JP2001019580A - Composting treatment for organic waste and apparatus used therefor - Google Patents

Composting treatment for organic waste and apparatus used therefor

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Publication number
JP2001019580A
JP2001019580A JP18395299A JP18395299A JP2001019580A JP 2001019580 A JP2001019580 A JP 2001019580A JP 18395299 A JP18395299 A JP 18395299A JP 18395299 A JP18395299 A JP 18395299A JP 2001019580 A JP2001019580 A JP 2001019580A
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JP
Japan
Prior art keywords
organic waste
composting
gas
fermentation
bacteria
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.)
Granted
Application number
JP18395299A
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Japanese (ja)
Other versions
JP3839188B2 (en
Inventor
Shigeaki Kamiya
成章 神谷
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.)
WAKABA KK
Original Assignee
WAKABA KK
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Classifications

    • 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
    • Y02W30/20Waste processing or separation
    • 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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  • Processing Of Solid Wastes (AREA)
  • Fertilizers (AREA)

Abstract

PROBLEM TO BE SOLVED: To eliminate the need of a deodorizing treatment and compost an organic waste without using an electrical energy by mixing the organic waste with a photophilic/thermophilic microorganism group, filling the resultant mixture in a hermetically sealed chamber, applying a light energy to the organic waste and fermenting and photolyzing the organic waste. SOLUTION: This apparatus A for a composting treatment is obtained by forming a hermetically sealed chamber 18 of a horizontal rectangular cross section from a peripheral wall 12, a ceiling wall and a floor wall 16 and dividing the hermetically sealed chamber 18 into a first treating chamber 18a, a second treating chamber 18b and a third treating chamber 18c with partition walls 20. A mixture prepared by mixing a garbage with KN bacteria is initially piled up in the first treating chamber 18a to prepare starter bacteria while repeating, gas stirring and scattering of a photolytic and fermentation liquor. The garbage is then mixed with the starter bacteria and piled up in the second treating chamber 18b and the third treating chamber 18c and the composting treatment is performed while similarly repeating the gas stirring and scattering of the photolytic and fermentation liquor. At this time, sunshine is used as the light energy for light emission and photolysis.

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、有機廃棄物を、光
好性/好熱性の微生物群を利用して堆肥化(コンポスト
化)処理する新規な方法及び装置に関する。特に、市街
地・公園等の臭気発生を嫌う場所で行なうのに好適な有
機廃棄物堆肥化処理方法及び装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a novel method and apparatus for composting organic waste using photophilic / thermophilic microorganisms. In particular, the present invention relates to an organic waste composting method and apparatus suitable for performing in places where odor generation is disliked, such as urban areas and parks.

【0002】[0002]

【背景技術】昨今、有機廃棄物を従来の焼却ないしその
まま埋立地等に投棄する代わりに、環境フレンドリーの
見地から、微生物(細菌・酵母等)を使用して、有機廃
棄物を発酵・分解させて堆肥化(コンポスト(compost)
化)する方法が提案され実施化されつつある。
2. Description of the Related Art Recently, instead of conventional incineration or dumping of organic waste in landfills, from the viewpoint of environmental friendliness, microorganisms (such as bacteria and yeast) are used to ferment and decompose organic waste. Composting (compost)
Method has been proposed and is being implemented.

【0003】[0003]

【発明が解決しようとする課題】しかし、従来の堆肥化
する生ごみ処理装置(有機廃棄物堆肥化処理装置)は、
特に大型のものにおいては、脱臭処理装置を付設する必
要があった。通常の微生物処理においては、特に、投入
時及び発酵・分解開始後しばらくは、無臭化が困難なた
めである。
However, the conventional composting garbage processing apparatus (organic waste composting processing apparatus) is
Particularly in the case of large-sized ones, it was necessary to add a deodorizing treatment device. This is because in ordinary microorganism treatment, it is difficult to deodorize, especially at the time of introduction and for a while after the start of fermentation and decomposition.

【0004】また、生ごみ処理装置は、時々攪拌すると
ともに、発酵温度(処理温度)になるまで加温する必要
があり、それぞれ加温のための電気エネルギーを必要と
した。
In addition, the garbage disposal apparatus needs to be stirred occasionally and heated up to the fermentation temperature (treatment temperature), and each requires electric energy for heating.

【0005】さらには、生ごみの中には、漬物、みそ
類、しょうゆ、食塩等の塩(シオ)高含有物が混在して
おり、堆肥化されても、そのまま肥料として使用すると
き塩害が発生するおそれがあった。
[0005] Furthermore, garbage contains high content of salt (shio) such as pickles, miso, soy sauce, and salt. There was a risk of occurrence.

【0006】本発明は、上記にかんがみて、脱臭処理が
不要な新規な有機廃棄物堆肥化処理方法及び装置を提供
することを目的とする。
In view of the above, an object of the present invention is to provide a novel method and apparatus for composting an organic waste that does not require deodorization.

【0007】本発明の他の目的は、電気エネルギーの大
幅な低減が可能な有機廃棄物堆肥化処理方法及び装置を
提供することにある。
It is another object of the present invention to provide a method and an apparatus for composting an organic waste capable of significantly reducing electric energy.

【0008】本発明のさらに他の目的は、肥料としてそ
のまま使用しても塩害が発生するおそれがない有機廃棄
物堆肥化処理方法及び装置を提供することにある。
It is still another object of the present invention to provide a method and an apparatus for composting an organic waste, which do not cause salt damage even when used directly as a fertilizer.

【0009】[0009]

【課題を解決するための手段】本発明の有機廃棄物堆肥
化処理方法の一つは、有機廃棄物を、光好性/好熱性の
微生物群(元菌を含む)と混合して密閉室に充填(投
入)後、該有機廃棄物に光エネルギーを与えて発酵させ
て堆肥化を行なうことにより、上記第一の課題(目的)
を解決するものである。
According to one aspect of the present invention, an organic waste composting method comprises mixing an organic waste with a group of photophilic / thermophilic microorganisms (including original bacteria) and mixing the organic waste with the microorganism. After filling (injecting) the organic waste, light energy is given to the organic waste for fermentation and composting, thereby achieving the first problem (object).
Is to solve.

