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JP2594498B2 - High-concentration organic matter treatment method - Google Patents
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JP2594498B2 - High-concentration organic matter treatment method - Google Patents

High-concentration organic matter treatment method

Info

Publication number
JP2594498B2
JP2594498B2 JP5504493A JP5504493A JP2594498B2 JP 2594498 B2 JP2594498 B2 JP 2594498B2 JP 5504493 A JP5504493 A JP 5504493A JP 5504493 A JP5504493 A JP 5504493A JP 2594498 B2 JP2594498 B2 JP 2594498B2
Authority
JP
Japan
Prior art keywords
organic matter
fermentation
fermenter
concentration organic
organic
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.)
Expired - Lifetime
Application number
JP5504493A
Other languages
Japanese (ja)
Other versions
JPH06246284A (en
Inventor
弘 山本
裕介 角田
悟 亀山
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.)
TOYO. SS. CO., LTD.
Original Assignee
TOYO. SS. CO., LTD.
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 TOYO. SS. CO., LTD. filed Critical TOYO. SS. CO., LTD.
Priority to JP5504493A priority Critical patent/JP2594498B2/en
Publication of JPH06246284A publication Critical patent/JPH06246284A/en
Application granted granted Critical
Publication of JP2594498B2 publication Critical patent/JP2594498B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Treatment Of Sludge (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は高濃度有機排水中の有機
物を、担体に付着する微生物との発酵消化作用により処
理する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating organic matter in high-concentration organic wastewater by fermentation and digestion with microorganisms adhering to a carrier.

【0002】[0002]

【従来の技術】現在、高濃度有機排水及び有機固形物を
処理する方法としては、これら有機物を木質細片(おが
屑)や活性炭よりなる微生物担体と混合して発酵消化さ
せることが行われている。
2. Description of the Related Art At present, as a method for treating high-concentration organic wastewater and organic solids, these organic substances are mixed with a microbial carrier made of wood chips (sawdust) or activated carbon and fermented and digested. .

【0003】この方法によれば、担体と混合した有機物
は、担体に担持されている微生物によって発酵消化さ
れ、炭酸ガス、水、無機塩、アンモニアなどに分解され
てドレンとして排出される。
According to this method, an organic substance mixed with a carrier is fermented and digested by microorganisms carried on the carrier, decomposed into carbon dioxide, water, inorganic salts, ammonia and the like, and discharged as drain.

【0004】この際、木質細片も有機物であることから
その一部が発酵消化作用によって分解され、木質中のフ
ェノール性高分子であるリグニンがドレン中に排出され
る。フェノール類は排出規制物質であるとともに、リグ
ニンは植物の根腐れを引き起こす原因となるので、ドレ
ンを2次処理しなければ放流することはできない。ま
た、発酵処理中に発酵臭が発生するので、処理装置を設
置する場所によっては大型の脱臭槽が必要となる。
At this time, since the wood fragments are also organic substances, a part thereof is decomposed by fermentation and digestion, and lignin, which is a phenolic polymer in the wood, is discharged into the drain. Phenols are emission control substances, and lignin causes root rot of plants. Therefore, drainage cannot be released without secondary treatment of drainage. Further, since fermentation odor is generated during the fermentation treatment, a large deodorization tank is required depending on the place where the treatment device is installed.

【0005】活性炭はその吸着作用から担体として使用
できるが、吸着した有機物を除去して吸着能力を再生し
なければならず、その再生には高温下で吸着成分を焼却
するなどの高価な装置が必要とされる。さらに、活性炭
は有機物と混合するとかたまり易く、塊状となって通気
性が損なわれ、好気性菌の活動が阻害され、また、攪拌
機には動力の大なるモータが必要とされる。
[0005] Activated carbon can be used as a carrier because of its adsorption function. However, it is necessary to remove the adsorbed organic substances to regenerate the adsorbing ability. Needed. Further, activated carbon is liable to clump when mixed with an organic substance, and becomes clumpy, impairs air permeability, inhibits the activity of aerobic bacteria, and requires a high-power motor for the stirrer.

