JP3818706B2 - Biological treatment method and apparatus for waste water - Google Patents

Biological treatment method and apparatus for waste water Download PDF

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Publication number
JP3818706B2
JP3818706B2 JP27238196A JP27238196A JP3818706B2 JP 3818706 B2 JP3818706 B2 JP 3818706B2 JP 27238196 A JP27238196 A JP 27238196A JP 27238196 A JP27238196 A JP 27238196A JP 3818706 B2 JP3818706 B2 JP 3818706B2
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biological
treatment
fixed bed
wastewater
inert gas
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JPH10113692A (en
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智 毛塚
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Fujitsu Ltd
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Fujitsu Ltd
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    • 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

Description

【0001】
【発明の属する技術分野】
本発明は排水の生物学的処理方法及び装置に関し、さらに詳しく述べると、製造プロセスから排出された工場排水等の排水を生物学的に処理する方法及び装置に関する。
【0002】
【従来の技術】
近年、事業所において製造プロセスから排出された工場排水、例えば有機排水やフッ素等の各種の化学物質を含む排水を、それを下水道に放流するかもしくは公共用水域(河川等)に直接に放流する前、有害物質、汚染物質等の除去のために処理することが非常に重要になっている。例えば、国や地方自治体は、環境の保全や排水に原因する水質の汚濁を防止するため、水質汚濁防止法といった法律や、各種化学物質の排出基準等の条例を定めており、また、したがって、事業所等は、排水を処理するに当たって、その排水中の有害物質等の濃度が規準値以下になるように、完全な形で処理を行わなければならない。
【0003】
排水処理の1手法として、排水を生物学的に処理する生物排水処理が幅広く用いられており、良好な成績を収めている。生物処理は、排水中に含まれる生物の代謝作用を利用して、排水中の有機物を安定化させることと、沈殿しやすい固形分に変化させることを目的とした処理法である。生物処理のプロセスは、大きく分けると、例えば活性汚泥法などのように生物を浮遊させて処理を行う生物浮遊法と、生物を担体等に固着して処理を行う生物固定法とがある。
【0004】
従来の典型的な生物排水処理は、例えば、酸素の不存在下で排水を処理し、排水中に含まれる生物の作用により有機物を分解する嫌気処理である。この方法は、しかし、処理槽内を嫌気状態に保つため、その実施のために生物浮遊式処理槽を使用しなければならず、生物濃度の維持や管理が困難であるという問題をかかえている。すなわち、この方法の場合、処理の安定化のために、処理槽内の生物濃度を高くかつ一定に保つ必要があり、この作業に多くの工数と時間がかかっていた。
【0005】
また、従来のフッ素を含有する生物排水の処理では、生物処理に先がけて例えば消石灰(水酸化カルシウム)などで予め凝集沈殿させる作業が行われている。この作業により残存し、かつ元々排水中に含まれる各種のアルカリ土類金属の塩類が生物処理に対して悪い影響を及ぼすのを回避するため、通常、炭酸ナトリウム等を用いた追加の凝集沈殿処理を併用している。また、この追加の凝集沈殿処理のため、処理装置の設置スペースを広くとらなければならない。
【0006】
【発明が解決しようとする課題】
本発明の目的は、上記したような従来の技術の問題点を解決して、複雑な排水処理運営を必要とせず、生物処理を必要とする排水の安定な処理を可能とするような生物排水処理方法を提供することにある。
本発明の目的は、また、このような生物排水処理方法を実施するためのものであって、大きな設置スペースを必要としないような生物排水処理装置を提供することにある。
【0007】
本発明のその他の目的は、以下の詳細な説明から容易に理解することができるであろう。
【0008】
【課題を解決するための手段】
本発明は、その1つの面において、排水を生物学的に処理するに当たって、嫌気性生物固定床における生物処理及びそれに引き続く不活性ガスを用いた逆洗処理を組み合わせて実施することを特徴とする生物排水処理方法にある。
また、本発明は、そのもう1つの面において、排水を生物学的に処理する装置であって、アルカリ土類凝集沈殿の後段に純酸素曝気を伴う生物固定床装置を組み合わせて含んでなることを特徴とする生物排水処理装置にある。
