JPH05169090A - Device for supplying nitrification bacteria in biological activated carbon treatment tower - Google Patents

Device for supplying nitrification bacteria in biological activated carbon treatment tower

Info

Publication number
JPH05169090A
JPH05169090A JP3340548A JP34054891A JPH05169090A JP H05169090 A JPH05169090 A JP H05169090A JP 3340548 A JP3340548 A JP 3340548A JP 34054891 A JP34054891 A JP 34054891A JP H05169090 A JPH05169090 A JP H05169090A
Authority
JP
Japan
Prior art keywords
activated carbon
nitrifying bacteria
treatment tower
biological
culture tank
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
Application number
JP3340548A
Other languages
Japanese (ja)
Inventor
Hiroshi Tsukura
洋 津倉
Keiichi Tsukitari
圭一 月足
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.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing 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 Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP3340548A priority Critical patent/JPH05169090A/en
Publication of JPH05169090A publication Critical patent/JPH05169090A/en
Pending legal-status Critical Current

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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

  • Biological Treatment Of Waste Water (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

PURPOSE:To provide the device which enables early starting of a biological activated carbon treatment tower utilized for purifying treatment of water and also performs excellent treatment in removal performance of trace organic substance or the like and removal performance of ammoniac nitrogen. CONSTITUTION:A biological activated carbon treatment tower 2 packed with a granular activated carbon 3 is provided. Separately a nitrification bacterial culture tank 4 is provided. Moreover a mechanism for supplying oxygen to nitrification bacteria 6 in the tank and an agitating mechanism are equipped in the nitrification bacteria culture tank 4. Furthermore a device for supplying nitrification bacteria is equipped with both a return system 11 for feeding one part of granular activated carbon 3 to the culture tank 4 from the treatment tower 2 and a supply system 12 for feeding granular activated carbon 3 deposited with cultured nitrification bacteria 6 to the treatment tower 2 from the culture tank 4.

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、水道水の浄化処理に利
用される生物活性炭処理塔(生物濾過処理塔を含む)へ
の硝化菌供給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 device for supplying nitrifying bacteria to a biological activated carbon treatment tower (including a biological filtration treatment tower) used for purification of tap water.

【0002】[0002]

【従来の技術】一般に河川などから取水した原水とか下
水2次処理水を浄化するに際して、先ず凝集沈殿池で原
水中に凝集剤を注入,混合し、撹拌及び滞留処理により
原水中の懸濁物質(砂,粘土,藻類等の有機物等)を凝
集して沈澱,分離する。このプロセスでは殺藻処理や
鉄,マンガンなどの色度成分の除去を目的とした塩素処
理が組み込まれている。特に大都市近郊においては、河
川の汚濁が著しいため、アンモニアや、発ガン性物質の
THM(トリハロメタン)の前駆物質であるフミン質を
含む色度成分の含有率が高く、塩素処理により塩素とア
ンモニアが反応してクロラミンを生成し、必要以上の塩
素を消費してしまう結果、塩素注入率が高くなってTH
M生成能(THMFP)が増大する。
2. Description of the Related Art Generally, when purifying raw water or secondary sewage treated water taken from rivers, etc., first, a flocculant is injected and mixed in raw water in a flocculation sedimentation tank, and suspended substances in raw water are treated by stirring and retaining. (Sand, clay, algae, and other organic substances) are aggregated, precipitated, and separated. This process incorporates algae treatment and chlorine treatment for the purpose of removing chromaticity components such as iron and manganese. Particularly in the suburbs of large cities, rivers are highly polluted, so the content of ammonia and chromaticity components including humic substances, which are precursors of the carcinogenic THM (trihalomethane), is high. React to produce chloramine and consume more chlorine than necessary, resulting in a high chlorine injection rate and TH
Increases the ability to generate M (THMFP).

