system is to use water as flush water for flushing toilet bowls.
  • Complex fermentation culture solution A solution that induces complex fermentation, in which extracts extracted from leaves selected from pine, bamboo, plum, fig, chestnut, peach, and persimmon, okara, and molasses are added to water.
  • inoculating aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria in A certain complex fermentation malt is produced, and to the complex fermentation malt is added charging water, molasses for aerobic fermentation, and anaerobic basis for anaerobic fermentation.
  • the treatment is clearly divided into the primary treatment of liquefying the solid and the secondary treatment of purifying and cleaning the liquefied material, and the primary treatment is combined fermentation.
  • the sludge is eliminated by the action of microorganisms through complex fermentation.
  • the sewage is purified by the action of microorganisms through complex fermentation, and is used as cleaning water. Treated water used for flushing toilet bowls is obtained. Since it is a complete circulation type, there is no need for water or sewage or pumping, and since it does not decompose, it does not generate bad odors.Furthermore, it does not generate E. coli, various bacteria, or pathogenic bacteria, so there is no need for sterilization with chemicals.
  • the complex fermentation malt used to create the complex fermentation culture is the seed for the complex fermentation, and contains polymer-bonded crystals of carbon.
  • Composite fermentation malt is made by combining water with extracts extracted from leaves selected from pine, bamboo, plum, fig, chestnut, peach, and persimmon as a natural material and used as a culture medium.
  • the mixture with molasses becomes a bacterial bed, in which aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria are planted. It is possible to create the foundation for complex fermentation of coexistence, co-prosperity, and symbiosis through bacteria. By planting aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria at the same time, aerobic bacteria and anaerobic bacteria can coexist through facultative anaerobic bacteria, but coexistence, mutual prosperity, and symbiosis are not antagonistic.
  • microorganisms bacteria
  • the microorganisms create a state of suspended animation, where they no longer kill each other and the bacteria die. can be reduced.
  • the microbial enzyme is combined and crystallized with the plant enzymes contained in the leaves of pine, bamboo, fig, chestnut, peach, and persimmon to produce antioxidant derivatives.
  • Antioxidants are physiologically active substances such as enzymes, vitamins, minerals, and amino acids, and are polymer-bound crystals of carbon. When this is returned to water, it reverts to microorganisms. This can be seen in proteins.
  • actinomycetes appear and produce antibacterial substances, which purify anaerobic harmful bacteria such as bacteria, pathogens, viruses, and rickettsia, and the two bactericidal actions work together, Azotobacter, Amylobacter, root-knot bacteria, etc. work to take in nitrogen from the air and fix it (nitrogen-fixing bacteria).
  • Photosynthetic bacteria, algae, and chemophotosynthetic microorganisms take in carbon dioxide and nitrogen gas to produce energy such as photosynthesis. This is possible through substitution and exchange.
  • Composite fermentation malt is obtained by removing the precipitate (coagulated solid matter of microorganisms) from the supernatant liquid of the solution containing antioxidants.
  • the complex fermentation culture solution is made by adding water, molasses for aerobic fermentation, and anaerobic base for anaerobic fermentation to complex fermentation malt, which is the seed for complex fermentation, to induce complex fermentation.
  • the anaerobic base here refers to chicken manure, dried okara, and rice bran.
  • Chicken manure is dried before it oxidizes, spoils, or rots.
  • Dried okara is the soybean residue left after squeezing the soy milk during tofu production, and is dried in its fresh state before it oxidizes, spoils, or rots.
  • Rice bran is the rice bran that is produced during rice polishing.
  • fermentation begins when a complex fermentation culture solution that induces complex fermentation is added to the complex fermentation liquefaction tank that receives excrement from the toilet bowl, and organic matter is broken down at the molecular bond level by lactic acid fermentation. Become. Complex fermentation further progresses in the fermentation tank, causing decomposition bacteria and decomposition enzymes to exist, decomposing and eliminating the sludge from human waste into water, carbon, and gas.
  • a solid fermenter having an SS removal layer by collecting the composite fermentation MLSS bacterial bed and returning it to the initial fermentation and liquefaction tank, it becomes easier to ferment, synthesize, or propagate the composite fermentation in the fermentation and liquefaction tank.
  • the MLSS fungal bed is created by processing human waste using a complex fermentation technology to cause anaerobic fermentation and solid fermentation, allowing microorganisms in a complex fermentation state to attach to the MLSS (seedling) and anaerobic fungi to take root (implantation). It is further colonized (bacteria bed) by anaerobic fungi.
  • the sewage from which the sludge has been removed is purified, and is sequentially introduced into a combined septic tank, a synthesis tank, and a treated water tank, where combined fermentation is continued.
  • biocatalyst cloth impregnated with the accumulated combined fermentation malt is suspended at predetermined intervals in the secondary treatment synthesis tank to perform purification by combined fermentation.
  • the main points are as follows.
  • a biocatalyst cloth impregnated with the accumulated combined fermentation malt is provided in the synthesis tank to further promote the combined fermentation.
  • Photosynthetic bacteria and algae that are present or expressed on the biocatalyst fabric take in carbon dioxide and nitrogen gases by light and perform energy replacement and exchange through photosynthetic processing, producing bioactive substances and protein crystals.
  • bio-treatment and photosynthesis treatment almost completely eliminates oxidation, deterioration, and putrefaction of the water to be treated, eliminates bacteria, and converts all harmful effects of microorganisms into effective effects.
  • the bio-treatment and photosynthesis treatment enable the coexistence, co-prosperity, and symbiosis of each of the bacteria, bring out the effective action of the microorganisms, cut off oxidation, deterioration, and putrefaction, and use the treatment as flush water for flushing toilet bowls. water is available.
  • the recyclable bio-toilet of the present invention can reliably decompose organic matter and human waste, and can effectively utilize treated water as flushing water for flushing the toilet bowl.
  • FIG. 1 is a flow diagram showing one embodiment of the recyclable bio-style toilet of the present invention.
  • FIG. 2 is a longitudinal sectional side view showing details of the composite fermentation and liquefaction toilet tank used in the recycling type bio-toilet of the present invention.
  • FIG. 3 is a plan view showing details of the composite fermentation and liquefaction toilet tank used in the recycling type bio-toilet of the present invention.
  • FIG. 4 is a photograph showing the treatment status of each tank about one week after the start of operation of the recycling type bio-toilet of the present invention.
  • FIG. 5 is a photograph showing the processing state approximately 60 minutes after the pumping shown in FIG. 4.
  • FIG. 6 is a side view showing a conventional example.
  • FIG. 7 is a plan view showing a conventional example.
  • FIG. 1 is a flow diagram showing one form of the recyclable bio-toilet of the present invention.
  • 1 is a toilet bowl 2 (a urinal, a toilet bowl in the case of a men's restroom, only a toilet bowl in the case of a women's restroom, other hand-washing, This is a toilet with washroom facilities, etc.).
  • Toilet 1 uses two jet flush toilets, and the two men's restrooms have a set of 2 urinals x 2 and 2 urinals x 2, and a complex fermentation liquefaction system that receives excrement from toilet 2.
  • the composite fermentation liquefaction tank 3 is a fermentation tank equipped with an aeration blower equipment (0.2 m 3 /min) 4 having a desk-type diffuser 10, and includes a fermentation liquefaction tank 5, a fermentation tank 6, a solid fermentation tank 7 and It consists of a flow rate adjustment tank 8, and the water is fed into these tanks in sequence.
  • the feeding method may be overflow.
  • the fermentation liquefaction tank 5 and the fermentation tank 6 have an area of 2.1 m 3
  • the solid fermentation tank 7 and the flow rate adjustment tank 8 have an area of 0.8 m 3 . Details of the composite fermentation and liquefaction toilet tank 3 are shown in FIGS.
  • the solid fermentation tank 7 is provided with an SS removal layer 11 using a crushed stone filter, and the flow rate adjustment tank 8 is provided with a submersible pump as a relay pump 9.
  • the fermentation liquefaction tank 5 was provided with a wastewater inflow area 5a, and an outflow baffle 23 for sending wastewater to the fermentation tank 6 was formed.
  • the fermenter 6 is provided with an outflow baffle 23 for feeding into the solid fermenter 7, and an inflow opening 24 is provided between the solid fermenter 7 and the flow rate adjustment tank 8.
  • the equipment for secondary treatment includes a combined septic tank (fermentation synthesis tank) 12, synthesis tanks 13, 14, 16, sand/carbon catalyst tanks (material carbon filtration tank) 21, 21 equipped with a carbon filter 18, and a treated water tank.
  • the combined septic tank (fermentation synthesis tank) 12, synthesis tanks 13, 14, and 16 are each equipped with blower equipment 4, and a pump 20 is also installed to send the water to the next tank. .
  • the combined septic tank has a combined septic tank (fermentation synthesis tank) 12a as a first treatment tank and a combined septic tank (fermentation synthesis tank) 12b as a second treatment tank, and the synthesis tank also has synthesis tanks 13 and 14.
  • a synthesis tank 16 was added to bring the total to three.
  • the synthesis tanks 13, 14, 16 have a capacity of 1 m 3 .
  • biocatalyst cloths 25 made of band-shaped nonwoven fabric impregnated with composite fermentation malt, which is accumulated enzyme water, were suspended at predetermined intervals to form synthesis catalyst tanks. .
  • the biocatalyst cloth 25 serves as a catalyst for inducing microorganisms into fermentation and synthesis, and then providing information to guide the synthesis.
  • the treated water from the final synthesis tank 16 is sent to a sand carbon catalyst tank (material carbon filtration tank) 21 equipped with a carbon filter 18, and further stored in a treated water tank 15, and used for cleaning the toilet bowl 2 by a fully automatic water supply pump 20.
  • the primary treatment is a combined fermentation liquefaction tank system in which a combined fermentation culture solution is added to cause the combined fermentation
  • the secondary treatment is a combined fermentation biosystem in which the combined fermentation is continued and treated as degrading enzyme water. There is a way to obtain water (purified water) and achieve 100% recycling.
  • the fermentation liquefaction tank 5 is the tank into which human waste first flows, and water is poured into it under aerated conditions to fill it with water.
  • a composite fermentation culture solution was added thereto at a weight ratio of 0.01% to the amount of water.
  • Water is injected into the fermentation tank 6 installed in such a way that the water overflowing from the fermentation liquefaction tank 5 enters the bottom via a convection pipe and is filled with water in an aerated state.
