JPH1043731A - Inorganic/organic waste mixture treating device - Google Patents

Inorganic/organic waste mixture treating device

Info

Publication number
JPH1043731A
JPH1043731A JP23572596A JP23572596A JPH1043731A JP H1043731 A JPH1043731 A JP H1043731A JP 23572596 A JP23572596 A JP 23572596A JP 23572596 A JP23572596 A JP 23572596A JP H1043731 A JPH1043731 A JP H1043731A
Authority
JP
Japan
Prior art keywords
tank
treatment
water
inorganic
decomposition
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP23572596A
Other languages
Japanese (ja)
Inventor
Shintaro Takenaka
伸太郎 竹中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHINYOU SANGYO KK
Original Assignee
SHINYOU SANGYO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SHINYOU SANGYO KK filed Critical SHINYOU SANGYO KK
Priority to JP23572596A priority Critical patent/JPH1043731A/en
Publication of JPH1043731A publication Critical patent/JPH1043731A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00Constructional details, e.g. recesses, hinges
    • C12M23/34Internal compartments or partitions
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/10Rotating vessel
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/04Filters; Permeable or porous membranes or plates, e.g. dialysis
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M33/00Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
    • C12M33/20Ribbons
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

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  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Chemical & Material Sciences (AREA)
  • Zoology (AREA)
  • Biochemistry (AREA)
  • Genetics & Genomics (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Sustainable Development (AREA)
  • Clinical Laboratory Science (AREA)
  • Molecular Biology (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Treating Waste Gases (AREA)
  • Processing Of Solid Wastes (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Fertilizers (AREA)
  • Refuse Collection And Transfer (AREA)

Abstract

PROBLEM TO BE SOLVED: To improve a waste treating capability by loading a perforated rotary inside tank into a treating vessel body in a rotatable state by means of plural revolving rollers to annihilate and dissolve org matter into a decomposition treating water by the rotation of the perforated rotary inside tank and allowing nondecomposable residues, such as inorg. materials, to remain. SOLUTION: The perforated rotary inside tank 3 loaded with a belt gear 2 is rotatably supported by means of the revolving rollers 4... and is installed on the outside wall of the treating vessel body 1 and is rotated by an inside tank driving machine 5. The charging port 8 of the treating vessel body 1 is connected to an untreated waste storage tank 11 by an expansion joint 9 and a waste washing pipe 34 is installed in the untreated waste storage tank 11. The waste washed in such a manner is charged into the treating vessel body 1 by an auto-transporting machine 10. Org. decomposition enzyme groups consisting essentially of enzyme are added to the decomposition treating water to be injected into the treating vessel body 1 and a solid residue discharge machine 13 is installed to the solid residue discharge port side in the treating vessel body 1.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、地球規模の環境汚
染防止に基づく、有機生ごみの微生物による分解消滅に
係る処理機に関するもので、業務用から家庭用に至るま
での幅広い利用分野を有する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a processor for eliminating organic garbage by microorganisms based on the prevention of environmental pollution on a global scale, and has a wide field of use from business use to home use. .

【0002】[0002]

【従来の技術】従来、有機廃棄物の処理は、有機廃棄物
を処理槽に投入し発酵助成菌を添加、発酵、熟成を促進
して有機肥料に変えるものか、水分調整分解媒体剤を使
って発酵させ、ある程度の分解をさせ、残渣は1次発酵
的有機物でそのまま肥料としては使用不能でありなが
ら、有機肥料と称している処理機ばかりである。
2. Description of the Related Art Conventionally, organic waste is treated by adding organic waste into a treatment tank, adding a fermentation-assisting bacterium, and promoting fermentation and maturation to convert to organic fertilizer. The fermenter is allowed to decompose to a certain extent, and the residue is a primary fermentative organic substance, which cannot be used as a fertilizer as it is, but is only a processing machine called an organic fertilizer.

【0003】同時に、無機廃棄物、有機廃棄物の混合廃
棄物については、その両者を分別して処理せざるを得
ず、特に業務用の有機無機分別不能の廃棄物、例えば養
殖貝類の処分等についてはその使用法において問題を残
している。
[0003] At the same time, mixed waste of inorganic waste and organic waste must be separated and treated. Particularly, wastes that cannot be separated for business use, such as cultured shellfish, cannot be separated. Leaves a problem in its use.

【0004】これらは、家庭用の1槽式でも、大半が大
型の原形生ごみ貯留容器タイプとなり、分解水の発生の
為土壌上への設置を条件とし、近年、一槽式の分解媒体
剤として木粉のみ装填する自動の有機廃棄物の分解処理
機が発売されたが、無機廃棄物に近い卵のから、魚の骨
類は全く分解せず、その上残飯の塊状も分解不能である
処理機が大半を締め、特に、油脂分を含む有機廃棄物の
分解処理は不能といっても良い。
[0004] Even in the case of a single tank type for home use, most of them are large-sized original garbage storage containers, which are required to be installed on soil in order to generate decomposed water. An automatic organic waste decomposer that loads only wood flour was released as a product.However, since eggs are similar to inorganic waste, fish bones are not decomposed at all, and the lump of remaining food is indestructible. It can be said that most of the machines are closed, and in particular, the decomposition treatment of organic waste containing oils and fats is impossible.

【0005】又、蛆虫の発生を押さえる為に殺虫剤を添
加し、同時に、処理槽内で分解させる条件で必ず大容量
加熱ヒーターを設置してエネルギーを消費し、又、強烈
な発酵臭気が発生する為、消臭装置を設置しているが、
複合臭的な生ごみ分解臭気は消臭出来ないと同時に駆動
装置の騒音が激しく市街地、団地では使用出来ない。
In addition, an insecticide is added to suppress the generation of maggots, and at the same time, a large-capacity heating heater is always installed under the condition of decomposing in the treatment tank, energy is consumed, and a strong fermentation odor is generated. In order to do that, we have installed a deodorant device,
The combined odor-like garbage decomposition odor cannot be deodorized, and at the same time the drive unit is so noisy that it cannot be used in urban areas and housing complexes.

【0006】分解媒体材の有機廃棄物の分解に要する必
要量も極端に多く、当然ながら処理槽も大きくなり、バ
イオ剤と称して菌着床材を廃棄物と共に毎日、或は一定
間隔で処理槽に投入する手間もあり、その上、分解に限
度がある為に内部残渣の取り出しを要し、分解媒体剤の
攪拌抵抗に負けない機構として大きなコストを要し、そ
の分解媒体剤の有機肥料化は一次発酵であってそのまま
有機肥料化は不能の上、分解媒体剤の一定期間後の交換
労力は特に大型機器に至っては相当なものであり、交換
廃棄に至っては殆どが有機廃棄物になる可能性があり、
イニシアル及びランニング経費が高いのが現状である。
[0006] The amount of decomposition medium required for the decomposition of organic waste is extremely large, and of course, the treatment tank becomes large, and the fungus-implanted material is treated daily or at regular intervals together with the waste as a bio-agent. It takes time to put it into the tank, and furthermore, the decomposition is limited, so it is necessary to take out the internal residue, a large cost is required as a mechanism not to lose the stirring resistance of the decomposition medium, and the organic fertilizer of the decomposition medium This is a primary fermentation that cannot be used as an organic fertilizer as it is, and the replacement labor after a certain period of time for the decomposition medium agent is considerable, especially for large equipment. May be
Currently, initial and running costs are high.

【0007】近年、湿式処理器と称して、沈殿槽、ばっ
き処理槽、浄水槽、消臭槽の各槽を持った有機物分解槽
と称するものがあるが、これは従来の合併処理槽、トイ
レ浄化槽をそのまま地上に形を変えて置き換えたもので
あり、分解不能物質沈殿量が大半の為に、ディスポーザ
ーを使用して細かく破砕したり、貯留槽内の沈殿物のく
み取りを頻繁に行ったり、臭気等々で斬新性は全くな
い。
[0007] In recent years, there has been a wet processing apparatus called an organic substance decomposition tank having each of a sedimentation tank, a bath treatment tank, a water purification tank, and a deodorization tank. The toilet septic tank is replaced on the ground as it is, and the amount of non-decomposable substance sediment is large, so it is necessary to use a disposer to crush it finely or to frequently remove sediment in the storage tank. There is no novelty with odor etc.

【0008】[0008]

【発明が解決しようとする課題】従来の技術の課題は、
有機廃棄物の発酵分解過程で必然的に起きる分解臭気の
発生が、分解媒体剤及び有機物の発酵の発酵熱によっ
て、有機廃棄物自体の臭気と共に、分解媒体剤の発酵も
加わり、複合臭気となって一旦発生した臭気は複合集で
消臭不能である事から可能な限り臭気発生を防止しなけ
ればならない。
Problems of the prior art are as follows.
The generation of decomposition odor, which is inevitable in the process of fermentation and decomposition of organic waste, is combined with the odor of the organic waste itself and the fermentation of the decomposition medium, due to the fermentation heat of the fermentation of the decomposition medium and organic matter, resulting in a complex odor. Since the odor once generated cannot be deodorized in the complex collection, it must be prevented as much as possible.

【0009】有機廃棄物の処理に大量の分解媒体材を要
する為に処理機が大型化し、攪拌機トルクの増大により
駆動装置の、故障、騒音、設置スペースの増大等の問題
がある。
Since a large amount of decomposition medium is required for the treatment of organic waste, the treatment machine becomes large, and there is a problem in that the drive unit is broken down, noise is increased, and the installation space is increased due to an increase in the agitator torque.

【0010】発酵助成には温暖地域での使用に於ても熱
原が必要であるが、原形廃棄物の場合、熱伝導が悪い為
に、常時、大量の電源を使うヒーターによって加熱する
必要がある。
[0010] A heat source is necessary for the fermentation subsidy even in use in a warm region, but in the case of original waste, it is necessary to always heat it with a heater that uses a large amount of power because of poor heat conduction. is there.

【0011】分解水が発生し、BOD,COD共に浄化
装置が必要にもかかわらず価格的に安くアピールする為
に浄化装置を併設販売せず、廃水汚染の危険性と分解水
臭気の発生、分解水自体に蛆が発生する衛生上の問題も
ある。
Decomposed water is generated, and despite the necessity of a purifying device for both BOD and COD, no purifying device is attached and sold in order to appeal at a low price, and the risk of wastewater contamination and the generation and decomposition of decomposed water odors There is also a hygiene problem where maggots form in the water itself.

