JPH0691286A - Method for treating highly concentrated organic material - Google Patents
Method for treating highly concentrated organic materialInfo
- Publication number
- JPH0691286A JPH0691286A JP26650692A JP26650692A JPH0691286A JP H0691286 A JPH0691286 A JP H0691286A JP 26650692 A JP26650692 A JP 26650692A JP 26650692 A JP26650692 A JP 26650692A JP H0691286 A JPH0691286 A JP H0691286A
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- carrier
- activated carbon
- charcoal
- organic material
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
Description
【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 highly-concentrated organic wastewater by fermentation and digestion with microorganisms attached 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)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 solid matter, the organic matter is mixed with a microbial carrier composed of wood chips (sawdust) and fermented and digested.
【0003】この方法によれば、担体と混合した有機物
が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, the organic matter mixed with the carrier is fermented and digested by the microorganisms carried on the carrier,
It is decomposed into carbon dioxide, water, inorganic salts, ammonia, etc. 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す
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次処理を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 chips are also organic substances, a part thereof is decomposed by the fermentation digestion action, and lignin, which is a phenolic polymer in wood, is discharged into the drain. Phenols are emission control substances, and lignin causes root rot of plants, so drain cannot be discharged without secondary treatment. In addition, since a fermentation odor is generated during the fermentation process, a large deodorizing tank is required depending on the place where the processing device is installed.
【0005】活性炭や木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
を焼却するなどの方法が採られている。Activated carbon or charcoal can be used as a carrier due to its adsorption action, but it is necessary to remove the adsorbed organic matter to regenerate the adsorption capacity. For regeneration, there is a method such as incineration of the adsorbed component at high temperature. Has been taken.
【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.微生物担体として活性炭または木炭を使用し、その
再生を図る c.処理中に発生する発酵臭を抑える ことを目的とする。DISCLOSURE OF THE INVENTION PROBLEM TO BE SOLVED BY THE INVENTION Regarding fermentation digestion treatment of high-concentration organic matter, Preventing the discharge of lignin, which is a phenolic polymer b. Use activated charcoal or charcoal as a microorganism carrier to regenerate it c. The purpose is to suppress the fermentation odor generated during processing.
【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通気口、攪拌装置
を備える発酵槽内に活性炭または木炭を微生物の担体と
して充填し、この中に有機物を供給して有機物と担体と
を前記攪拌装置によって混合しながら前記通気口から空
気を連続供給し、高温、好気性発酵させることにより有
機物を分解することを特徴としている。In order to achieve the above object, the method for treating high-concentration organic matter according to the present invention is a method in which a fermenter equipped with a vent and a stirrer is filled with activated carbon or charcoal as a microbial carrier. The organic substance is decomposed by aerobically fermenting it at a high temperature by continuously supplying air from the vent while mixing the organic substance and the carrier with the stirring device.
【0008】[0008]
【作用】活性炭や木炭と攪拌、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。担体たる活性炭や木炭は発酵消化
によって分解されることはないので、堆肥や余剰汚泥を
出すことなく、高濃度有機物が効率的に消化される。[Function] The organic matter that is stirred and mixed with activated charcoal or charcoal is provided with air necessary for fermentation through a vent and fermented and digested under high temperature and aerobic conditions. Since activated carbon or charcoal as a carrier is not decomposed by fermentation digestion, high-concentration organic matter can be efficiently digested without producing compost or excess sludge.
【0009】また、発酵処理中に活性炭や木炭中に微生
物が繁殖し、活性炭や木炭に吸着された有機物質を分解
するので、吸着作用が回復、維持される。さらに、活性
炭または木炭の脱臭作用によって発酵臭の発生が抑えら
れる。Further, during the fermentation treatment, microorganisms propagate in activated carbon or charcoal and decompose organic substances adsorbed on the activated carbon or charcoal, so that the adsorption action is restored and maintained. Further, the deodorizing action of activated carbon or charcoal suppresses the generation of fermentation odor.