【0006】[0006]

【発明が解決しようとする課題】高濃度の有機物の発酵
消化処理に関し、 a.フェノール性高分子であるリグニンの排出を防止す
る b.通気性を確保することにより好気性菌の活動を促進
し、処理能力の向上を図る C.攪拌動力の低減を図る ことを目的とする。
SUMMARY OF THE INVENTION The present invention relates to a fermentation digestion treatment of high-concentration organic matter, comprising: a. Prevent the emission of lignin, a phenolic polymer b. B. Promote the activity of aerobic bacteria by ensuring air permeability, and improve treatment capacity. The purpose is to reduce the stirring power.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、本発明の高濃度有機物処理方法は、有機物と、微生
物の担体との混合物を撹拌しながらこの混合物に空気を
連続供給し、高温、好気性発酵させることにより有機物
を分解する高濃度有機物処理方法において、前記微生物
の担体に火山灰の一種である白砂を特別に加工処理を施
すことなくそのまま使用することを特徴としている。
To achieve the above object, according to the Invention The high concentration organic matter treatment process of the present invention, the organic substance, microorganism
While stirring the mixture with the material carrier, air is added to the mixture.
Organic matter by continuous supply and high temperature, aerobic fermentation
The method for treating a high-concentration organic substance for decomposing
Specially processed white sand, a type of volcanic ash,
It is characterized in that it is used as it is without being used .

【0008】[0008]

【作用】白砂と攪拌、混合された有機物は発酵に必要な
空気を通気口から与えられ、高温・好気の条件下で発酵
消化される。担体たる白砂は発酵消化によって分解され
ることはないので、堆肥や余剰汚泥を出すことはなく、
高濃度有機物が効率的に消化される。
[Function] The organic matter mixed with white sand is stirred and mixed, and the air required for fermentation is provided through a vent, and fermented and digested under high temperature and aerobic conditions. Since the carrier, white sand, is not decomposed by fermentation and digestion, it does not emit compost or excess sludge,
Highly concentrated organic matter is efficiently digested.

【0009】また、白砂は有機物と混合されてもかたま
り難く、通気性が損なわれない。その結果、好気性菌の
活動が活発になり、有機物処理能力が向上する。
[0009] Further, white sand is hard to clump even when mixed with organic matter, and does not impair the air permeability. As a result, the activity of the aerobic bacteria becomes active, and the organic matter treatment capacity is improved.

【0010】[0010]

【実施例】以下本発明による高濃度有機物処理方法の具
体例を図1に基づいて詳細に説明する。図1は本発明方
法に使用する装置の一具体例を示すもので、図中の符号
1は発酵槽、3は微生物を担持するための担体たる白砂
(例えば大隅、薩摩両半島、都城付近に広く分布する火
山灰)、4は有機排水と白砂3とを混合するための攪拌
装置、5は発酵槽1内に空気を連続供給するブロア、9
は発酵槽内に有機排水を供給するための流入管である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A specific example of the method for treating a high-concentration organic substance according to the present invention will be described below in detail with reference to FIG. FIG. 1 shows a specific example of an apparatus used in the method of the present invention. In the figure, reference numeral 1 denotes a fermenter, and 3 denotes white sand as a carrier for supporting microorganisms (for example, in the vicinity of Osumi, Satsuma Peninsula, and Miyakonojo). 4 is a stirrer for mixing organic wastewater and white sand 3, 5 is a blower for continuously supplying air into the fermenter 1, 9
Is an inflow pipe for supplying organic wastewater into the fermenter.

【0011】発酵槽1は断熱材2で囲まれており、槽内
の下部には処理中に発生した水分を分離するために割栗
石6a、砂礫6b等からなる濾過層6を設け、発酵槽1
の底には濾過水を排出するためのドレン口7を設けてあ
る。
The fermenter 1 is surrounded by a heat insulating material 2. At the lower part of the tank, there is provided a filter layer 6 made of cracked stone 6a, gravel 6b, etc. for separating water generated during the treatment. 1
Is provided with a drain port 7 for discharging filtered water.

【0012】流入管9から供給された有機排水と、発酵
槽1内に充填された白砂3とを混合するための攪拌装置
4は、発酵槽1上部に設けられたモータMによって回転
させられるようになっている。
The stirring device 4 for mixing the organic wastewater supplied from the inflow pipe 9 and the white sand 3 filled in the fermenter 1 is rotated by a motor M provided on the upper part of the fermenter 1. It has become.

