JPH08332075A - Culture of microbe and culture system - Google Patents

Culture of microbe and culture system

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Publication number
JPH08332075A
JPH08332075A JP7144710A JP14471095A JPH08332075A JP H08332075 A JPH08332075 A JP H08332075A JP 7144710 A JP7144710 A JP 7144710A JP 14471095 A JP14471095 A JP 14471095A JP H08332075 A JPH08332075 A JP H08332075A
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JP
Japan
Prior art keywords
raw material
activator
material liquid
liquid
aeration
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
JP7144710A
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Japanese (ja)
Other versions
JP3447846B2 (en
Inventor
Shunsaku Kokubu
俊作 国分
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KOKUBU NOJO KK
Original Assignee
KOKUBU NOJO KK
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Priority to JP14471095A priority Critical patent/JP3447846B2/en
Publication of JPH08332075A publication Critical patent/JPH08332075A/en
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    • 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
    • C12M23/58Reaction vessels connected in series or in parallel
    • 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
    • C12M23/20Material Coatings
    • 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
    • C12M35/00Means for application of stress for stimulating the growth of microorganisms or the generation of fermentation or metabolic products; Means for electroporation or cell fusion
    • C12M35/08Chemical, biochemical or biological means, e.g. plasma jet, co-culture

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  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Organic Chemistry (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Biotechnology (AREA)
  • Genetics & Genomics (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • Biomedical Technology (AREA)
  • Sustainable Development (AREA)
  • General Health & Medical Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Clinical Laboratory Science (AREA)
  • Molecular Biology (AREA)
  • Physiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Cell Biology (AREA)
  • Immunology (AREA)
  • Fodder In General (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE: To easily provide at low cost both efficient culture method and culture system for microbes. CONSTITUTION: An activator, facultative anaerobic bacteria and indigenous bacteria are put into a 1st reaction vessel 1 which is then fed with a stock liquor, and the stock liquor is anaerobically reacted under a small amount of aeration to effect primary activation. A second batch of the activator is put into a 2nd reaction vessel 2 which is then fed with the primarily activated stock liquor to make an anaerobic reaction of the stock liquor under a small amount of aeration to effect secondary activation. A third batch of the activator is put into a 3rd reaction vessel 3 which is then fed with the secondarily activated stock liquor to make an anaerobic reaction of the stock liquor under a small amount of aeration to effect tertiary activation.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は微生物の培養方法及と培
養装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a microorganism culturing method and a culturing apparatus.

【0002】[0002]

【従来の技術と発明が解決しようとする課題】従来、微
生物の培養方法と装置は効率が低く、高価な欠点があっ
た。本発明は微生物の培養により従来よりも遙かに簡単
で、効率良く、然も安価に原料を処理できる微生物の培
養方法と装置を提供しようとするものである。
2. Description of the Related Art Conventionally, methods and apparatuses for culturing microorganisms have the drawbacks of low efficiency and high cost. The present invention intends to provide a method and a device for culturing a microorganism, which can treat a raw material much more easily, efficiently, and cheaper than ever by culturing a microorganism.

【0003】[0003]

【課題を解決するための手段】本発明は微生物の培養に
より、簡単で効率良く、安価に原料を処理できる微生物
の培養方法と装置を提供することを目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method and an apparatus for culturing a microorganism, by which the raw material can be treated simply, efficiently and inexpensively by culturing the microorganism.

【0004】本発明はまた、微生物の培養により、簡単
で効率良く、安価に、人畜の屎尿を処理できる微生物の
培養方法と装置を提供することを目的とする。
Another object of the present invention is to provide a method and an apparatus for culturing microorganisms, which can treat human waste in humans in a simple, efficient and inexpensive manner by culturing the microorganisms.

【0005】本発明はまた、微生物の培養により、池又
は河川を浄化する微生物の培養方法及び装置を提供する
ことを目的とする。
Another object of the present invention is to provide a method and an apparatus for culturing microorganisms, which purifies a pond or a river by culturing microorganisms.

【0006】本発明は、第1反応槽中に活性剤と、通性
嫌気性菌と、土着菌とを収容して原料液の供給を受け、
小量の通気下で原料液を嫌気性反応させて一次活性化
し、第2反応槽中には活性剤を収容し、一次活性化した
原料液を供給し、小量の通気下で一次活性化した原料液
を嫌気性反応させて二次活性化し、第3反応槽中に活性
剤を収容し、二次活性化した原料液を供給し、小量の通
気下で二次活性化した原料液を嫌気性反応させて三次活
性化することを特徴とする微生物の培養方法である。
In the present invention, an activator, a facultative anaerobic bacterium, and an indigenous bacterium are contained in a first reaction tank to receive a supply of a raw material liquid,
The raw material liquid is anaerobically reacted under a small amount of aeration for primary activation, the activator is contained in the second reaction tank, and the primary activated raw material liquid is supplied to perform primary activation under a small amount of aeration. The activated raw material liquid is secondarily activated by anaerobic reaction, the activator is accommodated in the third reaction tank, the secondary activated raw material liquid is supplied, and the raw material liquid is secondarily activated under a small amount of aeration. Is a method for culturing a microorganism, characterized in that the bacterium is subjected to an anaerobic reaction to carry out tertiary activation.

【0007】本発明はまた、通性嫌気性菌と、活性剤
と、土着菌とを収容して原料液の供給を受け、小量の通
気下で原料液を嫌気性反応させて一次活性化する第1反
応槽と、活性剤を収容して一次活性化した原料液の供給
を受け、小量の通気下で原料液を嫌気性反応させて二次
活性化する第2反応槽と、活性剤を収容して二次活性化
した原料液の供給を受け、小量の通気下で原料液を嫌気
性反応させて三次活性化する第3反応槽と、第1、第2
及び第3反応槽に通気する通気装置と、を有することを
特徴とする微生物の培養装置を提供する。
The present invention also accommodates a facultative anaerobic bacterium, an activator, and an indigenous bacterium to receive a supply of a raw material liquid, and anaerobically reacts the raw material liquid under a small amount of aeration to perform primary activation. And a second reaction tank that receives the supply of the raw material liquid that contains the activator and is primarily activated, and secondarily activates the raw material liquid by anaerobic reaction under a small amount of aeration. A third reaction tank that receives the supply of the raw material liquid that contains the agent and is secondarily activated, and anaerobically reacts the raw material liquid under a small amount of aeration to perform the third activation;
And a ventilating device for ventilating the third reaction tank.