【0009】
【発明の実施の形態】
本発明による生物排水処理方法及び装置は、いろいろな好ましい実施の形態を有することができる。下記のものに限定されるわけではないけれども、本発明の好ましい実施の形態を以下において説明する。
本発明の生物排水処理方法は、上記したように、生物固定床における生物処理及びそれに引き続く不活性ガスを用いた逆洗処理を組み合わせて実施することに特徴がある。ここで、嫌気槽としての生物固定床は、この技術分野で通常使用されている構造を有することができ、したがって、生物固定のための充填材も、この技術分野で良く知られている材料であることができる。適当な充填材として、例えば、多孔質の鉱石、繊維材料などを挙げることができる。この充填材により、生物処理の間じゅう、固定床内の生物濃度を高濃度で一定に保持することができる。また、固定床の大きさ及びその中に詰められる充填材の形状及び大きさは、排水処理の規模や所望とする結果などのファクタに応じて広く変更することができる。
【0010】
生物固定床に固着されるべき生物は、排水の組成などによって変更があるというものの、適当な生物の一例を示すと、ゾーグレア、アメーバー、ツリガネムシなどの微生物である。このような生物は自然に固着し、増殖していく。
本発明方法では、一定時間にわたって生物処理を行った後あるいは所定量の排水を生物固定床に供給して生物処理を行った後、不活性ガスを用いて逆洗処理を実施する。逆洗処理は、固定床内の余剰生物を除去するためのもので、この技術分野において一般的に行われているように、固定床に空気の代りに不活性ガスを吹き込むことによって行うことができる。適当な不活性ガスとしては、純酵素より安価な窒素ガスやアルゴンガスなどが挙げられ、また、このガスの吹き込みのための手段としては、例えば、散気管、スプレーノズル、有孔導管などが挙げられる。不活性ガスによる逆洗処理は、時間により自動的に行うのが好ましい。また、この不活性ガスによる逆洗処理に組み合わせて、必要ならば、水を用いた水逆洗を併用してもよい。
【0011】
本発明の生物排水処理方法は、上記した嫌気生物処理に代えて、好気生物処理として実施することもできる。この場合には、生物固定床における生物処理を実施する際、その固定床に対して純酸素の曝気を行う。また、可能ならば、純酸素に代えて酸素富化のガスを使用してもよい。曝気の方法は、上記した逆洗処理に準じて行ってもよく、さもなければ、その他の公知の手法に従って実施してもよい。この純酸素曝気により、高負荷処理が可能となり、また、したがって、従来実施されていた凝集沈殿処理を省略することができる。すなわち、本発明によれば、排水をそのままの状態で生物固定床に直接に送り込むことができる。生物固定床で所定の処理を行った後、排水の逆洗処理を行う。この逆洗処理は、純酵素を用いて行うことができるというものの、先に述べたように窒素ガス等の不活性ガスを使用して行う逆洗が、コストの面などから有利である。
【0012】
さらに、生物処理を必要とする排水にフッ素等の有害物質が含まれる場合には、排水中のアルカリ土類金属の塩類を例えば消石灰などで凝集沈殿させた後に続けて、そのままの状態で、後段の生物固定床にて処理を行うことができる。凝集沈殿物を回収するための特別の手段を生物固定床の前に設置することは不要である。ここで、好気生物処理を行うのであるならば、純酸素を固定床に供給し、また、嫌気生物処理を行うのであるならば、窒素ガス等の不活性ガスを固定床に供給する。生物固定床で所定の処理を行った後、必要に応じて、排水の逆洗処理を行う。この逆洗処理は、先に述べたように窒素ガス等の不活性ガスを使用して行うのが有利である。
【0013】
本発明の生物排水処理装置は、生物固定床装置及びそれに引き続く不活性ガス逆洗処理装置を組み合わせて含んでなることを特徴としている。ここで、生物固定床装置は、上記したような生物固定床を含む常用の装置であることができ、逆洗、曝気等のための散気管あるいはそれに類する手段及びエア抜きのための自動弁を装備することができる。さらに、この装置には、好ましくは導管を介して不活性ガス逆洗処理装置が接続される。逆洗処理装置は、この技術分野において一般的なように、バッファータンクをもって構成することができる。
【0014】
生物固定床装置は、好ましくは、純酸素曝気装置を装備することができる。純酸素曝気装置は、先に説明した逆洗処理装置と同様、バッファータンクをもって構成することができ、さもなければ、その他の常用の構成としてもよい。
また、生物排水処理装置は、好ましくは、生物固定床装置とそれに引き続く不活性ガス逆洗処理装置の前段にアルカリ土類塩凝集沈殿処理装置を有することができる。アルカリ土類塩凝集沈殿処理装置は、この技術分野において一般的に用いられているものをそのままあるいは改良して使用することができる。アルカリ土類塩凝集沈殿処理装置と生物固定床装置の間に沈殿回収装置等の余分な装置を設置することは不要である。
【0015】
本発明による生物排水処理装置において、それを構成する個々の装置は、ここで特に説明するまでもなく、この技術分野において通常行われているようにして相互を接続し、また、必要に応じて、自動弁、計測器、その他の手段を取り付けることができる。
【0016】
【実施例】
以下、添付の図面を参照しながら本発明の実施例を詳細に説明する。なお、本発明はこれらの実施例に限定されるものではないことを理解されたい。