【0012】乾式の分解媒体剤が有機物の為、温度調節
器の故障等による火災の危険性、絶えず発酵に必要な水
分調整、煩雑な機器の為の処理機攪拌装置等の保守管
理、故障処理、その為の処理機自体の価格高騰等の課題
がある。
Since the dry decomposition medium is an organic substance, there is a danger of fire due to failure of the temperature controller, constant adjustment of water required for fermentation, maintenance management of troublesome equipment such as a stirrer for complicated equipment, and troubleshooting. Therefore, there are problems such as a rise in the price of the processing machine itself.

【0013】従来の有機廃棄物の、水による分解方式で
も、分解処理水中の有機廃棄物の完全消滅には程遠い
上、貯留槽、ばっき槽、等々の為に2槽、3槽の設備を
要し、上澄み液の或る程度の浄化が限界であり、ディス
ポーザーを使用する為に、破砕加水の量の一定化は不可
能となり、加水量の不安定化によって貯留タンクの増大
と、破砕加水の下水への廃棄、排水しない条件での加熱
蒸散に至っては100℃の熱源の高温発散による臭気の
為に、消臭剤、マスキング芳香剤等の添加投入が条件で
ある。
The conventional organic waste decomposition method using water is far from complete extinction of the organic waste in the decomposed water, and requires two tanks and three tanks for storage tanks, tanks and the like. In short, the purification of the supernatant liquid to a certain degree is the limit, and the use of a disposer makes it impossible to stabilize the amount of crushed water. Disposal to sewage and heating and evaporation under the condition of no drainage are caused by the addition of a deodorant, a masking fragrance and the like due to the odor caused by the high-temperature emission of a heat source of 100 ° C.

【0014】[0014]

【課題を解決するための手段】従来の課題を次の通り解
決した。病原菌対策安全性の観点から、一定間隔時間で
処理水の温度を75℃に上昇可能とし、常時は25℃と
40℃前後を維持して、分解過程での雑菌繁殖を防止
し、有機廃棄物種類によっては、分解に必要な有機物分
解微生物群、有機物分解酵素群の夫々を、又は単独で添
加した分解処理水で速やかに分解し、処理槽本体内の空
気を強制吸し、消臭装置で引消臭する事により、継続的
に回転処理槽内の臭気を発散する事なく、処理器周辺
で、無臭に近い状態で分解を行う。
Means for Solving the Problems The conventional problems have been solved as follows. From the viewpoint of pathogen control safety, the temperature of the treated water can be raised to 75 ° C at regular intervals, and it is maintained at 25 ° C and around 40 ° C at all times to prevent the propagation of various bacteria in the decomposition process and to reduce organic waste. Depending on the type, each of the organic matter-decomposing microorganisms and organic matter-degrading enzymes required for the decomposition is quickly decomposed with decomposed water added alone, and the air in the treatment tank body is forcibly sucked, and deodorized by By deodorizing, the odor in the rotary processing tank is not continuously emitted, and decomposition is performed in the vicinity of the processing unit in an almost odorless state.

【0015】同時に、有機物分解微生物群、有機物分解
酵素群を添加した一槽式の処理槽本体内の分解処理水
は、一定量を保って有機廃棄物を処理する事から余分な
スペースを取らないと同時に、処理槽本体内の分解処理
水により廃棄物を消滅させる事から、装置の極端な簡略
化、無騒音化が可能である。
At the same time, the decomposed water in the single-tank type treatment tank body to which the organic substance-decomposing microorganisms and the organic substance-decomposing enzymes are added does not take up extra space because the organic waste is treated while maintaining a fixed amount. At the same time, the waste is eliminated by the decomposed water in the processing tank body, so that the apparatus can be extremely simplified and the noise can be reduced.

【0016】処理装置の小型化については、従来の処理
機の様に、1日当たりの処理能力としての有機廃棄物の
処理量の何十倍もの木粉等の有機物分解媒体材を装填す
る必要がなく、従来の処理器本体の二分の一以下の小型
化が達成された。
As for the miniaturization of the processing apparatus, it is necessary to load an organic substance decomposition medium material such as wood flour which is tens of times the processing amount of organic waste per day as a conventional processing apparatus. In addition, the size of the conventional processor body was reduced by half or less.

【0017】又、処理装置の構造も、分解処理水が入っ
た処理槽と、多孔回転内槽のみを考慮すれば良い為に、
機構的にも簡単になり、処理機本体各機構も全く簡素化
出来、従来の処理器の様に機械強度的な故障に悩まされ
る事なく、耐用年数計算は単に自然衰耗計算強度のみで
充分となった。
Also, the structure of the processing apparatus is only required to consider the processing tank containing the decomposition water and the multi-hole rotary tank.
The mechanism is also simplified, and each mechanism of the processor itself can be simplified at all.There is no need to worry about mechanical strength failure as in the conventional processor. It became.

【0018】駆動音等による騒音は、機器の攪拌装置に
大きく影響し、又、機器の大型化による分解媒体剤の攪
拌駆動機トルクの増大によるが、本発明は処理槽本体内
には多孔回転内槽しかなく、回転も、水中間欠回転させ
る為、静粛稼働とした。
The noise due to the driving noise or the like greatly affects the stirring device of the equipment, and the torque of the stirring drive of the decomposition medium increases due to the increase in the size of the equipment. There was only the inner tank, and the operation was quiet, as the rotation was halfway through the water.

【0019】同時に換気ファンも、密閉装置的な処理装
置であり、微弱な強制吸引ファン似よ炉消臭装置出良
く、風量が極微小で良い為、無騒音に近い静粛さであ
る。
At the same time, the ventilation fan is also a treatment device like a hermetic device, similar to a faint forced suction fan, has a good furnace deodorizing device, and has a very small air volume, so it is quiet with almost no noise.

【0020】分解処理水の温度は、冬期寒冷地における
低温化現象を避ける為に、一定温度を維持する分解処理
水温度制御付きヒーターが装着されるが、定期的に75
℃に温度上昇させて病原菌、雑菌、害幼虫の消滅と同時
に、有機物分解酵素群等最大適用温度によって分解促進
に役立てるが、それ以外は通常25℃前後と、40℃前
後に交互に維持して有機物分解微生物群等によって分解
を行い、短時間分解が必要な場合は、40℃前後の温度
時間帯を長くする事によって。分解時間が半減した。
The temperature of the decomposed water is controlled by a heater equipped with a decomposed water temperature control for maintaining a constant temperature in order to avoid a low temperature phenomenon in cold winter regions.
Increase the temperature to ℃ to eliminate the pathogens, germs, and harmful larvae, and at the same time, use the maximum application temperature of the organic matter degrading enzyme group to help the decomposition, but otherwise keep the temperature around 25 ℃ and around 40 ℃ alternately Decomposition is carried out by an organic matter decomposing microorganism group or the like, and when short-time decomposition is required, the temperature period around 40 ° C. is extended. The decomposition time has been halved.

【0021】有機廃棄物を破砕して投入する場合は、破
砕による表面積の拡大を行い、分解時間の短縮と限界ま
での消滅を行う為、ディスポーザーの様な加水破砕によ
る排水を処理槽本体に導入し、分解処理水蒸散装置によ
って余剰分は処理し、分解水の多少の加温による事と、
油脂類、蛋白質類、及び繊維素類の有機物分解酵素群の
働きと相まって有機廃棄物の消滅が可能である。
When organic waste is crushed and charged, wastewater generated by water crushing such as a disposer is introduced into the treatment tank main body in order to increase the surface area by crushing, shorten the decomposition time and eliminate the organic waste to the limit. Then, the excess is treated by the decomposition water evaporator, and by slightly heating the decomposition water,
The organic waste can be eliminated in combination with the action of the organic substance degrading enzyme group of fats, oils, proteins, and fibrils.

【0022】又、無機有機廃棄物の混合投入は、分解不
能物質は多孔回転内槽内に残渣として貯留され、有機廃
棄物の根物野菜の様に堅いものであっても、前述の様に
分解処理水は間欠的に温度上昇させている為に、投入後
一定時間で軟弱化分解され、定期的に無機残渣は固形残
渣排出機によって、分解処理水を排出する事なく、自動
的に処理槽本体から排出される。
In addition, when the inorganic organic waste is mixed and charged, the non-decomposable substance is stored as a residue in the porous rotating inner tank, and even if the organic waste is as hard as the root vegetable of organic waste, Since the temperature of the decomposed water is intermittently raised, it is softened and decomposed within a certain period of time after being put in, and the inorganic residue is automatically treated regularly by a solid residue discharger without discharging the decomposed water. It is discharged from the tank body.

【0023】万一、処理槽内に一時的に大量の廃棄物を
投入され、分解水が規定量以上のレベルになった場合、
オーバーフロー管よって自動的に分解処理水蒸散装置に
導入されて気中放散される為、これも分解水の排出は全
くない上、場合によっては定期的に75℃に加温上昇さ
せているため病原菌等は無く安全である。
In the event that a large amount of waste is temporarily put into the treatment tank and the amount of decomposed water exceeds a specified level,
Since it is automatically introduced into the decomposed water evaporator by the overflow pipe and released into the air, it does not emit any decomposed water, and in some cases, it is heated to 75 ° C periodically to increase the pathogenic bacteria. There is no security.

【0024】処理槽本体内の多孔回転内槽は微速回転の
みで良く、従来の樹木分等の分解媒体材攪拌による方式
では、有機廃棄物1日当たり1Kgの処理装置が減速し
ても90W以上のモーターを要しているのに対し、本発
明は、処理槽本体内の多孔回転内槽の微速回転動力は、
1Kgの無機有機混合廃棄物処理当たりに換算すれば、
減速機付き3ワットモーター前後で十分である。
[0024] The perforated rotary inner tank in the treatment tank main body only needs to be rotated at a very low speed. In the conventional method of stirring the decomposition medium material such as trees, even if the processing apparatus of 1 kg per day of organic waste is decelerated, 90 W or more is required. Whereas a motor is required, the present invention provides a low-speed rotation power of the perforated rotary inner tank in the processing tank main body,
In terms of 1 kg of inorganic / organic mixed waste treatment,
A 3-watt motor with a reducer is enough.

【0025】本発明は、従来の樹木粉の様な有機物分解
媒体材自体が、有機物分解微生物群、有機物分解酵素群
を添加した分解処理水に変わることにより、分解媒体剤
の材料費、取り替え費用等が不要となり、ランニングコ
ストは超僅少である上、非常に有効な有機液体肥料とし
ても付加価値が発生し、分解処理水は長期にわたって継
続使用が出来る。
According to the present invention, the material cost and replacement cost of the decomposition medium are changed by replacing the conventional organic decomposition medium, such as wood flour, with decomposed water to which an organic decomposition microorganism group and an organic decomposition enzyme group are added. And the like, the running cost is extremely low, and added value is generated even as a very effective organic liquid fertilizer, and the decomposed water can be used continuously for a long time.