【0008】土着菌はその土地に土着する菌で、例えば
土壌、池の泥、ヘドロ、下水汚泥及び/又は腐植土等が
あり、場合によってはその土地の空気中に存在する乳酸
菌も用いられる。土着菌はその土地の既製の堆肥と土着
菌を混ぜて醗酵させるものの形で、原料液1t当り5〜
20Kg、通常5〜10Kg使用する。
The indigenous bacteria are bacteria that are indigenous to the land, and include, for example, soil, pond mud, sludge, sewage sludge, and / or humus soil. In some cases, lactic acid bacteria existing in the air of the land are also used. The indigenous bacteria are in the form of fermented by mixing ready-made compost and indigenous bacteria of the land, and the amount is 5 to 1 ton of the raw material liquid.
20 kg, usually 5-10 kg is used.

【0009】原料液は蛋白質、セルロース、澱粉、糖
蜜、炭水化物、動植物油脂及び動物屎尿の少なくとも一
種以上と、ミネラル液及び水とから成るが、既に充分な
量の水を含有している場合は、新たな水の添加は省略す
る。
The raw material liquid comprises at least one or more of protein, cellulose, starch, molasses, carbohydrate, animal and vegetable fats and animal excrement, mineral liquid and water, but when it already contains a sufficient amount of water, The addition of new water is omitted.

【0010】ミネラル液は商品名「ミネックスG」、
「ミクロールA」、「ミクロールB」、「ミクロール
C」、「ミクロールD」及び「微生物用ミクロール」と
して市販されているものが好適である。原料液1t当り
立上り時に10lを使用し、次回補充の場合から原料液
1t当り1l使用する。
The mineral liquid is trade name "MINEX G",
Those commercially available as “Microl A”, “Microl B”, “Microl C”, “Microl D” and “Microl for microorganisms” are suitable. 10 l is used per 1 t of the raw material liquid at the start-up, and 1 l is used per 1 t of the raw material liquid from the next replenishment.

【0011】通性嫌気性菌は、例えば、放線菌に属する
ものとして、例えばStrepto-mycessp. (ATCC 3004), St
reptoverticillium sp. (ATCC 23654), Nocardia sp.
(ATCC 19247), Micromonospora sp. (ATCC 12452), Rho
dococcus sp.:光合成細菌に属するものとして、例えば
Rhodopseudomonas sp. (R. sphaeroides), Rhodospiri
llum sp. (R. fulum), Chromatium sp. (C. okenii), C
hlorobium sp. (C. Limicola) : 乳酸菌(乳酸生成菌)
に属するものとして、例えば Lactobacillus sp. (IFO
3070) ,Propionibactrium sp. (P. freudonreichii),
Pediococcus sp. (P. halophilus), Streptococcus sp.
(S. lactis, S. faecalis) ; 糸状菌に属するものとし
て、例えば Aspergillus sp. (RIFY 5770, RIFY 5024),
Mucor sp. (IFO 8567) ; 酵母に属するものとして、例
えば Saccharomyces sp. (NRRL 1346, Y 977), Candida
sp. (C. utilis)がある。
Facultative anaerobic bacteria are, for example, Strepto-mycessp. (ATCC 3004), St.
reptoverticillium sp. (ATCC 23654), Nocardia sp.
(ATCC 19247), Micromonospora sp. (ATCC 12452), Rho
dococcus sp .: As belonging to photosynthetic bacteria, for example
Rhodopseudomonas sp. (R. sphaeroides), Rhodospiri
llum sp. (R. fulum), Chromatium sp. (C. okenii), C
hlorobium sp. (C. Limicola): Lactic acid bacteria (lactic acid-producing bacteria)
Belong to, for example, Lactobacillus sp. (IFO
3070), Propionibactrium sp. (P. freudonreichii),
Pediococcus sp. (P. halophilus), Streptococcus sp.
(S. lactis, S. faecalis); As a filamentous fungus, for example, Aspergillus sp. (RIFY 5770, RIFY 5024),
Mucor sp. (IFO 8567); As belonging to yeast, for example, Saccharomyces sp. (NRRL 1346, Y 977), Candida
There is sp. (C. utilis).

【0012】通性嫌気性菌は「カルスNC−R」の商品
名で市販されているものが好適である。その他、蛋白消
化バクテリア、澱粉消化バクテリア、セルロース消化バ
クテリア、活性剤消化バクテリア及び/又は動植物油脂
消化バクテリアが好適である。そのようなものとしてこ
れ等の5種混合バクテリアがあり、(株)ニッテクから
「グリースカッティング」の商品名で市販されている5
種混合バクテリアがある。表1はカルスNC−Rの特性
を示す。
As the facultative anaerobic bacterium, one commercially available under the trade name of "Callus NC-R" is preferable. In addition, protein-digesting bacteria, starch-digesting bacteria, cellulose-digesting bacteria, activator-digesting bacteria and / or animal and vegetable oil and fat-digesting bacteria are preferable. As such, there are five kinds of mixed bacteria, which are commercially available from Nittek Co., Ltd. under the trade name of "grease cutting".
There are mixed-species bacteria. Table 1 shows the characteristics of Callus NC-R.

【0013】[0013]

【表1】 「グリースカッティング」又は「カルスNC−R」は原
料液1t当り1〜5Kg使用する。
[Table 1] "Grease cutting" or "Callus NC-R" is used in an amount of 1 to 5 kg per ton of raw material liquid.

