JP2000024680A - High temperature and aerobic treatment of organic matter and device therefor - Google Patents
High temperature and aerobic treatment of organic matter and device thereforInfo
- Publication number
- JP2000024680A JP2000024680A JP21028298A JP21028298A JP2000024680A JP 2000024680 A JP2000024680 A JP 2000024680A JP 21028298 A JP21028298 A JP 21028298A JP 21028298 A JP21028298 A JP 21028298A JP 2000024680 A JP2000024680 A JP 2000024680A
- Authority
- JP
- Japan
- Prior art keywords
- reaction tank
- aerobic treatment
- temperature
- org
- organic matter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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
-
- 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
- Y02W10/20—Sludge processing
Landscapes
- Activated Sludge Processes (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は有機物の高温,好気
処理方法及び装置、特に、高温,好気法による高濃度有
機廃液の処理方法及び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 method and an apparatus for high-temperature, aerobic treatment of organic substances, and more particularly to a method and an apparatus for treating high-concentration organic waste liquid by a high-temperature, aerobic method.
【0002】[0002]
【従来の技術】高濃度有機排水としては、し尿,食品工
業排水,醸造排水,畜舎ふん尿,濃縮汚泥などがある。
従来、高濃度有機排水に対しては、希釈後、活性汚泥法
などの好気処理が行なわれてきた。この方法は多量の希
釈水が必要であり、活性汚泥処理は電力などのコストが
高く、且つ、かなりの量の余剰汚泥が発生する。2. Description of the Related Art High-concentration organic wastewater includes night soil, food industry wastewater, brewery wastewater, livestock manure, and concentrated sludge.
Conventionally, aerobic treatment such as an activated sludge method has been performed on highly concentrated organic wastewater after dilution. This method requires a large amount of dilution water, and the activated sludge treatment is expensive in terms of electric power and the like, and generates a considerable amount of excess sludge.
【0003】このため、高濃度有機排水を適切な担体に
吸収させた後、空気を供給することにより有機物を二酸
化炭素にまで完全分解し、また、有機物が分解される際
生成する熱により、水分を蒸発させる高温,好気処理法
が用いられている。[0003] For this reason, after absorbing high-concentration organic wastewater into a suitable carrier, air is supplied to completely decompose organic substances into carbon dioxide. A high-temperature, aerobic treatment method for evaporating water is used.
【0004】図2はこのような処理方法及び装置を示
し、1は例えば高さ2200mm、内径2000mmの
断熱構造の反応槽、2はこの反応槽1内に充填した吸水
性が良く、微生物のすみ家(habitat)として適
切で、安価で、生物分解しにくいもの例えば、木質材,
木炭,活性炭及びゼオライト,おがくず,もみがら等の
担体、3は二酸化炭素等の生成物を排気するため上記反
応槽1の上端に設けた開口、4はドレン水排出用の下端
開口、5は上記反応槽1内の上部に配置した有機廃液等
の原水散布管、6は下部に配置した空気噴出管である。FIG. 2 shows such a treatment method and apparatus. 1 is a reaction tank having a heat insulating structure having a height of, for example, 2200 mm and an inner diameter of 2000 mm. Suitable as a habitat, inexpensive, and difficult to biodegrade, such as wood,
Carriers such as charcoal, activated carbon and zeolites, sawdust, rice cake, etc., 3 is an opening provided at the upper end of the reaction tank 1 for exhausting products such as carbon dioxide, 4 is a lower end opening for drain water discharge, and 5 is the above. A pipe for dispersing raw water such as organic waste liquid disposed at the upper part in the reaction tank 1 and an air jetting pipe 6 disposed at the lower part.
【0005】このような処理方法及び装置では、担体2
を機械駆動式の攪拌手段(図示せず)により攪拌しなが
ら担体2内に原水散布管5を介して原水を給水し、その
後空気噴出管6から空気を送り、担体2に含まれる微生
物によって原水中の有機物を、その発酵温度を60℃程
度に保ちながら分解処理せしめている。[0005] In such a processing method and apparatus, the carrier 2
The raw water is supplied into the carrier 2 via the raw water spray pipe 5 while stirring the raw water by a mechanical drive type stirring means (not shown). The organic matter in the water is decomposed while maintaining the fermentation temperature at about 60 ° C.