【0026】有機物分解微生物群、有機物分解酵素群
の、毎日一定量自動添加により、又は一定間隔で自動添
加により、投入を忘れた為の分解不能発生の危険性がな
く安全である。
By automatically adding a fixed amount of the organic substance-decomposing microorganisms and the organic substance-decomposing enzyme group every day or at regular intervals, there is no danger of inability to decompose due to forgetting to put in, and it is safe.

【0027】従来の有機物分解処理機は、電気機器、攪
拌装置、分解媒体剤の乾燥等のファンの粉塵発散、分解
媒体剤の過湿度固形化による機器オーバーロード等々に
よる故障が多いが、本発明は全く故障の箇所がない程シ
ンプルな機構である。
The conventional organic matter decomposer has many failures due to electric equipment, a stirrer, fan dust emission such as drying of the decomposition medium, equipment overload due to solidification of the decomposition medium due to excessive humidity. Is a simple mechanism with no failure points.

【0028】社会的に有機廃棄物の処理がクローズアッ
プされている現在、全ての所得階級の家庭に於て購入可
能な価格、業務用において廃棄物処理費用が商品に価格
転化する必要の無い価格でなければならないが、本発明
は機構の超簡素化と素材の選択、組み立て部品の僅少さ
によって人件費の賦課が僅かで済み、ユーザーにおいて
はランニングコストも殆ど掛からず、全階級家庭を含め
て全ての層に於て購入可能なコストでの製作が可能であ
る。
At present, when the treatment of organic waste is becoming increasingly popular in society, the price can be purchased in households of all income classes, and the price at which waste treatment costs do not need to be converted into commodities in business use. However, the present invention requires only a small labor cost due to the super simplification of the mechanism, the choice of materials, and the small number of assembled parts, the running cost is hardly required for the user, and the present invention includes all classes of households. All layers can be manufactured at affordable cost.

【0029】処理槽本体内の分解処理水の酸素保有量を
促進する為と、水中の有機物分解促進各種添加剤の効率
向上の為に、気泡を供給した場合、多孔回転内槽の微速
回転による分解処理水の対流によって気泡は単なる水中
での上昇運動でなく、分解処理水の回転によって、従来
の気泡上昇時間のほぼ倍の時間は分解処理水中にあり酸
素供給効率増大の寄与を図った。
When air bubbles are supplied to promote the oxygen holding amount of the decomposition water in the processing tank body and to improve the efficiency of various additives for promoting the decomposition of organic substances in the water, the porous rotary inner tank is rotated at a low speed. Due to the convection of the decomposed water, the bubbles are not merely a rising motion in the water, but the rotation of the decomposed water is in the decomposed water for almost twice as long as the conventional bubble rising time, thereby contributing to an increase in oxygen supply efficiency.

【0030】有機廃棄物の中には、魚の骨、卵の殻等も
必然的に発生するが、魚の骨はカルシュウムと蛋白質等
の他の有機物の結合によって構成されているが、これら
の投入量が多い場合、或は業務用の魚のはらわた、骨の
みの処理、殻付き貝類の処理等々の場合は、処理目的に
合った酵素添加によって蛋白質等の分解で短時間で目視
不能となり、処理槽内部にも油脂、蛋白等々の積層付着
も僅少であった。
Fish bones, egg shells and the like are inevitably generated in the organic waste. Fish bones are formed by combining calcium and other organic substances such as proteins. In many cases, or for the treatment of fish for business use, treatment of only bones, treatment of shellfish with shells, etc., the addition of enzymes suitable for the purpose of treatment renders proteins and the like invisible in a short time due to decomposition of proteins, etc. Also, the adhesion of oils, fats, proteins, etc. to the laminate was very small.

【0031】[0031]

【発明の実施の形態】以下、発明の実姉の形態を、いく
つかの実施例に基いて、図面1、2によって説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The embodiments of the present invention will be described below with reference to FIGS.

【0032】処理槽本体(1)は、円筒形、又は多角形
のいずれも実施例はあるが、本実施例については円筒形
の処理槽本体(1)で説明し、各請求項も説明する。
The processing tank body (1) may be either cylindrical or polygonal, but this embodiment will be described with reference to the cylindrical processing tank body (1), and each claim will be described. .

【0033】処理槽本体(1)内で回転する帯歯車
(2)が装着された多孔回転内槽(3)は、処理槽本体
(1)内に装着されたいくつかの、回転ローラー(4)
によって回転可能な状態で挿入設置される。
The perforated rotary inner tank (3) equipped with the band gear (2) rotating in the processing tank body (1) comprises several rotating rollers (4) mounted in the processing tank body (1). )
It is inserted and installed in a rotatable state.

【0034】この多孔回転内槽(3)を設置する目的
は、種々雑多の無機有機混合廃棄物の内、分解消滅不能
の金属、ガラス、陶器、貝殻、木片等を残留残渣として
一定期間毎に排出させる目的で、又、分解処理水中で回
転させる事によって、分解可能物質の分解効率を上げる
為である。
The purpose of installing the perforated rotary inner tank (3) is that, among various miscellaneous inorganic and organic mixed wastes, metal, glass, pottery, shells, wood chips, etc., which cannot be eliminated, are set as residual residues at regular intervals. The purpose of this is to increase the efficiency of decomposition of decomposable substances by rotating in decomposed water for the purpose of discharging.

【0035】多孔回転内槽(3)の一端の円周には、帯
上歯車(2)が装着されているが、この帯状歯車(2)
に代わって、多孔回転内槽(3)の一端壁に、円形歯車
を装着した実施例もある。
A belt-like gear (2) is mounted on the circumference of one end of the multi-hole rotary inner tank (3).
Instead of this, there is an embodiment in which a circular gear is mounted on one end wall of the perforated rotary inner tank (3).

【0036】この理由は、処理槽本体(1)が小型で、
多孔回転内槽(3)の直径が小さい場合は、帯状歯車
(2)は円形曲げ加工、端部溶接、仕上げ加工、多孔回
転内槽(3)装着溶接等々の工賃コストが丸型歯車より
も割高につくからであると共に万一の歯車の歯折損の場
合の交換メンテナンスを容易にする為でもある。
The reason is that the processing tank body (1) is small,
When the diameter of the perforated rotary inner tank (3) is small, the belt-shaped gear (2) requires a round bending process, end welding, finish processing, perforated rotatable inner bath (3) installation welding, etc., and the labor cost is lower than that of the round gear. This is because it is expensive, and it is also to facilitate replacement maintenance in case of gear breakage.

【0037】処理槽本体(1)の外部壁には多孔回転内
槽(3)を回転駆動させる、内槽駆動機(5)が設置さ
れ、駆動歯車(7)が装着された内槽駆動軸(6)が処
理槽本体(1)の円形の壁を貫通して多孔回転内槽
(3)の帯状歯車(2)と噛み合い、内槽駆動機(5)
の起動によって多孔回転内槽(3)は回転する。
On the outer wall of the processing tank main body (1), an inner tank driving device (5) for rotating and driving the porous rotary inner tank (3) is installed, and an inner tank driving shaft equipped with a driving gear (7). (6) penetrates the circular wall of the processing tank body (1) and meshes with the band gear (2) of the perforated rotary inner tank (3), and the inner tank driving device (5)
The rotation of the perforated rotary inner tank (3) is caused by the start of the operation.

【0038】処理槽本体(1)の投入口(8)は、伸縮
ジョイント(9)によって未処理廃棄物貯留槽(11)
に接続されるが、未処理廃棄物貯留槽(11)を併設せ
ずに廃棄物を直接処理槽本体(1)に投入する場合は、
処理槽本体(1)の投入口(8)に別途廃棄物投入蓋を
設置される。
The input port (8) of the treatment tank body (1) is connected to an untreated waste storage tank (11) by an expansion joint (9).
When the waste is directly charged into the treatment tank body (1) without the untreated waste storage tank (11),
A waste input lid is separately installed at the input port (8) of the processing tank body (1).

【0039】未処理廃棄物貯留槽(11)内には、汚泥
混入の無機有機混合廃棄物の処理を想定して廃棄物洗浄
管(34)を設置し、洗浄後の排水をする洗浄水排出バ
ルブ(35)を底部に設け、洗浄された廃棄物は、廃棄
物自動搬送機(10)によって処理槽本体(1)内に自
動的に送られる。
In the untreated waste storage tank (11), a waste washing pipe (34) is installed assuming the treatment of inorganic-organic mixed waste mixed with sludge, and a washing water discharge for draining water after washing. A valve (35) is provided at the bottom, and the washed waste is automatically sent into the treatment tank body (1) by the automatic waste transporter (10).

【0040】この未処理廃棄物貯留槽(11)内の廃棄
物洗浄に当たり、洗浄効果を高める為に、未処理廃棄物
貯留槽(11)内で、天地交換自動攪拌の目的で、廃棄
物自動搬送機(10)を稼働させながら処理槽本体
(1)に廃棄物を送らない方法として、未処理廃棄物貯
留槽(11)の側面壁に設置した未処理廃棄物貯留槽傾
斜昇降装置(33)を稼働させる事によって未処理廃棄
物貯留槽(11)が反対側に傾斜し、対流洗浄も可能で
ある。
In washing the waste in the untreated waste storage tank (11), in order to enhance the washing effect, the automatic waste mixing is performed in the untreated waste storage tank (11) for the purpose of automatic stirring. As a method of not sending waste to the treatment tank main body (1) while operating the transporter (10), an untreated waste storage tank inclined lifting device (33) installed on a side wall of the untreated waste storage tank (11) is used. ), The untreated waste storage tank (11) is inclined to the opposite side, and convection washing is also possible.

【0041】処理槽本体(1)内の多孔回転内槽(3)
の回転運動での前後移動をなくす為に、多孔回転内槽
(3)の回転ローラー(4)が凹部溝付きとなってお
り、多孔回転内槽(3)の回転ローラー(4)の接触部
は凸部帯状として多孔回転内槽(3)のスラスト移動を
防止した。
A multi-hole rotating inner tank (3) in the processing tank body (1)
The rotating roller (4) of the inner perforated rotary tank (3) is provided with a concave groove so as to eliminate the forward and backward movement due to the rotational motion of the perforated rotary inner tank (3). Has a belt-like convex shape to prevent thrust movement of the inner perforated rotary tank (3).