図1は、不活性ガスを逆洗に使用した嫌気生物排水処理装置の系統図である。FRP製の排水原水槽1の排水は、送水パイプ11により生物処理槽4に供給される。ここで、生物処理槽4は、軟鋼製で硬質ゴムライニングを有している嫌気生物固定床であって、図示のように、固定床41、散気管42及びエア抜きのための自動弁43を装備している。固定床41の充填材は多孔質の鉱石であり、また、それに固着された生物はBacillus、メタン生成菌などである。生物処理槽4は、固定床であるので、生物濃度が高濃度に保たれており、したがって、安定に生物処理を行うことができる。一定時間にわたって生物処理を行った後あるいは所定流量の排水の処理が完了した後、自動弁15を開いて、バッファータンク5内の不活性ガス(ここでは窒素ガスを使用)を生物処理槽4に導入する。不活性ガスが散気管42から噴射されるので、固定床41をその下方から逆洗することができる。この不活性ガスによる逆洗の間、エア抜きのため、自動弁43も開放する。また、必要があれば、逆洗用ポンプ17により処理水槽6の水を自動弁16を介して導入して、生物処理槽4の下部にて追加の水逆洗を行ってもよい。水逆洗のため、通常、処理水量の2〜3倍量の水を送水するのが好ましい。逆洗処理の完了後、生物処理槽4において生成した処理水は、自動弁19を介して処理水槽6に送られ、また、逆洗排水は、自動弁18を介して逆洗排水槽7に送られる。
【0017】
上記した嫌気生物排水処理装置の変形として、同じ装置を使用してかつ基本的に同様な手法に従って好気生物排水処理も行うことができる。この場合には、不活性ガスに代えて純酸素をバッファータンク5内で使用し、この純酸素を、自動弁15を開いて、散気管42から生物処理槽4に導入し、曝気する。曝気の条件は、槽内溶存酸素量が1〜1.2ppm となるように調整する。この処理により、高負荷処理が可能となり、アルカリ土類塩凝集沈殿処理後の生物処理も可能となる。生物処理が完了した後、排水の逆洗を行う。ここで、自動弁15を開いて、バッファータンク5内の純酸素を生物処理槽4に導入することができるけれども、コストの低減のため、窒素ガス等の不活性ガスを使用することが好ましい。すなわち、開放していた自動弁15を自動弁14に切替え、バッファータンク5の別のチャンバ内の不活性ガス(ここでは窒素ガスを使用)を生物処理槽4に導入することが好ましい。
【0018】
図2は、アルカリ土類金属塩の凝集沈殿処理とその後の生物処理を連続的に行うことのできる生物排水処理装置の系統図である。この生物排水処理装置は、フッ素等を含有する要生物処理排水の処理に有利に使用することができる。
PE製の排水原水槽1の排水は、送水パイプ11により軟鋼製で硬質ゴムライニングを有している反応槽2に、そしてさらに軟鋼製でタールエポキシライニングを有している沈殿槽3に供給される。沈殿槽3で、消石灰を用いて、常用の手法に従ってアルカリ土類金属塩の凝集沈殿処理を行う。この凝集沈殿処理の結果として生成した沈殿は、送泥ポンプ13を介して汚泥として排出される。そして、沈殿処理後の排水は、送液ポンプ12を介して生物処理槽4に直接にかつ連続的に供給される。生物処理槽4における処理は、基本的に図1を参照して説明した手法に従って実施することができる。なお、本例でも、好気生物処理を行うのであるならば、純酸素をバッファータンク5に収容して、自動弁14の開放により生物処理槽4に導入し、また、嫌気生物処理を行うのであるならば、不活性ガスをバッファータンク5に収容して、自動弁14の開放により生物処理槽4に導入する。
【0019】
また、図2では特に固定床式生物処理について説明したけれども、所望ならば、それに代えて浮遊式生物処理も使用することが可能である。
【0020】
【発明の効果】
以上に説明したように、本発明によれば、生物固定床において不活性ガスを用いて逆洗を行うので、高負荷処理を行うことができ、安定性の高い嫌気生物処理を行うことができ、また、その際、複雑な排水処理運営を行うことは不必要である。また、上記のような嫌気生物処理に代えて好気生物処理を行う場合には、生物固定床において純酸素曝気を行うことにより、同じく高負荷処理を行うことができ、アルカリ土類塩除去用の凝集沈殿槽を特別に設けずに、アルカリ土類塩凝集沈殿処理後の排水をそのまま直接に、連続して生物固定床で処理することができる。また、凝集沈殿槽が不要となるので、装置の設置スペースをコンパクトにおさめることができる。本発明による生物排水処理方法及び装置は、したがって、有機排水、フッ素等を含有する要生物処理排水の排出を余儀なくされている事業所等において、処理経費及び処理スペースの削減あるいは水質汚濁の防止及び環境の保全に寄与するところが大である。
【図面の簡単な説明】
【図1】本発明による生物排水処理装置の好ましい1態様を示した系統図である。
【図2】本発明による生物排水処理装置のもう1つの好ましい態様を示した系統図である。
【符号の説明】
1…排水原水槽
2…反応槽
3…沈殿槽
4…生物処理槽
5…バッファータンク
6…処理水槽
7…逆洗排水槽
11…送水ポンプ
12…送液ポンプ
13…送泥ポンプ
14…自動弁
15…自動弁
16…自動弁
17…逆洗用ポンプ
18…自動弁
19…自動弁
41…固定床
42…散気管
43…自動弁
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a biological treatment method and apparatus for wastewater, and more particularly to a method and apparatus for biologically treating wastewater such as factory wastewater discharged from a manufacturing process.