【0014】活性剤はカーボン、珪藻土、フェライト及
びゼオライトから成る成形物又は珪藻土から成る成形物
を、150〜250℃で10〜20時間一次焼成し、次
いで600〜900℃で4〜24時間二次焼成したもの
である。成形物は板、球、その他任意の形状とすること
ができるが、通常は球である。球の場合は単層の球から
構成するか又は核、一層以上の中間相及び多孔質外層か
ら構成する。
As the activator, a molded product composed of carbon, diatomaceous earth, ferrite and zeolite or a molded product composed of diatomaceous earth is primarily calcined at 150 to 250 ° C. for 10 to 20 hours, and then secondarily at 600 to 900 ° C. for 4 to 24 hours. It was baked. The molded product can be a plate, a sphere, or any other shape, but is usually a sphere. In the case of spheres, it is composed of a single layer of spheres or of a core, one or more mesophases and a porous outer layer.

【0015】核は珪藻土から成り、中間層は導電性カー
ボン、フェライト及びゼオライトから成り、多孔質外層
は珪藻土及びゼオライトから成る。
The core is made of diatomaceous earth, the intermediate layer is made of conductive carbon, ferrite and zeolite, and the porous outer layer is made of diatomaceous earth and zeolite.

【0016】中間層に混合されているフェライトは、天
然の堆積作用によるマグネタイト(Fe3 4 )とマグ
ヘマイト(γ−Fe2 3)である。これは溶出しない利
点がある。
The ferrite mixed in the intermediate layer is magnetite (Fe 3 O 4 ) and maghemite (γ-Fe 2 O 3 ) by natural deposition. This has the advantage of not eluting.

【0017】活性剤は超波長(104 Hz)〜X線(1
19Hz)、特に60〜200MHzの電磁波を吸収し
(それよりも短い波長の電磁波は個数を増やすことよっ
て吸収し)、位相の揃った干渉性の良いいわゆるコヒー
レントな電磁波を放射し、4〜10μm の波長の遠赤外
線を放射し、ミネラル分を溶出し、不純物を吸着する作
用を有し、水分子のクラスターを小さくする。
The activator is a super wavelength (10 4 Hz) to X-ray (1
0 19 Hz), especially electromagnetic waves of 60 to 200 MHz are absorbed (electromagnetic waves of wavelengths shorter than that are absorbed by increasing the number), and so-called coherent electromagnetic waves of uniform phase and good coherence are emitted. It emits far-infrared rays with a wavelength of 10 μm, has the function of eluting minerals and adsorbing impurities, and reduces the clusters of water molecules.

【0018】活性剤を多数1カ所に集めると、発信、共
鳴、増幅が起きる。活性剤は直径約10、20、30、
40、50及び60mmの球体として、「みね丸くん」の
商品名の下に本出願人から市販されているものが好適で
ある。活性剤は各反応槽中に原料液1t当り約5〜20
Kg、通常7〜15Kg使用する。
When a large number of active agents are collected in one place, transmission, resonance and amplification occur. The active agent has a diameter of about 10, 20, 30,
As the spheres of 40, 50 and 60 mm, those commercially available from the applicant under the trade name of "Minemaru-kun" are suitable. The activator is about 5 to 20 per 1 t of the raw material liquid in each reaction tank.
Kg, usually 7 to 15 kg is used.

【0019】[0019]

【作用】原料槽で原料液の成分を混合攪拌すると、原料
液中の有機物群をミネラルによる酵素反応によって腐敗
を防止し、且つ原料液の微生物叢を腐敗菌が出ないよう
に制御する。ミネラルによる酵素反応がうまく進行しな
いと、腐敗臭が漂う。
When the components of the raw material liquid are mixed and stirred in the raw material tank, the organic matter group in the raw material liquid is prevented from spoiling by an enzymatic reaction with minerals, and the microbial flora of the raw material liquid is controlled so that spoilage bacteria are not generated. If the enzymatic reaction with minerals does not proceed well, it will have a rotten odor.

【0020】第1反応槽には、その地域の土着菌を装入
し、通性嫌気性菌を添加し、活性剤を懸吊し、20〜3
0日間エアレーションを行なう。原料槽で原料液中の有
機物と微生物群がその地域の土着菌に触れ、有機物を餌
飼として増殖し、ミネラルで活性化する。その地域の土
着菌を使うのは、その地域の微生物を活性化し、増殖す
る為である。
The first reaction tank is loaded with indigenous bacteria of the area, facultative anaerobic bacteria are added, and the activator is suspended, and 20 to 3 is added.
Aerate for 0 days. In the raw material tank, organic substances and microbial groups in the raw material liquid come into contact with indigenous bacteria in the area, and the organic substances grow as food and are activated by minerals. The indigenous bacteria in the area are used to activate and multiply the microorganisms in the area.

【0021】ミネラルで活性化した原料槽からの原料液
は、通性嫌気性菌という新しい菌の混入によって、一だ
んと強化した微生物群が残る。活性剤がミネラル効果を
一そう持続し、水と微生物菌叢の安定化を図る上で空間
エネルギーを電磁波として吸収し放散する為、高エネル
ギー混合溶液ができ上る。
In the raw material liquid from the raw material tank activated with minerals, a group of microorganisms that have been gradually strengthened by the mixing of new bacteria called facultative anaerobic bacteria remains. Since the active agent further maintains the mineral effect and absorbs and dissipates space energy as electromagnetic waves in order to stabilize water and microbial flora, a high energy mixed solution is completed.

【0022】第1反応槽中のミネラル、有機物、通性嫌
気性菌及び土着菌が20〜30日間の反応で十分馴染
み、それが20〜30日間の第2反応槽の反応でさらに
馴染む。
Minerals, organic substances, facultative anaerobic bacteria and indigenous bacteria in the first reaction tank are well adapted in the reaction for 20 to 30 days, and are further adapted in the reaction in the second reaction tank for 20 to 30 days.