  • the above-mentioned composite fermentation culture solution may be introduced into the fermenter 6, or a composite fermentation MLSS bacterial bed (described later) may be introduced at a concentration of 1000 ppm.
  • MLSS is an abbreviation for Mixed Liquor Suspended Solids, which refers to suspended solids in a sludge mixture in an aeration tank during activated sludge treatment. By returning it to the tank, endings and beginnings, life and death are connected. The maximum energy obtained by microorganisms is transformed into new substances and new microscopic objects, and information evolves.
  • the composite fermentation MLSS fungal bed does not allow bacteria to rot, and the more time passes, the more the bacteria evolve and grow and become smarter.
  • the treated water that does not generate sludge is sent from the flow rate adjustment tank 8 to the combined septic tank (fermentation synthesis tank) 12a, and purification as secondary treatment begins.
  • aerobic bacteria such as lactic acid bacteria and yeast create physiological substances such as amino acids, sugars, vitamins, and minerals, and E. coli, miscellaneous bacteria, Inhibits general bacteria and prevents oxidation, deterioration, and putrefaction due to its antioxidant effect.
  • aerobic and anaerobic fungi such as lactic acid bacteria and actinomycetes produce antibiotics for Streptomyces, Penicillium, etc., which suppress pathogenic bacteria, viruses, Rickettsia, and the like.
  • anaerobic bacteria such as Azotobacter, Amylobacter, and root-knot bacteria fix nitrogen in the air.
  • biocatalyst cloths 25 made of band-shaped nonwoven fabrics impregnated with composite fermentation malt are suspended at predetermined intervals, and the biocatalyst cloths 25 absorb the existing/expressed photosynthesis.
  • Bacteria and algae take in carbon dioxide and nitrogen gases through light and perform energy replacement and exchange through photosynthetic processing, producing bioactive substances and protein crystals.
  • the treated water from the synthesis tanks 13, 14, and 16 is sent to a sand/carbon catalyst tank 21 that has a carbon filter 18 formed by stacking a silica catalyst layer, a carbon catalyst layer, and a material catalyst layer.
  • the cylinders show the state in the fermentation liquefaction tank 5, the state in the solid fermentation tank 7, the state in the combined septic tank (fermentation synthesis tank) 12a, which is the first treatment layer, and the state in the combined septic tank (fermentation synthesis tank), which is the second treatment layer. ) 12b, the state in the synthesis tank 16 which is a synthesis catalyst tank, and the state in the sand carbon catalyst tank 21 which is a material carbon filtration tank.
  • the sludge has not yet been completely liquefied in the combined septic tank (fermentation synthesis tank) 12a, but in the state shown in FIG. ing.
  • the difference between FIG. 4 and FIG. 5 is that the composite fermentation MLSS bacterial bed sinks after 60 minutes.
  • each tank is equipped with a blower equipment (0.2 m 3 /min) 4 for aeration, and the blower equipment 4 is operated after 20 hours of continuous operation. Stop driving for hours.
  • the sinking of the combined fermentation MLSS bacterial bed in Figure 5 occurs when the blower is stopped, and the microorganisms in the combined fermentation MLSS bacterial bed are aggregated, and if only the supernatant is transferred to the next tank while the combined fermentation MLSS bacterial bed is stopped, the composite fermentation occurs. Fermenting MLSS bacterial beds can be transported without containing microorganisms. This eliminates the need for a flocculant to flocculate microorganisms.

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Hydrology & Water Resources (AREA)
  • Microbiology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Aviation & Aerospace Engineering (AREA)
  • Health & Medical Sciences (AREA)
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  • Treatment Of Sludge (AREA)

Abstract

The present invention provides a recycling biological restroom with which organic matter and excreta can be reliably broken down and treatment water can be utilized effectively. A recycling biological restroom characterized in that: as a primary treatment, a composite fermentation liquid for inducing composite fermentation is added to a composite fermentation liquefied stool tank in which human waste is received from a toilet bowl; as a secondary treatment, the resultant mixture is guided through a merging purification tank, a synthesis tank, and a treatment water tank in the stated order; treatment water from the treatment water tank is used as cleansing water to cleanse the toilet bowl; the composite fermentation liquefied stool tank is configured from a fermentation liquefaction tank into which a composite fermentation culture liquid is added, a fermentation tank in which composite fermentation is carried out, a solids fermentation tank having an SS removal tank, and a flow rate adjustment tank, liquefaction being carried out by feeding stool into these tanks in the stated order; and in the synthesis tank during the secondary treatment, biocatalyst cloths soaked with accumulated composite fermentation malt are arranged in a suspended manner at prescribed intervals to carry out purification through composite fermentation.

Description

リサイクル型バイオ式トイレRecycled bio toilet
 本発明は、有機物及び、し尿の分解が確実に達成され処理水の有効活用が可能なリサイクル型バイオ式トイレに関するものである。 The present invention relates to a recyclable bio-type toilet that can reliably decompose organic matter and human waste and make effective use of treated water.
 従来のリサイクルトイレによる生屎尿の処理方法に大別して二種類ある。加熱乾燥処理と微生物利用処理である。加熱乾燥処理方式では、高額の電気代コストがかかること、乾燥した生屎尿を別途廃棄物として廃棄物処理業者に有料で引き取ってもらう必要がある。
 さらに悪臭の発生を抑制することは不可能で、プラチナ脱臭装置や活性炭などの物理的処理か化学薬品、芳香剤などで悪臭の抑制を図っているのが現状であるが、多少の抑制はできても、悪臭を根本的に除去することは成功していない。
 一方、微生物利用処理のバイオ式トイレは、便所の方式の一つで、「コンポストトイレ」「コンポスティングトイレ」(Composting toilet)とも呼ばれ、水洗式でないために、どんな場所にでも設置できるという利点がある。
 また、汲取り作業を必要としないため、屎尿汲取り車両の立ち入れない場所への設置も可能。排泄物を垂れ流す事も無いため、近年問題になっている登山愛好者の排泄物問題解決の糸口としても注目されている。
 このようなバイオ式トイレには、チップ(おが屑)式と特定の菌(微生物)による液体処理方式があり、好気性微生物の活動によって排泄物を分解する。水を全く使わないか、使う場合であっても水洗トイレ等に比べて少量で済む。
 下記非特許文献1にもあるが、チップ(おが屑)式は、排泄物を木質材(おがくず、ヤシ皮繊維、ピートモスなど)と混ぜ合わることによって、(1)好気性微生物による分解、(2)水分吸収、(3)悪臭の軽減を行う。
 おかくず等を便槽の中に詰め込んであり、排泄された糞尿を、おがくず等とともに攪拌して好気性微生物を活発化させ、分解・堆肥化させる。
  先行技術文献
  非特許文献
 非特許文献1:NETIS(新技術情報提供システム)(登録No.HK−040017)「水を使わないトイレ」
 微生物を利用したリサイクルトイレでは、発酵菌、酵母、乳酸菌、耐熱土壌菌等を曝気槽に投入し、発酵させることで生屎尿の減容と悪臭の抑制、及び処理水の循環利用を行なっているが、通常1ヶ月~3ヶ月、長いものでも6ヶ月を経過すると、空中浮遊菌、落下菌などの自然に存在する微生物との間で拮抗を起こし、投入した菌が死滅してしまい、腐敗に転じてメタンガス等の有毒、引火性ガスが発生し、爆発、火災等の危険が生じると共に、循環している処理水が腐敗し、黒く濁ってしまい、かつ悪臭が発生するため、腐敗した汚泥を取り出して別途廃棄物として廃棄物処理業者に有料で引き取ってもらい、装置全体を洗浄して再度注水してやり直すのが通例である。
 また、先に、出願人は下記特許文献に示すように、複合発酵法を用いて、屎尿処理槽における腐敗を完全に抑制し、屎尿を水と炭素とガスに分解するサイクルを起す微生物を利用したリサイクルトイレを提案している。
  先行技術文献
  特許文献
 特許文献1:特開2005−319445号公報
 この特許文献1のリサイクルトイレは、ジェット水洗式トイレを二つ使用し、1日30人~60人の使用を条件とし、図6、図7に示すようにトイレ101の下部及び背後に屎尿を処理して水をリサイクルするリサイクルトイレシステムを配置し、4tトラックで移送可能としたものである。
 27mの発酵液状化槽102にブロワー104とエアー配管105を通じ、散気管103でエアーレーションした状態で水を注入し、満水状態とする。
 それに糖蜜を発酵液状化槽102の容量の0.05%投入し、15分間曝気し、EMBC(複合発酵)固形バイオを水の量に対し重量比0.01%の割合で混合して、1時間曝気し、MLSS菌床を発酵液状化槽102内の濃度500ppmになるように投入し、30分曝気する。EMBC培養液を容量の0.1%散布して強曝気とする。
 発酵液状化槽102をオーバーフローした水が移流管116を通じて底部に入るように設置された0.65mの第一発酵槽106にブロワー104とエアー配管105を通じ、散気管103でエアーレーションした状態で水を注入し、満水状態とする。
 それに糖蜜を第一発酵槽106の容量の0.05%投入し、15分間曝気し、EMBC(複合発酵)固形バイオを水の量に対し重量比0.01%の割合で混合して、1時間曝気し、MLSS菌床を第一発酵槽106内の濃度300ppmになるように投入し、30分曝気する。
 EMBC培養液を容量の0.1%散布して強曝気とする。
 第一発酵槽106をオーバーフローした水が移流管116を通じて底部に入るように設置された0.65mの第二発酵槽107にブロワー104とエアー配管105を通じ、散気管103でエアーレーションした状態で水を注入し、満水状態とする。
 それに糖蜜を第二発酵槽107の容量の0.05%投入し、1時間曝気し、MLSS菌床を第二発酵槽107内の濃度100ppmになるように投入し、30分曝気する。
 EMBC培養液を容量の0.1%散布して強曝気とする。
 第二発酵槽107をオーバーフローした水がマテリアル触媒槽108を通じて入るように設置された0.38mの固型発酵槽109にブロワー104とエアー配管105を通じ、散気管103でエアーレーションした状態で水を注入し、満水状態とする。EMBC培養液を容量の0.1%散布して微弱曝気とする。
 固型発酵槽109からポンプ110で汲み上げた水が移送管111を通じて入るように設置された第一発酵合成槽112にブロワー104とエアー配管105を通じ、散気管103でエアーレーションした状態で水を注入し、満水状態とする。
 MLSS菌床を第一発酵合成槽112内の濃度1000ppmになるように投入し、30分曝気する。
 EMBC培養液を容量の0.1%散布して曝気し、DOが8.0~8.5となるようにエアー量を調整する。
 第一発酵合成槽112をオーバーフローした水が移流管116を通じて底部に入るように設置された第二発酵合成槽113、及び第二発酵合成槽113の次に同様に設置された第三発酵合成槽114をいずれも第一発酵合成槽112と同じように準備する。
 第三発酵合成槽114から移流管117を通じて沈澱槽115の満水時の水面と同じ高さに水が入るように設置された沈澱槽115に水を注入し、満水状態とする。
 沈澱槽115からオーバーフローした水が溜まるように設置された貯水槽119、及びトイレ101内の給水タンク(水と空気を高圧で流出させ、屎尿を便器から第一発酵液状化槽に水洗投入する為のもの)に沈澱槽115と同様に満水にしてEMBC培養液を散布して準備する。
 このすべての準備が終了した後、エアーレーションを維持し、72時間放置した後、通常のトイレとして使用する。