【0006】[0006]
【発明が解決しようとする課題】然しながら、上記従来
の高温,好気処理方法及び装置においては、担体2の容
積を処理すべき原水の15〜20倍程度とする必要があ
り、反応槽1を大型としなければならない欠点があっ
た。However, in the above-described conventional high-temperature, aerobic treatment method and apparatus, the volume of the carrier 2 needs to be about 15 to 20 times that of the raw water to be treated. There was a disadvantage that it had to be large.
【0007】本発明者は種々実験,研究の結果、上記担
体2を用いなくても、反応槽1内において原水を加熱空
気のジェット流によるエアレーションと混合攪拌によっ
て原水中の有機物を発酵処理できることを見出した。As a result of various experiments and studies, the present inventor has found that the organic matter in the raw water can be fermented in the reaction tank 1 by aeration and mixing and stirring of the raw water in the reaction tank 1 without using the carrier 2. I found it.
【0008】本発明はこのような知見に基づいてなされ
たものである。The present invention has been made based on such findings.
【0009】[0009]
【課題を解決するための手段】本発明の有機物の高温,
好気処理方法は、反応槽内上部に有機物を散布する工程
と、反応槽内下部に加熱空気を供給して上記散布された
有機物をエアレーションせしめる工程と、生成されたガ
スを反応槽内から除去する工程とより成ることを特徴と
する。The organic substance of the present invention has a high temperature,
The aerobic treatment method includes a step of spraying organic matter in the upper part of the reaction tank, a step of supplying heated air to a lower part of the reaction tank to aerate the sprayed organic matter, and removing generated gas from the inside of the reaction tank. And a step of performing
【0010】本発明の有機物の高温,好気処理装置は、
反応槽と、この反応槽内で生成された生成物を排出する
ため上記反応槽に設けた開口と、上記反応槽内の上部及
び下部に配置した有機物散布手段及び加熱空気の供給手
段またはジェット噴出手段とより成ることを特徴とす
る。The high-temperature, aerobic treatment apparatus for organic matter according to the present invention comprises:
A reaction tank, an opening provided in the reaction tank for discharging a product generated in the reaction tank, an organic substance spraying means and a heating air supply means or jet ejection disposed at an upper and a lower part in the reaction tank. Means.
【0011】また、本発明の有機物の高温,好気処理装
置は、上記加熱空気の温度を上記反応室内の温度に応じ
て制御せしめる手段を更に有することを特徴とする。Further, the high-temperature, aerobic treatment apparatus for organic substances according to the present invention is characterized in that the apparatus further comprises means for controlling the temperature of the heated air in accordance with the temperature in the reaction chamber.
【0012】[0012]
【発明の実施の形態】以下図面によって本発明の実施例
を説明する。Embodiments of the present invention will be described below with reference to the drawings.
【0013】本発明においては図1に示すように従来の
担体2とその機械駆動式の攪拌手段及び空気噴出管6を
用いず、代りに加熱手段7によって約60℃に加熱した
空気を定量ポンプ8及び反応槽1の底部に配置した供給
手段またはジェットノズル9を介して反応槽1内に送
り、その結果生成された二酸化炭素等のガスを脱臭した
後、上記上端開口3から排出せしめるようにする。In the present invention, as shown in FIG. 1, the conventional carrier 2 and its mechanically driven agitating means and air blowing tube 6 are not used, and instead, air heated to about 60.degree. 8 and the supply means arranged at the bottom of the reaction tank 1 or the jet nozzle 9 to feed the reaction tank 1 into the reaction tank 1 and degas the resulting gas such as carbon dioxide. I do.