【0023】第2反応槽で、ミネラル、土着菌及び活性
剤と生成する有機酸によって、一般細菌は激減し、糸状
菌群が増える。
In the second reaction tank, minerals, indigenous bacteria, and organic acids produced together with the activator drastically reduce general bacteria and increase filamentous fungus groups.

【0024】第3反応槽でさらに15〜30日間馴染ま
せると、放射菌群と酵母群(これらは何れもその地域の
土着菌群)が増殖し、糸状菌は殆どいなくなる。第1〜
第3反応槽と槽が変るにつれて菌相が変る。
When acclimated to the third reaction tank for another 15 to 30 days, a group of radiant bacteria and a group of yeasts (both of which are indigenous bacterial groups in the area) proliferate, and filamentous fungi almost disappear. First to first
The bacterial flora changes as the third reaction tank and the tank change.

【0025】第3反応槽でこれら菌群と水に活性剤から
の電磁波としての波動エネルギーを十分に受け取り、著
しく活性化した溶液(菌群を含む)が出来上がる。この
溶液はミネラル、放線菌群、酵母、水から成り、しかも
空間エネルギーを十分吸収している。
In the third reaction tank, the bacterium group and water sufficiently receive the wave energy from the activator as an electromagnetic wave, and a remarkably activated solution (including the bacterium group) is completed. This solution consists of minerals, actinomycetes, yeast, and water, and also absorbs enough space energy.

【0026】第3反応槽の生成液は貯溜槽に入り、これ
が動植物の活性化液の原液となる。この液は高濃度なの
で、このままでは動物は下痢したり、農作物は生育が止
まるという障害が現れるので、使用に当っては通常は適
宜水を用いて希釈する。
The product liquid of the third reaction tank enters the storage tank, and this becomes the stock solution of the animal and plant activating liquid. Since this liquid has a high concentration, diarrhea in animals and disorders such as growth stop of crops appear if they are left as they are. Therefore, they are usually diluted appropriately with water before use.

【0027】希釈槽では、貯溜槽の高濃度溶液を約50
0〜1500倍に希釈する。これは希釈するだけではな
く、高濃度液を水の中に一様に分散させることによって
溶液を安定化させる。
In the diluting tank, the high-concentration solution in the storage tank is about 50
Dilute 0-1500 times. This not only dilutes, but stabilizes the solution by uniformly dispersing the concentrated solution in water.

【0028】安定化液にさらにエネルギーを与えるため
に、希釈槽でも活性剤を液1t当り10〜15Kg使うこ
とが好ましい。安定化された生成液は、動物の飲み水と
全農作物の育成に使うことができる。
In order to give more energy to the stabilizing solution, it is preferable to use 10 to 15 kg of activator per 1 ton of the solution even in the diluting tank. The stabilized product can be used for drinking water for animals and for growing whole crops.

【0029】活性剤は網製容器に収容し、これを各槽に
懸持すると、活性剤の設置、交換等の処理取扱いに便利
である上に、目詰りが無く流通及びエアレーションが容
易であり、活性化が促進される。
If the activator is housed in a net container and suspended in each tank, it is convenient for treatment such as installation and replacement of the activator, and there is no clogging so that distribution and aeration are easy. , Activation is promoted.

【0030】網製容器は金属網製が好ましい。ステンレ
スは耐食性の面から好ましい。活性剤の活性化作用は収
容する活性剤の量のみならず、網製容器の底面から上面
迄の高さに依っても定まり、この高さが電磁波吸収能力
を定める。網製容器にアンテナを取り付けると、アンテ
ナの先端が網製容器の上面と同じ作用をするので、網製
容器の高さが延長されたと同じことになり、電磁波吸収
能力が高まるので活性剤の作用が促進される。アンテナ
は少なくとも図1及び図2に示す程度の高さが好まし
い。第1〜3反応槽の反応液が連通しているときは、3
本のアンテナを1本に纏めて高くすることが好ましい。
1mのアンテナで、1Voltの電位差が発生する。電位差
は天候によって異なり、雨の日が高い。
The mesh container is preferably made of metal mesh. Stainless steel is preferable from the viewpoint of corrosion resistance. The activation action of the activator is determined not only by the amount of the activator contained but also by the height from the bottom surface to the top surface of the net container, and this height determines the electromagnetic wave absorption capacity. When the antenna is attached to the net container, the tip of the antenna works the same as the upper surface of the net container, so the height of the net container is the same as the height of the net container. Is promoted. The antenna preferably has a height at least as shown in FIGS. 1 and 2. 3 when the reaction liquids of the first to third reaction tanks are in communication
It is preferable to increase the height of the antennas of the book collectively.
A 1 m antenna produces a potential difference of 1 Volt. The potential difference varies depending on the weather, and it is rainy frequently.

【0031】第1反応槽の前に原料槽を設け、ここで原
料液の各成分を受け混合すると、第1反応槽に腐敗防止
した均質な原料液を供給できる。
If a raw material tank is provided in front of the first reaction tank and each component of the raw material liquid is received and mixed therein, it is possible to supply a homogeneous raw material liquid which is rot-proof to the first reaction tank.

【0032】三次活性化した原料液は活性な生成液とな
る。第3反応槽の後に生成液を貯蔵する貯溜槽を設ける
と、生成液の貯溜と取扱いと処理及び販売に好都合であ
る。
The raw material liquid which has been tertiary activated becomes an active product liquid. Providing a storage tank for storing the product liquid after the third reaction tank is convenient for storing, handling, treating and selling the product liquid.

【0033】生成液は使用に当っては、約500〜20
00倍、通常約1000倍に希釈して、野菜、畜産、稲
作その他に使用する。希釈の目的の為に希釈槽を設け、
活性剤を保持した網製容器を槽内に懸持して、生成液を
希釈した後、数日間保持した後に順次使用すると、活性
の高い希釈液を使用できる。
The product liquid is about 500 to 20 in use.
It is diluted to 00 times, usually about 1000 times, and used for vegetables, livestock, rice cultivation and so on. A diluting tank is provided for the purpose of diluting,
A highly active diluting liquid can be used by suspending a net-shaped container holding an activator in a tank, diluting the produced liquid, and then holding it for several days and then sequentially using it.