【0010】本発明の有機廃棄物堆肥化処理方法の他の
一つは、上記構成において光エネルギーとして太陽エネ
ルギーを利用又は主体とすることにより、上記第二の課
題を解決するものである。
[0010] Another one of the organic waste composting treatment methods of the present invention solves the above second problem by using or mainly using solar energy as light energy in the above configuration.

【0011】上記方法において、有機廃棄物の充填部の
上方に気体貯留部を形成し、該気体貯留部に貯留するガ
スを、前記有機廃棄物充填部の底部側に循環・導入させ
て有機排気物の気体攪拌を行なったり、さらには、有機
廃棄物充填部の底部側に廃液貯留部を形成し、廃液貯留
部に貯留する廃液を前記有機廃棄物充填部の上面に散布
することにより、上記第二の課題をより効率的に解決で
きる。
[0011] In the above method, a gas storage section is formed above the organic waste filling section, and the gas stored in the gas storage section is circulated and introduced to the bottom side of the organic waste filling section to form an organic exhaust gas. By performing gas agitation of the material, and further, by forming a waste liquid storage portion on the bottom side of the organic waste filling portion, and spraying the waste liquid stored in the waste liquid storage portion on the upper surface of the organic waste filling portion, The second problem can be solved more efficiently.

【0012】本発明の有機廃棄物堆肥化処理方法の他の
一つは、上記第一の構成において、微生物群が、好塩性
微生物を含むものとすることにより、上記第三の課題を
解決するものである。
Another one of the organic waste composting treatment methods of the present invention solves the above third problem by providing the microorganism group in the above first configuration, wherein the microorganism group includes a halophilic microorganism. It is.

【0013】[0013]

【手段の詳細な説明】次に、上記手段の各構成について
詳細な説明をおこなう。
[Detailed Description of Means] Next, each component of the above means will be described in detail.

【0014】本発明の有機廃棄物堆肥化方法は、有機廃
棄物を、光好性/好熱性の微生物群(元菌を含む)と混
合して密閉室に充填(投入)後、該有機廃棄物に光エネ
ルギーを与えて発酵させて堆肥化を行なうことを特徴と
するものである。
In the method for composting organic waste according to the present invention, the organic waste is mixed with a group of photophilic / thermophilic microorganisms (including original bacteria), filled (closed) into a closed chamber, and then charged with the organic waste. It is characterized in that composting is performed by giving light energy to a product and fermenting it.

【0015】ここで、有機廃棄物としては、家庭を初め
として、ホテル、レストラン、給食センター、さらに
は、食品加工工場、食品市場等から排出される生ごみ
(残飯、オカラ、卵から、等)の他に、芝生、家畜排泄
物(鶏糞、牛糞、馬糞、豚糞)等が含まれる。
Here, the organic waste includes garbage discharged from households, hotels, restaurants, food service centers, food processing factories, food markets, etc. (from garbage, okara, eggs, etc.). Besides, grass, livestock excrement (chicken dung, cow dung, horse dung, pig dung) and the like are included.

【0016】また、好光性/好熱性の微生物群とは、好
光性/好熱性の双方を備えている微生物の一群をいう。
例えば、光合成細菌のうち好熱性を備えているものを使
用できる。そして、光合成細菌としては、紅色細菌、緑
色細菌、好気性光合成細菌、ヘリオバクテリウム等、特
に限定されない。当然、光をエネルギーとして増殖する
耐熱性の酵母も使用可能である。
The term "photophilic / thermophilic microorganisms" refers to a group of microorganisms having both photophilic / thermophilic properties.
For example, photosynthetic bacteria having thermophilicity can be used. The photosynthetic bacteria are not particularly limited, such as red bacteria, green bacteria, aerobic photosynthetic bacteria, heliobacterium and the like. Naturally, a heat-resistant yeast that grows using light as energy can also be used.

【0017】ここで、好熱性細菌とは、「生育至適温度
が、50〜105℃で、30℃以下の温度ではほとんど
増殖しない細菌の総称。通常の細菌は中性温(mesophil
ic)、すなわち生育の至適温度が25〜40℃であり、
50℃以上では一般に生育し難い。なお、高温でも定温
でも生育可能な可能な細菌は耐熱性細菌( thermore-si
stant bacteria )とよんで区別される。」(八杉他編
「岩波生物学辞典第4版」(1996−3−21)岩
波、p452参照)とされているが、本明細書では、好
熱性細菌には耐熱性細菌も含む。昼間は密閉室内は高温
となるが、夜間は、温調しなければ、通常細菌の生育至
適温度25〜40℃に下がる場合もあるためである。
Here, the thermophilic bacterium is a general term for a bacterium that has an optimum growth temperature of 50 to 105 ° C. and hardly grows at a temperature of 30 ° C. or less.
ic), that is, the optimal temperature for growth is 25 to 40 ° C.,
Above 50 ° C., it is generally difficult to grow. Bacteria capable of growing at high or constant temperatures are thermore- tive bacteria.
stant bacteria). (See Iwanami Biological Dictionary, 4th Edition, edited by Yasugi et al. (1996-3-21) Iwanami, p. 452), but in the present specification, thermophilic bacteria also include thermostable bacteria. This is because the temperature in the closed room becomes high in the daytime, but in the nighttime, if the temperature is not adjusted, the temperature is usually lowered to the optimal growth temperature of bacteria of 25 to 40 ° C.