【0014】上記加熱手段7は、断熱構造の容器10
と、この容器10内に外気を取り入れるためのブロワ1
1と、上記反応槽1内の温度が60℃以下となったとき
作動され、70℃以上になったとき停止される吸引ファ
ン12によって吸引した上記容器10内の空気を60〜
70℃に加熱して上記容器10内に戻す熱交換器13と
により構成する。The heating means 7 includes a container 10 having a heat insulating structure.
And a blower 1 for introducing outside air into the container 10.
1 and the air in the container 10 sucked by the suction fan 12 which is activated when the temperature in the reaction vessel 1 becomes 60 ° C. or less and stopped when the temperature in the reaction vessel 1 becomes 70 ° C. or more.
The heat exchanger 13 is heated to 70 ° C. and returned into the container 10.
【0015】熱交換器13の熱源としてはゴミの焼却
余熱,温泉の廃熱などの未利用熱エネルギーが資源の
有効利用の観点から好ましい。As a heat source of the heat exchanger 13, unused heat energy such as residual heat of incineration of garbage and waste heat of hot springs is preferable from the viewpoint of effective utilization of resources.
【0016】なお、14及び15は夫々上記反応槽1の
上部と上記上端開口3間に介挿した排気ファン及び脱臭
剤、16は原水受入槽、17,18は夫々上記原水受入
槽16内に配置した定流量ポンプ及び攪拌手段である。Reference numerals 14 and 15 denote an exhaust fan and a deodorant inserted between the upper portion of the reaction tank 1 and the upper end opening 3, respectively, 16 a raw water receiving tank, and 17 and 18 a raw water receiving tank 16 respectively. The constant flow pump and the stirring means arranged.
【0017】本発明の有機物の高温,好気処理方法及び
装置は、上記の通りであるから、上記原水散布管5から
散布された原水はジェットノズル9からの加熱空気によ
って反応槽1内で加熱,攪拌されて泡状となり、反応槽
1内で浮遊し、その泡の表面が微生物のすみ家の役割を
果たして高温,好気処理されるようになる。Since the method and apparatus for high temperature and aerobic treatment of organic matter of the present invention are as described above, the raw water sprayed from the raw water spray pipe 5 is heated in the reaction tank 1 by the heated air from the jet nozzle 9. The foam is agitated and floats in the reaction tank 1, and the surface of the foam plays a role of a house for microorganisms and is subjected to high-temperature aerobic treatment.
【0018】なお、本発明においては上記泡によって反
応槽1内が充満されるのを防ぐため、上記ジェットノズ
ル9からの排出空気量を適当に制御するのが好ましい。In the present invention, it is preferable to appropriately control the amount of air discharged from the jet nozzle 9 in order to prevent the inside of the reaction tank 1 from being filled with the foam.
【0019】[0019]
【発明の効果】上記のように本発明によれば、従来用い
られていた担体を使用することなく、多量の有機排水を
短時間で処理できるため反応槽として小型のものを使用
できるとともに機械駆動式の攪拌手段が不要になる大き
な利益がある。As described above, according to the present invention, a large amount of organic wastewater can be treated in a short time without using a conventionally used carrier. There is a great advantage that a stirrer is not required.
【図1】本発明の有機物の高温,好気処理方法及び装置
の説明図である。FIG. 1 is an explanatory view of a high-temperature, aerobic treatment method and apparatus of an organic substance according to the present invention.
【図2】従来の有機物の高温,好気処理方法及び装置の
説明図である。FIG. 2 is an explanatory view of a conventional high-temperature, aerobic treatment method and apparatus for organic substances.