[0002]
[Prior art]
In recent years, industrial wastewater discharged from manufacturing processes at business establishments, for example, organic wastewater and wastewater containing various chemical substances such as fluorine, are discharged into sewers or directly into public water bodies (rivers, etc.) Before, it is very important to process for removing harmful substances, pollutants and the like. For example, the national and local governments have established laws such as the Water Pollution Control Act and regulations on the emission standards of various chemical substances to prevent environmental pollution and water pollution caused by wastewater. When setting up wastewater, business establishments, etc., must treat the wastewater in a complete form so that the concentration of harmful substances in the wastewater is below the standard value.
[0003]
As one method of wastewater treatment, biological wastewater treatment that biologically treats wastewater is widely used, and has achieved good results. Biological treatment is a treatment method aimed at stabilizing organic matter in the wastewater and changing it to a solid content that tends to settle by utilizing the metabolic action of the organisms contained in the wastewater. The biological treatment process can be roughly classified into a biological suspension method in which an organism is suspended and treated, such as an activated sludge method, and a biological fixation method in which treatment is performed by fixing the organism to a carrier or the like.
[0004]
Conventional typical biological wastewater treatment is, for example, anaerobic treatment in which wastewater is treated in the absence of oxygen, and organic substances are decomposed by the action of organisms contained in the wastewater. However, this method has a problem that it is difficult to maintain and manage the concentration of organisms because it is necessary to use a biological suspension treatment tank for its implementation in order to keep the inside of the treatment tank in an anaerobic state. . That is, in the case of this method, it is necessary to keep the biological concentration in the treatment tank high and constant in order to stabilize the treatment, and this work takes a lot of man-hours and time.