【0018】さらに、本発明では、堆肥化したものを施
肥した場合、塩害の発生のおそれがないように、微生物
が好塩性のものを含むことが望ましい。ここで、「好塩
性」とは、「5〜10wt%あるいはそれ以上の食塩濃度
の培地を好む細菌や菌類の性質」をいい、菌体内に多量
のNa+ を取り入れて塩濃度を低下させると推定され
る。(同p424参照)これらの好光性/好熱性の特性
を備えた微生物群としては、これらの要件を満たしてい
る限り、特に限定されない。例えば、吉良微生物研究所
(愛知県幡豆郡吉良町大字鮫馬字内の山23)から製造
販売している「ケイエヌ菌」群を好適に使用できる。該
「ケイエヌ菌」は、好塩性も有している。
Further, in the present invention, it is preferable that the microorganisms include those which are halophilic so that there is no risk of salt damage when the compost is fertilized. Here, the term "halophilic" means "the property of bacteria or fungi that prefer a medium having a salt concentration of 5 to 10 wt% or more", and a large amount of Na + is taken into the cells to lower the salt concentration. It is estimated to be. (See p. 424) The microorganism group having these photophilic / thermophilic characteristics is not particularly limited as long as these requirements are satisfied. For example, the "KN fungi" group manufactured and sold by the Kira Microbial Research Institute (Yama 23 in the Samema character, Kira-cho, Hazu-gun, Aichi Prefecture) can be suitably used. The "Kay fungi" also has halophilicity.

【0019】「ケイエヌ菌」群は、本発明者らが、下記
の如く、日本各地から採取した種菌(微生物種)を工場
で40年以上、培養・安定化させた一連の微生物群であ
る。
[0019] The "Kay fungus" group is a group of microorganisms in which the present inventors have cultured and stabilized seed microorganisms (species of microorganisms) collected from various parts of Japan for more than 40 years in factories as described below.

【0020】日本各地の山や神社の大木(通常、樹齢
100年以上)の根っこに小穴(径・深さとも約10〜
15cm)を掘りそこへ、砂糖50〜100cc、酢10
〜15ccを添加して、土を被せて2〜3日放置後、種
菌を採取する。
At the root of a large tree (usually over 100 years old) at a mountain or shrine in various parts of Japan, a small hole (both in diameter and depth is about 10 to 10)
15cm) and dig there, sugar 50-100cc, vinegar 10
Add ~ 15 cc, cover the soil and leave for 2-3 days before collecting the inoculum.

【0021】上記種菌を工場に持ち帰り、栄養源とな
るカット野菜(レタス、キャベツ、白菜、スイカ、なす
等)と混合して、加温(30〜40℃)しながら発酵さ
せて培養する。
The inoculum is brought back to the factory, mixed with cut vegetables (lettuce, cabbage, Chinese cabbage, watermelon, eggplant, etc.) as a nutrient source, fermented while heating (30 to 40 ° C.), and cultured.

【0022】菌が安定してきたら(約1年後)、太陽
光を培地に直接照射した後、残存生菌のみを取り出し、
上記と同様にして培養を1年間行なう。この工程を繰り
返す。この際、直接照射の期間は、1日、3日、1週
間、1ケ月、2ケ月、3ケ月と順次増やして行く。培養
期間が5年程経過したら、直接照射の際に、培地が60
℃以上となるように温調を行なう。
When the bacteria become stable (after about one year), the medium is directly irradiated with sunlight, and only the remaining viable bacteria are taken out.
Culture is performed for one year as described above. This step is repeated. At this time, the direct irradiation period is sequentially increased to one day, three days, one week, one month, two months, and three months. After the cultivation period of about 5 years, the medium is grown to 60
Adjust the temperature so that the temperature is at least ℃.

【0023】こうして、微生物群は、好光性とともに好
熱性を備えたもののみとなる。該「ケイエヌ菌」の特性
は、下記の如くである。
As described above, the microorganism group is only those having both thermophilicity and thermophilicity. The characteristics of the "Kay fungus" are as follows.

【0024】主として太陽光線の光で反応し、好気性
・嫌気性のどちらの状態でも活動する。
It reacts mainly with the light of the sun's rays and is active in both aerobic and anaerobic conditions.

【0025】有機廃棄物の水分(湿量含量基準)が7
0wt%以下(望ましくは45〜65%)、温度40〜1
00℃(望ましくは50〜70℃)において、太陽光線
があれば増殖して、有機廃棄物の発酵・分解を促進させ
る。
The water content (based on the wet content) of the organic waste is 7
0 wt% or less (preferably 45-65%), temperature 40-1
At 00 ° C (preferably 50-70 ° C), it proliferates in the presence of sunlight and promotes fermentation and decomposition of organic waste.

【0026】塩のNa+ を選択的に取り込み、通常の
発酵分解の場合に比して、発酵残渣・発酵残水中の塩濃
度(主としてNaCl)が半分以下となる。したがっ
て、有機物の発酵を促進させ、高温発酵と相まって、処
理物が早く乾燥する。
The Na + of the salt is selectively taken in, and the salt concentration (mainly NaCl) in the fermentation residue / fermentation residue water is reduced to half or less as compared with the case of ordinary fermentation decomposition. Therefore, the fermentation of organic matter is promoted, and the treated material dries quickly in combination with high-temperature fermentation.

【0027】分解・発酵時に70℃以上の高温とな
る。腐敗菌及び雑菌が死滅して、それらのメタン菌等に
起因するアンモニアガス、メタンガス、ブタンガス等の
発生が抑制される。
During decomposition and fermentation, the temperature rises to 70 ° C. or higher. The spoilage bacteria and various germs are killed, and the generation of ammonia gas, methane gas, butane gas, and the like due to the methane bacteria and the like is suppressed.

【0028】有機物と無機塩との分離作用を有する。It has an action of separating organic substances and inorganic salts.