【0013】発酵槽1下部の濾過層6側部にあけた通気
口5aには外部からの空気を連続供給するためのブロア
5を接続してあり、また発酵槽1の上部には発酵によっ
て発生する臭気を処理するための脱臭器8を設けてあ
る。
A blower 5 for continuously supplying air from the outside is connected to a vent 5a opened on the side of the filtration layer 6 at the lower part of the fermenter 1, and the upper part of the fermenter 1 is formed by fermentation. A deodorizer 8 is provided for treating odors.

【0014】次にこのように構成される発酵消化槽によ
って高濃度有機物を高温好気性処理する手順を説明す
る。発酵槽1内に白砂3を充填した後、この白砂3に流
入管9を通して外部から高濃度有機排水を供給する(有
機物が固形のばあいにはコンベア等によって発酵槽1内
に供給する)。この有機排水の供給は微生物との接触に
より発酵消化に必要とされる処理時間を基に計算した間
隔をおいて間欠的に行う。
Next, a procedure for subjecting high-concentration organic matter to high-temperature aerobic treatment by the fermentation digester constructed as described above will be described. After the white sand 3 is filled in the fermenter 1, high-concentration organic wastewater is supplied to the white sand 3 from the outside through the inflow pipe 9 (when the organic matter is solid, the organic sand is supplied into the fermenter 1 by a conveyor or the like). The supply of the organic wastewater is performed intermittently at intervals calculated based on the treatment time required for fermentation and digestion by contact with microorganisms.

【0015】続いて、攪拌装置4によって白砂3と有機
排水の混合物を撹拌し、好気性微生物が均一に繁殖する
ようにするとともに、ブロア5により通気口5aを通し
て50〜400リットル/分・m3 の空気を発酵槽1内
に連続供給し、好気性発酵を促進させる。
Subsequently, the mixture of the white sand 3 and the organic waste water is stirred by the stirrer 4 so that the aerobic microorganisms can be uniformly propagated, and the blower 5 can be used to blow the mixture of 50 to 400 liter / min.m 3 through the vent 5a. Is continuously supplied into the fermenter 1 to promote aerobic fermentation.

【0016】ブロア5からの充分な空気の供給と断熱材
2での保温により、発酵槽1内は適度な酸素・温度条件
が保たれて高温、好気性発酵が起こり、この発酵が促進
されて有機物を消化、分解する。この際、担体の含水率
を80%未満となるように有機物に含まれる水分を調節
する。含水率がこれ以上になると発酵条件がくずれ、発
酵が停止する。
By supplying sufficient air from the blower 5 and keeping the heat in the heat insulating material 2, the fermenter 1 is maintained in an appropriate oxygen and temperature condition, and a high-temperature, aerobic fermentation occurs, and this fermentation is promoted. Digest and decompose organic matter. At this time, the water content of the organic matter is adjusted so that the water content of the carrier is less than 80%. If the water content exceeds this, the fermentation conditions are disrupted and the fermentation stops.

【0017】有機物中の余分な水分は白砂3に吸収、保
水され、好気性微生物が活発に活動し、槽内は50〜7
0℃の高温を発生する。有機物が分解されると水分が発
生するが、発酵によって発酵槽内が高温となるためにこ
の水分は水蒸気となって蒸発し、若干の水分は濾過層6
を経てドレン口7から槽外部へ排出される。なお、発酵
槽の直径が5〜6mを超えるばあいには処理容量あたり
の表面積が小さくなるので、断熱材2を設ける必要はな
い。
Excess water in the organic matter is absorbed and retained in the white sand 3, and aerobic microorganisms are actively activated.
Generates a high temperature of 0 ° C. When the organic matter is decomposed, water is generated. However, since the temperature in the fermenter becomes high due to the fermentation, the water is vaporized and evaporated, and a small amount of water is removed from the filtration layer 6.
Through the drain port 7 to the outside of the tank. In addition, when the diameter of the fermenter exceeds 5 to 6 m, the surface area per processing capacity becomes small, so that it is not necessary to provide the heat insulating material 2.