【0003】このような背景から、近年上述した物質の
除去を目的として高度浄水処理システムを浄水プロセス
に組み込む方式が行われるようになってきた。この高度
浄水処理方法には、オゾン処理や生物活性炭処理があ
り、例えば塩素処理の代替としてオゾン処理塔によりオ
ゾン処理を行い、更に活性炭処理塔もしくは生物濾過塔
により色度成分などを除去する。この後、砂濾過池等で
濾過し、浄水池に送水する。
From such a background, in recent years, a method of incorporating an advanced water purification system into the water purification process has been used for the purpose of removing the above-mentioned substances. This advanced water purification method includes ozone treatment and biological activated carbon treatment. For example, as an alternative to chlorine treatment, ozone treatment is performed by an ozone treatment tower, and further a chromaticity component is removed by an activated carbon treatment tower or biological filtration tower. After that, it is filtered with a sand filter, etc. and sent to a water purification tank.

【0004】活性炭処理塔に充填される粒状活性炭は、
硝化菌などの微生物を表面に繁殖させたものであり、流
入される水中の微量有機物の吸着及び除去だけでなく、
アンモニアの除去も可能となっている。更に生物活性炭
処理の前にオゾン処理を行うことにより、負荷変動に対
する許容度や活性炭の寿命の向上をはかることができ
る。
The granular activated carbon packed in the activated carbon treatment tower is
Microorganisms such as nitrifying bacteria are propagated on the surface, and not only the adsorption and removal of trace organic substances in the inflowing water,
It is also possible to remove ammonia. Further, by performing the ozone treatment before the biological activated carbon treatment, it is possible to improve the tolerance against load fluctuation and the life of the activated carbon.

【0005】[0005]

【発明が解決しようとする課題】上記の高度浄水処理シ
ステムに用いられる生物活性炭処理では、活性炭処理塔
の立ち上げに時間がかかることが問題となる。つまり活
性炭処理塔の運転開始の際とか、活性炭交換後の運転再
開の際に、活性炭の表面に微生物を増殖させ、その生物
相を安定させるために立ち上げ運転を行う必要がある。
そして活性炭表面における微生物の増殖速度が低下した
場合、換言すれば硝化菌の活性度が低下した場合には、
前記立ち上げ時間の延長に加えて微生物によるアンモニ
アの除去率が著しく低下してしまうという難点が生じ
る。
In the biological activated carbon treatment used in the above advanced water treatment system, it takes a long time to start up the activated carbon treatment tower. That is, at the time of starting the operation of the activated carbon treatment tower or restarting the operation after exchanging the activated carbon, it is necessary to perform the start-up operation in order to grow the microorganisms on the surface of the activated carbon and stabilize the biota.
And when the growth rate of microorganisms on the surface of activated carbon is decreased, in other words, when the activity of nitrifying bacteria is decreased,
In addition to the extension of the startup time, there is a problem that the removal rate of ammonia by microorganisms is significantly reduced.

【0006】上記硝化菌の活性は、水温にも影響される
ことが知られており、夏期の高水温時に比して水温が1
0℃以下に下がる冬期は硝化菌の活性度が低下してしま
い、河川等の水量低減に伴ってアンモニア濃度は逆に増
加するという現象が発生する。特に硝化菌の増殖速度
は、有機物等を除去する他の微生物に比して相当遅くて
少なくとも1〜3日程度は必要であり、特に水温が20
℃の時の硝化菌による定常的なアンモニア除去処理が達
成される期間に比べて、水温が10℃の場合には同定常
的処理に要する期間が2倍以上もかかってしまうことが
あり、アンモニア処理効率が著しく悪化するという問題
点が生じる。
It is known that the activity of the above nitrifying bacteria is also affected by the water temperature, and the water temperature is 1 when compared to the high water temperature in summer.
The activity of nitrifying bacteria decreases in the winter when the temperature falls below 0 ° C, and a phenomenon occurs in which the concentration of ammonia increases conversely as the amount of water in rivers decreases. In particular, the growth rate of nitrifying bacteria is considerably slower than that of other microorganisms that remove organic substances, etc., and it is necessary for at least about 1 to 3 days.
When the water temperature is 10 ° C., the time required for the stationary treatment may be more than twice as long as the time required for the steady ammonia removal process by nitrifying bacteria at the temperature of ℃. There is a problem that the processing efficiency is significantly deteriorated.

【0007】更に表面に生物相が形成された活性炭は、
生物相により微量有機物の吸着,除去性能が阻害される
可能性があり、生物活性炭処理を行うにあたって、この
点も考慮する必要がある。
Further, the activated carbon having a biota formed on the surface is
There is a possibility that the biota may impair the adsorption and removal performance of trace organic substances, and it is necessary to take this into consideration when performing treatment with biological activated carbon.