【0029】上記有機廃棄物と微生物群との混合比は、
有機廃棄物及び微生物群の種類により異なるが、通常の
生ごみ(残飯)の場合、生ごみ(水分50〜60%)1
00重量部に対して、「ケイエヌ菌」元菌10〜50重
量部、望ましくは、20〜40重量部とする。
The mixing ratio between the organic waste and the microorganism group is as follows:
Although it depends on the type of organic waste and microorganisms, in the case of ordinary garbage (garbage), garbage (moisture 50 to 60%) 1
With respect to 00 parts by weight, 10 to 50 parts by weight, preferably 20 to 40 parts by weight, of the original strain of "K.

【0030】元菌とするのは、処理物である有機廃棄物
に慣らすためである。例えば、有機廃棄物と微生物とを
適宜混合比で混ぜ合わせ、4〜10週、望ましくは6〜
8週寝かし、増殖させて元菌とする。このときの、微生
物群と有機廃棄物群の混合比は、上記有機廃棄物及び微
生物群の種類により異なるが、通常の生ごみ(残飯)の
場合、生ごみ(水分50〜60%)100Lに対して、
「ケイエヌ菌」1〜3L、望ましくは、2Lとする。
The original bacteria are used to adjust to the organic waste which is a processed product. For example, the organic waste and the microorganism are mixed at an appropriate mixing ratio, and 4 to 10 weeks, preferably 6 to
Let it rest for 8 weeks and let it multiply to get the original bacteria. At this time, the mixing ratio between the microorganism group and the organic waste group differs depending on the type of the organic waste and the microorganism group. In the case of ordinary garbage (remaining garbage), 100 L of garbage (50 to 60% water) is used. for,
"Kay fungi" 1 to 3L, preferably 2L.

【0031】密閉室で堆肥化処理するのは、有機廃棄物
から発生する臭気(特に、投入直後から発酵初期・中期
まで)の外部へ放出させないためである。
The composting treatment is carried out in a closed room in order to prevent the odor generated from the organic waste (especially from immediately after introduction to the initial and middle stages of fermentation) from being released to the outside.

【0032】該有機廃棄物に与える、光エネルギー源
は、通常、太陽光とするが、紫外線照射ランプ等であっ
てもよい。例えば、夜間や曇天・雨天の日に、紫外線照
射ランプを補助的に使用して、有機廃棄物の発酵を促進
させてもよい。
The light energy source given to the organic waste is usually sunlight, but may be an ultraviolet irradiation lamp or the like. For example, at night or on cloudy or rainy days, an ultraviolet irradiation lamp may be used as an auxiliary to promote fermentation of organic waste.

【0033】有機排気物(被処理物)の攪拌は、機械的
方法によってもよいが、上記構成において、有機廃棄物
の充填部の上方に気体貯留部を形成し、該気体貯留部に
貯留するガスを、前記有機廃棄物充填部の底部側に循環
・導入させて前記有機排気物の気体攪拌を行なうこと
が、微生物の繁殖を増大させて望ましい。
Stirring of the organic exhaust material (object to be treated) may be performed by a mechanical method. In the above structure, a gas storage portion is formed above the organic waste filling portion and stored in the gas storage portion. It is desirable to circulate and introduce a gas to the bottom side of the organic waste filling section to agitate the organic exhaust gas so as to increase the growth of microorganisms.

【0034】即ち、気体貯留部の貯留する気体(ガス)
は、分解・発酵熱により加温され、さらに、太陽熱によ
り加熱された高温ガスである。該高温ガス(通常、60
℃以上)を有機廃棄物の底部側から導入することによ
り、有機廃棄物(処理物)温度が、好熱性の微生物群の
繁殖が促進され、さらに、通常雑菌(60℃以上では死
滅する。)の繁殖が抑制される。したがって、堆肥化処
理が促進されるとともに、無菌堆肥化がより確実とな
る。当然、処理物表面側は、太陽光殺菌される。
That is, the gas (gas) stored in the gas storage unit
Is a high-temperature gas heated by decomposition / fermentation heat and further heated by solar heat. The hot gas (typically 60
(° C. or more) is introduced from the bottom side of the organic waste, the temperature of the organic waste (processed material) promotes the proliferation of thermophilic microorganisms, and furthermore, usually various bacteria (kill at 60 ° C. or more). Breeding is suppressed. Therefore, the composting process is promoted, and the aseptic composting becomes more reliable. Naturally, the surface side of the processed object is sterilized by sunlight.

【0035】なお、このときの有機廃棄物充填部と気体
貯留部の容量比は、通常、4/1〜1/3、望ましく
は、3/1〜1/2とする。充填部比率が高すぎると、
貯留部容積が相対的に小さくなり、分解・発酵ガスによ
るガス圧が高くなり易く、密閉室に耐圧性が要求され
る。逆に、充填部比率が低過ぎると、密閉室容積が大き
くなって、密閉室コンパクト化の要請に反する。
At this time, the volume ratio between the organic waste filling section and the gas storage section is usually 4/1 to 1/3, preferably 3/1 to 1/2. If the filling ratio is too high,
The storage volume is relatively small, the gas pressure due to the decomposition / fermentation gas is likely to be high, and pressure resistance is required for the closed chamber. Conversely, if the filling portion ratio is too low, the volume of the closed chamber increases, which is contrary to the demand for a compact closed chamber.

【0036】また、高温ガス循環量は、有機処理物10
0kg当たり、5〜100L/minとする。通常、当該
ガス循環量を得るためには、気体循環路に気体搬送機を
配する。
The high-temperature gas circulation amount depends on the amount of the organic processed material 10.
5 to 100 L / min per 0 kg. Usually, in order to obtain the gas circulation amount, a gas carrier is arranged in the gas circulation path.