[0005]
Moreover, in the conventional treatment of biological wastewater containing fluorine, an operation of pre-aggregating and precipitating with, for example, slaked lime (calcium hydroxide) is performed prior to biological treatment. In order to avoid various alkaline earth metal salts remaining in this work and originally contained in the wastewater from adversely affecting biological treatment, additional coagulation and precipitation treatment using sodium carbonate or the like is usually used. Are used together. Moreover, the installation space of a processing apparatus must be taken wide for this additional coagulation sedimentation processing.
[0006]
[Problems to be solved by the invention]
The object of the present invention is to solve the problems of the conventional technology as described above, and does not require complicated wastewater treatment operation, and biological wastewater that enables stable treatment of wastewater that requires biological treatment. It is to provide a processing method.
Another object of the present invention is to provide such a biological wastewater treatment apparatus for carrying out such a biological wastewater treatment method and does not require a large installation space.
[0007]
Other objects of the present invention will be readily understood from the following detailed description.
[0008]
[Means for Solving the Problems]
In one aspect of the present invention, when wastewater is biologically treated, the biological treatment in the anaerobic biological fixed bed and the subsequent backwashing treatment using an inert gas are performed in combination. Biological wastewater treatment method.
In another aspect, the present invention is a device for biologically treating waste water, and comprises a combined biological fixed bed device with pure oxygen aeration after the alkaline earth coagulation sedimentation. It is in the biological wastewater treatment equipment characterized by.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
The biological wastewater treatment method and apparatus according to the present invention can have various preferred embodiments. Although not limited to the following, preferred embodiments of the present invention are described below.
As described above, the biological wastewater treatment method of the present invention is characterized in that the biological treatment in the biological fixed bed and the subsequent backwash treatment using an inert gas are performed in combination. Here, the biological fixed bed as an anaerobic tank can have a structure usually used in this technical field, and therefore, the filler for biological fixation is also a material well known in this technical field. Can be. Examples of suitable fillers include porous ores and fiber materials. With this filler, the biological concentration in the fixed bed can be kept constant at a high concentration throughout the biological treatment. In addition, the size of the fixed bed and the shape and size of the filler packed therein can be widely changed depending on factors such as the scale of the wastewater treatment and the desired result.
[0010]
The organisms to be fixed on the organism fixed bed may be changed depending on the composition of the drainage, but as examples of suitable organisms, microorganisms such as zoglea, amoeba, and worm beetle. Such organisms naturally settle and multiply.
In the method of the present invention, after performing biological treatment for a certain period of time, or after performing biological treatment by supplying a predetermined amount of waste water to the biological fixed bed, backwashing treatment is performed using an inert gas. The backwashing treatment is for removing surplus organisms in the fixed bed, and can be performed by blowing an inert gas instead of air into the fixed bed, as is generally done in this technical field. it can. Examples of suitable inert gas include nitrogen gas and argon gas, which are cheaper than pure enzymes, and examples of means for injecting this gas include a diffuser tube, a spray nozzle, and a perforated conduit. It is done. The backwash process with an inert gas is preferably performed automatically with time. Further, in combination with this inert gas backwashing treatment, if necessary, water backwashing using water may be used in combination.
[0011]
The biological wastewater treatment method of the present invention can be implemented as an aerobic biological treatment instead of the above-described anaerobic biological treatment. In this case, when performing biological treatment on the biological fixed bed, pure oxygen is aerated on the fixed bed. If possible, an oxygen-enriched gas may be used instead of pure oxygen. The aeration method may be performed in accordance with the above-described back washing treatment, or may be performed according to other known methods. This pure oxygen aeration makes it possible to perform a high-load treatment, and therefore, it is possible to omit the coagulation-precipitation treatment conventionally performed. That is, according to the present invention, the wastewater can be directly fed into the biological fixed bed as it is. After performing the predetermined treatment on the biological fixed bed, the waste water is backwashed. Although this backwashing treatment can be performed using a pure enzyme, as described above, backwashing using an inert gas such as nitrogen gas is advantageous in terms of cost.