 使用開始後のエアーレーションは、発酵液状化槽102を中、第一発酵槽106を強、第二発酵槽107を中、固型発酵槽109を微弱、第一発酵合成槽112を強、第二発酵合成槽113を中、第三発酵合成槽114を中とする。
 使用開始後一週間は、朝と晩にEMBC培養液を発酵液状化槽102の容量の0.02%をトイレの排水口から投入する。
 各槽の状態を見ながら、合成を強くしたい場合は、EMBC培養液を投入し、発酵を強くする場合は、EMBC(複合発酵)固形バイオを投入し、沈澱槽115内に菌床が溜まってきた場合に、手動で第一発酵合成槽112に、さらに溜まる量が増えてきた場合に、手動で発酵液状化槽102に移送する。
 この状態でトイレを使用することによって、発酵液状化槽102で発酵が始まり、有機物の液状化が起こり、第一発酵槽106、第二発酵槽107で完全発酵が起き、固型発酵槽109で嫌気発酵、固形発酵を起こさせ、分解菌並びに分解酵素を現生させ、第一発酵合成槽112、第二発酵合成槽113、第三発酵合成槽114で複合発酵、発酵合成を起こさせ、沈殿槽115で嫌気発酵、固形発酵を起こさせ、さらに分解菌、分解酵素を原生させて、屎尿を水と炭素とガスに分解消失させ、水の減少を補給するのみで、処理水をリサイクルし、汚泥を発生させない。
 前記EMBC固形バイオは、米糠90重量%、水5重量%、籾殻2.5重量%、藁2.5重量%からなる材料に、複合発酵状態にある微生物が出す酵素を材料の全体量の3重量%を添加混合し、加湿し、材料の上下切り返しを数回繰り返し、空気中から微生物を混入させて、1ccあたりの微生物数(生菌数)が、10~10から10に増加させ、菌の死滅を無くし、それによって、1020~1030へと生菌数が飛躍的に増大し、微生物の高密度化がおき、この状態でしばらく寝かせた後、乾燥させて粉砕したものである。
 前記EMBC酵素液は、水90重量%、松、笹、梅、無花果、栗、桃、柿の葉から抽出した抽出液6重量%、オカラ3重量%、糖蜜1重量%からなる原液に、空気中から微生物を混入させて、1ccあたりの微生物数(生菌数)が、10~10から10に増加すると菌の死滅がなくなり、それによって、1020~1030へと飛躍的に増大し、微生物の高密度化がおき、さらにこの水溶液内で微生物酵素の高濃度化が起き、前記松、笹、無花果、栗、桃、柿の葉に含まれる植物酵素とともに結合結晶化(合成融合)し、誘導体たる抗酸化物質が生成される。この抗酸化物質を含む溶液を濾過して前記酵素液を得るのである。
 前記MLSS菌床は、屎尿あるいは生活排水を複合発酵技術で処理し、沈澱槽等で嫌気発酵、固形発酵を起こし、MLSSに複合発酵状態にある微生物が付着(着子)し、嫌気性菌類が根付く(着床)ようにし、さらに嫌気性菌類がコロニー化(菌床)したものである。
There are two main types of methods for processing human waste using conventional recycling toilets. These are heat drying treatment and treatment using microorganisms. The heat-drying method requires high electricity costs and requires a waste disposal company to collect the dried human waste as separate waste for a fee.
Furthermore, it is impossible to suppress the generation of bad odors, and currently efforts are being made to suppress the bad odors using physical treatments such as platinum deodorizing equipment and activated carbon, chemicals, and fragrances, but it is not possible to suppress them to some extent. However, it has not been successful in fundamentally eliminating the odor.
On the other hand, bio-type toilets that utilize microorganisms are a type of toilet, and are also called ``composting toilets'' or ``composting toilets.'' Because they are not flushable, they have the advantage of being able to be installed in any location. There is.
Additionally, since it does not require pumping work, it can be installed in areas that are inaccessible to human waste pumping vehicles. Since it does not cause excrement to flow away, it is attracting attention as a possible solution to the problem of excrement among mountain climbers, which has become a problem in recent years.
There are two types of bio-type toilets: chip (sawdust) type and liquid treatment type using specific bacteria (microorganisms), which decompose excrement through the activity of aerobic microorganisms. It does not use water at all, or even if it does, it uses less water than flush toilets.
As described in Non-Patent Document 1 below, the chip (sawdust) method mixes excrement with wood materials (sawdust, coconut fiber, peat moss, etc.) to achieve (1) decomposition by aerobic microorganisms, (2) Absorbs moisture and (3) reduces bad odors.
Sawdust etc. are packed in the toilet tank, and the excreted excrement is stirred with the sawdust etc. to activate aerobic microorganisms and decompose and compost it.
Prior art documents Non-patent documents Non-patent document 1: NETIS (New Technology Information System) (Registration No. HK-040017) "Toilet that does not use water"
In recycling toilets that use microorganisms, fermenting bacteria, yeast, lactic acid bacteria, heat-resistant soil bacteria, etc. are put into an aeration tank and fermented to reduce the volume of human waste, suppress bad odors, and recycle treated water. However, after 1 to 3 months, or even 6 months at most, antagonism occurs between naturally existing microorganisms such as airborne bacteria and fallen bacteria, and the introduced bacteria die, resulting in spoilage. In turn, toxic and flammable gases such as methane gas are generated, creating a danger of explosions and fires.In addition, the circulating treated water rots, becomes black and turbid, and produces a foul odor. It is customary to take it out and have a waste disposal company take it away as separate waste for a fee, then clean the entire device and refill it with water to start over.
In addition, as shown in the following patent document, the applicant has previously used microorganisms that completely suppress putrefaction in the human waste treatment tank and initiate a cycle of decomposing human waste into water, carbon, and gas using a complex fermentation method. We are proposing recycled toilets.
Prior art documents Patent documents Patent document 1: Japanese Patent Application Laid-open No. 2005-319445 The recycling toilet of Patent document 1 uses two jet flush toilets and is used by 30 to 60 people a day. As shown in FIG. 7, a recycling toilet system that processes human waste and recycles water is placed below and behind the toilet 101, and can be transported by a 4-ton truck.
Water is injected into a 27 m 3 fermentation liquefaction tank 102 through a blower 104 and an air pipe 105 while being aerated with a diffuser pipe 103 to fill it with water.
0.05% of the capacity of the fermentation liquefaction tank 102 was charged with molasses, aerated for 15 minutes, and EMBC (complex fermentation) solid bio was mixed at a weight ratio of 0.01% with respect to the amount of water. After aeration for a period of time, the MLSS fungal bed was introduced into the fermentation and liquefaction tank 102 so that the concentration was 500 ppm, and the mixture was aerated for 30 minutes. Sprinkle 0.1% of the volume of EMBC culture solution to provide strong aeration.
A blower 104 and air piping 105 are passed through the first fermentation tank 106 of 0.65 m 3 installed so that the water overflowing from the fermentation liquefaction tank 102 enters the bottom through the advection pipe 116, and is aerated with the aeration pipe 103. Inject water and make it full.
Molasses was added at 0.05% of the capacity of the first fermenter 106, aerated for 15 minutes, and EMBC (complex fermentation) solid bio was mixed at a weight ratio of 0.01% to the amount of water. After aeration for a period of time, the MLSS fungal bed was introduced into the first fermenter 106 to a concentration of 300 ppm, and aerated for 30 minutes.
Sprinkle 0.1% of the volume of EMBC culture solution to provide strong aeration.
A blower 104 and air piping 105 are passed through a blower 104 and an air pipe 105 to a second fermentation tank 107 of 0.65 m 3 installed so that water that overflows from the first fermentation tank 106 enters the bottom through a convection pipe 116, and aeration is performed with an aeration pipe 103. Inject water and make it full.
Molasses is added in an amount of 0.05% of the capacity of the second fermenter 107 and aerated for 1 hour, and the MLSS bacterial bed is added to the second fermenter 107 to a concentration of 100 ppm, and aerated for 30 minutes.
Sprinkle 0.1% of the volume of EMBC culture solution to provide strong aeration.
A blower 104 and air piping 105 are passed through a blower 104 and air piping 105 to a 0.38 m 3 solid fermentation tank 109 installed so that the water overflowing from the second fermentation tank 107 enters through the material catalyst tank 108 , and the water is aerated with an aeration pipe 103 . Fill it with water and fill it with water. Sprinkle 0.1% of the volume of EMBC culture solution to provide slight aeration.
The water pumped up from the solid fermentation tank 109 by the pump 110 is injected into the first fermentation and synthesis tank 112 installed through the transfer pipe 111 through the blower 104 and the air pipe 105 while being aerated by the aeration pipe 103. and fill it with water.
The MLSS bacterial bed was introduced into the first fermentation synthesis tank 112 to a concentration of 1000 ppm, and aerated for 30 minutes.
Sprinkle 0.1% of the volume of EMBC culture solution and aerate it, and adjust the amount of air so that the DO is 8.0 to 8.5.
A second fermentation and synthesis tank 113 is installed so that water that overflows the first fermentation and synthesis tank 112 enters the bottom through the advection pipe 116, and a third fermentation and synthesis tank is similarly installed next to the second fermentation and synthesis tank 113. 114 are prepared in the same manner as the first fermentation synthesis tank 112.