【0034】原料液は予備槽と第1〜第3反応槽でpH
が変って来る。通常pHの目安は予備槽約8.4、第1
反応槽8.4、第2反応槽8.8、第3反応槽9.1で
ある。pHが9以上になると、大腸菌とかサルモネラ菌
が死滅する。
The pH of the raw material liquid is adjusted in the preliminary tank and the first to third reaction tanks.
Is changing. Normal pH is about 8.4 in preliminary tank, first
A reaction tank 8.4, a second reaction tank 8.8, and a third reaction tank 9.1. When the pH becomes 9 or more, Escherichia coli and Salmonella die.

【0035】通気は第1、第2及び第3の各反応槽の容
積1m3当り約3〜5l /分が好ましい。約3l /分未満
では通気の効果が乏しく、約5l /分より大では通性嫌
気性菌の嫌気性反応が損なわれる。
Aeration is preferably about 3 to 5 l / min per 1 m 3 of volume of each of the first, second and third reaction tanks. Below about 3 l / min, the effect of aeration is poor, and above about 5 l / min, the anaerobic reaction of facultative anaerobic bacteria is impaired.

【0036】土着菌にミネラルを作用させると、当初、
一般細菌と糸状菌群が主であったものが2〜3日で一般
細菌や糸状菌群が激減し、放線菌や酵母が著しく増加す
ることが判ってきた。また、加工後の魚貝類の悪臭や堆
肥作りに際しての悪臭もミネラルを散布すると時間と共
に悪臭は激減し、堆肥などの醗酵経路が変化する。
When minerals are allowed to act on the indigenous bacteria, initially,
It has been found that the general bacteria and the filamentous fungus group are mainly contained, but the general bacteria and the filamentous fungus group are drastically reduced in 2 to 3 days, and the actinomycetes and yeast are remarkably increased. Further, if the malodor of processed fish and shellfish and the malodor of compost making are sprinkled with minerals, the malodor will decrease drastically with time, and the fermentation route of compost will change.

【0037】希釈した生成液を堆肥化のために堆肥原料
に散布すると、従来では考えられない良質の堆肥が出来
た。
When the diluted production liquid was sprayed on the compost raw material for composting, a high quality compost which could not be considered in the past was produced.

【0038】生成液は人間や家畜の浄化槽に槽液1t当
り濃厚なまま1l散布すると臭いが無くなり、畜舎に5
00〜1500倍に薄めたものを散布すると臭いが無く
なった。
When the produced liquid is sprayed in a septic tank for humans or livestock in an amount of 1 liter per 1 ton of the tank liquid, the odor disappears and 5
The odor disappeared when the powder diluted to 100 to 1500 times was sprayed.

【0039】生成液を原料槽に戻すと、土着菌の活性化
と通性嫌気性菌の馴染みを早めることができる。戻す量
は原料液1t当り通常20〜40Kgである。
By returning the produced liquid to the raw material tank, the activation of indigenous bacteria and the familiarization of facultative anaerobic bacteria can be accelerated. The amount to be returned is usually 20 to 40 kg per ton of the raw material liquid.

【0040】[0040]

【実施例】次に本発明を実施例につきさらに詳細に説明
する。
EXAMPLES The present invention will now be described in more detail with reference to examples.

【0041】実施例1 図1に示す装置において、容量500lの予備槽Pは牛
尿と、「ミクロール」の商品名で市販されているミネラ
ル液と、庭からの汚水とを15%:1%:84%の重量
割合で含有する原料液を、pH約8.4で、容量100
0lの第1反応槽1に約40l/日の割合で定常的に供
給する。原料槽Rをポンプにより随時通気攪拌した。
Example 1 In the apparatus shown in FIG. 1, a preparatory tank P having a capacity of 500 l contains cow urine, a mineral liquid marketed under the trade name of "Microl", and sewage from the garden 15%: 1% : A raw material liquid containing 84% by weight at a pH of about 8.4 and a volume of 100
It is constantly supplied to 0 l of the first reaction tank 1 at a rate of about 40 l / day. The raw material tank R was aerated and agitated by a pump at any time.

【0042】第1反応槽は、活性剤4を10Kg装入した
ステンレス製容器5を収容し、通性嫌気性菌を「カルス
NC−R」の形で5Kgと、土着菌を本出願人から商品名
「グリーントップ」で市販している堆肥に竹やぶから採
取した白い土着菌と栄養源(米糠)を混合して7日醗酵
させたものの形で20Kgとを装入し、容器5の下方から
毎分3lの割合で通気し、原料液をpH約8.4で約2
0〜30日処理して一次活性化し、容量1000lの第
2反応槽2に溢硫により供給した。
The first reaction tank contains a stainless steel container 5 containing 10 kg of the activator 4, 5 kg of facultative anaerobic bacteria in the form of "Callus NC-R", and indigenous bacteria from the applicant. Compost sold under the trade name "Green Top" is mixed with white indigenous bacteria collected from bamboo yam and nutrient source (rice bran) and fermented for 7 days. Aeration is performed at a rate of 3 liters per minute, and the raw material liquid is adjusted to about 8.4 at pH 8.4
It was treated for 0 to 30 days to be primary activated, and then supplied to the second reaction tank 2 having a capacity of 1000 l by vulcanization.

【0043】第2反応槽2は一次化活性化した原料液を
受け、活性剤4を10Kg装入した金属網製容器5を懸持
し、容器5の下方から毎分3lの割合で通気し、pH
8.8で20日〜30日の処理日数の後、二次活性化し
た原料液を溢流により容量1000lの第3反応槽3に
供給した。
The second reaction vessel 2 receives the raw material liquid which has been activated by the primary activation, suspends a metal mesh container 5 charged with 10 kg of the activator 4, and ventilates from below the container 5 at a rate of 3 l / min. , PH
After 20 to 30 days of treatment at 8.8, the secondary activated raw material liquid was supplied to the third reaction tank 3 having a volume of 1000 l by overflow.