【0008】本発明はこれらの問題点に鑑み、生物活性
炭処理塔の早期立ち上げを可能とし、しかも微量有機物
等の除去性能およびアンモニア態窒素の除去性能ともに
優れた処理を行える装置を提供することを目的とするも
のである。
In view of these problems, the present invention provides an apparatus which enables early startup of a biological activated carbon treatment tower, and which is capable of treating both trace organic substances and ammonia nitrogen with excellent removal performance. The purpose is.

【0009】[0009]

【課題を解決するための手段】上記の目的を達成するた
めに、先ず請求項1により、粒状活性炭が充填された生
物活性炭処理塔とは別途に硝化菌培養槽を配設するとと
もに、該硝化菌培養槽に、槽内の硝化菌への酸素供給機
構及び撹拌機構を配備し、更に上記生物活性炭処理塔か
ら硝化菌培養槽へ粒状活性炭の一部を送り込む返送系
と、硝化菌培養槽から生物活性炭処理塔へ培養された硝
化菌が付着された粒状活性炭を送り込む供給系とを具備
した生物活性炭処理塔の硝化菌供給装置の構成にしてあ
る。又、請求項2により、上記生物活性炭処理塔に代え
て微生物活性の高い生物濾材が充填された生物濾過処理
塔を用いており、請求項3により、前記硝化菌培養槽
を、20℃〜30℃の範囲に保持された恒温槽内に配置
してあり、更に請求項4により、前記硝化菌培養槽に、
アンモニアを含有する原水を一定時間毎又は連続的に供
給する原水供給部を配備した構成にしてある。
In order to achieve the above object, first, according to claim 1, a nitrifying bacteria culture tank is provided separately from a biological activated carbon treatment tower filled with granular activated carbon, and the nitrification is performed. The bacterial culture tank is provided with an oxygen supply mechanism and a stirring mechanism for nitrifying bacteria in the tank, and further, a return system for sending a part of the granular activated carbon from the biological activated carbon treatment tower to the nitrifying bacteria culture tank, and from the nitrifying bacteria culture tank A nitrifying bacteria supply device for a biological activated carbon treatment tower is provided with a supply system for feeding granular activated carbon to which the cultured nitrifying bacteria adhered to the biological activated carbon treatment tower. Further, according to claim 2, a biological filtration treatment tower filled with a biological filter medium having high microbial activity is used instead of the biological activated carbon treatment tower, and according to claim 3, the nitrifying bacteria culture tank is maintained at 20 ° C to 30 ° C. Placed in a constant temperature bath maintained in the range of ° C, further according to claim 4, in the nitrifying bacteria culture tank,
A raw water supply unit for supplying raw water containing ammonia is provided at regular intervals or continuously.

【0010】[0010]

【作用】かかる構成によれば、平常の原水処理時には原
水が生物活性炭処理塔又は生物濾過処理塔内の粒状活性
炭もしくは生物濾材により浄化処理されるとともに、こ
の粒状活性炭とか生物濾材の表面に繁殖している硝化菌
の作用により、微量有機物の吸着,除去だけでなく、ア
ンモニアも除去される。
According to this structure, during normal raw water treatment, the raw water is purified by the granular activated carbon or the biological filter medium in the biological activated carbon treatment tower or the biological filtration treatment tower, and at the same time, the granular activated carbon or the surface of the biological filter medium is propagated. Due to the action of nitrifying bacteria, not only the trace organic substances are adsorbed and removed, but also ammonia is removed.