Water is injected from the third fermentation/synthesis tank 114 through an advection pipe 117 into a settling tank 115 installed so that the water enters at the same level as the water level of the settling tank 115 when the water is full, thereby filling the settling tank 115 with water.
A water storage tank 119 installed to collect water overflowing from the settling tank 115, and a water supply tank in the toilet 101 (to drain water and air at high pressure and flush human waste from the toilet bowl into the first fermentation and liquefaction tank) Prepare the tank by filling it with water in the same way as the sedimentation tank 115 and spraying the EMBC culture solution.
After all this preparation is completed, maintain aeration and leave it for 72 hours before using it as a regular toilet.
After starting to use the aeration, the fermentation liquefaction tank 102 is medium, the first fermentation tank 106 is high, the second fermentation tank 107 is medium, the solid fermentation tank 109 is low, the first fermentation and synthesis tank 112 is high, and the aeration is high. The second fermentation synthesis tank 113 is the middle one, and the third fermentation synthesis tank 114 is the middle one.
For one week after the start of use, 0.02% of the capacity of the fermentation liquefaction tank 102 is filled with EMBC culture solution from the toilet drain in the morning and evening.
While checking the status of each tank, if you want to strengthen the synthesis, add EMBC culture solution, and if you want to strengthen the fermentation, add EMBC (complex fermentation) solid bio, until the bacterial bed accumulates in the sedimentation tank 115. When the amount accumulated is increased, it is manually transferred to the first fermentation synthesis tank 112, and when the amount accumulated further increases, it is manually transferred to the fermentation and liquefaction tank 102.
By using the toilet in this state, fermentation begins in the fermentation liquefaction tank 102, liquefaction of organic matter occurs, complete fermentation occurs in the first fermentation tank 106 and second fermentation tank 107, and in the solid fermentation tank 109. Anaerobic fermentation and solid fermentation are caused, degrading bacteria and degrading enzymes are made to exist, and complex fermentation and fermentation synthesis are caused in the first fermentation and synthesis tank 112, second fermentation and synthesis tank 113, and third fermentation and synthesis tank 114, and precipitation is carried out. Anaerobic fermentation and solid fermentation are caused in the tank 115, and decomposition bacteria and decomposition enzymes are allowed to proliferate to decompose and eliminate human waste into water, carbon, and gas, and the treated water is recycled by simply replenishing the loss of water. Does not generate sludge.
The EMBC solid bio is a material consisting of 90% by weight of rice bran, 5% by weight of water, 2.5% by weight of rice husk, and 2.5% by weight of straw, and an enzyme released by microorganisms in a complex fermentation state is added to the material by 3% of the total amount of the material. The number of microorganisms (live bacteria) per 1 cc increased from 10 7 to 10 8 to 10 9 by adding and mixing % by weight, humidifying, and turning the material upside down several times to mix in microorganisms from the air. As a result, the number of viable bacteria increases dramatically to 10 20 ~ 10 30 , resulting in a high density of microorganisms, and after being left in this state for a while, it is dried and crushed. It is.
The EMBC enzyme solution is a stock solution consisting of 90% by weight of water, 6% by weight of extracts extracted from pine, bamboo, plum, fig, chestnut, peach, and persimmon leaves, 3% by weight of okara, and 1% by weight of molasses, and air. When microorganisms are mixed in from inside and the number of microorganisms (live bacteria) per cc increases from 10 7 to 10 8 to 10 9 , the bacteria no longer die, and as a result, the number dramatically increases to 10 20 to 10 30 . This results in a high density of microorganisms, and a high concentration of microbial enzymes within this aqueous solution, resulting in combined crystallization (synthesis) with the plant enzymes contained in the pine, bamboo, fig, chestnut, peach, and persimmon leaves. fusion), and antioxidant derivatives are produced. The enzyme solution is obtained by filtering the solution containing the antioxidant.
The MLSS fungal bed is made by treating human waste or domestic wastewater using a complex fermentation technology, causing anaerobic fermentation and solid fermentation in a sedimentation tank, etc., and microorganisms in a state of complex fermentation attach to the MLSS, and the anaerobic fungi It is allowed to take root (implantation) and is further colonized (bed) by anaerobic fungi.
 前記バイオ式トイレでチップ(おが屑)式のものは、オガクズの量は、その処理能力によって様々であるが、1日当たり処理数×0.01m程度が必要である。処理能力相応の使用状態での、おがくずの寿命は6ヶ月程度であるが、処理能力を上回る使用下での寿命は著しく低下してしまう。
 さらに、限られた処理槽の中では、発酵分解出来る量は微量である。そのため、連続して能力以上に使用すると、分解しきれない汚泥が溜まり悪臭が発生して、菌床の交換をせざるをえない状態になる。年に何回かと言っても、それは人力で行うしかない。大変な負担であり、ベタベタした状態でのコンポスト使用は、環境衛生上問題になる。また、災害時やイベント等で1日の使用限度を超えた使用を続けると、溜の状態になり汲み取りが必要となる。
 このようにチップ(おが屑)式のものは維持・管理としてチップの補充・交換が必要であり、水道は原則的に使用不可で、トイレツトペーパーは分別回収または投入可だが、環境負荷としては交換されたチップ(おが屑)の焼却などにより大気を汚染するおそれがある。
 さらに、好気性微生物の活性化のため、便槽の撹拌が必要であり、手動ハンドルなどによって撹拌するものと、電気モーターで撹拌するものとに分類される。
 悪臭発生については、使用頻度や時間の経過による。
 特定の菌(微生物)による液体処理方式でも、同じく悪臭発生については、使用頻度や時間の経過による。
 また、特定の菌(微生物)による液体処理方式では維持・管理として汚泥の引き抜きが必要となり、引抜かれた汚泥は尿処理場等へ運ばれ、汲み取り式と岡様の汚染を引き起こすおそれがある。さらに、トイレツトペーパーは分別回収しなければならない。
 前記特許文献1のリサイクルトイレシステムでは、EMBC培養液なるものが使用され、強曝気とする場合にこのEMBC培養液が散布されるが、EMBC培養液がいかなるものであるかの説明はなされていない。
 また、最終段階として処理水をリサイクルし、汚泥を発生させないとしているが、リサイクルの具体的内容や処理水がどのようなものであり、どのように用いるかは示されていない。
 本発明の目的は前記従来例の不都合を解消し、有機物及び、し尿の分解が確実に達成され、かつ、処理水を洗浄水として便器洗浄に用いることの有効活用が可能なリサイクル型バイオ式トイレを提供することにある。
The amount of sawdust in the chip (sawdust) type of bio-based toilets varies depending on the processing capacity, but the amount of sawdust required is approximately 0.01 m 3 x the number of times the toilet is processed per day. The lifespan of sawdust is about 6 months under conditions of use commensurate with its processing capacity, but its lifespan is significantly reduced when it is used in a manner that exceeds its processing capacity.
Furthermore, in the limited processing tank, the amount that can be fermented and decomposed is very small. Therefore, if it is used continuously beyond its capacity, undecomposed sludge accumulates and a bad odor is generated, making it necessary to replace the bacterial bed. Even if it is done several times a year, it has to be done manually. It is a heavy burden, and using compost in a sticky state poses environmental health problems. Additionally, if the water is used beyond the daily usage limit during disasters or events, it will accumulate and need to be drained.
In this way, chip (sawdust) type toilets require replenishment and replacement of chips for maintenance and management, and in principle, water supply cannot be used, and toilet paper can be collected separately or thrown away, but replacing it is an environmental burden. There is a risk of air pollution due to incineration of the chips (sawdust).
Furthermore, in order to activate aerobic microorganisms, it is necessary to stir the toilet tank, which is classified into those that are stirred using a manual handle or the like, and those that are stirred using an electric motor.
The occurrence of bad odors depends on the frequency of use and the passage of time.
Even with liquid treatment methods using specific bacteria (microorganisms), the occurrence of bad odors also depends on the frequency of use and the passage of time.
In addition, liquid treatment methods using specific bacteria (microorganisms) require the removal of sludge for maintenance and management, and the removed sludge is transported to urine treatment plants, etc., which may cause contamination. Additionally, toilet paper must be collected separately.
In the recycling toilet system of Patent Document 1, an EMBC culture solution is used, and this EMBC culture solution is sprayed during strong aeration, but there is no explanation as to what the EMBC culture solution is. .
Furthermore, as a final step, the treated water will be recycled and no sludge will be generated, but the details of the recycling, what kind of treated water is used, and how it will be used are not specified.
The purpose of the present invention is to provide a recyclable bio-type toilet that eliminates the disadvantages of the conventional example, reliably achieves the decomposition of organic matter and human waste, and allows effective use of treated water for flushing the toilet bowl. Our goal is to provide the following.