【0044】第3反応槽は二次活性化した原料液を受
け、活性剤4を10Kg装入したステンレス網製容器5を
収容し、容器5の下方から毎分3l/分の割合で通気
し、pH約9.1で約15〜30日の処理日数の後、三
次活性化した原料液(生成液)を溢流により貯溜槽Qに
放出した。活性剤は第1〜3反応槽共、種々の粒径の
「みね丸くん」を混合したものを用いた。
The third reaction tank receives the secondarily activated raw material liquid, accommodates a stainless mesh container 5 charged with 10 kg of the activator 4, and aerates from below the container 5 at a rate of 3 l / min per minute. After about 15 to 30 days of treatment at pH of about 9.1, the tertiary activated raw material liquid (production liquid) was discharged to the storage tank Q by overflow. As the activator, a mixture of "Minemaru-kun" having various particle sizes was used in the first to third reaction tanks.

【0045】貯溜槽Qは生成液を受け、貯蔵するする為
のもので、容量は500lである。網製容器5は高さ
1.5mのアンテナ6を有する。
The storage tank Q is for receiving and storing the produced liquid and has a capacity of 500 liters. The net container 5 has an antenna 6 having a height of 1.5 m.

【0046】かくて製造した生成液はこのままでは濃過
ぎるので、通常は水を用いて約1000倍に希釈して、
野菜、稲作に散布して、収率の向上、品質の向上、連作
障害防止等の優れた効果を得、畜産の飲水に用いて畜舎
の悪臭防止、病気発生率の低下、死亡率の低下、乳量の
増加等の良好な成績を得た。
Since the product solution thus produced is too thick as it is, it is usually diluted with water about 1000 times,
It is applied to vegetables and rice crops to obtain excellent effects such as yield improvement, quality improvement, and continuous crop failure prevention, and it is used for drinking water for livestock production to prevent stench from stalls, reduce disease incidence, and reduce mortality. Good results such as increased milk yield were obtained.

【0047】実施例2 図2に示す装置は図1に示す装置と略々同じであるが、
原料液に商品名「ミクロール」で市販されているミネラ
ル液1重量%、合併浄化槽の上澄液99重量%から成る
液を用い、第1反応槽に(株)ニッテクから「グリース
カッティング」の商品名で市販の通性嫌気性菌を原料液
1t当り5Kgを入れた容器7と土着菌を入れた容器8を
懸吊し、活性剤4を10Kg入れた容器5を受水槽6にも
懸吊し、処理した結果、浄化能力が対照装置に比べ50
%向上した。
Example 2 The apparatus shown in FIG. 2 is almost the same as the apparatus shown in FIG.
A product consisting of 1% by weight of mineral liquid marketed under the trade name "MICROL" and 99% by weight of the supernatant of the combined septic tank is used as the raw material liquid, and the product of "Grease cutting" from Nitek Co., Ltd. in the first reaction tank. Under the name, a container 7 containing 5 kg of commercially available facultative anaerobic bacteria and a container 8 containing indigenous bacteria were suspended, and a container 5 containing 10 kg of the activator 4 was also suspended in the water tank 6. As a result of the treatment, the purification capacity is 50 compared with the control device.
% Improved.

【0048】実施例3 原料液の牛尿の代りに糖蜜を用い、実施例1と同様に操
作して実施例1と略々同様な結果を得た。原料液に糖蜜
を使うときは、黒砂糖から作ることが好ましかった。白
砂糖ではミネラル分が無いので、ミネラル分を添加する
必要があつた。
Example 3 Molasses was used instead of cow urine as a raw material liquid, and the same operation as in Example 1 was carried out to obtain almost the same results as in Example 1. When molasses was used as the raw material liquid, it was preferable to make it from brown sugar. Since white sugar has no mineral content, it was necessary to add mineral content.

【0049】実施例4 新潟の養豚場は豚の尿4m3/日に対し処理能力が足りな
かったが、実施例2と同様に操作することにより従来の
2.5m3/日の浄化槽で足りるようになり、然もpH調
整剤が不要となった。
Example 4 The pig farm in Niigata did not have sufficient treatment capacity for 4 m 3 / day of urine from pigs, but by operating in the same manner as in Example 2, a conventional septic tank of 2.5 m 3 / day is sufficient. As a result, the pH adjusting agent is no longer needed.

【0050】[0050]

【発明の効果】効果を次に示す。 (i) 連作障害の克服。 (ii)作物の品質向上及び収量の増加。 (iii) 肥料、農薬代の低減によるコストダウン。 (iv)畜舎の悪臭とハエの除去。 (V) 病気発生率と死亡率の低下。 (Vi)抗生物質等の薬剤使用量の大幅減少。 (Vii) 肉、卵、乳の安全性の確保。 (Viii)飼料効率の向上。 (iX)乳量と乳質の安定向上。 (X) 乳房炎の大幅低減。 (Xi)屎尿から生産される堆肥と生成液の活用で良質の飼
料作物とサイレージ生産の実現。 (Xii) 素牛のストレス解消が早い。堆肥の畜舎への還元
で敷料が大幅低減。 (Xiii)肉質の向上、一日当りの増体量の向上。 (XiV) 破卵率の低減。卵質の向上。ワクチンの抗体化が
安定。喧噪性緩和。 (XV)ブロイラーの増体の向上。肉質の向上。尻つつきの
減少。 (XVi) 飲料水に適用すると、美味しい水が簡単にでき
る。 (XVii)浄化槽能力の40〜50%能力向上。
The effects are shown below. (i) Overcoming continuous cropping obstacles. (ii) Improvement of crop quality and increase of yield. (iii) Cost reduction by reducing fertilizer and pesticide costs. (iv) Removal of stench and flies in the barn. (V) Reduced morbidity and mortality. (Vi) Significant reduction in drug usage such as antibiotics. (Vii) Ensuring the safety of meat, eggs and milk. (Viii) Improvement of feed efficiency. (iX) Improving milk quantity and milk quality stability. (X) Significantly reduced mastitis. (Xi) Realization of high quality feed crops and silage production by utilizing compost and produced liquid produced from human waste. (Xii) The stress of the cow is released quickly. The litter is greatly reduced by returning the compost to the livestock shed. (Xiii) Improvement of meat quality and increase of body weight gain per day. (XiV) Reduced egg breaking rate. Improvement of egg quality. Stable antibodyization of vaccine. Alleviation of noise. (XV) Improvement of gain of broiler. Improvement of meat quality. Decrease in butt pecking. (XVi) Applying to drinking water makes delicious water easy. (XVii) 40-50% improvement in septic tank capacity.