【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、2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
活性炭、4は有機排水と活性炭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。EXAMPLE A specific example of the method for treating high-concentration organic matter according to the present invention will be described in detail below with reference to FIGS. FIG. 1 shows a specific example of the apparatus used in the method of the present invention. In the figure, reference numeral 1 is a fermenter, 3 is activated carbon as a carrier for supporting microorganisms, and 4 is a mixture of organic waste water and activated carbon 3. A stirring device 5 for supplying air to the fermenter 1 for continuously supplying air,
Reference numeral 9 is an inflow pipe for supplying organic waste water 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, and at the lower part of the fermenter 1 is provided a filter layer 6 composed of split stones 6a, gravel 6b, etc. for separating the water generated during the treatment. 1
A drain port 7 for discharging filtered water is provided at the bottom of the.
【0012】流入管9から供給された有機排水と、発酵
槽1内に充填された活性炭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 waste water supplied from the inflow pipe 9 and the activated carbon 3 filled in the fermentation tank 1 is rotated by a motor M provided above the fermentation tank 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 formed in the side of the filtration layer 6 at the bottom of the fermenter 1, and the upper part of the fermenter 1 is generated by fermentation. A deodorizer 8 is provided for treating the odor that is generated.
【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内に活性炭3を充填した後、この活性炭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, the procedure for high-temperature aerobic treatment of high-concentration organic matter by the fermentation digester thus constructed will be described. After filling the fermenter 1 with activated carbon 3, the activated carbon 3
High-concentration organic wastewater is supplied from the outside through the inflow pipe 9 (when the organic matter is solid, it is supplied into the fermenter 1 by a conveyor or the like). This organic wastewater is supplied intermittently at intervals calculated based on the treatment time required for fermentation and digestion due to contact with microorganisms.
【0015】続いて、攪拌装置4によって活性炭3と有
機排水の混合物を攪拌し、好気性微生物が均一に繁殖す
るようにするとともに、ブロワ5により通気口5aを通
して50〜400l/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 activated carbon 3 and the organic waste water is stirred by the stirrer 4 so that the aerobic microorganisms are uniformly propagated, and the blower 5 is used to blow 50 to 400 l / min · m 3 through the ventilation port 5a. Air 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 insulation by the heat insulating material 2, moderate oxygen and temperature conditions are maintained in the fermenter 1, high temperature aerobic fermentation occurs, and this fermentation is promoted. Digests and decomposes 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 is higher than this, the fermentation conditions will collapse and the fermentation will stop.
【0017】有機物中の余分な水分は活性炭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〜
70℃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、若干の水分は濾過槽
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。The excess water in the organic matter is absorbed by the activated carbon 3,
Water is retained, aerobic microorganisms are active, and the inside of the tank is 50 ~
It produces a high temperature of 70 ° C. When organic matter is decomposed, water is generated, but due to the high temperature in the fermentation tank due to fermentation, this water becomes vapor and evaporates, and some water is discharged from the drain port 7 through the filtration tank 6 to the outside of the tank. To be done. When the diameter of the fermenter exceeds 5 to 6 m, the surface area per processing volume becomes small, so that it is not necessary to provide the heat insulating material 2.
【0018】次に活性炭3の吸着力の再生について説明
する。図2は担体として活性炭を使用し、有機物たる残
飯の発酵消化処理を1か月にわたって行った結果を示す
グラフである。Next, the regeneration of the adsorption force of the activated carbon 3 will be described. FIG. 2 is a graph showing the results of fermentative digestion treatment of organic rice leftovers over one month using activated carbon as a carrier.