【0037】また、発酵・分解により生成する発酵・分
解液はそのまま排出してもよいが、底部側から取り出し
て上側から散布することが望ましい。即ち、本発明の堆
肥化処理は、60℃以上の高温雰囲気で行なうため、分
解・発酵に伴い炭化物も生成し、この炭化物(黒色)が
分解・発酵液(水を含む)中に含まれる。このため、該
分解・発酵液を充填部表面に散布することにより、充填
部(被処理物)表面が黒色化して太陽光線(特に、熱
線)の吸収効率が増大し、より、好熱性微生物の繁殖増
大が期待できる。なお、この散布量は、発生する分解・
発酵液の量により異なり、所定量貯留した後、間欠的に
散布する。
The fermentation / decomposition liquid produced by fermentation / decomposition may be discharged as it is, but it is desirable to take it out from the bottom and spray it from the top. That is, since the composting process of the present invention is performed in a high-temperature atmosphere of 60 ° C. or more, carbides are also generated along with decomposition / fermentation, and the carbides (black) are contained in the decomposition / fermentation liquid (including water). For this reason, by spraying the decomposition / fermentation liquid on the surface of the filling portion, the surface of the filling portion (object to be treated) is blackened, the absorption efficiency of sunlight (especially, heat rays) is increased, and the thermophilic microorganisms Reproduction can be expected to increase. In addition, this spraying amount is
It depends on the amount of fermentation liquid, and after storing a predetermined amount, it is sprayed intermittently.

【0038】次に、上記の有機廃棄物堆肥化処理方法に
使用する装置について説明する。
Next, an apparatus used in the above-mentioned method for composting organic waste will be described.

【0039】本発明の有機廃棄物堆肥化処理装置は、当
該構成に限定されるものではない。
The organic waste composting treatment apparatus of the present invention is not limited to this configuration.

【0040】図1は本実施形態の有機廃棄物堆肥化処理
装置の外観概略図、図2は同じく床面図である。
FIG. 1 is a schematic external view of an organic waste composting treatment apparatus according to this embodiment, and FIG. 2 is a floor plan of the same.

【0041】該装置Aは、周壁12と天井壁14と床壁
16とで水平断面矩形の密閉室18が形成されている。
該密閉室18は、図例では隔壁20により3室、即ち、
第一処理室18a、第二処理室18b、第三処理室18
cに区画されている。周壁12は、図例では、前面壁1
2aが後面壁12bより高く形成された構成で、天井壁
14は太陽光を透過可能な傾斜壁で形成され、床壁16
は、気体攪拌及び発酵・分解液を回収するために多孔板
で形成されている。図例では、多孔板(パンチングプレ
ート)の孔形状は、長孔であるが、丸、三角、多角形状
等任意であり、さらには、場合によっては、網体で形成
してもよい。
In the device A, a closed chamber 18 having a rectangular horizontal cross section is formed by the peripheral wall 12, the ceiling wall 14, and the floor wall 16.
In the illustrated example, the closed chamber 18 is divided into three chambers by a partition wall 20, that is,
First processing chamber 18a, second processing chamber 18b, third processing chamber 18
c. In the illustrated example, the peripheral wall 12 is the front wall 1.
2a is formed higher than the rear wall 12b, the ceiling wall 14 is formed of an inclined wall that can transmit sunlight, and the floor wall 16
Is formed of a perforated plate for gas agitation and recovery of the fermentation / decomposition liquid. In the illustrated example, the hole shape of the perforated plate (punching plate) is a long hole, but may be any shape such as a circle, a triangle, and a polygon, and may be formed of a net in some cases.

【0042】そして、各処理室18a、18b、18c
に処理物を投入可能に、それぞれ扉付きの出入口21が
形成されている。
The processing chambers 18a, 18b, 18c
An entrance 21 with a door is formed so that a processing object can be put into the apparatus.

【0043】ここで、該出入口21を密閉構造とするた
め、図3〜5に示すような扉開閉構造とされている。
Here, in order to make the entrance 21 a closed structure, a door opening / closing structure as shown in FIGS.

【0044】H形支柱22で形成された対向する各溝C
内を扉体(鋼板製ゲート)24が、減速機26の出力軸
と連結されたスプロケットで駆動されるチェーン28と
連結されて昇降するようになっている。なお、扉体24
が連結されているチェーン端と反対側のチェーン端には
カウンターウェート30が連結されている。
Each of the opposed grooves C formed by the H-shaped support 22
Inside, a door (steel plate gate) 24 is connected to a chain 28 driven by a sprocket connected to an output shaft of a speed reducer 26 to move up and down. The door 24
A counterweight 30 is connected to the chain end opposite to the chain end to which the is connected.

【0045】そして、扉体24の出入口密閉性を確保す
るために、出入口21には、門型戸当たり部材32が形
成されているとともに、それに対応させて扉体24の内
側には、処理物出入口21に対応して門型で断面P型の
P型パッキン34を介して貼着されている。
A gate-shaped door stop member 32 is formed at the entrance 21 in order to ensure the sealing of the entrance of the door 24, and a treated material is provided inside the door 24 correspondingly. It is attached via a P-shaped packing 34 having a gate-shaped and P-shaped cross section corresponding to the entrance 21.

【0046】そして、処理物出入口21の床側にはH字
形鋼でシール受け面36が形成されているとともに、斜
め下方へ突出する傾斜直状(平型)断面の平型パッキン
38が座を介して貼着されている。
A seal receiving surface 36 made of H-shaped steel is formed on the floor side of the treated material entrance 21 and a flat packing 38 having an inclined straight (flat) cross section protruding obliquely downward is seated. Is pasted through.

【0047】また、扉体の外側の天井側及び床部側に
は、H型支柱の内側に形成された案内傾斜ブロック(4
個)40に対応させて作動傾斜ブロック42がそれぞれ
2個づつ計4個形成されて、閉時に傾斜ブロック40、
42相互の楔作用により、扉体24は閉じ方向に移動
し、門型のP型パッキン34が同じく門型の戸当たり部
材32に圧接するとともに、平型パッキン38は、床面
であるシール受け面36に圧接する。こうして、扉体2
4は処理物出入り口を密閉する。
Further, on the ceiling side and the floor side outside the door body, a guide inclined block (4) formed inside the H-shaped support is provided.
4), two operation inclined blocks 42 are formed in total corresponding to the two inclined inclined blocks 42.
The door body 24 moves in the closing direction by the mutual wedge action, the gate-shaped P-type packing 34 comes into pressure contact with the gate-shaped door stop member 32, and the flat-type packing 38 serves as a seal receiving member on the floor surface. It presses against the surface 36. Thus, door 2
4 seals the entrance and exit of the processed material.