【0042】処理槽本体(1)の上部を貫通して、処理
物質分解過程の臭気の処理槽本体(1)からのリーク発
臭を避ける為、排気管(14)を取付、消臭装置(1
5)に接続され、処理槽本体(1)周囲の臭気リークを
防止する為、排気管(14)を経て、強制的に消臭装置
(15)に吸引される。
An exhaust pipe (14) is provided to prevent the odor from leaking from the processing tank main body (1) due to the odor in the process of decomposing the processing substance through the upper part of the processing tank main body (1). 1
5), and is forcibly sucked into the deodorizing device (15) through the exhaust pipe (14) in order to prevent odor leakage around the processing tank body (1).

【0043】消臭装置(15)は、市販の消臭剤を使用
したが、複合臭気の為に完全とは言えず、又、消臭剤自
体の飽和状態後の廃棄処分に困惑した為、本実施例で
は、酸性、アルカリ性2段の臭気ガス水洗消臭装置を実
施し、又別途、活性炭素繊維による臭気吸着法も実施
し、その効果の確認を得た。
Although a commercially available deodorant was used for the deodorizer (15), it was not perfect due to the complex odor, and it was confusing to dispose of the deodorant itself after saturation. In this example, an acidic and alkaline two-stage odor gas washing and deodorizing apparatus was implemented, and separately, an odor adsorption method using activated carbon fibers was also conducted, and the effect was confirmed.

【0044】処理槽本体(1)の下部には処理槽排水バ
ルブ(16)を設置し、分解水移送伸縮管(17)を取
付け、処理槽本体内の清掃、部品交換、或は、無機有機
固形物の除去の為、分解処理水交換除去等の目的のた
め、分解処理水浄水槽(36)の設置も行った。
A treatment tank drain valve (16) is installed at the lower part of the treatment tank body (1), and a decomposition water transfer telescopic pipe (17) is attached, and the inside of the treatment tank body is cleaned, parts are replaced, or an inorganic organic substance is removed. For the purpose of removing solids and exchanging the decomposed water, a decomposed water purification tank (36) was also installed.

【0045】処理槽本体(1)内の分解処理水は、有機
物酵素群の効率向上と、安全衛生の為に加温するので、
或る程度は蒸散されて減水量の補給が必要となり、一般
水道管又は清水タンクから電磁弁(21)を経由して処
理槽本体(1)に供給されるが、その供給量は、高低位
水位センサー(20)によって電気的に電磁弁(21)
をコントロールして、定量供給が行われる。
The decomposed water in the treatment tank body (1) is heated for improving the efficiency of the organic enzyme group and for safety and health.
To a certain extent, it is necessary to replenish the reduced amount of water due to evaporation, and the water is supplied from the general water pipe or fresh water tank to the treatment tank body (1) via the solenoid valve (21). Electromagnetic valve (21) electrically by water level sensor (20)
Is controlled to perform a fixed amount supply.

【0046】分解水の一定温度上昇の為に、電気的、又
はサーモスタットによる温度制御可能な、分解処理水温
度制御加熱装置(24)と分解処理水温度計(22)が
設置される。
In order to raise the temperature of the decomposed water by a certain level, a decomposed water temperature control heating device (24) and a decomposed water thermometer (22) capable of controlling the temperature electrically or by a thermostat are provided.

【0047】処理槽本体(1)の中に注入する分解処理
水には、有機物を水中で容易に分解消滅させる酵素を主
成分とする有機物分解酵素群を添加し、酵素の最大許容
温度迄の分解水の温度上昇と相まって分解効率を上げた
が、分解水温度が45℃前後の時には酵素分泌有機物分
解微生物群の投入も行い、効果の実証を得た。
To the decomposition water to be injected into the treatment tank body (1), a group of organic substance-decomposing enzymes mainly composed of an enzyme capable of easily dissolving and eliminating organic substances in water is added. Degradation efficiency was increased in conjunction with the rise in the temperature of the decomposed water. However, when the temperature of the decomposed water was around 45 ° C., a group of microorganisms degrading enzyme-secreting organic substances was also introduced, and the effect was verified.

【0048】以上が何例かの実姉例による機構である
が、以下、各実施例のうち、請求項毎の実施例を述べ
る。
The above is the mechanism based on some actual examples. Hereinafter, of each embodiment, an embodiment according to each claim will be described.

【0049】請求項2の高低位センサー(20)は、分
解処理水の高位、低位レベルを感知して清水を供給する
センサーであるが、処理槽本体(1)内で有機廃棄物の
分解処理の過程に於ける種々の不純物が付着し、センサ
ー精度の劣化、或は不作動の要因を除去する為に、処理
槽本体(1)に設置された高低位センサー(20)に近
接する固形残渣排出機(13)の高低位水位センサー
(20)近接部に、センサー清掃ブラシ(25)を装置
し、固形残渣排出機(13)の回転、移動によって自動
的に高低位センサー(20)の表面付着物を清掃し、機
能の維持を図るものである。
The high and low level sensor (20) according to the second aspect is a sensor that senses high and low levels of the decomposed water and supplies fresh water, but decomposes organic waste in the processing tank body (1). In order to eliminate various factors that may cause the impurities in the process, such as deterioration of sensor accuracy or malfunction, solid residue near the high / low sensor (20) installed in the processing tank body (1) A sensor cleaning brush (25) is installed in the vicinity of the high and low water level sensor (20) of the discharging machine (13), and the surface of the high and low water sensor (20) is automatically turned by rotation and movement of the solid residue discharging machine (13). The purpose is to clean the deposits and maintain the function.

【0050】請求項3は、処理槽本体(1)内の水位が
低下した場合の自動供給で、如何に機構上の安全を図っ
ても、電磁弁(21)高低位センサー(20)等々の機
械故障の永久皆無はあり得ないために、安全策として、
分解処理水の高水位レベルの近接上部の処理槽本体
(1)を貫通してオーバーフロー管(26)を設置し
た。
A third aspect of the present invention is an automatic supply when the water level in the processing tank main body (1) is lowered. Regardless of how the mechanical safety is ensured, the solenoid valve (21), the high / low position sensor (20), etc. As there is no permanent failure of the machine, as a safety measure,
An overflow pipe (26) was installed so as to penetrate the treatment tank body (1) in the upper vicinity of the high level of the decomposition treatment water.

【0051】請求項4、の分解処理水蒸散装置(27)
は、処理槽本体(1)内の分解処理水がオーバーフロー
した場合、その排水によって環境公害が発生する恐れが
ある為、オーバーフローした分解処理水を、分解処理水
蒸散装置(27)に導き、消臭剤が添加されて自動的に
大気に放散させるものである。
An apparatus for evaporating decomposed water according to claim 4 (27).
When the decomposed water in the treatment tank body (1) overflows, the drainage thereof may cause environmental pollution, so the overflowed decomposed water is guided to the decomposed water evaporator (27), and the water is removed. The odorant is added and automatically released to the atmosphere.

【0052】請求項5は、駆動歯車(7)と噛み合う帯
状歯車の多孔回転内槽(3)への取付に当たり、多孔回
転内槽(3)、帯状歯車(2)等の真円加工に工数を取
られる場合がある事から、処理槽本体(1)内におい
て、円形歯車を多孔回転内槽(3)の壁に固着ししたも
のも実施した。
In mounting the belt-shaped gear meshing with the drive gear (7) to the porous rotary inner tank (3), it is necessary to add a man-hour to the round processing of the porous rotary inner tank (3), the belt-shaped gear (2) and the like. In some cases, a circular gear was fixed to the wall of the perforated rotary inner tank (3) in the processing tank main body (1).

【0053】請求項6は、多孔回転内槽(3)の開口壁
の中心にシャフトを取付、このシャフトを処理槽本体
(1)の壁を貫通して処理槽本体(1)の外部に呼び出
してベアリングで受け、帯状歯車(2)に代わって円形
歯車を装着し、駆動歯車(7)と噛み合うものである
が、この場合は、処理槽本体(1)の外部での駆動によ
り、チェーン、又はタイミングベルトによるものも実施
し効果を確認し、万一のギアー噛み合い不良の確認が容
易目視可能なメリットがある。
In the sixth aspect, a shaft is mounted at the center of the opening wall of the perforated rotary inner tank (3), and this shaft is passed through the wall of the processing tank body (1) and is called out of the processing tank body (1). In this case, a circular gear is mounted in place of the band gear (2) and meshes with the drive gear (7). In this case, the chain is driven by the drive outside the processing tank body (1). Alternatively, there is a merit that the effect can be confirmed by implementing the method using a timing belt, and it is possible to easily confirm the possibility of the gear meshing failure.

【0054】請求項7、8、9は、多孔回転内槽(3)
の、処理槽本体(1)内面に近接する内壁と、外壁に攪
拌翼を設置し、多孔回転内槽(3)の内壁に設けた攪拌
翼(28)は、多孔回転内槽(3)内の有機廃棄物の処
理槽本体(1)内での分解促進の為の攪拌で、多孔回転
内槽(3)の外壁に設けた攪拌翼(28)は処理槽本体
(1)の分解処理水中の沈殿物の分解促進用の目的であ
る。
The seventh, eighth and ninth aspects of the present invention relate to a perforated rotary inner tank (3).
The agitating blades (28) provided on the inner wall of the perforated rotary inner tank (3) are provided with stirring blades on the inner wall and the outer wall adjacent to the inner surface of the processing tank main body (1). The agitation blade (28) provided on the outer wall of the perforated rotary inner tank (3) is used for agitation to promote the decomposition of the organic waste in the processing tank body (1). The purpose is to promote the decomposition of the precipitate.

【0055】又、多孔回転内槽(3)の内側壁に装着し
た攪拌翼(28)の形状は、中心線と平行に設置した直
線形状の攪拌翼(28)と、多孔回転内槽(3)の内壁
に沿って螺旋形状で設置した攪拌翼(28)、並びに、
各攪拌翼が断片的に構成されたものをも実施し、螺旋状
の攪拌翼(28)の場合は、多孔回転内槽(3)の回転
方向を間欠逆転稼働、又は任意に回転方向を変えられる
様にし、無機廃棄物の排出、廃棄物処理の為の有機廃棄
物の投入時に、夫々、回転方向を変えることによって自
動排出、繰り込みが可能であった。
Further, the shape of the stirring blade (28) mounted on the inner wall of the porous rotary inner tank (3) includes a linear stirring blade (28) installed in parallel with the center line, and a porous rotary inner tank (3). ), A stirring blade (28) installed in a spiral shape along the inner wall, and
In the case of a spiral stirring blade (28), the rotation direction of the perforated rotary inner tank (3) is intermittently reversed, or the rotation direction is arbitrarily changed. Thus, when discharging inorganic waste and charging organic waste for waste treatment, automatic discharge and re-rolling were possible by changing the rotation direction, respectively.