 前記目的を達成するため請求項1記載の本発明は、一次処理として、便器からの糞尿を受け入れる複合発酵液化便槽に複合発酵を誘発するものとして、水に、松、笹、梅、無花果、栗、桃、柿のいずれかから選択された葉から抽出した抽出液とオカラと糖蜜を加え、ここに好気性菌と嫌気性菌、および通性嫌気性菌を植付けて、好気性菌と嫌気性菌とを通性嫌気性菌を介して共存・共栄・共生を可能とし、その上澄液である複合発酵モルトを製造し、該複合発酵モルトに仕込み水および、好気発酵をする糖蜜、嫌気発酵をする嫌気基礎を加えてなる下記複合発酵培養液を加え、複合発酵液化便槽は、複合発酵培養液を加える槽である発酵液化槽、複合発酵がおこなわれる発酵槽、SS除去層を有する固形発酵槽、流量調整槽からなり、これらに順次送ることで液化を行い、二次処理として、合併浄化槽、合成槽、処理水槽に順次導き、複合発酵による浄化を行い、 処理水槽からの処理水を洗浄水として便器洗浄に用いることを要旨とするものである。
 複合発酵培養液:複合発酵を誘導するもので、水に、松、笹、梅、無花果、栗、桃、柿のいずれかから選択された葉から抽出した抽出液とオカラと糖蜜を加え、ここに好気性菌と嫌気性菌、および通性嫌気性菌を植付けて、好気性菌と嫌気性菌とを通性嫌気性菌を介して共存・共栄・共生を可能とし、その上澄液である複合発酵モルトを製造し、該複合発酵モルトに仕込み水および、好気発酵をする糖蜜、嫌気発酵をする嫌気基礎を加えてなる。
 請求項1記載の本発明によれば、処理を固体から液化する第1次処理と、液化したものを浄化してきれいにする第2次処理を明確に分けたものであり、一次処理として合発酵培養液を便器からの糞尿を受け入れる発酵槽に加えることで、複合発酵による微生物の働きで汚泥の消失が得られ、二次処理としてさらに複合発酵による微生物の働きで汚水が浄化され、洗浄水として便器洗浄に用いる処理水が得られる。
 完全循環型なので、上下水道不要・汲み取り不要であり、腐敗しないので悪臭も発生せず、さらに、大腸菌・雑菌・病原菌が発生しないので、薬剤による殺菌も不要である。
 また、エアーレーション用プロワーと、移送用ポンプのための電気は必要だが、停電になっても小型発電機で充分対応できる。
 避難所、公園などに備えて、普段は公共トイレとして使用し、災害時にもそのまま使用可能なトイレとして常備することも可能である。
 複合発酵培養液を作成する複合発酵モルトは、複合発酵をおこさせる種となるものであり、ここには炭素の高分子結合結晶が含まれている。複合発酵モルトは、水に、松、笹、梅、無花果、栗、桃、柿のいずれかから選択された葉から抽出した抽出液は自然の素材として培地媒体として使用され、水に、これと糖蜜を加えたものは菌床となり、ここに好気性菌と嫌気性菌、および通性嫌気性菌を植付け、その上澄液であることで、好気性菌と嫌気性菌が通性嫌気性菌を介して共存、共栄、共生する複合発酵をおこさせる下地を作ることができる。
 好気性菌と嫌気性菌、および通性嫌気性菌を同時に植付けることで、通性嫌気性菌を介して好気性菌と嫌気性菌が共存できるが、共存・共栄・共生とは拮抗しないこと(殺し合わないこと)であり、微生物(菌)が10分の1のサイズになり、1ccあたりの微生物数が増加すると微生物の仮死状態を作ることでお互いに殺し合わなくなり、菌の死滅を減少させることができる。
 この状態では、微生物酵素は、前記松、笹、無花果、栗、桃、柿の葉に含まれる植物酵素とともに結合結晶化して誘導体たる抗酸化物質が生成される。抗酸化物質は酵素、ビタミン、ミネラル、アミノ酸などの生理活性物質であり、炭素の高分子結合結晶となるものである。これを水中に戻すと微生物に戻る。その姿をたんぱく質で見ることができる。
 通性嫌気性菌を介して好気性菌と嫌気性菌が共存・共栄・共生する複合発酵は、酵母、乳酸菌類等の好気性発酵微生物が働き出すことから始まり、好気性発酵微生物がアミノ酸、糖類、ビタミン、ミネラル等の生理活性物質を造り、大腸菌、糸状菌、雑菌類等の好気性有害菌を浄菌し、次に好気性発酵微生物の乳酸菌が通性嫌気性乳酸菌及び通性嫌気性菌類へとリレーし、それによって放線菌が現れて抗菌性物質を造り、これが細菌、病原菌、ウイルス、リケッチャ等の嫌気性有害菌を浄菌し、前記二つの浄菌作用が連動することで、アゾトバクター、アミロバクター、根瘤菌等が空気中から窒素を取り込み固定する働きをし(窒素固定菌)、最後に光合成細菌、藻菌類、化学光合成微生物が炭酸ガス、窒素ガスを取り込んで光合成等、エネルギー・置換と交換を行うことで可能となる。
 この抗酸化物質を含む溶液の上澄液として沈殿物(微生物の凝固固形物)を取り除いたものが複合発酵モルトである。
 複合発酵培養液は、複合発酵の種となる複合発酵モルトに仕込み水および、好気発酵をする糖蜜、嫌気発酵をする嫌気基礎を加えてなり、複合発酵を惹起させるものである。
 ここで嫌気基礎とは、鶏糞と乾燥オカラと米糠をいう。鶏糞は、酸化・変敗・腐敗する前の状態で乾燥させたものである。乾燥オカラは、豆腐製造の際に豆乳を絞った後の残りの大豆かすで、これを酸化・変敗・腐敗する前の新鮮な状態で乾燥させたものである。米糠は、精米の際出る米糠である。
 一次処理として、便器からの糞尿を受け入れる便器からの糞尿を受け入れる複合発酵液化便槽に複合発酵を誘発する複合発酵培養液を加えると発酵が始まり、乳酸発酵によって、有機物を分子結合レベルでばらばらになる。
 発酵槽ではさらに複合発酵が進行し、分解菌並びに分解酵素を現生させ、屎尿による汚泥を水と炭素とガスに分解消失させる。SS除去層を有する固形発酵槽では複合発酵MLSS菌床を採取して最初の発酵液化槽に戻すことで、より酵、または合成あるいは増殖させて複合発酵を発酵液化槽で起こし易くなる。
 なお、MLSS菌床は、屎尿を複合発酵技術で処理し、嫌気発酵、固形発酵を起こし、MLSSに複合発酵状態にある微生物が付着(着子)し、嫌気性菌類が根付く(着床)ようにし、さらに嫌気性菌類がコロニー化(菌床)したものである。
 二次処理では、前記汚泥を消失させた汚水を浄化する処理であり合併浄化槽、合成槽、処理水槽に順次導き、合併浄化槽では複合発酵を継続させる。
 請求項2記載の本発明は、二次処理の合成槽には、集積した複合発酵モルトを沁み込ませたバイオ触媒布を所定間隔を置いて吊り下げ配設して複合発酵による浄化を行うことを要旨とするものである。
 請求項2記載の本発明によれば、合成槽では集積した複合発酵モルトを沁み込ませたバイオ触媒布を配設することで、さらに複合発酵を助長させる。
 バイオ触媒布に現生・発現した光合成菌、藻菌類が、光によって、炭酸ガス、窒素ガスを取り込んで光合成処理によるエネルギー置換及び交換を行い、生活性物質及びタンパク質結晶が生成される。
 このように、バイオ処理と光合成処理とによって、被処理水のほぼ完全な酸化、変敗、腐敗を断ち切り、細菌類を消滅させ、微生物の全ての有害作用を有効作用に導く。換言すれば、前記バイオ処理及び光合成処理によって、前記各菌の共存、共栄、共生を可能とし、微生物の有効作用を引き出して、酸化、変敗、腐敗を断ち切り、洗浄水として便器洗浄に用いる処理水が得られる。
In order to achieve the above object, the present invention as set forth in claim 1 provides a method for inducing complex fermentation in a complex fermentation and liquefaction toilet tank that receives excrement and urine from a toilet bowl as a primary treatment. Extract extracted from leaves selected from chestnuts, peaches, and persimmons, okara, and molasses are added, and aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria are inoculated, and aerobic bacteria and anaerobic bacteria are added. It is possible to coexist, co-prosperate, and coexist with sexual bacteria through facultative anaerobic bacteria, to produce composite fermentation malt that is the supernatant liquid, and to prepare water for the composite fermentation malt and molasses for aerobic fermentation. Add the following complex fermentation culture solution made by adding an anaerobic base for anaerobic fermentation, and create a complex fermentation liquefaction tank with a fermentation liquefaction tank that is a tank to which the complex fermentation culture solution is added, a fermentation tank in which complex fermentation is carried out, and an SS removal layer. It consists of a solid fermentation tank and a flow rate adjustment tank, and liquefies it by sending it to these sequentially.As a secondary treatment, it is sequentially led to a combined septic tank, a synthesis tank, and a treated water tank, where it is purified by combined fermentation, and then processed from the treated water tank. The gist of the system is to use water as flush water for flushing toilet bowls.
Complex fermentation culture solution: A solution that induces complex fermentation, in which extracts extracted from leaves selected from pine, bamboo, plum, fig, chestnut, peach, and persimmon, okara, and molasses are added to water. By inoculating aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria in A certain complex fermentation malt is produced, and to the complex fermentation malt is added charging water, molasses for aerobic fermentation, and anaerobic basis for anaerobic fermentation.
According to the present invention as set forth in claim 1, the treatment is clearly divided into the primary treatment of liquefying the solid and the secondary treatment of purifying and cleaning the liquefied material, and the primary treatment is combined fermentation. By adding the culture solution to the fermentation tank that receives excrement from the toilet bowl, the sludge is eliminated by the action of microorganisms through complex fermentation.As a secondary treatment, the sewage is purified by the action of microorganisms through complex fermentation, and is used as cleaning water. Treated water used for flushing toilet bowls is obtained.
Since it is a complete circulation type, there is no need for water or sewage or pumping, and since it does not decompose, it does not generate bad odors.Furthermore, it does not generate E. coli, various bacteria, or pathogenic bacteria, so there is no need for sterilization with chemicals.
Additionally, although electricity is required for the aeration blower and transfer pump, a small generator can be used in the event of a power outage.
In preparation for evacuation centers, parks, etc., it is possible to use the toilet as a public toilet on a regular basis, and to keep it as a toilet that can be used as is in the event of a disaster.
The complex fermentation malt used to create the complex fermentation culture is the seed for the complex fermentation, and contains polymer-bonded crystals of carbon. Composite fermentation malt is made by combining water with extracts extracted from leaves selected from pine, bamboo, plum, fig, chestnut, peach, and persimmon as a natural material and used as a culture medium. The mixture with molasses becomes a bacterial bed, in which aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria are planted. It is possible to create the foundation for complex fermentation of coexistence, co-prosperity, and symbiosis through bacteria.
By planting aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria at the same time, aerobic bacteria and anaerobic bacteria can coexist through facultative anaerobic bacteria, but coexistence, mutual prosperity, and symbiosis are not antagonistic. When microorganisms (bacteria) become 1/10th the size and the number of microorganisms per cc increases, the microorganisms create a state of suspended animation, where they no longer kill each other and the bacteria die. can be reduced.
In this state, the microbial enzyme is combined and crystallized with the plant enzymes contained in the leaves of pine, bamboo, fig, chestnut, peach, and persimmon to produce antioxidant derivatives. Antioxidants are physiologically active substances such as enzymes, vitamins, minerals, and amino acids, and are polymer-bound crystals of carbon. When this is returned to water, it reverts to microorganisms. This can be seen in proteins.