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

【図1】本発明装置の一例を示す説明図である。FIG. 1 is an explanatory diagram showing an example of a device of the present invention.

【図2】本発明装置の他の例を示す説明図である。FIG. 2 is an explanatory diagram showing another example of the device of the present invention.

【符号の説明】[Explanation of symbols]

P 原料槽 1 第1反応槽 2 第2反応槽 3 第3反応槽 4 活性剤 5 金属製網製容器 6 アンテナ 7 通性嫌気性菌を入れた容器 8 土着菌を入れた容器 Q 貯溜槽 R 希釈槽 P Raw material tank 1 1st reaction tank 2 2nd reaction tank 3 3rd reaction tank 4 Activator 5 Metal net container 6 Antenna 7 Container containing facultative anaerobic bacteria 8 Container containing indigenous bacteria Q Storage tank R Dilution tank

Claims (21)

【特許請求の範囲】[Claims] 【請求項1】 第1反応槽中に活性剤と、通性嫌気性菌
と、土着菌とを収容して原料液の供給を受け、小量の通
気下で原料液を嫌気性反応させて一次活性化し、 第2反応槽中には活性剤を収容し、一次活性化した原料
液を供給し、小量の通気下で一次活性化した原料液を嫌
気性反応させて二次活性化し、 第3反応槽中に活性剤を収容し、二次活性化した原料液
を供給し、小量の通気下で二次活性化した原料液を嫌気
性反応させて三次活性化することを特徴とする微生物の
培養方法。
1. An activator, a facultative anaerobic bacterium, and an indigenous bacterium are contained in a first reaction tank to receive a supply of a raw material liquid, and the raw material liquid is anaerobically reacted under a small amount of aeration. Primary activation, the activator is housed in the second reaction tank, the primary activated raw material liquid is supplied, and the primary activated raw material liquid is secondarily activated by anaerobic reaction under a small amount of aeration. It is characterized in that the activator is contained in the third reaction tank, the secondary activated raw material liquid is supplied, and the secondary activated raw material liquid is anaerobically reacted under a small amount of aeration for tertiary activation. Method for culturing microorganisms to be used.
【請求項2】 請求項1記載の方法において、原料液が
蛋白質、セルロース、糖蜜、澱粉、炭水化物、動植物油
脂及び動物屎尿の少なくとも1種以上と、ミネラル液と
を含有する方法。
2. The method according to claim 1, wherein the raw material liquid contains at least one kind of protein, cellulose, molasses, starch, carbohydrate, animal and vegetable fats and animal excrement, and a mineral liquid.
【請求項3】 請求項1記載の方法において、通性嫌気
性菌がカルスNC−Rである方法。
3. The method according to claim 1, wherein the facultative anaerobic bacterium is callus NC-R.
【請求項4】 請求項1記載の方法において、活性剤が
珪藻土から成る成形物又はカーボン、珪藻土、フェライ
ト及びゼオライトから成る成形物を150〜250℃で
10〜20時間一次焼成し、次いで600〜900℃で
4〜24時間二次焼成したものである方法。
4. The method according to claim 1, wherein a molded article in which the activator is made of diatomaceous earth or a molded article made of carbon, diatomaceous earth, ferrite and zeolite is primarily calcined at 150 to 250 ° C. for 10 to 20 hours, and then 600 to A method in which secondary firing is performed at 900 ° C. for 4 to 24 hours.
【請求項5】 請求項4記載の方法において、活性剤が
単層の球又は核、1層以上の中間層及び多孔質外層から
成る球である方法。
5. The method of claim 4, wherein the active agent is a sphere consisting of a single layer of spheres or nuclei, one or more intermediate layers and a porous outer layer.
【請求項6】 請求項5記載の方法において、活性剤の
核が珪藻土から成り、中間層が導電性カーボン、フェラ
イト及びゼオライトから成り、多孔質外層が珪藻土及び
ゼオライトから成る方法。
6. The method according to claim 5, wherein the activator core comprises diatomaceous earth, the intermediate layer comprises conductive carbon, ferrite and zeolite, and the porous outer layer comprises diatomaceous earth and zeolite.
【請求項7】 請求項1記載の方法において、第1反応
槽の前段に原料槽を設け、ここで原料液の成分を混合し
て原料液とする方法。
7. The method according to claim 1, wherein a raw material tank is provided before the first reaction tank, and the components of the raw material liquid are mixed therein to form a raw material liquid.
【請求項8】 請求項1記載の方法において、ミネラル
液が市販のミネラル液である方法。
8. The method according to claim 1, wherein the mineral liquid is a commercially available mineral liquid.
【請求項9】 請求項1記載の方法において、第3反応
槽の後で生成液を貯蔵する方法。
9. The method according to claim 1, wherein the product liquid is stored after the third reaction tank.
【請求項10】 請求項9記載の方法において、貯溜槽
の後で活性化液を希釈すると共に活性剤によりさらに活
性化する方法。
10. The method according to claim 9, wherein the activation liquid is diluted after the storage tank and is further activated by an activator.
【請求項11】 通性嫌気性菌と、活性剤と、土着菌と
を収容して原料液の供給を受け、小量の通気下で原料液
を嫌気性反応させて一次活性化する第1反応槽と、 活性剤を収容して一次活性化した原料液の供給を受け、
小量の通気下で原料液を嫌気性反応させて二次活性化す
る第2反応槽と、 活性剤を収容して二次活性化した原料液の供給を受け、
小量の通気下で原料液を嫌気性反応させて三次活性化す
る第3反応槽と、 第1、第2及び第3反応槽に通気する通気装置と、を有
することを特徴とする微生物の培養装置。
11. A first activation for accommodating a facultative anaerobic bacterium, an activator, and an indigenous bacterium, receiving a supply of a raw material liquid, and causing an anaerobic reaction of the raw material liquid under a small amount of aeration to perform primary activation. Receiving the supply of the reaction tank and the raw material liquid that contains the activator and is primarily activated,