[0012]
In addition, when wastewater that requires biological treatment contains harmful substances such as fluorine, the alkaline earth metal salts in the wastewater are coagulated and precipitated with, for example, slaked lime, and the state is kept as it is. The treatment can be carried out on a biological fixed bed. It is not necessary to install a special means for collecting the aggregated sediment in front of the biological fixed bed. Here, if an aerobic treatment is performed, pure oxygen is supplied to the fixed bed, and if an anaerobic treatment is performed, an inert gas such as nitrogen gas is supplied to the fixed bed. After performing the predetermined treatment on the biological fixed bed, the wastewater is backwashed as necessary. This backwashing treatment is advantageously performed using an inert gas such as nitrogen gas as described above.
[0013]
The biological wastewater treatment apparatus of the present invention is characterized by comprising a biological fixed bed apparatus and a subsequent inert gas backwashing treatment apparatus in combination. Here, the biological fixed bed apparatus can be an ordinary apparatus including the biological fixed bed as described above, and includes an air diffuser for backwashing, aeration, or the like, and an automatic valve for venting air. Can be equipped. Furthermore, an inert gas backwashing device is preferably connected to this device via a conduit. The backwashing apparatus can be configured with a buffer tank, as is common in this technical field.
[0014]
The biological fixed bed apparatus can preferably be equipped with a pure oxygen aeration apparatus. The pure oxygen aeration apparatus can be configured with a buffer tank, similarly to the backwash processing apparatus described above, or may have other conventional configurations.
In addition, the biological wastewater treatment apparatus can preferably have an alkaline earth salt coagulation sedimentation treatment apparatus upstream of the biological fixed bed apparatus and the subsequent inert gas backwashing treatment apparatus. As the alkaline earth salt agglomeration sedimentation treatment apparatus, an apparatus generally used in this technical field can be used as it is or after modification. It is not necessary to install an extra device such as a sediment collection device between the alkaline earth salt coagulation sedimentation treatment device and the biological fixed bed device.
[0015]
In the biological wastewater treatment apparatus according to the present invention, the individual devices constituting the same are connected to each other in the normal manner in this technical field, and need not be described here. Automatic valves, measuring instruments, and other means can be attached.
[0016]
【Example】
Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings. It should be understood that the present invention is not limited to these examples.
FIG. 1 is a system diagram of an anaerobic biological wastewater treatment apparatus using an inert gas for backwashing. The wastewater from the FRP drainage raw water tank 1 is supplied to the biological treatment tank 4 through a water pipe 11. Here, the biological treatment tank 4 is an anaerobic fixed bed made of mild steel and having a hard rubber lining. As shown in the drawing, the fixed tank 41, the diffuser pipe 42, and an automatic valve 43 for venting air are provided. Equipped. The filler of the fixed bed 41 is a porous ore, and the organisms fixed to it are Bacillus, methanogen, and the like. Since the biological treatment tank 4 is a fixed bed, the biological concentration is kept at a high concentration, and therefore biological treatment can be performed stably. After the biological treatment is performed for a certain period of time or after the treatment of the waste water at a predetermined flow rate is completed, the automatic valve 15 is opened, and the inert gas (here, nitrogen gas) in the buffer tank 5 is transferred to the biological treatment tank 4. Introduce. Since the inert gas is injected from the diffuser tube 42, the fixed bed 41 can be backwashed from below. During the backwashing with the inert gas, the automatic valve 43 is also opened to release air. If necessary, the water in the treatment water tank 6 may be introduced through the automatic valve 16 by the backwash pump 17, and additional water backwash may be performed in the lower part of the biological treatment tank 4. For backwashing with water, it is usually preferable to feed 2 to 3 times the amount of treated water. After completion of the backwash treatment, the treated water generated in the biological treatment tank 4 is sent to the treated water tank 6 via the automatic valve 19, and the backwash drainage is sent to the backwash drainage tank 7 via the automatic valve 18. Sent.