【0056】請求項10は、処理槽本体(1)内部下部
壁と、多孔回転内槽(3)の外壁との空間に、気泡発生
器(29)を設置して空気を供給し、分解水への酸素供
給と、分解水の対流攪拌、気泡破裂時の超音波発生によ
る壁付着物の減少をも図ったものである。
A bubble generator (29) is installed in the space between the inner lower wall of the processing tank main body (1) and the outer wall of the perforated rotary inner tank (3) to supply air and to decompose water. It also aims at reducing oxygen adhering to the wall, convective stirring of decomposed water, and generation of ultrasonic waves at the time of bursting of bubbles.

【0057】請求項11については、本発明は有機物分
解酵素群による有機物の分解消滅をも行う為、処理槽本
体(1)内壁、及び多孔回転内槽(3)の付着物は微小
であるが、多孔回転内槽(3)の内部の有機物分解途中
の物質によって、多孔性が失われる事を防御して分解処
理水の流入、流出を円滑に行い、同時に、内部清掃の目
的によって、処理槽本体(12)内壁に多孔回転内槽清
掃ブラシ(30)を、多孔回転内槽(3)の外周に、処
理槽内壁清掃ブラシ(31)を夫々設置したもので、多
孔回転内槽(3)の回転によって、常に清掃され、尚、
分解処理水中にある未分解有機物質の分解促進にもなっ
た。
According to the eleventh aspect, since the present invention also eliminates and eliminates organic matter by the organic matter decomposing enzyme group, deposits on the inner wall of the treatment tank main body (1) and on the porous rotary inner tank (3) are minute. In order to prevent the loss of porosity due to the organic substances in the inner part of the porous rotating inner tank (3) during the decomposition, the inflow and outflow of the decomposed water are smoothly carried out. A cleaning brush (30) is installed on the inner wall of the main body (12) and a cleaning brush (31) on the inner wall of the processing tank is provided on the outer periphery of the inner rotating tank (3). Is always cleaned by the rotation of
It also accelerated the decomposition of undecomposed organic substances in the decomposed water.

【0058】請求項12は、処理槽本体(1)の外部側
面に、処理槽本体傾斜昇降装置(31)を設け、無機有
機混合廃棄物の固形残渣を排出する際、残渣排出口(1
2)側に傾斜させる事によって、固形残渣の自動排出を
確実に、容易に行う事とするもので、その効果は大きか
った。
A twelfth aspect of the present invention provides a processing tank main body inclined lifting device (31) on the outer side surface of the processing tank main body (1), and discharges the solid residue of the inorganic-organic mixed waste when the residue discharge port (1) is discharged.
2) By inclining the solid residue to the side, the automatic discharge of the solid residue is surely and easily performed, and the effect is great.

【0059】請求項13、14、15は、分解排水蒸散
装置(27)が加熱ヒーター蒸散によるものと、超音波
発振蒸散によるものとを実施したが、加熱ヒーターの場
合は温度が高い為に臭気が高く、やむを得ず消臭剤添加
器(32)を付設したところ、非常に有効であったが、
超音波発振蒸散装置の場合は常温で蒸散する為に臭気
は、さほど気にならなかった。
The thirteenth, fourteenth, and fifteenth aspects are characterized in that the decomposition waste water evaporating apparatus (27) employs a heating heater evaporating method and an ultrasonic oscillation evaporating method. It was very effective when the deodorant additive (32) was unavoidably attached.
In the case of the ultrasonic oscillation evaporator, the odor was not noticeable because it evaporates at room temperature.

【0060】請求項16は、多孔回転内槽(3)の回転
が一方向に回転する方式に加えて、攪拌翼(28)が螺
旋形状の場合に、廃棄物の分解不能残渣が一方方向に集
積される事を防止しする為に、一定間隔で正転逆転を繰
り返す事でその解消を得た。
According to a sixteenth aspect, in addition to the system in which the rotation of the perforated rotary inner tank (3) rotates in one direction, when the stirring blade (28) has a helical shape, the non-decomposable residue of waste is discharged in one direction. In order to prevent the accumulation, the normal rotation and the reverse rotation are repeated at a constant interval to solve the problem.

【0061】請求項17は、未処理廃棄物貯留槽(1
1)の設置に当たり、廃棄物自動搬送機(10)を傾斜
させる事が可能な様に、未処理廃棄物貯留槽傾斜昇降装
置(33)を設置し、汚泥等の混合有機無機廃棄物の洗
浄の場合は洗浄水排出バルブ(35)側に傾斜させて、
廃棄物洗浄管(34)殻の散水とともに、未処理廃棄物
貯留槽(11)内で廃棄物自動搬送機(10)の稼働に
よって循環洗浄し、処理槽本体(1)に廃棄物を投入す
る場合は逆に傾斜させて書理想本体(1)内に自動搬出
するものである。
In the seventeenth aspect, the untreated waste storage tank (1)
In the installation of 1), an untreated waste storage tank tilting elevating device (33) is installed so that the automatic waste transporter (10) can be tilted, and the mixed organic and inorganic waste such as sludge is washed. In the case of, it is inclined to the washing water discharge valve (35) side,
Along with sprinkling of the shell of the waste washing pipe (34), the automatic washing machine (10) performs circulation washing in the untreated waste storage tank (11) by operating the automatic waste transporter (10), and throws the waste into the treatment tank body (1). In this case, the paper is automatically conveyed into the ideal body (1) while being inclined in the opposite manner.

【0062】請求項18、19は、未処理廃棄物貯留槽
(11)内に設置している、廃棄物自動搬出機(10)
が、ベルトタイプのコンベアーの場合と、螺旋状の搬出
機の場合とであるが、実施例ではその両者の検証を行
い、両者共良好であったが、未処理廃棄物貯留槽(1
1)内の洗浄効果はベルトタイプのコンベアーの方が有
利であった。
The automatic waste discharging machine (10) is provided in the untreated waste storage tank (11).
However, in the case of the belt type conveyor and the case of the spiral unloader, both were verified in the embodiment, and both were good. However, the untreated waste storage tank (1)
The cleaning effect in 1) was more advantageous for the belt type conveyor.

【0063】請求項20は、未処理廃棄物貯留槽(1
1)内に、上部からの散水と、下部からの放水塔による
廃棄物洗浄管(34)を設置し、廃棄物自動搬出機(1
0)がベルトタイプの場合はそれを避けて設置し、その
効果を実証した。
In the twentieth aspect, the untreated waste storage tank (1)
In 1), a waste washing pipe (34) with water sprinkling from the top and a water discharge tower from the bottom is installed, and the automatic waste unloader (1) is installed.
In the case of the belt type 0), it was installed avoiding the belt type, and its effect was verified.

【0064】請求項21は、分解処理水を連続半永久的
に使用する事を目的として、多少の清水を導入しながら
浄化して自然廃棄する為の、浄化槽機構を持たせた分解
処理水浄水槽(36)であて、その分解処理水浄水槽
(36)上に各機器を設置することによって設置台板と
もなり、省スペースともなり、処理浄化水の排水不能な
場所も想定して、分解処理水浄水槽(36)の浄化排水
口(38)に、排水蒸散装置(39)を設置し、浄化能
力に応じて毎時間40リッターのほう酸テストも行っ
た。
In order to continuously and semi-permanently use the decomposed water, a decomposed water purification tank having a septic tank mechanism for purifying and natural disposal while introducing some fresh water is provided. In (36), by disposing each device on the decomposed water purifying tank (36), it becomes a mounting base plate, saves space, and assumes a place where the treated purified water cannot be drained. A drainage evaporator (39) was installed at the purification drainage port (38) of the water purification tank (36), and a boric acid test at 40 liters per hour was also performed according to the purification capacity.

【0065】請求項22は、処理槽本体(1)の固形残
渣排出口(12)に隣接して、固形残渣乾燥炉(4
0)、又は、固形残渣焼却炉(41)、又は固形残渣乾
燥炉(41)に代わって固形残渣焼却炉を設置し、処理
槽本体(1)内の分解処理水で濡れた状態を乾燥させ、
又は、分解処理水内の付着有機物のみを焼却して、無機
残渣にするものである。
A solid residue drying furnace (4) is provided adjacent to the solid residue discharge port (12) of the processing tank body (1).
0) Or, a solid residue incinerator is installed in place of the solid residue incinerator (41) or the solid residue drying furnace (41), and the wet state with the decomposed water in the treatment tank body (1) is dried. ,
Alternatively, only the adhered organic matter in the decomposed water is incinerated to produce an inorganic residue.

【0066】請求項23は、処理槽本体(1)の固形残
渣排出口(12)に隣接して、固形残渣粉砕機(41)
をもので、無機類廃棄物の処分を容易にする目的と、再
利用する場合の用途に合った固形残渣粉砕機(41)を
設置する事が可能であり、その再利用の目的によって
は、処理槽本体(1)の固形残渣排出口(12)に続い
て設置せず、固形残渣乾燥炉(40)、又は固形残渣焼
却炉(41)の次に、固形残渣粉砕機(41)を設置す
る事もある。
A solid residue pulverizer (41) is provided adjacent to the solid residue discharge port (12) of the processing tank body (1).
It is possible to install a solid residue crusher (41) suitable for the purpose of facilitating the disposal of inorganic waste and for reuse, and depending on the purpose of the reuse, A solid residue pulverizer (41) is installed after the solid residue drying furnace (40) or the solid residue incinerator (41) without being installed following the solid residue discharge port (12) of the processing tank body (1). Sometimes I do.

【0067】[0067]

【発明の効果】本発明は上述の通り、処理槽本体内に注
入された一定の量の分解処理水によって、非常に簡単な
機構で、種々雑多の混合有機廃棄物を分解処理しようと
するものであり、酵素を主成分とした処理の場合は、定
期的に75℃に温度上昇させて酵素分解を図り、病原菌
に対する安全性の効果と共に、無排水をも達成したもの
である。
As described above, the present invention intends to decompose various mixed organic wastes with a very simple mechanism by using a fixed amount of decomposed water injected into the processing tank body. In the case of a treatment containing an enzyme as a main component, the temperature is periodically raised to 75 ° C. to perform enzymatic decomposition, thereby achieving a safety effect against pathogenic bacteria and also achieving no drainage.

【0068】以下、その効果を説明する。Hereinafter, the effect will be described.