Complex fermentation, in which aerobic bacteria and anaerobic bacteria coexist, coexist, and coexist through facultative anaerobic bacteria, begins with the activation of aerobic fermenting microorganisms such as yeast and lactic acid bacteria, and aerobic fermenting microorganisms produce amino acids, It produces physiologically active substances such as sugars, vitamins, and minerals, and purifies harmful aerobic bacteria such as Escherichia coli, filamentous fungi, and miscellaneous bacteria.Then, lactic acid bacteria, which are aerobic fermentation microorganisms, produce facultative anaerobic lactic acid bacteria and facultative anaerobic bacteria. relays to fungi, and as a result, actinomycetes appear and produce antibacterial substances, which purify anaerobic harmful bacteria such as bacteria, pathogens, viruses, and rickettsia, and the two bactericidal actions work together, Azotobacter, Amylobacter, root-knot bacteria, etc. work to take in nitrogen from the air and fix it (nitrogen-fixing bacteria).Finally, photosynthetic bacteria, algae, and chemophotosynthetic microorganisms take in carbon dioxide and nitrogen gas to produce energy such as photosynthesis. This is possible through substitution and exchange.
Composite fermentation malt is obtained by removing the precipitate (coagulated solid matter of microorganisms) from the supernatant liquid of the solution containing antioxidants.
The complex fermentation culture solution is made by adding water, molasses for aerobic fermentation, and anaerobic base for anaerobic fermentation to complex fermentation malt, which is the seed for complex fermentation, to induce complex fermentation.
The anaerobic base here refers to chicken manure, dried okara, and rice bran. Chicken manure is dried before it oxidizes, spoils, or rots. Dried okara is the soybean residue left after squeezing the soy milk during tofu production, and is dried in its fresh state before it oxidizes, spoils, or rots. Rice bran is the rice bran that is produced during rice polishing.
As a primary treatment, fermentation begins when a complex fermentation culture solution that induces complex fermentation is added to the complex fermentation liquefaction tank that receives excrement from the toilet bowl, and organic matter is broken down at the molecular bond level by lactic acid fermentation. Become.
Complex fermentation further progresses in the fermentation tank, causing decomposition bacteria and decomposition enzymes to exist, decomposing and eliminating the sludge from human waste into water, carbon, and gas. In a solid fermenter having an SS removal layer, by collecting the composite fermentation MLSS bacterial bed and returning it to the initial fermentation and liquefaction tank, it becomes easier to ferment, synthesize, or propagate the composite fermentation in the fermentation and liquefaction tank.
The MLSS fungal bed is created by processing human waste using a complex fermentation technology to cause anaerobic fermentation and solid fermentation, allowing microorganisms in a complex fermentation state to attach to the MLSS (seedling) and anaerobic fungi to take root (implantation). It is further colonized (bacteria bed) by anaerobic fungi.
In the secondary treatment, the sewage from which the sludge has been removed is purified, and is sequentially introduced into a combined septic tank, a synthesis tank, and a treated water tank, where combined fermentation is continued.
In the second aspect of the present invention, biocatalyst cloth impregnated with the accumulated combined fermentation malt is suspended at predetermined intervals in the secondary treatment synthesis tank to perform purification by combined fermentation. The main points are as follows.
According to the second aspect of the present invention, a biocatalyst cloth impregnated with the accumulated combined fermentation malt is provided in the synthesis tank to further promote the combined fermentation.
Photosynthetic bacteria and algae that are present or expressed on the biocatalyst fabric take in carbon dioxide and nitrogen gases by light and perform energy replacement and exchange through photosynthetic processing, producing bioactive substances and protein crystals.
In this way, bio-treatment and photosynthesis treatment almost completely eliminates oxidation, deterioration, and putrefaction of the water to be treated, eliminates bacteria, and converts all harmful effects of microorganisms into effective effects. In other words, the bio-treatment and photosynthesis treatment enable the coexistence, co-prosperity, and symbiosis of each of the bacteria, bring out the effective action of the microorganisms, cut off oxidation, deterioration, and putrefaction, and use the treatment as flush water for flushing toilet bowls. water is available.
 以上述べたように本発明のリサイクル型バイオ式トイレは、有機物及び、し尿の分解が確実に達成され、かつ、処理水を洗浄水として便器洗浄に用いることの有効活用が可能なものである。 As described above, the recyclable bio-toilet of the present invention can reliably decompose organic matter and human waste, and can effectively utilize treated water as flushing water for flushing the toilet bowl.
 図1は本発明のリサイクル型バイオ式トイレの1実施形態を示すフロー図である。
 図2は本発明のリサイクル型バイオ式トイレで使用する複合発酵液化便槽の詳細を示す縦断側面図である。
 図3は本発明のリサイクル型バイオ式トイレで使用する複合発酵液化便槽の詳細を示す平面図である。
 図4は本発明のリサイクル型バイオ式トイレでの運転開始後1週間程度経過後の各槽の処理状態を示す写真である。
 図5は図4の汲み上げ直後の状態から60分程度経過後の処理状態を示す写真である。
 図6は従来例を示す側面図である。
 図7は従来例を示す平面図である。
FIG. 1 is a flow diagram showing one embodiment of the recyclable bio-style toilet of the present invention.
FIG. 2 is a longitudinal sectional side view showing details of the composite fermentation and liquefaction toilet tank used in the recycling type bio-toilet of the present invention.
FIG. 3 is a plan view showing details of the composite fermentation and liquefaction toilet tank used in the recycling type bio-toilet of the present invention.
FIG. 4 is a photograph showing the treatment status of each tank about one week after the start of operation of the recycling type bio-toilet of the present invention.
FIG. 5 is a photograph showing the processing state approximately 60 minutes after the pumping shown in FIG. 4.
FIG. 6 is a side view showing a conventional example.
FIG. 7 is a plan view showing a conventional example.
 以下、図面について本発明の実施の形態を詳細に説明する。図1は本発明のリサイクル型バイオ式トイレの1形態を示すフロー図で、図中1は便器2(男子トイレの場合は小便器、大便器、女性トイレの場合は大便器のみ、その他手洗い、洗面施設等)を設置したトイレである。トイレ1は、ジェット水洗式トイレを二つ使用し、男子用トイレ2棟では小便器2台×2、大便器2台×2を1セットし、これに便器2からの糞尿を受け入れる複合発酵液化便槽3を付設した。
 複合発酵液化便槽3はデスクタイプのデフューザー10を有するエアーレーション用のブロアー設備(0.2m/min)4を備えた発酵槽として、発酵液化槽5、発酵槽6、固形発酵槽7および流量調整槽8とからなり、これらに順次送り込むものとする。送り込みの方式はオーバーフローでよい。発酵液化槽5、発酵槽6は2.1m、固形発酵槽7、流量調整槽8は0.8mである。
 図3、図4に複合発酵液化便槽3の詳細を示すが、深さ660mm程度の浅いものですみ、トイレ1の下部構造として形成することができる。また、トイレ1とともにトレーラーに載置して移動可能とすることもできる。
 固形発酵槽7には砕石フィルターによるSS除去層11を設け、流量調整槽8には中継ポンプ9としての水中ポンプを設置する。
 発酵液化槽5には汚水流入エリア5aを設け、また、発酵槽6へ送るための流出部バッフル23を形成した。
 発酵槽6には固形発酵槽7に送るための流出部バッフル23を形成し、固形発酵槽7と流量調整槽8との間には流入開口24を設ける。
 以上が一次処理のための装置であり、このように一次処理として、便器2からの糞尿を受け入れる発酵液化槽5に複合発酵を誘発する複合発酵培養液を加える。
 また、二次処理用の装置は、合併浄化槽(発酵合成槽)12、合成槽13、14、16、カーボンフィルター18を備えたサンド・カーボン触媒タンク(マテリアルカーボン濾過槽)21,21、処理水槽15で構成し、合併浄化槽(発酵合成槽)12、合成槽13、14、16にもそれぞれブロアー設備4を設置してあり、また、次の槽に送り込むためのポンプ20を配設している。
 合併浄化槽(発酵合成槽)は第1処理槽としての合併浄化槽(発酵合成槽)12aと第2処理槽としての合併浄化槽(発酵合成槽)12bがあるものとし、合成槽も合成槽13、14の他に合成槽16を加えて3個とした。合成槽13、14、16は1mの容量である。
 合成槽13、14、16には集積した酵素水である複合発酵モルトを沁み込ませた帯状の不織布によるバイオ触媒布25を所定間隔を置いて吊り下げ配設して、合成触媒槽として形成した。バイオ触媒布25は微生物を発酵合成に誘導し、次に合成に誘導する情報の触媒の役割を果たす。
 最後の合成槽16からの処理水はカーボンフィルター18を設けたサンド・カーボン触媒タンク(マテリアルカーボン濾過槽)21におくり、さらに処理水槽15に貯め、全自動給水ポンプ20で便器2の洗浄に用いるように送水する。
 前記一次処理は複合発酵液化便槽システムとして、複合発酵培養液を添加し、複合発酵を惹起させるものであり、二次処理は複合発酵バイオシステムとして複合発酵を継続させて分解酵素水としての処理水(浄水)を得て、100%のリサイクルを実現するものある。
 次に使用法について説明する。発酵液化槽5は屎尿が最初に流入する槽であるが、エアーレーションした状態で水を注入し、満水状態とする。それに複合発酵培養液を水の量に対し重量比0.01%の割合で投入する。
 発酵液化槽5からオーバーフローした水が移流管を経て底部に入るように設置された発酵槽6にエアーレーションした状態で水を注入し、満水状態とする。
 なお、この発酵槽6に前記複合発酵培養液を投入してもよいし、後述の複合発酵MLSS菌床を濃度1000ppmになるように投入してもよい。
 このすべての準備が終了した後、エアーレーションを維持し、72時間放置した後、通常のトイレとして使用する。
 以上が準備段階であり、使用開始後一週間は、朝と晩に前記複合発酵培養液を発酵液化槽5の容量の0.02%をトイレの排水口から投入する。
 各槽の状態を見ながら、合成を強くしたい場合は、複合発酵培養液を投入する。この状態でトイレを使用することによって、発酵液化槽5で発酵が始まり、乳酸発酵によって、有機物を分子結合レベルでばらばらになり、液状化が起こり、発酵槽6で完全発酵が起き、発酵合成を起こさせ、分解菌並びに分解酵素を現生させ、嫌気発酵、固形発酵を起こさせ、さらに分解菌、分解酵素を原生させて、屎尿を水と炭素とガスに分解消失させ、汚泥を発生させない。
 また、固形発酵槽7ではSS除去層11に複合発酵MLSS菌床が蓄積されるが、定期的にこのSS除去層11での複合発酵MLSS菌床を採取して最初の槽である発酵液化槽5に戻してやる。