【0018】表1は担体として木質細片、活性炭、白砂
を使用したばあいにおける有機物たる残飯の発酵消化処
理を行った結果を示す実験データである。
Table 1 shows experimental data showing the results of fermentation and digestion of residual rice as an organic substance when wood chips, activated carbon and white sand are used as carriers.

【0019】[0019]

【表1】 このデータより、担体として白砂を使用したばあいに
は、木質細片のばあいの約1.6倍、活性炭のばあいの
約1.7倍の処理能力があることが判明した。
[Table 1] From this data, it was found that when white sand was used as the carrier, the processing capacity was about 1.6 times that of the wood chips and about 1.7 times that of the activated carbon.

【0020】[0020]

【発明の効果】本発明方法によれば次のような効果を奏
し得る。
According to the method of the present invention, the following effects can be obtained.

【0021】高濃度の有機物の発酵消化処理に関し、 a.ドレン中に、フェノール性高分子であるリグニンが
排出するのが防止されるので、ドレンを2次処理する必
要がなく、その装置が不要である。 b.有機物と混合してもかたまりにくいので通気性が確
保され、好気性菌の活動が促進されて、その結果処理能
力が向上させられる。 C.前述のようにかたまりにくいので、攪拌動力が低減
させられ、低コストに処理できる。
Regarding the fermentation digestion treatment of a high concentration of organic matter, a. Since lignin, which is a phenolic polymer, is prevented from being discharged into the drain, there is no need for secondary treatment of the drain, and the device is unnecessary. b. Even if mixed with organic matter, it is hard to clump, so that air permeability is ensured, and the activity of aerobic bacteria is promoted, and as a result, processing capacity is improved. C. As described above, since it is hard to clump, the stirring power is reduced, and the processing can be performed at low cost.

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

【図1】本発明方法に使用する発酵槽の実施例を示す断
面図。
FIG. 1 is a sectional view showing an embodiment of a fermenter used in the method of the present invention.

【符号の説明】[Explanation of symbols]

1 発酵槽 2 断熱材 3 白砂 4 攪拌装置 5 ブロア 6 濾過層 7 ドレン口 8 脱臭器 9 流入管 DESCRIPTION OF SYMBOLS 1 Fermenter 2 Insulation material 3 White sand 4 Stirrer 5 Blower 6 Filtration layer 7 Drain port 8 Deodorizer 9 Inflow pipe

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】有機物と、微生物の担体との混合物を撹拌
しながらこの混合物に空気を連続供給し、高温、好気性
発酵させることにより有機物を分解する高濃度有機物処
理方法において、前記微生物の担体に火山灰の一種であ
る白砂を特別に加工処理を施すことなくそのまま使用す
高濃度有機物処理方法。
1. A mixture of an organic substance and a carrier of a microorganism is stirred.
While continuously supplying air to this mixture, high temperature, aerobic
High-concentration organic matter treatment that decomposes organic matter by fermentation
In the method, the carrier of the microorganism is a kind of volcanic ash.
White sand without any special processing
High concentration organic matter treatment how.
JP5504493A 1993-02-20 1993-02-20 High-concentration organic matter treatment method Expired - Lifetime JP2594498B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5504493A JP2594498B2 (en) 1993-02-20 1993-02-20 High-concentration organic matter treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5504493A JP2594498B2 (en) 1993-02-20 1993-02-20 High-concentration organic matter treatment method

Publications (2)

Publication Number Publication Date
JPH06246284A JPH06246284A (en) 1994-09-06
JP2594498B2 true JP2594498B2 (en) 1997-03-26

Family

ID=12987675

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5504493A Expired - Lifetime JP2594498B2 (en) 1993-02-20 1993-02-20 High-concentration organic matter treatment method

Country Status (1)

Country Link
JP (1) JP2594498B2 (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60143896A (en) * 1984-01-04 1985-07-30 Onoda Cement Co Ltd Purifying medium by contact oxidation of filthy water
JPS60220198A (en) * 1984-04-18 1985-11-02 Cosmo Saikon Kogyo Kk Excretion fermentative decomposition apparatus

Also Published As

Publication number Publication date
JPH06246284A (en) 1994-09-06

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