【0069】処理槽本体内に装填している多孔回転内槽
の中に、原形、又は破砕された有機廃棄物、無機物、有
機固形物の混合体を選別する事なく投入するだけで、多
孔回転内槽の回転によって、無機物を除く有機廃棄物は
消滅し、手動又は自動的に有機物分解酵素群、有機物分
解微生物群等による分解促進剤の添加と、一定温度上
昇、酸性度の調整等々によって急速に分解消滅する結果
が判明した。
The original or crushed mixture of organic wastes, inorganic substances, and organic solids is put into the multi-hole rotating inner tank loaded in the processing tank body without sorting, and the multi-hole rotation is performed. By rotating the inner tank, organic waste excluding inorganic substances disappears, and it is quickly or manually added by adding decomposition accelerators by organic matter decomposing enzymes, organic matter decomposing microorganisms, etc., and by raising the temperature, adjusting acidity, etc. It turned out that the result disappeared.

【0070】大型処理器から、家庭用小型機に至るもの
まで、超シンプル化によって格安で生産が可能となり、
現状の地球環境保全に大きく貢献するものである。
From a large-scale processor to a small household machine, super-simplification enables low-cost production.
It will greatly contribute to the preservation of the current global environment.

【0071】分解処理水の攪拌と分解速度との関係は、
分解処理水の攪拌回転が低速回転から、中速回転、場合
によっては高速回転迄まで行ったがどの範囲でも分解は
出来るが、速度が速ければ速い程良いものでもなく、
又、極端に遅いのも分解速度に支障を来し、低速省動力
で、仮に一般家庭用の1日1Kgの有機廃棄物処理機に
於ては微速回転とした駆動電動機を使用した場合、従来
の100ワットモーターが、僅かなワット数の減速機付
きモーターで十分であるが、実施例では10ワット減速
付きモーターで相当な余裕があり、省エネルギーにも貢
献した。
The relationship between the agitation of the decomposition water and the decomposition rate is as follows:
The agitation rotation of the decomposed water was performed from low-speed rotation to medium-speed rotation, and in some cases, to high-speed rotation, but decomposition can be performed in any range.
Also, the extremely slow speed impedes the decomposition speed, and the low speed power saving. If a 1Kg / day organic waste treatment machine for ordinary households uses a drive motor that rotates at a low speed, the conventional Although a small wattage motor with a speed reducer is sufficient for the 100 watt motor, a motor with a 10 watt reducer has a considerable margin in the embodiment, and also contributes to energy saving.

【0072】又、本発明は、本来、加温ヒーターの設置
は必要ないが、分解処理水温度が冬期の様に極端に低下
する場合を考慮して常時25℃の常温で維持させ、処理
槽本体内の有機廃棄物処理での、病原菌の繁殖防止の意
味もあって、常時は25℃、高速分解時と低温滅菌作用
を要する場合は、40°C前後、病原菌消滅と、有機物
分秋酵素群の効果増進を目的とする場合は、最高75℃
迄、分解処理水の温度上昇をさせた。
In the present invention, it is not necessary to install a heating heater. However, in consideration of a case where the temperature of the decomposed water is extremely lowered as in winter, the temperature of the decomposed water is always maintained at a normal temperature of 25 ° C. It also has the meaning of preventing the propagation of pathogenic bacteria in the treatment of organic waste in the body, usually at 25 ° C. When high-speed decomposition and low-temperature sterilization are required, it is around 40 ° C. Up to 75 ° C for the purpose of improving the effect of the group
Until then, the temperature of the decomposed water was increased.

【0073】処理槽本体内の換気は、微小容量換気で良
い事から消臭装置も小型化が出来、小型モーターのみの
為に低周波の電磁振動音もなく、ローター振動共振もな
く、無騒音に近いものとなり、家庭用小型処理器から1
メートル離れて、通常の雰囲気で36dBの騒音数値で
あったが、大型業務用処理器の場合でも多孔回転内槽は
分解処理水の中で微速回転の為、騒音は全くといって良
いほど皆無であった。
The ventilation inside the processing tank body can be made with a small volume ventilation, so that the deodorizing device can be downsized. Since only a small motor is used, there is no low frequency electromagnetic vibration noise, no rotor vibration resonance, no noise. And a small household processor
Meters away, the noise level was 36 dB in a normal atmosphere. However, even in the case of a large commercial processor, the perforated rotary inner tank rotates at a very low speed in the decomposed water, so there is almost no noise at all. Met.

【0074】従来の浄化槽的な処理装置は、分解処理水
は蝿等の害虫が発生する為に、従来は薬品を投入してい
るが、本発明は、病原菌、雑菌の滅菌目的とともに、害
虫の幼虫の棲息も不能な状況を造っているため、分解処
理の酵素との関係で、常時は25℃と40℃前後上昇を
交互に繰り返し、必要ある場合には、75℃に温度上昇
させられる様にし、病原菌等の安全性を図った結果、8
0℃限界の分解酵素との関係もあって分解速度も大きく
上昇した。
In the conventional treatment apparatus like a septic tank, chemicals are conventionally added to the decomposed water in order to generate pests such as flies. However, the present invention is not only for the purpose of sterilizing pathogenic bacteria and various bacteria, but also for the purpose of sterilizing pests. Since the larvae cannot be inhabited, the temperature rises to 25 ° C and 40 ° C alternately at all times, depending on the enzyme of the decomposition treatment, and if necessary, the temperature can be raised to 75 ° C. To improve the safety of pathogenic bacteria, etc.
Degradation rate also increased significantly due to the relationship with the degradation enzyme at the 0 ° C limit.

【0075】有機廃棄物の投入が規定量以上に一時的に
多量投入した場合、処理槽本体内の分解処理水量が増大
する為、分解処理水蒸散装置で処理槽内の分解処理水の
余剰分は処理し、又、分解処理水の温度上昇によっての
自然蒸散等の為、給水管を経由して一定量を供給して、
常時規定水位を保つ事が出来た。
When a large amount of organic waste is temporarily supplied in excess of the specified amount, the amount of decomposed water in the treatment tank body increases. Process, and also supply a certain amount via a water supply pipe for spontaneous transpiration due to the temperature rise of the decomposed water,
It was possible to keep the specified water level at all times.

【0076】減速駆動機が、直流の駆動機を設置した場
合、電力消費が非常に小さいので、回転処理槽の駆動は
太陽光発電による蓄電池の電力源で充分に稼働が確認さ
れ、分解処理水の加熱は従来のニクロム線ヒーターで
は、太陽光発電では不能であるが、家庭用の小型機種の
場合、炭素繊維ヒーターを処理槽本体の外壁に装着して
使用すれば電力は微小であった。
When a DC drive is used as the reduction drive, the power consumption is very small. Therefore, it is confirmed that the operation of the rotary processing tank is sufficiently operated by the power source of the storage battery by solar power generation, and Although conventional nichrome wire heaters cannot be used for photovoltaic power generation, conventional home-use small-sized heaters require only a small amount of power if a carbon fiber heater is mounted on the outer wall of the processing tank body.

【0077】減速駆動機を含めての電力が、太陽光発電
動力によるものは、現在の発電装置が少々割高につく
が、社会的にクリーン電力意識の効用と、政府機関の助
成策もあって、近い将来に於ては、格安の太陽光発電、
風力発電も格安費用で使用が可能であると思われる。
When the electric power including the reduction drive is based on the photovoltaic power, the current power generation device is a little expensive, but there is a social awareness of clean power and subsidies from government agencies. , In the near future, cheap solar power,
It seems that wind power can also be used at low cost.

【0078】分解処理水の加熱保温に必要な分解処理水
温度制御付きヒーターは、処理槽本体外部に装着する場
合と、分解処理水に挿入する場合の両者共有効に働いた
が、処理槽本体の外部からの加熱は、炭素繊維不織布に
よるヒーターは、電力の消費が非常に少なく、又、断線
による故障もないのでこの上ない効果を表した。
The heater with temperature control of the decomposed water required for heating and keeping the temperature of the decomposed water worked effectively both when installed outside the treatment tank main body and when inserted into the decomposed water. Heating from the outside of the heater exhibited an extremely excellent effect because the heater made of the carbon fiber nonwoven fabric consumes very little electric power and has no failure due to disconnection.

【0079】寒冷地において使用する為の、自然温度に
よる放熱、冷却を防止する為に、処理槽本体(3)の内
部又は外部に断熱材を施したもので、処理槽の外部に施
行する場合は発泡スチロール、軟質ウレタン、硬質ウレ
タン、その他何でもよいが、処理槽本体の内部に施行さ
れる場合は、温度制御付きヒーターが処理槽本体内部に
装填される場合に使用し、分解処理水との関係で、硬質
ウレタンが、吸水率が少なく、持続効果があった。
In order to prevent heat radiation and cooling due to natural temperature for use in cold regions, heat treatment is applied to the inside or outside of the treatment tank body (3), and it is applied outside the treatment tank. May be styrofoam, soft urethane, hard urethane, or any other material.However, if it is applied inside the treatment tank body, use it when the heater with temperature control is loaded inside the treatment tank body, and Thus, the hard urethane had a low water absorption and a sustaining effect.

【0080】分解処理水は、多孔回転内槽の回転によっ
ても処理槽本体内で攪拌されるが、気泡発生器によって
も、分解処理水は攪拌される。
The decomposed water is agitated in the main body of the processing tank by the rotation of the multi-hole rotary tank, but the decomposed water is also agitated by the bubble generator.

【0081】従来の処理槽本体内の分解処理水を別途の
浄化槽及び合併処理槽と同様な構成によって、単なる微
生物着床物質を挿入して、冷清水のみで稼働させた場合
は、有機廃棄物の分解目的には程遠く全く意味がなかっ
たが、この理由は従来の様な沈殿槽を持って、その上澄
み水のみを浄化する事しか能力がない事が判明した為、
各種有機物分解酵素群、有機物分解微生物群等の有機物
の分解促進剤を添加して、分解処理水温度を上昇させ、
同時に酸性度の調整によって分解を急進させ、有機廃棄
物である家庭生ごみの殆どが、早いもので1日、遅いも
のでも2日乃至3日で分解消滅したが、温度を75℃に
上昇させる時は、温度の関係で、有機物分解酵素群を主
力とした。
In the case where the decomposed water in the conventional treatment tank main body is operated in a similar manner to the separate septic tank and the combined treatment tank by simply inserting the microorganism-implanted substance and operating only with the cold and clean water, the organic waste is not treated. The purpose of decomposing was far from meaningless at all, but the reason was that it was only possible to purify the supernatant water with a sedimentation tank as before,
Various organic matter degrading enzymes, organic matter degrading microorganisms, etc.
At the same time, the acidity is adjusted to accelerate the decomposition, and most of the household garbage, which is an organic waste, is eliminated in one day if it is early and two to three days if it is late, but the temperature is raised to 75 ° C. At the time, due to the temperature, the group of organic matter-decomposing enzymes was the mainstay.