【0048】そして、周壁12は処理物充填高さ位置ま
で、コンクリート、金属、プラスチック等の不透明壁と
し、それより上の周壁12c及び天井壁14は、太陽光
が透過可能な透明材で形成する。なお、不透明壁は、保
温性の見地から断熱性を有するコンクリート壁又はプラ
スチック壁が望ましく、その厚みは、コンクリート壁の
場合、20〜100mmとし、さらには、プラスチック壁
の場合、5〜10mmとする。
The peripheral wall 12 is an opaque wall of concrete, metal, plastic or the like up to the processing object filling height position, and the peripheral wall 12c and the ceiling wall 14 above it are formed of a transparent material through which sunlight can pass. . The opaque wall is desirably a concrete wall or a plastic wall having heat insulating properties from the viewpoint of heat insulation, and the thickness is set to 20 to 100 mm in the case of a concrete wall, and further to 5 to 10 mm in the case of a plastic wall. .

【0049】この透明材は、ガラスでもよいが、通常、
太陽光の内、主として光合成に使用される波長域(68
0〜700nm)を透過し易い透明プラスチック材が望
ましい。透明プラスチック材としては、ポリカーボネー
ト、アクリル系樹脂、ポリスチレン、ポリ塩化ビニル等
の非晶性樹脂を好適に使用可能である。
The transparent material may be glass, but usually,
Of the sunlight, the wavelength range (68
(0-700 nm) is desirable. As the transparent plastic material, an amorphous resin such as polycarbonate, acrylic resin, polystyrene and polyvinyl chloride can be suitably used.

【0050】このとき、天井壁の厚さは、太陽光吸収の
見地からは可及的に薄い方が望ましいが、通常、強度
(耐圧性を含む)及び耐久性さらには保温性を考慮し
て、1〜10mmとする。
At this time, it is desirable that the thickness of the ceiling wall be as thin as possible from the viewpoint of absorption of sunlight, but usually, the strength (including pressure resistance) and durability, and further, heat insulation are taken into consideration. 1 to 10 mm.

【0051】さらに、本装置においては、図6に示す如
く、気体攪拌装置44及び分解・発酵液散布装置46が
付設されている。
Further, in the present apparatus, as shown in FIG. 6, a gas stirring device 44 and a decomposition / fermentation liquid spraying device 46 are additionally provided.

【0052】気体攪拌装置44は、密閉室18の後壁側
12bから床壁下側空間(分解・発酵液貯留部を兼ね
る。)に導通する気体配管(気体循環路)48と気体配
管48の途中に配設される気体輸送機(気体ポンプ)5
0とからなる。
The gas stirrer 44 includes a gas pipe (gas circulation path) 48 and a gas pipe 48 that communicate from the rear wall 12b of the closed chamber 18 to the space below the floor wall (also serving as a decomposition / fermentation liquid storage section). Gas transporter (gas pump) 5 installed on the way
It consists of 0.

【0053】また、分解・発酵液散布装置46は、分解
・発酵液貯留部と密閉処理室の天井壁との間に、液体輸
送機(液体ポンプ)52を介して液体配管(散布配管)
54が配され、天井側先端には、散布ノズル56が取り
付けられている。
The decomposition / fermentation liquid spraying device 46 is provided between the decomposition / fermentation liquid storage section and the ceiling wall of the sealed processing chamber via a liquid transporter (liquid pump) 52 for liquid piping (spraying piping).
54, and a spray nozzle 56 is attached to the top end on the ceiling side.

【0054】なお、図1において、58は換気扇口で、
その反対側には、吸気口が配され、それぞれ、温度上昇
(例えば30〜40℃)により温度センサーが働き自動
開閉するようになっている。ただし、換気扇口が開くの
は、発酵後期になり、匂いがほとんど発生しなくなって
からとする。
In FIG. 1, reference numeral 58 denotes a ventilation fan,
On the opposite side, air intake ports are arranged, and a temperature sensor is activated by a temperature rise (for example, 30 to 40 ° C.) to automatically open and close. However, it is assumed that the ventilation fan is opened in the late stage of fermentation and after almost no odor is generated.

【0055】次に、上記装置を使用しての、有機廃棄物
(生ごみ)の処理方法について、説明をする。なお、使
用する生ゴミの水分は、40〜60%の範囲のものを使
用する。
Next, a method of treating organic waste (garbage) using the above apparatus will be described. The garbage used has a water content in the range of 40 to 60%.

【0056】まず、第一処理室に、生ごみ1000kg
当たり、ケイエヌ菌20L袋を2袋混ぜ合わせ、積み上
げ、気体攪拌及び分解・発酵液散布を繰り返しながら、
元菌調製を行なう。その期間は、通常、30〜60日と
する。
First, 1000 kg of garbage is placed in the first treatment room.
Hit, mix 2 bags of 20L of Caenium fungus, pile up, repeat gas agitation and decomposition / fermentation liquid spraying,
Prepare the original bacteria. The period is usually 30 to 60 days.

【0057】次に、第二・第三処理室で、生ごみ100
0kg当たり、元菌300〜400kgを混ぜ合わせ積
み上げて、上記同様、気体攪拌及び分解・発酵液散布を
繰り返しながら、堆肥化処理を行なう。
Next, in the second and third treatment chambers, 100 garbage
A composting process is performed by mixing and stacking 300 to 400 kg of the original bacteria per 0 kg and repeating gas stirring and decomposition / fermentation liquid spraying as described above.