【0019】縦軸は活性炭と投入した残飯の混合物合計
重量、横軸は処理開始からの日数を示しており、残飯の
投入量は累積的に増加しているにもかかわらず、混合物
合計重量は1か月余り経過してもほとんど変化がない。
これは有機物の処理が有効に行われ、かつ活性炭中に繁
殖する微生物によって活性炭に吸着した有機物を分解し
て吸着力の再生がおこなわれていることを示している。The vertical axis shows the total weight of the mixture of activated carbon and the leftover rice, and the horizontal axis shows the number of days from the start of the treatment. Even though the amount of leftover rice was cumulatively increased, the total weight of the mixture was Almost no change after a month.
This indicates that the treatment of organic matter is effectively performed, and that the microorganisms that propagate in the activated carbon decompose the organic matter adsorbed on the activated carbon to regenerate the adsorptive power.
【0020】なお、上記実施例においては微生物担体と
して活性炭を用いているが、木炭を用いてもよい。Although activated carbon is used as the microorganism carrier in the above-mentioned embodiment, charcoal may be used.
【0021】[0021]
【発明の効果】担体として使用する活性炭や木炭にはリ
グニン成分が存在していないので、排出規制物質である
フェノール類が排出されることはなくドレン水の2次処
理をせずに放流することができる。EFFECTS OF THE INVENTION Since activated carbon and charcoal used as a carrier do not have lignin components, phenols, which are emission control substances, are not emitted, and discharged without secondary treatment of drain water. You can
【0022】また、担体としての活性炭や木炭の吸着作
用は発酵処理中に微生物によって再生されるので、再生
のための焼却などの手間、装置が不要であり、しかも活
性炭や木炭を補充する必要がないので経済的である。Further, the adsorbing action of activated carbon or charcoal as a carrier is regenerated by microorganisms during the fermentation process, so that labor and equipment such as incineration for regeneration are unnecessary, and it is necessary to supplement activated carbon or charcoal. It's economical because it doesn't exist.
【0023】さらに、活性炭や木炭には脱臭作用がある
ので、発酵の際に生ずる発酵臭を抑えることができ、脱
臭槽などの付属装置も小型のもので済む。Furthermore, since activated carbon and charcoal have a deodorizing action, it is possible to suppress the fermentation odor generated during fermentation, and a small accessory device such as a deodorizing tank is sufficient.
【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.
【図2】活性炭を担体として残飯処理を行った実験の結
果を示すグラフ。FIG. 2 is a graph showing the results of an experiment in which activated carbon is used as a carrier to treat leftover food.
1 発酵槽 2 断熱材 3 活性炭 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 1 Fermenter 2 Heat insulation material 3 Activated carbon 4 Stirrer 5 Blower 6 Filtration layer 7 Drain port 8 Deodorizer 9 Inflow pipe
Claims (1)
炭または木炭を微生物の担体として充填し、この中に有
機物を供給して有機物と担体とを前記攪拌装置によって
混合しながら前記通気口から空気を連続供給し、高温、
好気性発酵させることにより有機物を分解することを特
徴とする高濃度有機物処理方法。1. A fermenter equipped with a vent and a stirrer is filled with activated carbon or charcoal as a carrier for microorganisms, and an organic substance is supplied into the fermenter to mix the organic substance and the carrier with the stirrer while the vent is provided. Air is continuously supplied from
A method for treating high-concentration organic matter, which comprises decomposing organic matter by aerobic fermentation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26650692A JP2581636B2 (en) | 1992-09-09 | 1992-09-09 | High-concentration organic matter treatment method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26650692A JP2581636B2 (en) | 1992-09-09 | 1992-09-09 | High-concentration organic matter treatment method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0691286A true JPH0691286A (en) | 1994-04-05 |
JP2581636B2 JP2581636B2 (en) | 1997-02-12 |
Family
ID=17431863