【0082】有機廃棄物の内、魚の骨、卵のから等に於
ても、その物質構成上から、攪拌混合の繰り返しによ
り、生物体のカルシュウムを結着形成している物質の分
解によって、魚の骨は判別不能となったが、処理槽本体
内部を加圧すれば尚速く、分解不能と思われた牡蛎殻迄
も一部分解可能が判明した。
Of the organic wastes, fish bones, egg roe, and the like, due to the decomposition of the substance binding and forming the calcium of the organism by repeated stirring and mixing, due to the composition of the substance. The bones could not be identified, but it was found that the oyster hulls, which seemed impossible to decompose, could be partially decomposed if the inside of the treatment tank was pressurized.

【0083】有機物の有機物分解酵素群、有機物分解微
生物群等の分解促進剤を分解処理水に添加した場合、有
機廃棄物の内、通常の生ごみは殆どの種類が三日以内に
判別不能となったが、繊維物質は分解に時間が掛かり、
又処理槽内壁に油脂類の積層が認められたので、繊維素
分解酵素、油脂類分解酵素、蛋白分解酵素を含む分解促
進剤を開発し、これらの酵素微生物群を追加添加したと
ころ、全く油脂を含む積層物も無くなり、処理槽本体内
の残渣も激減した。
When a decomposition accelerator such as an organic substance-decomposing enzyme group and an organic substance-decomposing microorganism group of organic substances is added to the decomposed water, most of ordinary organic garbage among organic wastes cannot be discriminated within three days. However, fiber material takes time to decompose,
In addition, since the accumulation of fats and oils was observed on the inner wall of the treatment tank, a decomposition accelerator containing fibrinolytic enzymes, fat and oil degrading enzymes, and proteases was developed. , And the residue in the treatment tank main body was drastically reduced.

【0084】最後に、本発明の特徴は、多孔回転内槽の
回転によって、有機物は消滅して処理槽本体内の分解処
理水に溶け込み、回転内槽の中には分解不能の無機類等
の残渣が残り、多孔回転内槽という、残渣自動選別的機
構を有しているため、一般廃棄処理に置ける選別不能の
混合廃棄物、その他に、貝毒発生時の牡蛎廃棄処分処
理、造船係船解除時の船体付着の牡蛎、ムール貝等、船
舶海水配管内の付着貝、造船所ドック排水溝側壁付着貝
類、等々の処理を前提に実施試験したがその効果は、絶
大なものがあった。
Finally, a feature of the present invention is that the rotation of the porous rotary inner tank causes the disappearance of the organic matter and the dissolution of the organic matter into the decomposed water in the main body of the processing tank. Residue remains and has a residue automatic sorting mechanism called a rotating inner tank, so it is impossible to sort mixed waste that can be placed in general waste treatment.In addition, oyster waste disposal processing when shellfish poisoning occurs, shipbuilding mooring canceled The tests were carried out on the assumption that oysters, mussels, etc. attached to the hull at the time, attached shells in the seawater piping of the ship, and attached shells attached to the shipyard dock drainage channel side wall, etc., but the effect was enormous.

【図面の簡単な説明】[Brief description of the drawings]

【図1】有機無機混合廃棄物処理装置の、廃棄物自動搬
送機がコンベアータイプを設置した未処理廃棄物貯留槽
と、処理槽本体が結続された、側面図、一部断面図であ
る。
FIG. 1 is a side view and a partial cross-sectional view of an organic-inorganic mixed waste treatment apparatus, in which an untreated waste storage tank in which an automatic waste transporter is provided with a conveyor type and a treatment tank main body are connected. .

【図2】無機有機混合廃棄物処理装置の、廃棄物自動搬
送機が、螺旋状の未処理廃棄物貯留槽と、処理槽本体が
結合された、側面図、一部断面図である。
FIG. 2 is a side view and a partial cross-sectional view of an inorganic / organic mixed waste treatment apparatus, in which an automatic waste transporter is connected to a spiral untreated waste storage tank and a treatment tank main body.

【図3】処理槽本体の、多孔回転内槽、等の主要部の正
面図である。
FIG. 3 is a front view of a main part of a processing tank main body, such as a multi-hole rotary tank.

【図4】無機有機混合廃棄物処理装置の、一貫ライン装
置図の側面図、一部断面図である。
FIG. 4 is a side view and a partial cross-sectional view of an integrated line apparatus diagram of an inorganic-organic mixed waste treatment apparatus.

【符号の説明】[Explanation of symbols]

1 処理槽本体 2 帯状歯車 3 多孔回転内槽 4 回転ローラー 5 内槽駆動器 6 内槽駆動軸 7 駆動歯車 8 投入口 9 伸縮ジョイント 10 廃棄物自動搬送機 11 未処理廃棄物貯留槽 12 固形残渣排出口 13 固形残渣排出機 14 排気管 15 消臭装置 16 処理槽排水バルブ 17 分解水移送伸縮管 18 給水バルブ 19 給水管 20 高低位センサー 21 電磁弁 22 分解処理水温度計 23 給水洗浄管 24 分解処理水温度制御加熱装置 25 センサー清掃ブラシ 26 オーバーフロー管 27 分解処理水蒸散装置 28 攪拌翼 29 気泡発生器 30 多孔回転内槽清掃ブラシ 31 処理槽本体傾斜昇降装置 32 消臭剤添加器 33 未処理廃棄物貯留槽傾斜昇降装置 34 廃棄物洗浄管 35 洗浄水排出バルブ 36 分解処理水浄水槽 37 分解処理水導入バルブ 38 浄化排水口 39 排水蒸散装置 40 固形残渣乾燥炉、又は固形残渣焼却炉 41 固形残渣粉砕機 DESCRIPTION OF SYMBOLS 1 Processing tank main body 2 Band gear 3 Perforated rotation inner tank 4 Rotating roller 5 Inner tank driver 6 Inner tank drive shaft 7 Drive gear 8 Input port 9 Telescopic joint 10 Automatic waste transporter 11 Untreated waste storage tank 12 Solid residue Discharge port 13 Solid residue discharger 14 Exhaust pipe 15 Deodorizer 16 Treatment tank drain valve 17 Decomposed water transfer telescopic pipe 18 Water supply valve 19 Water supply pipe 20 High / low sensor 21 Solenoid valve 22 Decomposition water thermometer 23 Water supply washing pipe 24 Disassembly Treated water temperature control heating device 25 Sensor cleaning brush 26 Overflow pipe 27 Decomposition treated water evaporation device 28 Stirrer blade 29 Bubble generator 30 Perforated rotating inner tank cleaning brush 31 Treatment tank main body tilt elevating device 32 Deodorant additive 33 Untreated waste Waste storage tank tilt elevating device 34 Waste washing pipe 35 Washing water discharge valve 36 Decomposition treated water purification tank 37 Disassembly Treated water introduction valve 38 Purification drainage outlet 39 Wastewater evaporator 40 Solid residue drying furnace or solid residue incinerator 41 Solid residue crusher

フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01D 53/81 2115−4H C05G 5/00 B63B 29/14 C08J 5/00 B65F 5/00 C12M 1/00 C05G 5/00 1/02 C08J 5/00 1/04 C12M 1/00 1/06 1/02 1/12 1/04 1/33 1/06 1/36 1/12 C12S 3/00 1/33 3/24 1/36 13/00 C12S 3/00 2115−4H C05F 9/02 3/24 2115−4H 17/00 13/00 B01D 53/34 116C // C05F 9/02 116A 17/00 Continued on the front page (51) Int.Cl. 6 Identification code Agency reference number FI Technical indication B01D 53/81 2115-4H C05G 5/00 B63B 29/14 C08J 5/00 B65F 5/00 C12M 1/00 C05G 5/00 1/02 C08J 5/00 1/04 C12M 1/00 1/06 1/02 1/12 1/04 1/33 1/06 1/36 1/12 C12S 3/00 1/33 3 / 24 1/36 13/00 C12S 3/00 2115-4H C05F 9/02 3/24 2115-4H 17/00 13/00 B01D 53/34 116C // C05F 9/02 116A 17/00

Claims (23)