 MLSSとは、Mixed Liquor Suspended Solidsの略称で、活性汚泥処理におけるばっ気槽(エアレーションタンク)内の汚泥混合液の浮遊物質のことをいうが、この菌床のもつ高度な情報とエネルギーを、初めの槽に戻すことで、終わりと始まりが、生と死がつながる。
 微生物が得た最大限のエネルギーをが、新しい物質、新しい微細物に生まれかわり、情報が進化する。複合発酵MLSS菌床は、菌が腐敗を起こさせないもので、これは時間が経てば経つほど、進化成長して賢くなる。
 汚泥を発生させない処理水は流量調整槽8から合併浄化槽(発酵合成槽)12aへと送られ、二次処理としての浄化が始まる。
 合併浄化槽12a,12bでは、エアーを供給されて、複合発酵が行われ、好気性菌類の乳酸菌、酵母菌等により、アミノ酸、糖類、ビタミン、ミネラル等の生理生活物質が創られ、大腸菌、雑菌、一般細菌類を抑制し、抗酸化作用による酸化、変敗、腐敗を防ぐ。また、好気性菌類及び嫌気性菌類の乳酸菌、放線菌により、ストレプトマイセス、ペニシリウム等の抗生物質が創られ、病原菌、ウイルス、リケッチャ等を抑制する。また、嫌気性菌のアゾトバクター、アミロバクター、根瘤菌等がエアーの窒素を固定する。
 合成槽13、14、16には複合発酵モルトを沁み込ませた帯状の不織布によるバイオ触媒布25を所定間隔を置いて吊り下げ配設してあり、バイオ触媒布25に現生・発現した光合成菌、藻菌類が、光によって、炭酸ガス、窒素ガスを取り込んで光合成処理によるエネルギー置換及び交換を行い、生活性物質及びタンパク質結晶が生成される。
 この合成槽13、14、16からの処理水は、シリカ触媒層、カーボン触媒層、マテリアル触媒層を積層してなるカーボンフィルター18を有するサンド・カーボン触媒タンク21に送られるが、処理水に含まれる有機性エネルギー培地を、無機性媒体(C・SiO,Ti,Fe,Al,Cu,Mg,Li,Be,etc)により、消失させる作用を発揮する。
 具体的には、タンパク高分子結晶の衝突により、残留したすべての水素基(H+)をカーボンフィルター18のカーボン触媒に含まれる無機性触媒体である炭素(C)に吸着させる。
 カーボンフィルター18をシリカ触媒層、カーボン触媒層、マテリアル触媒層を積層してなるものとした場合は、マテリアル触媒層では、エネルギー酵素を獲得して、処理された処理水をより浄化する作用を発揮する。
 さらにシリカ触媒層では、被処理水中の窒素(N)、生理活性物質、タンパク高分子結晶(酵素結合結晶)が、シリカ触媒に含まれる無機性触媒体であるイオン(C・SiO)に衝突することにより、+化したものを炭素イオン(C)に吸着させ、有機性エネルギー培地とタンパク高分子結晶のみを残す。
 このようにして得られた処理水は洗浄水として便器洗浄に用いる。
 図4、図5は処理の状況を示す写真で、図4は本発明のリサイクル型バイオ式トイレでの運転開始後1週間程度経過後の各槽の処理状態を示すもので、汲み上げ直後のもの、図5は図4の汲み上げ直後から60分程度置いた各槽の処理状態を示すものである。
 シリンダーは左から発酵液化槽5内の状態、固形発酵槽7内の状態、第1処理層である合併浄化槽(発酵合成槽)12a内の状態、第2処理層である合併浄化槽(発酵合成槽)12b内の状態、合成触媒槽である合成槽16内の状態、マテリアルカーボン濾過槽であるサンド・カーボン触媒タンク21内の状態である。
 図4の状態では合併浄化槽(発酵合成槽)12aではまだ汚泥が完全に液化されていないが、図4の状態ではほとんど液化されたおり、最後のサンド・カーボン触媒タンク21ではほぼ完全に浄化されている。
 図4と図5の差は、60分経過すると、複合発酵MLSS菌床が沈下する。
 前記のように各槽ではエアーレーション用のブロアー設備(0.2m/min)4を備えてブロアーを行うものであるが、このブロアー設備4の運転は、20時間の継続運転の後、4時間運転を止める。図5の複合発酵MLSS菌床の沈下はこのようなブロアー停止で生じるものであり、複合発酵MLSS菌床は微生物が凝集されており、止めた状態で上澄みのみ次の槽に移動させると、複合発酵MLSS菌床、微生物を含まないで移動させることができる。
 これにより、微生物を凝集させるための凝集剤は不要である。
Embodiments of the present invention will be described in detail below with reference to the drawings. Figure 1 is a flow diagram showing one form of the recyclable bio-toilet of the present invention. In the figure, 1 is a toilet bowl 2 (a urinal, a toilet bowl in the case of a men's restroom, only a toilet bowl in the case of a women's restroom, other hand-washing, This is a toilet with washroom facilities, etc.). Toilet 1 uses two jet flush toilets, and the two men's restrooms have a set of 2 urinals x 2 and 2 urinals x 2, and a complex fermentation liquefaction system that receives excrement from toilet 2. Added toilet tank 3.
The composite fermentation liquefaction tank 3 is a fermentation tank equipped with an aeration blower equipment (0.2 m 3 /min) 4 having a desk-type diffuser 10, and includes a fermentation liquefaction tank 5, a fermentation tank 6, a solid fermentation tank 7 and It consists of a flow rate adjustment tank 8, and the water is fed into these tanks in sequence. The feeding method may be overflow. The fermentation liquefaction tank 5 and the fermentation tank 6 have an area of 2.1 m 3 , and the solid fermentation tank 7 and the flow rate adjustment tank 8 have an area of 0.8 m 3 .
Details of the composite fermentation and liquefaction toilet tank 3 are shown in FIGS. 3 and 4, and the tank only needs to be as shallow as 660 mm in depth, and can be formed as the lower structure of the toilet 1. Further, the toilet 1 and the toilet 1 can be placed on a trailer and moved.
The solid fermentation tank 7 is provided with an SS removal layer 11 using a crushed stone filter, and the flow rate adjustment tank 8 is provided with a submersible pump as a relay pump 9.
The fermentation liquefaction tank 5 was provided with a wastewater inflow area 5a, and an outflow baffle 23 for sending wastewater to the fermentation tank 6 was formed.
The fermenter 6 is provided with an outflow baffle 23 for feeding into the solid fermenter 7, and an inflow opening 24 is provided between the solid fermenter 7 and the flow rate adjustment tank 8.
The above is an apparatus for primary treatment, and thus, as a primary treatment, a composite fermentation culture solution that induces composite fermentation is added to the fermentation liquefaction tank 5 that receives excrement from the toilet bowl 2.
In addition, the equipment for secondary treatment includes a combined septic tank (fermentation synthesis tank) 12, synthesis tanks 13, 14, 16, sand/carbon catalyst tanks (material carbon filtration tank) 21, 21 equipped with a carbon filter 18, and a treated water tank. The combined septic tank (fermentation synthesis tank) 12, synthesis tanks 13, 14, and 16 are each equipped with blower equipment 4, and a pump 20 is also installed to send the water to the next tank. .
The combined septic tank (fermentation synthesis tank) has a combined septic tank (fermentation synthesis tank) 12a as a first treatment tank and a combined septic tank (fermentation synthesis tank) 12b as a second treatment tank, and the synthesis tank also has synthesis tanks 13 and 14. In addition, a synthesis tank 16 was added to bring the total to three. The synthesis tanks 13, 14, 16 have a capacity of 1 m 3 .
In the synthesis tanks 13, 14, and 16, biocatalyst cloths 25 made of band-shaped nonwoven fabric impregnated with composite fermentation malt, which is accumulated enzyme water, were suspended at predetermined intervals to form synthesis catalyst tanks. . The biocatalyst cloth 25 serves as a catalyst for inducing microorganisms into fermentation and synthesis, and then providing information to guide the synthesis.
The treated water from the final synthesis tank 16 is sent to a sand carbon catalyst tank (material carbon filtration tank) 21 equipped with a carbon filter 18, and further stored in a treated water tank 15, and used for cleaning the toilet bowl 2 by a fully automatic water supply pump 20. Send water as shown.
The primary treatment is a combined fermentation liquefaction tank system in which a combined fermentation culture solution is added to cause the combined fermentation, and the secondary treatment is a combined fermentation biosystem in which the combined fermentation is continued and treated as degrading enzyme water. There is a way to obtain water (purified water) and achieve 100% recycling.
Next, how to use it will be explained. The fermentation liquefaction tank 5 is the tank into which human waste first flows, and water is poured into it under aerated conditions to fill it with water. A composite fermentation culture solution was added thereto at a weight ratio of 0.01% to the amount of water.
Water is injected into the fermentation tank 6 installed in such a way that the water overflowing from the fermentation liquefaction tank 5 enters the bottom via a convection pipe and is filled with water in an aerated state.
Note that the above-mentioned composite fermentation culture solution may be introduced into the fermenter 6, or a composite fermentation MLSS bacterial bed (described later) may be introduced at a concentration of 1000 ppm.
After all this preparation is completed, maintain aeration and leave it for 72 hours before using it as a regular toilet.
The above is the preparation stage, and for one week after the start of use, 0.02% of the capacity of the fermentation liquefaction tank 5 is poured into the composite fermentation culture solution from the drain of the toilet in the morning and evening.
While checking the condition of each tank, if you want to strengthen the synthesis, add a composite fermentation culture solution. By using the toilet in this state, fermentation begins in the fermentation and liquefaction tank 5, and by lactic acid fermentation, organic matter is broken down at the molecular bond level, liquefaction occurs, complete fermentation occurs in the fermentation tank 6, and fermentation synthesis begins. This causes decomposition bacteria and decomposition enzymes to exist, causing anaerobic fermentation and solid fermentation, and further allows decomposition bacteria and decomposition enzymes to grow, decomposes and eliminates human waste into water, carbon, and gas, and does not generate sludge.
In addition, in the solid fermentation tank 7, a composite fermentation MLSS fungal bed is accumulated in the SS removal layer 11, and the composite fermentation MLSS fungus bed in the SS removal layer 11 is periodically collected from the fermentation liquefaction tank, which is the first tank. I'll change it back to 5.