1 反応槽 2 担体 3 上端開口 4 下端開口 5 原水散布管 6 空気噴出管 7 加熱手段 8 ポンプ 9 ジェットノズル 10 容器 11 ブロワ 12 吸引ファン 13 熱交換器 14 排気ファン 15 脱臭剤 16 原水受入槽 17 定流量ポンプ 18 攪拌手段 DESCRIPTION OF SYMBOLS 1 Reaction tank 2 Carrier 3 Upper end opening 4 Lower end opening 5 Raw water spraying pipe 6 Air ejection pipe 7 Heating means 8 Pump 9 Jet nozzle 10 Container 11 Blower 12 Suction fan 13 Heat exchanger 14 Exhaust fan 15 Deodorant 16 Raw water receiving tank 17 Constant Flow pump 18 Stirring means
───────────────────────────────────────────────────── フロントページの続き (72)発明者 新垣 紀夫 栃木県那須郡西那須野町四区町1534番地1 ペンタテクノサービス株式会社内 Fターム(参考) 4D028 AA03 AB03 BC01 BD00 BD02 CA10 CB03 CD01 4D059 AA01 AA30 BA03 BA56 CA16 EA20 EB10 ────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Norio Aragaki 1534, 4-ku, Nishi-Nasuno-cho, Nasu-gun, Tochigi Prefecture F-term in Penta Techno Service Co., Ltd. 4D028 AA03 AB03 BC01 BD00 BD02 CA10 CB03 CD01 4D059 AA01 AA30 BA03 BA56 CA16 EA20 EB10
Claims (4)
と、 反応槽内下部に加熱空気を供給して上記散布された有機
物をエアレーションせしめる工程と、 生成されたガスを反応槽内から除去する工程とより成る
ことを特徴とする有機物の高温,好気処理方法。1. A step of spraying an organic substance in an upper part of a reaction tank, a step of supplying heated air to a lower part of the reaction tank to aerate the sprayed organic substance, and removing generated gas from the inside of the reaction tank. And a high-temperature, aerobic treatment method for an organic substance.
成物を排出するため上記反応槽に設けた開口と、上記反
応槽内の上部及び下部に配置した有機物散布手段及び加
熱空気の供給手段とより成ることを特徴とする有機物の
高温,好気処理装置。2. A reaction tank, an opening provided in the reaction tank for discharging a product generated in the reaction tank, an organic substance dispersing means and heating air disposed in upper and lower parts of the reaction tank. A high-temperature, aerobic treatment apparatus for organic matter, characterized by comprising supply means.
成物を排出するため上記反応槽に設けた開口と、上記反
応槽内の上部及び下部に配置した有機物散布手段及び加
熱空気のジェット噴出手段とより成ることを特徴とする
有機物の高温,好気処理装置。3. A reaction tank, an opening provided in the reaction tank for discharging a product generated in the reaction tank, an organic substance dispersing means and heating air disposed in upper and lower parts of the reaction tank. A high-temperature, aerobic treatment apparatus for organic matter, comprising jet ejection means.
度に応じて制御せしめる手段を更に有することを特徴と
する請求項2記載の有機物の高温,好気処理装置。4. The high-temperature aerobic treatment apparatus for organic matter according to claim 2, further comprising means for controlling the temperature of said heated air in accordance with the temperature in said reaction chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21028298A JP2000024680A (en) | 1998-07-10 | 1998-07-10 | High temperature and aerobic treatment of organic matter and device therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21028298A JP2000024680A (en) | 1998-07-10 | 1998-07-10 | High temperature and aerobic treatment of organic matter and device therefor |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2000024680A true JP2000024680A (en) | 2000-01-25 |
Family
ID=16586824
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21028298A Pending JP2000024680A (en) | 1998-07-10 | 1998-07-10 | High temperature and aerobic treatment of organic matter and device therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2000024680A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100374928B1 (en) * | 2000-07-26 | 2003-03-06 | 우진비엔지 주식회사 | Apparatus for processing an waste water of domestic animals |
CN105084563A (en) * | 2015-09-01 | 2015-11-25 | 江苏海纳精密装备有限公司 | Efficient and powerful oxygen dissolving device |
-
1998
- 1998-07-10 JP JP21028298A patent/JP2000024680A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100374928B1 (en) * | 2000-07-26 | 2003-03-06 | 우진비엔지 주식회사 | Apparatus for processing an waste water of domestic animals |
CN105084563A (en) * | 2015-09-01 | 2015-11-25 | 江苏海纳精密装备有限公司 | Efficient and powerful oxygen dissolving device |
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