【特許請求の範囲】[Claims] 【請求項1】 処理槽本体(1)内部には、帯状歯車
(2)が装着された多孔回転内槽(3)が、複数の回転
ローラー(4)によって回転可能な状態で装填される。
処理槽本体(1)の外部には、内槽駆動機(5)が設置
され、処理槽本体(1)を貫通した内槽駆動軸(6)に
装着された駆動歯車(7)は、帯状歯車(2)と噛み合
う。処理槽本体(1)の投入口(8)は、伸縮ジョイン
ト(9)が装着され、廃棄物自動搬送機(10)が付い
た未処理廃棄物貯留槽(11)に接続される。処理槽本
体(1)内の、固形残渣排出口(12)側には、固形残
渣排出機(13)が設置される。処理槽本体(1)の上
部を貫通した排気管(14)は、消臭装置(15)に結
続される。処理槽本体(1)下部に貫通して、処理槽排
水バルブ(16)が装着され、分解水移送伸縮管(1
7)が装着される。給水バルブ(18)が設置された給
水管(19)は、高低水位センサー(20)によって稼
働する電磁弁(21)を経由して、処理槽本体(1)を
貫通して装着される。処理槽本体(1)に、分解処理水
温度計(22)、給水洗浄管(23)、分解処理水温度
制御加熱装置(24)が設置され、処理槽本体(1)内
に、有機物分解有効微生物群、有機物分解酵素群を夫々
単独、又は両方を配合し、加えて雑菌繁殖防止剤を添加
した分解処理水を注入した、無機有機混合廃棄物処理装
置。
1. A porous inner rotating tank (3) to which a band-shaped gear (2) is attached is loaded in a processing tank main body (1) so as to be rotatable by a plurality of rotating rollers (4).
An inner tank driving device (5) is installed outside the processing tank body (1), and a drive gear (7) mounted on an inner tank drive shaft (6) penetrating the processing tank body (1) has a belt shape. Meshes with the gear (2). The inlet (8) of the treatment tank body (1) is connected to an untreated waste storage tank (11) equipped with an expansion joint (9) and equipped with an automatic waste transfer machine (10). On the solid residue discharge port (12) side of the processing tank body (1), a solid residue discharge machine (13) is installed. An exhaust pipe (14) penetrating the upper part of the processing tank body (1) is connected to a deodorizing device (15). A treatment tank drainage valve (16) is attached to the lower part of the treatment tank body (1), and the decomposed water transfer telescopic pipe (1) is attached.
7) is mounted. A water supply pipe (19) provided with a water supply valve (18) is attached to the treatment tank body (1) through an electromagnetic valve (21) operated by a high / low water level sensor (20). A decomposition water thermometer (22), a water supply washing pipe (23), and a decomposition water temperature control heating device (24) are installed in the treatment tank body (1), and organic matter decomposition is effective in the treatment tank body (1). An inorganic / organic mixed waste treatment apparatus in which a microorganism group and an organic matter decomposing enzyme group are used alone or in combination with each other, and decomposed water to which a fungus growth inhibitor is added is injected.
【請求項2】 高低位水位センサー(20)に接触す
る、センサー清掃ブラシ(25)が、固形残渣排出機
(13)に装着された、廃棄物処理装置。
2. A waste treatment device comprising a sensor cleaning brush (25) in contact with a high and low water level sensor (20) mounted on a solid residue discharger (13).
【請求項3】 処理槽本体(1)に、オーバーフロー管
(26)が設置された、無機有機混合廃棄物処理装置。
3. An inorganic-organic mixed waste treatment apparatus in which an overflow pipe (26) is installed in a treatment tank body (1).
【請求項4】 処理槽本体(1)に、分解処理水蒸散装
置(27)が装着された、無機有機混合廃棄物処理装
置。
4. An inorganic / organic mixed waste treatment apparatus comprising a treatment tank main body (1) and a decomposition treatment water evaporation apparatus (27) mounted thereon.
【請求項5】 帯状歯車(2)に代わって、開口板の円
形歯車が、多孔回転内槽(3)の壁に固着された、請求
項1記載の、無機有機混合廃棄物処理装置。
5. An apparatus according to claim 1, wherein a circular gear of an aperture plate is fixed to the wall of the inner perimeter tank (3) in place of the belt gear (2).
【請求項6】 多孔回転内槽(3)の壁中心に固着され
シャフトが処理槽本体(1)の奥部壁を貫通して外部に
突出し、それに帯状歯車(2)に代わって円形歯車が固
着され、処理槽本体(1)の外部で、駆動歯車(7)に
よって駆動される、請求項1記載の、無機有機混合廃棄
物処理装置。
6. A shaft fixed to the center of the wall of the perforated rotary inner tank (3) penetrates the inner wall of the processing tank main body (1) and protrudes to the outside, and a circular gear replaces the band gear (2). The inorganic / organic mixed waste treatment apparatus according to claim 1, wherein the apparatus is fixed and driven by a drive gear (7) outside the treatment tank body (1).
【請求項7】 多孔回転内槽(3)内壁に、攪拌翼(2
8)が装着された、請求項1記載の、無機有機混合廃棄
物処理装置。
7. A stirring blade (2) is provided on the inner wall of the perforated rotary inner tank (3).
The inorganic-organic mixed waste treatment apparatus according to claim 1, wherein the apparatus (8) is mounted.
【請求項8】 多孔回転内槽(3)内壁、及び外壁に、
攪拌翼(28)が装着された、請求項1記載の、無機有
機混合廃棄物処理装置。
8. An inner wall and an outer wall of a perforated rotary inner tank (3),
The inorganic / organic mixed waste treatment apparatus according to claim 1, further comprising a stirring blade (28).
【請求項9】 攪拌翼(28)が、螺旋状の、請求項1
記載の、無機有機混合廃棄物処理装置。
9. The stirrer according to claim 1, wherein the stirring blade is spiral.
An inorganic-organic mixed waste treatment apparatus as described in the above.
【請求項10】 処理槽本体(1)内に、気泡発生器
(29)を設置した、請求項1記載の、無機有機混合廃
棄物処理装置。
10. An apparatus according to claim 1, wherein a bubble generator (29) is provided in the processing tank body (1).
【請求項11】 処理槽本体(1)の内壁に、多孔回転
内槽清掃ブラシ(30)を装着した、請求項1記載の、
無機有機混合廃棄物処理装置。
11. The cleaning device according to claim 1, wherein a cleaning brush (30) for rotating a perforated inner tank is mounted on an inner wall of the processing tank body (1).
Inorganic-organic mixed waste treatment equipment.
【請求項12】 処理槽本体(1)の外部側面に、処理
槽本体傾斜昇降装置(31)を装着した、請求項1記載
の、無機有機混合廃棄物処理装置。
12. The inorganic-organic mixed waste treatment apparatus according to claim 1, wherein a treatment tank main body inclination raising / lowering device (31) is mounted on an outer side surface of the treatment tank main body (1).
【請求項13】 分解処理水蒸散装置(27)が、加
熱ヒーター蒸散による、請求項1記載の、無機有機混合
廃棄物処理装置。
13. The apparatus for treating an inorganic-organic mixed waste according to claim 1, wherein the decomposition water evaporating apparatus (27) is based on heating heater evaporation.
【請求項14】 分解処理水蒸散装置(27)が、超音
波発振蒸散による、請求項1記載の、無機有機混合廃棄
物処理装置。
14. The apparatus for treating an inorganic-organic mixed waste according to claim 1, wherein the decomposition water transpiration apparatus (27) uses ultrasonic oscillation transpiration.
【請求項15】 分解処理水蒸散装置(27)に、消臭
剤添加器(32)が付設された、請求項1記載の、無機
有機混合廃棄物処理装置。
15. The apparatus for treating an inorganic-organic mixed waste according to claim 1, wherein the deodorizing water evaporator (27) is provided with a deodorant additive (32).
【請求項16】 内槽駆動器(5)が、正回転、及び逆
回転も可能な、請求項1記載の、無機有機混合廃棄物処
理装置。
16. An apparatus according to claim 1, wherein the inner tank drive (5) is also capable of rotating forward and backward.
【請求項17】 未処理廃棄物貯留槽(11)の側面
に、未処理廃棄物貯留槽傾斜昇降装置(33)が装着さ
れた、請求項1記載の、無機有機混合廃棄物処理装置。
17. An inorganic-organic mixed waste treatment apparatus according to claim 1, wherein an untreated waste storage tank inclination raising / lowering device (33) is mounted on a side surface of the untreated waste storage tank (11).
【請求項18】 未処理廃棄物貯留槽(11)の、廃棄
物自動搬送機(10)が、コンベアーの、請求項1記載
の、無機有機混合廃棄物処理装置。
18. The inorganic / organic mixed waste treatment apparatus according to claim 1, wherein the automatic waste transporter (10) of the untreated waste storage tank (11) is a conveyor.
【請求項19】 未処理廃棄物貯留槽(11)の、廃棄
物自動搬送機(10)が、螺旋搬送機の、請求項1記載
の、無機有機混合廃棄物処理装置。
19. The apparatus according to claim 1, wherein the automatic waste transporter (10) of the untreated waste storage tank (11) is a spiral transporter.
【請求項20】 未処理廃棄物貯留槽(11)の層内に
廃棄物洗浄管(34)、並びに洗浄水排出バルブ(3
5)が装着された、請求項1記載の、無機有機混合廃棄
物処理装置。
20. A waste washing pipe (34) and a washing water discharge valve (3) in a layer of an untreated waste storage tank (11).
The inorganic-organic mixed waste treatment apparatus according to claim 1, wherein 5) is mounted.
【請求項21】 処理槽本体(1)に、分解処理水浄水
槽(36)を併設し、処理槽排水バルブ(16)と、分
解処理水浄水槽(36)の分解処理水導入バルブ(3
7)が接続され、分解処理水浄水槽(36)の浄化排水
口(38)に排水蒸散装置(39)が設置された、請求
項1記載の、無機有機混合廃棄物処理装置。
21. A treatment tank body (1) is provided with a decomposition treatment water purification tank (36), a treatment tank drain valve (16), and a decomposition treatment water introduction valve (3) of the decomposition treatment water purification tank (36).
7. The inorganic-organic mixed waste treatment apparatus according to claim 1, wherein the wastewater evaporator (39) is installed at the purification drainage port (38) of the decomposition treatment water purification tank (36).
【請求項22】 処理槽本体(1)の固形残渣排出口
(12)に隣接して、固形残渣乾燥炉(40)、又はそ
れに代わって固形残渣焼却炉が装着された、請求項1記
載の、無機有機混合廃棄物処理装置。
22. The solid residue drying furnace (40), or a solid residue incinerator instead of the solid residue incinerator, adjacent to the solid residue discharge port (12) of the treatment tank body (1). , Inorganic and organic mixed waste treatment equipment.
【請求項23】 処理槽本体(1)の固形残渣排出口
(12)に隣接して、固形残渣粉砕機(41)が設置さ
れた、請求項1記載の、無機有機混合廃棄物処理装置。
23. The inorganic / organic mixed waste treatment apparatus according to claim 1, wherein a solid residue pulverizer (41) is provided adjacent to the solid residue discharge port (12) of the treatment tank body (1).
JP23572596A 1996-08-02 1996-08-02 Inorganic/organic waste mixture treating device Pending JPH1043731A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23572596A JPH1043731A (en) 1996-08-02 1996-08-02 Inorganic/organic waste mixture treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23572596A JPH1043731A (en) 1996-08-02 1996-08-02 Inorganic/organic waste mixture treating device

Publications (1)

Publication Number Publication Date
JPH1043731A true JPH1043731A (en) 1998-02-17

Family

ID=16990310

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23572596A Pending JPH1043731A (en) 1996-08-02 1996-08-02 Inorganic/organic waste mixture treating device

Country Status (1)

Country Link
JP (1) JPH1043731A (en)

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JP2002310419A (en) * 2001-04-12 2002-10-23 Meidensha Corp Thermal decomposition facility by gas engine power generation facility using digestive gas
KR101259914B1 (en) 2007-05-25 2013-05-02 버전 인코포레이션 Multi-purpose discarded material treatment system
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002310419A (en) * 2001-04-12 2002-10-23 Meidensha Corp Thermal decomposition facility by gas engine power generation facility using digestive gas
KR101259914B1 (en) 2007-05-25 2013-05-02 버전 인코포레이션 Multi-purpose discarded material treatment system
JP2015519283A (en) * 2012-04-26 2015-07-09 ザ プロクター アンド ギャンブルカンパニー Composting equipment for controlling malodors and methods for eliminating odors in composting
JP2015520101A (en) * 2012-04-26 2015-07-16 ザ プロクター アンド ギャンブルカンパニー Composting device with odor sensor
CN105113398A (en) * 2015-07-10 2015-12-02 沈素春 Low-noise bridge expansion joint cleaning device
JP2019085296A (en) * 2017-11-07 2019-06-06 中部エコテック株式会社 Waste treatment equipment
CN113684116A (en) * 2021-09-14 2021-11-23 苏州西姆提纳米科技有限公司 New energy preparation device for decomposing organic garbage by using microorganisms
CN113684116B (en) * 2021-09-14 2023-08-15 苏州西姆提纳米科技有限公司 New energy preparation device for decomposing organic garbage by utilizing microorganisms

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