【0011】そして生物活性炭処理塔もしくは生物濾過
処理塔から返送系を介して硝化菌培養槽に硝化菌が付着
した粒状活性炭もしくは生物濾材の一部を返送すると、
硝化菌培養槽内での曝気と撹拌により、好気性菌である
硝化菌に酸素が供給されて該硝化菌が増殖し、粒状活性
炭もしくは生物濾材の表面に増殖した硝化菌が多量に付
着する。この時に原水供給部からアンモニアを含有する
原水を一定時間毎又は連続的に供給することにより、硝
化菌の増殖効率が向上する。
Then, when a part of the granular activated carbon or the biological filter medium with the nitrifying bacteria adhered to the nitrifying bacteria culture tank is returned from the biological activated carbon treatment tower or the biological filtration treatment tower through the return system,
Due to aeration and agitation in the nitrifying bacteria culture tank, oxygen is supplied to the nitrifying bacteria which are aerobic bacteria and the nitrifying bacteria grow, and a large amount of the grown nitrifying bacteria adhere to the surface of the granular activated carbon or the biological filter medium. At this time, by supplying raw water containing ammonia from the raw water supply unit at regular intervals or continuously, the growth efficiency of nitrifying bacteria is improved.

【0012】次に供給系を介して硝化菌が多量に付着し
た粒状活性炭もしくは生物濾材を生物活性炭処理塔又は
生物濾過処理塔に戻すことにより、生物活性炭処理塔も
しくは生物濾過処理塔内の活性炭表面における微生物の
付着量が増大して硝化菌の活性度が向上し、その結果と
して原水のアンモニアの除去率が高められる。
Next, the activated carbon surface in the biological activated carbon treatment tower or the biological filtration treatment tower is returned to the biological activated carbon treatment tower or the biological filtration treatment tower by returning the granular activated carbon or the biological filtration medium having a large amount of nitrifying bacteria attached thereto through the supply system. The amount of attached microorganisms increases, and the activity of nitrifying bacteria increases, and as a result, the removal rate of ammonia in raw water is increased.

【0013】[0013]

【実施例】以下、本発明にかかる生物活性炭処理塔の硝
化菌供給装置の一実施例を説明する。図1に示した本実
施例の概略図において、1は原水、2は原水1が流入さ
れる生物活性炭処理塔であり、この生物活性炭処理塔2
内に粒状活性炭3が充填されている。尚、上記生物活性
炭処理塔2に代えて生物濾過処理塔を用いることも可能
であり、この場合には該生物濾過処理塔内に微生物活性
の高い生物濾材が充填される。
EXAMPLES An example of a nitrifying bacteria supply device for a biological activated carbon treatment tower according to the present invention will be described below. In the schematic view of this embodiment shown in FIG. 1, 1 is a raw water, 2 is a biological activated carbon treatment tower into which the raw water 1 is introduced, and this biological activated carbon treatment tower 2
Granular activated carbon 3 is filled therein. It is also possible to use a biological filtration treatment tower in place of the biological activated carbon treatment tower 2, and in this case, a biological filter medium having a high microbial activity is filled in the biological filtration treatment tower.

【0014】一方、4は生物活性炭処理塔2とは別途に
配設した硝化菌培養槽であり、この硝化菌培養槽4は全
体的に恒温槽5内に配置されている。該恒温槽5によっ
て硝化菌培養槽4は20〜30℃の範囲に保持されてい
る。
On the other hand, 4 is a nitrifying bacteria culture tank which is arranged separately from the biological activated carbon treatment tower 2, and this nitrifying bacteria culture tank 4 is entirely arranged in a constant temperature tank 5. The nitrifying bacteria culture tank 4 is kept in the range of 20 to 30 ° C. by the constant temperature tank 5.

【0015】硝化菌培養槽4内には、活性炭もしくは生
物濾材に付着させる硝化菌6を流入し、好気性菌である
硝化菌に酸素を供給するため、硝化菌培養槽4の内方底
部に散気管7が配置されている。この散気管7には、外
部に配備されたブロワ8から空気が送り込まれるように
なっている。9はアンモニアを含有する原水を一定時間
毎又は連続的に硝化菌培養槽4に供給する原水供給部で
ある。
Into the nitrifying bacteria culture tank 4, nitrifying bacteria 6 adhering to the activated carbon or the biological filter medium are introduced and oxygen is supplied to the nitrifying bacteria which are aerobic bacteria. An air diffuser 7 is arranged. Air is sent to the air diffuser 7 from a blower 8 provided outside. Reference numeral 9 denotes a raw water supply unit for supplying raw water containing ammonia to the nitrifying bacteria culture tank 4 at regular intervals or continuously.