【0058】なお、上記方法で春季において堆肥化処理
を行なったが、その結果は、下記の如くであった。
The composting treatment was performed in the spring by the above method, and the results were as follows.

【0059】2日間で室内温度(気体貯留部)の温度
は、昼間で70〜80℃になった。また、生ゴミは10
日間で、約半分に減少した。さらに、10日間(合計2
0日間)で、水分が10〜15%となって、さらさらの
堆肥が得られた。
In two days, the temperature of the room temperature (gas storage part) became 70 to 80 ° C. in the daytime. The garbage is 10
In a day, it was reduced by about half. 10 days (total 2 days)
(0 days), the water content became 10 to 15%, and a smooth compost was obtained.

【0060】[0060]

【発明の作用・効果】本発明の有機廃棄物(被処理物)
を、光好性/好熱性の微生物群(元菌を含む)と混合し
て密閉室に充填(投入)後、該有機廃棄物に光エネルギ
ーを与えて発酵させることにより堆肥化を行なう構成で
あるため下記のような効果を奏する。
Operation and effect of the present invention Organic waste (substance to be treated) of the present invention
Is mixed with a group of photophilic / thermophilic microorganisms (including the original bacteria), filled (filled) in a closed chamber, and then fermented by giving light energy to the organic waste for composting. Therefore, the following effects are obtained.

【0061】原則的に、堆肥化処理において匂いの発生
し易い初期・中期を密閉室内で行なうため、脱臭処理が
不要となる。
In principle, in the composting process, the initial and middle stages in which odor is likely to occur are performed in a closed room, so that the deodorizing process becomes unnecessary.

【0062】高温下(60℃以上)で有機廃棄物を分解
・発酵させるため、雑菌が繁殖し難く無菌堆肥化が可能
となる。特に、光として太陽光を使用する場合、さら
に、紫外線による殺菌効果が増大して、無菌堆肥化がよ
り確実になる。
Since the organic waste is decomposed and fermented at a high temperature (60 ° C. or higher), it is difficult for germs to propagate and aseptic composting becomes possible. In particular, when sunlight is used as light, the sterilizing effect of ultraviolet rays is further increased, and aseptic composting becomes more reliable.

【0063】また、光として太陽光を使用することによ
り、従来の如く、温調(特に加温)のために、電気エネ
ルギーを使用する必要がなく、省エネルギーにつなが
る。
Further, by using sunlight as light, it is not necessary to use electric energy for temperature control (especially heating) as in the prior art, which leads to energy saving.

【0064】また、有機廃棄物充填部上方の気体貯留部
に貯留した高温空気を床壁から吹き出させて気体攪拌す
ることにより、有機廃棄物の処理物温度分布が均一とな
るとともに、高温空気中に浮遊している微生物が底部か
ら充填部に搬送される。このため、微生物の増殖が均一
となり、より、堆肥化処理が促進される。
Further, the high temperature air stored in the gas storage section above the organic waste filling section is blown out from the floor wall and gas is agitated, so that the temperature distribution of the processed organic waste becomes uniform and the high temperature air The microorganisms floating on the bottom are transported from the bottom to the filling section. For this reason, the growth of microorganisms becomes uniform, and the composting process is further promoted.

【0065】さらに、有機廃棄物充填部の下方の床壁下
方に貯留した分解・発酵液を、充填部上面に散布するこ
とにより、分解・発酵液中に含まれている炭化物により
充填部表面が黒体化して、吸熱効率が増大し、さらに、
堆肥化処理が促進される。
Further, the decomposition / fermentation liquid stored under the floor wall below the organic waste filling section is sprayed on the upper surface of the filling section, so that the surface of the filling section is formed by the charcoal contained in the decomposition / fermentation liquid. Black body, heat absorption efficiency increases, and
Composting is promoted.

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

【図1】本発明の有機廃棄物堆肥化処理装置の外観概略
斜視図
FIG. 1 is a schematic perspective view of the appearance of an organic waste composting treatment apparatus of the present invention.

【図2】同じく床面を示す概略断面図FIG. 2 is a schematic sectional view showing a floor surface in the same manner.

【図3】扉体の作動構成を示す概略斜視図FIG. 3 is a schematic perspective view showing an operation configuration of a door body.

【図4】扉体の密閉構造における扉体開状態の概略断面
FIG. 4 is a schematic cross-sectional view of the closed state of the door body when the door body is open.

【図5】同じく扉体閉状態の概略断面図FIG. 5 is a schematic sectional view of the door body in a closed state.

【図6】有機廃棄物堆肥化処理装置における気体攪拌装
置及び分解・発酵液散布装置の配管態様を示す斜視図
FIG. 6 is a perspective view showing a piping mode of a gas stirring device and a decomposition / fermentation liquid spraying device in the organic waste composting treatment device.

【符号の説明】[Explanation of symbols]

18 密閉室 44 気体攪拌装置 46 分解・発酵液散布装置 50 気体輸送機 18 Closed chamber 44 Gas stirring device 46 Decomposition / fermentation liquid spraying device 50 Gas transporter

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D004 AA02 AA03 BA04 CA15 CA18 CA43 CA48 CB04 CB05 CB21 CB36 CB44 CC01 CC07 CC20 DA02 DA06 4H061 AA02 AA03 CC36 CC38 CC42 CC47 CC55 EE66 GG15 GG43 GG47 GG48 GG62 GG67 HH50 ──────────────────────────────────────────────────続 き Continued on front page F term (reference) 4D004 AA02 AA03 BA04 CA15 CA18 CA43 CA48 CB04 CB05 CB21 CB36 CB44 CC01 CC07 CC20 DA02 DA06 4H061 AA02 AA03 CC36 CC38 CC42 CC47 CC55 EE66 GG15 GG43 GG47 GG48 HGG62GG

Claims (14)