[0017]
As a modification of the above-described anaerobic biological wastewater treatment apparatus, aerobic biological wastewater treatment can be performed using the same apparatus and basically according to the same technique. In this case, pure oxygen is used in the buffer tank 5 in place of the inert gas, and the pure oxygen is aerated by opening the automatic valve 15 and introducing it into the biological treatment tank 4 from the diffuser tube 42. The aeration conditions are adjusted so that the dissolved oxygen amount in the tank is 1 to 1.2 ppm. By this treatment, a high load treatment is possible, and a biological treatment after the alkaline earth salt coagulation sedimentation treatment is also possible. After biological treatment is complete, backwash the wastewater. Here, although the automatic valve 15 can be opened and pure oxygen in the buffer tank 5 can be introduced into the biological treatment tank 4, it is preferable to use an inert gas such as nitrogen gas in order to reduce costs. That is, it is preferable to switch the opened automatic valve 15 to the automatic valve 14 and introduce an inert gas (in this case, using nitrogen gas) in another chamber of the buffer tank 5 into the biological treatment tank 4.
[0018]
FIG. 2 is a system diagram of a biological wastewater treatment apparatus capable of continuously performing a coagulation sedimentation treatment of an alkaline earth metal salt and a subsequent biological treatment. This biological wastewater treatment apparatus can be advantageously used for the treatment of vital biological wastewater containing fluorine or the like.
The wastewater from the raw water tank 1 made of PE is supplied to a reaction tank 2 made of mild steel and having a hard rubber lining, and further to a precipitation tank 3 made of mild steel and having a tar epoxy lining. The In the sedimentation tank 3, the coagulation sedimentation treatment of the alkaline earth metal salt is performed using slaked lime according to a conventional technique. The precipitate generated as a result of this coagulation sedimentation process is discharged as sludge through the mud pump 13. The waste water after the precipitation treatment is directly and continuously supplied to the biological treatment tank 4 via the liquid feed pump 12. The treatment in the biological treatment tank 4 can be basically performed according to the method described with reference to FIG. In this example as well, if aerobic biological treatment is performed, pure oxygen is accommodated in the buffer tank 5 and introduced into the biological treatment tank 4 by opening the automatic valve 14, and anaerobic biological treatment is performed. If there is, an inert gas is accommodated in the buffer tank 5 and introduced into the biological treatment tank 4 by opening the automatic valve 14.
[0019]
Further, although FIG. 2 particularly describes fixed-bed biological treatment, floating biological treatment can be used instead if desired.
[0020]
【The invention's effect】
As described above, according to the present invention, since backwashing is performed using an inert gas in a biological fixed bed, high-load treatment can be performed, and highly stable anaerobic biological treatment can be performed. In that case, it is unnecessary to perform complicated wastewater treatment. In addition, when aerobic biological treatment is performed instead of the anaerobic biological treatment as described above, pure oxygen aeration is performed on the biological fixed bed, and thus high load treatment can be performed, and alkaline earth salt removal can be performed. The waste water after the alkaline earth salt coagulation sedimentation treatment can be directly and continuously treated on the biological fixed bed without providing a special coagulation sedimentation tank. In addition, since a coagulation sedimentation tank is not required, the installation space for the apparatus can be reduced. Therefore, the biological wastewater treatment method and apparatus according to the present invention can reduce the processing cost and the processing space or prevent water pollution in establishments where organic wastewater, wastewater containing biological treatment containing fluorine, etc. are forced to be discharged. There is a significant contribution to environmental conservation.
[Brief description of the drawings]
FIG. 1 is a system diagram showing a preferred embodiment of a biological wastewater treatment apparatus according to the present invention.