A second reaction tank that secondarily activates the raw material liquid by anaerobic reaction under a small amount of aeration, and is supplied with the raw material liquid that contains the activator and is secondarily activated.
Microorganisms characterized by comprising: a third reaction tank for anaerobically reacting a raw material liquid under a small amount of aeration for tertiary activation; and an aeration device for aeration of the first, second and third reaction tanks. Incubator.
【請求項12】 請求項11記載の装置において、通性
嫌気性菌がカルスNC−R(商品名)又はグリースカッ
ティング(商品名)として市販のものである装置。
12. The device according to claim 11, wherein facultative anaerobic bacteria are commercially available as Callus NC-R (trade name) or Grease Cutting (trade name).
【請求項13】 請求項11記載の装置において、活性
剤がカーボン、珪藻土、フェライト及びゼオライトから
成る成形物又は珪藻土から成る成形物を150〜250
℃で10〜20時間一次焼成し、次いで600〜900
℃で4〜24時間二次焼成したものである装置。
13. The apparatus according to claim 11, wherein the activator is a molded product made of carbon, diatomaceous earth, ferrite and zeolite or a molded product made of diatomaceous earth is 150 to 250.
Primary calcination for 10 to 20 hours at 600C, then 600 to 900
An apparatus which is secondarily baked at 4 ° C. for 4 to 24 hours.
【請求項14】 請求項13記載の装置において、カー
ボン、珪藻土、フェライト及びゼオライトから成る成形
物が核、1層以上の中間層及び多孔質外層から成る構造
を有し、核が珪藻土から成り、中間層が導電性カーボ
ン、フェライト及びゼオライトから成り、多孔質外層が
珪藻土及びゼオライトから成る球である装置。
14. The apparatus according to claim 13, wherein the molded product made of carbon, diatomaceous earth, ferrite and zeolite has a structure having a core, one or more intermediate layers and a porous outer layer, and the core is made of diatomaceous earth, A device in which the middle layer is made of conductive carbon, ferrite and zeolite and the porous outer layer is a sphere made of diatomaceous earth and zeolite.
【請求項15】 請求項13記載の装置において、成形
物が球である装置。
15. The device according to claim 13, wherein the molding is a sphere.
【請求項16】 請求項11記載の装置において、活性
剤を網製容器に収容し、これを各槽中に懸持した装置。
16. The device according to claim 11, wherein the activator is contained in a net container and suspended in each tank.
【請求項17】 請求項16記載の装置において、網製
容器が金属製である装置。
17. The apparatus according to claim 16, wherein the net container is made of metal.
【請求項18】 請求項17記載の装置において、網製
容器にアンテナを取付けた装置。
18. The device according to claim 17, wherein the antenna is attached to a net container.
【請求項19】 請求項11記載の装置において、第3
反応槽の後に生成液を貯蔵する貯溜槽を有する装置。
19. The apparatus according to claim 11, wherein the third
An apparatus having a storage tank for storing the produced liquid after the reaction tank.
【請求項20】 請求項19記載の装置において、貯溜
槽の後に生成液を希釈すると共に活性剤によりさらに活
性化する希釈槽を有する装置。
20. The device according to claim 19, further comprising a diluting tank for diluting the product liquid after the storage tank and further activating the resulting liquid with an activator.
【請求項21】 請求項1の培養方法により得た生成
液。
21. A product solution obtained by the culture method of claim 1.
JP14471095A 1995-06-12 1995-06-12 Activation liquid production method, activation liquid, activation liquid usage method, and activation liquid production apparatus Expired - Lifetime JP3447846B2 (en)

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Application Number Priority Date Filing Date Title
JP14471095A JP3447846B2 (en) 1995-06-12 1995-06-12 Activation liquid production method, activation liquid, activation liquid usage method, and activation liquid production apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14471095A JP3447846B2 (en) 1995-06-12 1995-06-12 Activation liquid production method, activation liquid, activation liquid usage method, and activation liquid production apparatus

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Publication Number Publication Date
JPH08332075A true JPH08332075A (en) 1996-12-17
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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001129580A (en) * 1999-11-02 2001-05-15 Kl Plant Kk Apparatus for treating waste water containing oil and fat
JP2002535941A (en) * 1999-01-25 2002-10-22 ノキア ネットワークス オサケ ユキチュア Interworking between wireless access networks
JP2011120984A (en) * 2009-12-09 2011-06-23 Sea Ray:Kk Method for cleaning water area
JP5308570B1 (en) * 2012-10-12 2013-10-09 昭司 野口 Method for urination treatment of livestock animals

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002535941A (en) * 1999-01-25 2002-10-22 ノキア ネットワークス オサケ ユキチュア Interworking between wireless access networks
JP2001129580A (en) * 1999-11-02 2001-05-15 Kl Plant Kk Apparatus for treating waste water containing oil and fat
JP2011120984A (en) * 2009-12-09 2011-06-23 Sea Ray:Kk Method for cleaning water area
JP5308570B1 (en) * 2012-10-12 2013-10-09 昭司 野口 Method for urination treatment of livestock animals

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