【0016】上記の硝化菌培養槽4,恒温槽5,散気管
7及びブロワ8によって硝化菌供給装置10が構成され
ている。
A nitrifying bacteria supply device 10 is constituted by the above-mentioned nitrifying bacteria culture tank 4, constant temperature tank 5, air diffuser 7 and blower 8.

【0017】11は生物活性炭処理塔2から硝化菌培養
槽4へ前記粒状活性炭3もしくは生物濾材の一部を送り
込む返送系であり、12は逆に硝化菌培養槽4から生物
活性炭処理塔2へ硝化菌が培養された粒状活性炭3もし
くは生物濾材を送り込む供給系である。この供給系12
の中途部には、ポンプ13及び流量調整弁14が設けら
れている。15は逆洗用排水口、16は処理水流出口で
ある。
Numeral 11 is a return system for feeding the granular activated carbon 3 or a part of the biological filter medium from the biological activated carbon treatment tower 2 to the nitrifying bacteria culture tank 4, and 12 is the reverse from the nitrifying bacteria culture tank 4 to the biological activated carbon treatment tower 2. It is a supply system for feeding the granular activated carbon 3 in which the nitrifying bacteria have been cultured or the biological filter medium. This supply system 12
A pump 13 and a flow rate adjusting valve 14 are provided in the middle of the area. Reference numeral 15 is a backwash drain, and 16 is a treated water outlet.

【0018】かかる構成によれば、平常の原水処理を行
う場合には、原水1が生物活性炭処理塔2又は図示しな
い生物濾過処理塔に流入して、粒状活性炭3もしくは生
物濾材により浄化処理されるとともに、この粒状活性炭
3とか生物濾材の表面に繁殖している硝化菌の作用によ
り、微量有機物の吸着,除去だけでなく、アンモニアも
除去される。尚、生物活性炭処理の前にオゾン処理を行
うことによって粒状活性炭3の寿命が向上する。
According to this structure, when the normal raw water treatment is carried out, the raw water 1 flows into the biological activated carbon treatment tower 2 or a biological filtration treatment tower (not shown) and is purified by the granular activated carbon 3 or the biological filter medium. At the same time, by the action of the granular activated carbon 3 and the nitrifying bacteria that propagate on the surface of the biological filter medium, not only the trace organic substances are adsorbed and removed, but also ammonia is removed. In addition, the life of the granular activated carbon 3 is improved by performing the ozone treatment before the biological activated carbon treatment.

【0019】他方で、生物活性炭処理塔2もしくは生物
濾過処理塔の処理能力を高めるために、該生物活性炭処
理塔2もしくは生物濾過処理塔から返送系11を介して
硝化菌培養槽4に硝化菌が付着した粒状活性炭3もしく
は生物濾材の一部を返送する。この硝化菌培養槽4は恒
温槽5によって20〜30℃の範囲に保持されており、
更に外部に配備されたブロワ8から硝化菌培養槽の内方
底部に配置された散気管7に空気を供給することによ
り、硝化菌培養槽4内で曝気と撹拌が行われ、好気性菌
である硝化菌6に酸素が供給されて、該硝化菌6が増殖
する。
On the other hand, in order to enhance the treatment capacity of the biological activated carbon treatment tower 2 or the biological filtration treatment tower, the nitrifying bacteria are transferred from the biological activated carbon treatment tower 2 or the biological filtration treatment tower to the nitrifying bacteria culture tank 4 through the return system 11. The granular activated carbon 3 or the part of the biological filter material attached with is returned. This nitrifying bacteria culture tank 4 is kept in a temperature range of 20 to 30 ° C. by a constant temperature tank 5.
Furthermore, by supplying air from the blower 8 arranged outside to the air diffuser 7 arranged at the inner bottom of the nitrifying bacteria culture tank, aeration and agitation are performed in the nitrifying bacteria culture tank 4, and aerobic bacteria are generated. Oxygen is supplied to a certain nitrifying bacterium 6, and the nitrifying bacterium 6 grows.