MLSS is an abbreviation for Mixed Liquor Suspended Solids, which refers to suspended solids in a sludge mixture in an aeration tank during activated sludge treatment. By returning it to the tank, endings and beginnings, life and death are connected.
The maximum energy obtained by microorganisms is transformed into new substances and new microscopic objects, and information evolves. The composite fermentation MLSS fungal bed does not allow bacteria to rot, and the more time passes, the more the bacteria evolve and grow and become smarter.
The treated water that does not generate sludge is sent from the flow rate adjustment tank 8 to the combined septic tank (fermentation synthesis tank) 12a, and purification as secondary treatment begins.
In the combined septic tanks 12a and 12b, air is supplied to perform complex fermentation, and aerobic bacteria such as lactic acid bacteria and yeast create physiological substances such as amino acids, sugars, vitamins, and minerals, and E. coli, miscellaneous bacteria, Inhibits general bacteria and prevents oxidation, deterioration, and putrefaction due to its antioxidant effect. Furthermore, aerobic and anaerobic fungi such as lactic acid bacteria and actinomycetes produce antibiotics for Streptomyces, Penicillium, etc., which suppress pathogenic bacteria, viruses, Rickettsia, and the like. In addition, anaerobic bacteria such as Azotobacter, Amylobacter, and root-knot bacteria fix nitrogen in the air.
In the synthesis tanks 13, 14, and 16, biocatalyst cloths 25 made of band-shaped nonwoven fabrics impregnated with composite fermentation malt are suspended at predetermined intervals, and the biocatalyst cloths 25 absorb the existing/expressed photosynthesis. Bacteria and algae take in carbon dioxide and nitrogen gases through light and perform energy replacement and exchange through photosynthetic processing, producing bioactive substances and protein crystals.
The treated water from the synthesis tanks 13, 14, and 16 is sent to a sand/carbon catalyst tank 21 that has a carbon filter 18 formed by stacking a silica catalyst layer, a carbon catalyst layer, and a material catalyst layer. It exhibits the effect of eliminating the organic energy medium contained in the organic energy medium by using an inorganic medium (C.SiO 2 , Ti, Fe, Al, Cu, Mg, Li, Be, etc.).
Specifically, all the remaining hydrogen groups (H+) are adsorbed to carbon (C), which is an inorganic catalyst contained in the carbon catalyst of the carbon filter 18, by the collision of the protein polymer crystals.
When the carbon filter 18 is formed by laminating a silica catalyst layer, a carbon catalyst layer, and a material catalyst layer, the material catalyst layer obtains an energy enzyme and exhibits the effect of further purifying the treated water. do.
Furthermore, in the silica catalyst layer, nitrogen (N), physiologically active substances, and protein polymer crystals (enzyme-bound crystals) in the water to be treated collide with ions (C・SiO 2 ), which are inorganic catalysts contained in the silica catalyst. By doing so, the positive substance is adsorbed by carbon ions (C), leaving only the organic energy medium and protein polymer crystals.
The treated water thus obtained is used as flushing water for flushing toilet bowls.
Figures 4 and 5 are photographs showing the treatment status. Figure 4 shows the treatment status of each tank approximately one week after the start of operation of the recycle-type bio-toilet of the present invention, immediately after pumping. , FIG. 5 shows the processing status of each tank after being left for about 60 minutes immediately after the pumping shown in FIG.
From the left, the cylinders show the state in the fermentation liquefaction tank 5, the state in the solid fermentation tank 7, the state in the combined septic tank (fermentation synthesis tank) 12a, which is the first treatment layer, and the state in the combined septic tank (fermentation synthesis tank), which is the second treatment layer. ) 12b, the state in the synthesis tank 16 which is a synthesis catalyst tank, and the state in the sand carbon catalyst tank 21 which is a material carbon filtration tank.
In the state shown in FIG. 4, the sludge has not yet been completely liquefied in the combined septic tank (fermentation synthesis tank) 12a, but in the state shown in FIG. ing.
The difference between FIG. 4 and FIG. 5 is that the composite fermentation MLSS bacterial bed sinks after 60 minutes.
As mentioned above, each tank is equipped with a blower equipment (0.2 m 3 /min) 4 for aeration, and the blower equipment 4 is operated after 20 hours of continuous operation. Stop driving for hours. The sinking of the combined fermentation MLSS bacterial bed in Figure 5 occurs when the blower is stopped, and the microorganisms in the combined fermentation MLSS bacterial bed are aggregated, and if only the supernatant is transferred to the next tank while the combined fermentation MLSS bacterial bed is stopped, the composite fermentation occurs. Fermenting MLSS bacterial beds can be transported without containing microorganisms.
This eliminates the need for a flocculant to flocculate microorganisms.
1…トイレ
2…便器
3…複合発酵液化便槽
4…ブロアー設備
5…発酵液化槽
5a…汚水流入エリア
6…発酵槽
7…固形発酵槽
8…流量調整槽
9…中継ポンプ
10…デフューザー
11…SS除去層
12a,12b…合併浄化槽
13、14、16…合成槽
15…処理水槽
18…カーボンフィルター
20…ポンプ
21…サンド・カーボン触媒タンク
23…流出部バッフル
24…流入開口
25…バイオ触媒布
101…トイレ
102…発酵液状化槽
103…散気管
104…ブロワー
105…エアー配管
106…第一発酵槽
107…第二発酵槽
108…マテリアル触媒槽
109…固形発酵槽
110…ポンプ
111…移送管
112…第一発酵合成槽
113…第二発酵合成槽
114…第三発酵合成槽
115…沈澱槽
116…移流管
117…移流管
119…貯水槽
1...Toilet 2...Toilet bowl 3...Combined fermentation and liquefaction toilet tank 4...Blower equipment 5...Fermentation and liquefaction tank 5a...Sewage inflow area 6...Fermentation tank 7...Solid fermentation tank 8...Flow rate adjustment tank 9...Relay pump 10...Diffuser 11... SS removal layers 12a, 12b...combined septic tank 13, 14, 16...synthesis tank 15...treated water tank 18...carbon filter 20...pump 21...sand/carbon catalyst tank 23...outlet baffle 24...inflow opening 25...biocatalyst cloth 101 …Toilet 102…Fermentation liquefaction tank 103…Diffusion pipe 104…Blower 105…Air piping 106…First fermentation tank 107…Second fermentation tank 108…Material catalyst tank 109…Solid fermentation tank 110…Pump 111…Transfer pipe 112… First fermentation and synthesis tank 113...Second fermentation and synthesis tank 114...Third fermentation and synthesis tank 115...Sedimentation tank 116...Advection pipe 117...Advection pipe 119...Water tank

Claims (2)

  1.  一次処理として、便器からの糞尿を受け入れる複合発酵液化便槽に複合発酵を誘発するものとして、水に、松、笹、梅、無花果、栗、桃、柿のいずれかから選択された葉から抽出した抽出液とオカラと糖蜜を加え、ここに好気性菌と嫌気性菌、および通性嫌気性菌を植付けて、好気性菌と嫌気性菌とを通性嫌気性菌を介して共存・共栄・共生を可能とし、その上澄液である複合発酵モルトを製造し、該複合発酵モルトに仕込み水および、好気発酵をする糖蜜、嫌気発酵をする嫌気基礎を加えてなる下記複合発酵培養液を加え、複合発酵液化便槽は、複合発酵培養液を加える槽である発酵液化槽、複合発酵がおこなわれる発酵槽、SS除去層を有する固形発酵槽、流量調整槽からなり、これらに順次送ることで液化を行い、二次処理として、合併浄化槽、合成槽、処理水槽に順次導き、複合発酵による浄化を行い、処理水槽からの処理水を洗浄水として便器洗浄に用いることを特徴とするリサイクル型バイオ式トイレ。
     複合発酵培養液:複合発酵を誘導するもので、水に、松、笹、梅、無花果、栗、桃、柿のいずれかから選択された葉から抽出した抽出液とオカラと糖蜜を加え、ここに好気性菌と嫌気性菌、および通性嫌気性菌を植付けて、好気性菌と嫌気性菌とを通性嫌気性菌を介して共存・共栄・共生を可能とし、その上澄液である複合発酵モルトを製造し、該複合発酵モルトに仕込み水および、好気発酵をする糖蜜、嫌気発酵をする嫌気基礎を加えてなる。
    As a primary treatment, the excrement is extracted from leaves selected from pine, bamboo, plum, fig, chestnut, peach, and persimmon, into water as a primary treatment that induces complex fermentation into a complex fermentation liquefaction toilet tank that receives excreta from the toilet bowl. Add the extracted liquid, okara, and molasses, and inoculate aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria, so that aerobic bacteria and anaerobic bacteria coexist and coexist through facultative anaerobic bacteria.・The following composite fermentation culture solution that enables symbiosis and produces composite fermentation malt, which is the supernatant thereof, and adds water, molasses for aerobic fermentation, and anaerobic base for anaerobic fermentation to the composite fermentation malt. The combined fermentation and liquefaction tank consists of a fermentation and liquefaction tank which is a tank for adding the combined fermentation culture liquid, a fermentation tank in which the combined fermentation is carried out, a solid fermentation tank with an SS removal layer, and a flow rate adjustment tank, and the liquid is sequentially sent to these tanks. This recycling process is characterized by liquefying the water, leading it sequentially to a combined septic tank, a synthesis tank, and a treated water tank as secondary treatment, performing purification through combined fermentation, and using the treated water from the treated water tank as cleaning water for toilet flushing. Type bio toilet.
    Complex fermentation culture solution: A solution that induces complex fermentation, in which extracts extracted from leaves selected from pine, bamboo, plum, fig, chestnut, peach, and persimmon, okara, and molasses are added to water. By inoculating aerobic bacteria, anaerobic bacteria, and facultative anaerobic bacteria in A certain complex fermentation malt is produced, and to the complex fermentation malt is added charging water, molasses for aerobic fermentation, and anaerobic basis for anaerobic fermentation.
  2.  二次処理の合成槽には、集積した複合発酵モルトを沁み込ませたバイオ触媒布を所定間隔を置いて吊り下げ配設して複合発酵による浄化を行う請求項1記載のリサイクル型バイオ式トイレ。 A recyclable bio-toilet according to claim 1, wherein biocatalyst cloth impregnated with the accumulated composite fermentation malt is suspended at predetermined intervals in the secondary treatment synthesis tank to perform purification through composite fermentation. .
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