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP26650692A Expired - Lifetime JP2581636B2 (en) | 1992-09-09 | 1992-09-09 | High-concentration organic matter treatment method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2581636B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR19980024969A (en) * | 1996-09-26 | 1998-07-06 | 다까노 야스아끼 | Organic waste disposal apparatus and method |
JP2007248021A (en) * | 2006-03-20 | 2007-09-27 | Sharp Corp | Cooling method and cooling apparatus |
Citations (10)
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---|---|---|---|---|
JPS5411469A (en) * | 1977-06-29 | 1979-01-27 | Fujitsu Ltd | Construction for cooling wiring board |
JPS5575794A (en) * | 1978-12-05 | 1980-06-07 | Mitsui Toatsu Chem Inc | Waste water treatment |
JPS57135088A (en) * | 1981-02-17 | 1982-08-20 | Kurita Water Ind Ltd | Purification of highly-concentrated organic waste water |
JPS60220198A (en) * | 1984-04-18 | 1985-11-02 | Cosmo Saikon Kogyo Kk | Excretion fermentative decomposition apparatus |
JPS60238196A (en) * | 1984-05-10 | 1985-11-27 | Niigata Eng Co Ltd | Method and apparatus for biological treatment of organic waste water |
JPS63256175A (en) * | 1987-04-10 | 1988-10-24 | Sharp Corp | Garbage disposer |
JPH02108609A (en) * | 1988-10-19 | 1990-04-20 | Norin Suisansyo Nogyo Kankyo Gijutsu Kenkyusho | Soil blight controlling and plant growth promoting agent |
JPH03123687A (en) * | 1989-10-05 | 1991-05-27 | Munakata Chiku Suido Kigiyoudan | Biological contact filter apparatus |
JPH0418988A (en) * | 1990-05-14 | 1992-01-23 | Ebara Infilco Co Ltd | Biomembrane filter device for organic sewage |
JPH0468102A (en) * | 1990-07-09 | 1992-03-03 | Tokai Yuki Kenkyusho:Kk | Golf course equipped with structure for purification of agricultural chemicals |
-
1992
- 1992-09-09 JP JP26650692A patent/JP2581636B2/en not_active Expired - Lifetime
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5411469A (en) * | 1977-06-29 | 1979-01-27 | Fujitsu Ltd | Construction for cooling wiring board |
JPS5575794A (en) * | 1978-12-05 | 1980-06-07 | Mitsui Toatsu Chem Inc | Waste water treatment |
JPS57135088A (en) * | 1981-02-17 | 1982-08-20 | Kurita Water Ind Ltd | Purification of highly-concentrated organic waste water |
JPS60220198A (en) * | 1984-04-18 | 1985-11-02 | Cosmo Saikon Kogyo Kk | Excretion fermentative decomposition apparatus |
JPS60238196A (en) * | 1984-05-10 | 1985-11-27 | Niigata Eng Co Ltd | Method and apparatus for biological treatment of organic waste water |
JPS63256175A (en) * | 1987-04-10 | 1988-10-24 | Sharp Corp | Garbage disposer |
JPH02108609A (en) * | 1988-10-19 | 1990-04-20 | Norin Suisansyo Nogyo Kankyo Gijutsu Kenkyusho | Soil blight controlling and plant growth promoting agent |
JPH03123687A (en) * | 1989-10-05 | 1991-05-27 | Munakata Chiku Suido Kigiyoudan | Biological contact filter apparatus |
JPH0418988A (en) * | 1990-05-14 | 1992-01-23 | Ebara Infilco Co Ltd | Biomembrane filter device for organic sewage |
JPH0468102A (en) * | 1990-07-09 | 1992-03-03 | Tokai Yuki Kenkyusho:Kk | Golf course equipped with structure for purification of agricultural chemicals |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR19980024969A (en) * | 1996-09-26 | 1998-07-06 | 다까노 야스아끼 | Organic waste disposal apparatus and method |
JP2007248021A (en) * | 2006-03-20 | 2007-09-27 | Sharp Corp | Cooling method and cooling apparatus |
Also Published As
Publication number | Publication date |
---|---|
JP2581636B2 (en) | 1997-02-12 |
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