【特許請求の範囲】[Claims] 【請求項1】 有機廃棄物(被処理物)を、少なくとも
光好性/好熱性の微生物群(元菌を含む)と混合して密
閉室に充填(投入)後、該有機廃棄物に光エネルギーを
与えて発酵・分解させことにより堆肥化を行なうことを
特徴とする有機廃棄物堆肥化処理方法。
Claims 1. An organic waste (substance to be treated) is mixed with at least a photophilic / thermophilic microorganism group (including original bacteria) and filled (filled) in a closed chamber. A method for composting organic waste, comprising composting by applying energy to ferment and decompose.
【請求項2】 前記光エネルギーが太陽光である又は主
体とするものであることを特徴とする請求項1記載の有
機廃棄物堆肥化処理方法。
2. The method for composting organic waste according to claim 1, wherein the light energy is sunlight or mainly.
【請求項3】 前記有機廃棄物の充填部の上方に気体貯
留部を形成し、該気体貯留部に貯留する気体(ガス)
を、前記有機廃棄物充填部の底部側に循環・導入させて
前記有機廃棄物の気体攪拌を行なうことを特徴とする請
求項2記載の有機廃棄物堆肥化処理方法。
3. A gas storage portion is formed above the organic waste filling portion, and a gas (gas) stored in the gas storage portion is provided.
The organic waste composting treatment method according to claim 2, wherein the organic waste is circulated and introduced to the bottom side of the organic waste filling section to perform gas agitation of the organic waste.
【請求項4】 前記気体の循環経路に気体輸送機を配す
ることを特徴とする請求項3の有機廃棄物堆肥化処理方
法。
4. The method for composting organic waste according to claim 3, wherein a gas transporter is disposed in the gas circulation path.
【請求項5】 前記発酵時に発生する有機廃棄物充填部
の底部側に廃液貯留部を形成し、該廃液貯留部に貯留す
る発酵・分解液を前記有機廃棄物充填部の上面に散布す
ることを特徴とする請求項2、3、又は4記載の有機廃
棄物堆肥化処理方法。
5. A waste liquid storage section is formed at the bottom of the organic waste filling section generated during the fermentation, and the fermentation / decomposition liquid stored in the waste liquid storage section is sprayed on the upper surface of the organic waste filling section. The organic waste composting treatment method according to claim 2, 3, or 4, wherein:
【請求項6】 前記微生物群がさらに好塩性を備えてい
ることを特徴とする請求項1記載の有機廃棄物堆肥化処
理方法。
6. The method for composting organic waste according to claim 1, wherein the microorganisms further have halophilicity.
【請求項7】 前記微生物群が、土壌微生物起源であ
り、且つ、好気性/嫌気性混合タイプであることを特徴
とする請求項6記載の有機廃棄物堆肥化処理方法。
7. The method for composting an organic waste according to claim 6, wherein the microorganism group is derived from soil microorganisms and is of a mixed aerobic / anaerobic type.
【請求項8】 前記部生物群が、「ケイエヌ菌」(吉良
微生物研究所製造販売)であることを特徴とする請求項
7記載の有機廃棄物堆肥化処理方法。
8. The method for composting organic waste according to claim 7, wherein the group of living organisms is “K.
【請求項9】 前記光合成微生物群が、「ケイエヌ菌」
(吉良微生物研究所製造販売)であることを特徴とする
請求項2記載の有機廃棄物堆肥化処理方法。
9. The photosynthetic microorganism group is “K.
The organic waste composting method according to claim 2, wherein the method is (manufactured and sold by Kira Microorganisms Research Laboratories).
【請求項10】 密閉空間で生ごみにケイエヌ菌を混ぜ
て積み上げて元菌を調製後、該元菌と有機廃棄物とを混
合させて前記堆肥化を行なうことを特徴とする請求項2
記載の有機廃棄物堆肥化処理方法。
10. The composting is carried out by mixing and stacking C. germ germ with garbage in an enclosed space to prepare an original bacterium, and then mixing the germ with an organic waste.
The organic waste composting method according to the above.
【請求項11】 請求項2記載の有機廃棄物堆肥化処理
方法に使用する装置であって、一個又は複数個の密閉室
を備え、該密閉室の少なくとも天井側が光透過材で形成
され、該密閉室の底部側に透き間をおいて多孔板が配さ
れ、該多孔板の下側透き間と前記密閉室の天井側との間
に気体配管が配されていることを特徴とする有機廃棄物
堆肥化処理装置。
11. An apparatus used in the method for composting organic waste according to claim 2, comprising one or more closed chambers, wherein at least the ceiling side of the closed chamber is formed of a light transmitting material, An organic waste compost, wherein a perforated plate is arranged on the bottom side of the closed chamber with a gap, and a gas pipe is arranged between the lower gap of the perforated plate and the ceiling side of the closed chamber. Processing equipment.
【請求項12】 前記光透過材がプラスチック透明板で
あることを特徴とする請求項11記載の有機廃棄物堆肥
化処理装置。
12. The organic waste composting treatment apparatus according to claim 11, wherein the light transmitting material is a plastic transparent plate.
【請求項13】 前記気体配管が、さらに気体輸送機を
備えていることを特徴とする請求項11記載の有機廃棄
物堆肥化処理装置。
13. The organic waste composting treatment apparatus according to claim 11, wherein the gas pipe further includes a gas transporter.
【請求項14】 さらに、前記多孔板の下側透き間と前
記密閉室の天井側との間に、中間に液体輸送機を備え、
先端に散布ノズルを備えた散布配管が配されていること
を特徴とする請求項11、12又は13に記載の有機廃
棄物堆肥化処理装置。
14. A liquid transporter is provided between the lower gap between the perforated plate and the ceiling of the closed chamber,
The organic waste composting treatment apparatus according to claim 11, 12 or 13, further comprising a spray pipe provided with a spray nozzle at a tip.
JP18395299A 1999-06-29 1999-06-29 Organic waste composting method and apparatus used therefor Expired - Lifetime JP3839188B2 (en)

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