FIG. 2 is a system diagram showing another preferred embodiment of the biological wastewater treatment apparatus according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Waste water source tank 2 ... Reaction tank 3 ... Precipitation tank 4 ... Biological treatment tank 5 ... Buffer tank 6 ... Treatment water tank 7 ... Backwash drain tank 11 ... Water feed pump 12 ... Liquid feed pump 13 ... Mud pump 14 ... Automatic valve DESCRIPTION OF SYMBOLS 15 ... Automatic valve 16 ... Automatic valve 17 ... Backwash pump 18 ... Automatic valve 19 ... Automatic valve 41 ... Fixed bed 42 ... Aeration pipe 43 ... Automatic valve

Claims (3)

製造プロセスから排出されたフッ素を含有する排水を生物学的に処理するに当たって、
前記排水を凝集沈殿槽に供給して凝集沈殿処理によりアルカリ土類金属の塩類を沈殿させ、
沈殿処理後の排水をそのままの状態で、嫌気性生物固定床及び不活性ガス吹き込み手段を備えた生物処理槽に直接に供給し、
前記生物処理槽において、前記嫌気性生物固定床における不活性ガスを用いた生物処理を行いかつ、一定時間にわたって生物処理を行った後あるいは所定量の排水を生物固定床に供給して生物処理を行った後、不活性ガスを用いた前記生物固定床の逆洗処理を実施し、前記逆洗処理では固定床内の余剰生物を除去すること
を特徴とする生物排水処理方法。
In treating biologically the wastewater containing fluorine discharged from the manufacturing process,
Supplying the waste water to a coagulation sedimentation tank to precipitate alkaline earth metal salts by coagulation sedimentation treatment,
The wastewater after the precipitation treatment is directly supplied to a biological treatment tank equipped with an anaerobic biological fixed bed and inert gas blowing means,
In the biological treatment tank, the biological treatment using the inert gas in the anaerobic biological fixed bed is performed, and the biological treatment is performed after the biological treatment is performed for a predetermined time or by supplying a predetermined amount of wastewater to the biological fixed bed. A biological wastewater treatment method, comprising: performing a backwashing treatment of the biological fixed bed using an inert gas after performing, and removing surplus organisms in the fixed bed in the backwashing treatment.
製造プロセスから排出されたフッ素を含有する排水を生物学的に処理するに当たって、
前記排水を凝集沈殿槽に供給して凝集沈殿処理によりアルカリ土類金属の塩類を沈殿させ、
沈殿処理後の排水をそのままの状態で、好気性生物固定床、純酸素吹き込み手段及び不活性ガス吹き込み手段を備えた生物処理槽に直接に供給し、
前記生物処理槽において、前記好気性生物固定床における純酸素を用いた生物処理を行いかつ、一定時間にわたって生物処理を行った後あるいは所定量の排水を生物固定床に供給して生物処理を行った後、不活性ガスを用いた前記生物固定床の逆洗処理を実施し、前記逆洗処理では固定床内の余剰生物を除去すること
を特徴とする生物排水処理方法。
In treating biologically the wastewater containing fluorine discharged from the manufacturing process,
Supplying the waste water to a coagulation sedimentation tank to precipitate alkaline earth metal salts by coagulation sedimentation treatment,
The wastewater after the precipitation treatment is directly supplied to a biological treatment tank equipped with an aerobic biological fixed bed, pure oxygen blowing means and inert gas blowing means,
In the biological treatment tank, the biological treatment using pure oxygen in the aerobic biological fixed bed is performed, and the biological treatment is performed for a predetermined time or by supplying a predetermined amount of waste water to the biological fixed bed. Then, the biological wastewater treatment method is characterized in that the biological fixed bed using an inert gas is backwashed, and the surplus organisms in the fixed bed are removed in the backwashing treatment.
製造プロセスから排出されたフッ素を含有する排水を生物学的に処理する装置であって、
前記排水からアルカリ土類金属の塩類を沈殿させる凝集沈殿槽、及び
前記凝集沈殿槽からの排水がそのままの状態で直接に供給される、嫌気性生物固定床及び不活性ガス吹き込み手段を備えた嫌気性生物固定床装置
を含んでなり、かつ
一定時間にわたって生物処理を行った後あるいは所定量の排水を生物固定床に供給して生物処理を行った後、不活性ガスを用いた前記生物固定床の逆洗処理を実施し、前記逆洗処理では固定床内の余剰生物を除去すること
を特徴とする生物排水処理装置。
The wastewater containing fluorine discharged from the manufacturing process a biologically processing apparatus,
Coagulation sedimentation tank for precipitating alkaline earth metal salts from the waste water, and anaerobic organism fixed bed to which the waste water from the coagulation sedimentation tank is directly supplied as it is and anaerobic means equipped with inert gas blowing means The biological fixed bed using an inert gas after having been subjected to biological treatment for a certain period of time or after biological treatment by supplying a predetermined amount of wastewater to the biological fixed bed. The biological wastewater treatment apparatus is characterized in that the backwash process is performed, and surplus organisms in the fixed bed are removed in the backwash process.
JP27238196A 1996-10-15 1996-10-15 Biological treatment method and apparatus for waste water Expired - Fee Related JP3818706B2 (en)

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JP3818706B2 true JP3818706B2 (en) 2006-09-06

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