【0020】図2の模式図に示したように、上記曝気と
撹拌によって粒状活性炭3もしくは図示しない生物濾材
の表面に、増殖した硝化菌6,6が多量に付着する。こ
の時、原水供給部9からアンモニアを含有する原水を一
定時間毎又は連続的に供給することにより、硝化菌6の
増殖効率が向上する。
As shown in the schematic view of FIG. 2, a large amount of the grown nitrifying bacteria 6, 6 adhere to the surface of the granular activated carbon 3 or the biological filter medium (not shown) by the aeration and stirring. At this time, by supplying the raw water containing ammonia from the raw water supply unit 9 at regular intervals or continuously, the growth efficiency of the nitrifying bacteria 6 is improved.

【0021】次に供給系12に設けられたポンプ13を
稼働しながら流量調整弁14を適度に開くことにより、
硝化菌6が多量に付着した粒状活性炭3もしくは生物濾
材が生物活性炭処理塔2もしくは生物濾過処理塔に戻る
ので、この生物活性炭処理塔2又は生物濾過処理塔内の
活性炭表面における微生物の付着量が増大して硝化菌の
活性度が向上し、その結果として原水1のアンモニアの
除去率を高めることができる。
Next, while operating the pump 13 provided in the supply system 12, by appropriately opening the flow rate adjusting valve 14,
Since the granular activated carbon 3 or the biological filter medium having a large amount of nitrifying bacteria 6 attached thereto returns to the biological activated carbon treatment tower 2 or the biological filtration treatment tower, the amount of microorganisms attached on the surface of the activated carbon in the biological activated carbon treatment tower 2 or the biological filtration treatment tower is As a result, the activity of nitrifying bacteria is improved, and as a result, the removal rate of ammonia in the raw water 1 can be increased.

【0022】上記硝化菌6の活性は水温にも影響され、
夏期の高水温時に比して水温が10℃以下に下がる冬期
には硝化菌6の活性度が低下し易いため、冬期に本実施
例にかかる硝化菌供給装置10を用いることが有効であ
り、それに伴って水温低下時における硝化菌6による定
常的なアンモニア除去処理を達成する時間が短縮され
る。そして処理水は処理水流出口16から流出する。
The activity of the nitrifying bacteria 6 is also affected by the water temperature,
Since the activity of the nitrifying bacteria 6 tends to decrease in the winter when the water temperature falls below 10 ° C. as compared to the high water temperature in the summer, it is effective to use the nitrifying bacteria supply device 10 according to the present embodiment in the winter. Along with this, the time required to achieve the regular ammonia removal treatment by the nitrifying bacteria 6 when the water temperature drops is shortened. Then, the treated water flows out from the treated water outlet 16.

【0023】更に生物活性炭処理塔2の運転開始の際、
又は活性炭交換後の運転再開の際に、活性炭の表面に微
生物を増殖させ、生物相を安定させるための立ち上げ運
転を行う場合にあっても、硝化菌供給装置10から硝化
菌6を供給することによって微生物の増殖速度が加速さ
れるので、立ち上げ運転時間を短縮することが可能とな
る。
Further, when the operation of the biological activated carbon treatment tower 2 is started,
Alternatively, when the operation is restarted after the activated carbon is exchanged, the nitrifying bacteria 6 are supplied from the nitrifying bacteria supply device 10 even when the microorganisms are grown on the surface of the activated carbon and the startup operation for stabilizing the biota is performed. As a result, the growth rate of microorganisms is accelerated, and the start-up operation time can be shortened.

【0024】図3は上記生物活性炭処理塔2内での硝化
菌層の厚みの変化を示す模式図であり、図中のA層は硝
化菌層、B層はTHM生成能除去層である。前記したよ
うに生物活性炭処理塔2から返送系11を介して硝化菌
培養槽4に硝化菌が付着した粒状活性炭3の一部を返送
すると、硝化菌層であるA層が厚みが小さくなり、その
分だけ流入する原水の処理量が高められ、又、硝化菌層
Aの厚みを大きくすることによって前記したように該硝
化菌の活性によりアンモニアの除去率が高められる。従
って原水1の状態とか生物活性炭処理塔2の処理能力等
を勘案して、硝化菌供給装置10に対する粒状活性炭2
もしくは生物濾材の返送量と、硝化菌培養槽4から生物
活性炭処理塔2に対する硝化菌の供給量を決定すること
により、アンモニア濃度の負荷変動に対応することがで
きる。
FIG. 3 is a schematic diagram showing the change in the thickness of the nitrifying bacteria layer in the biological activated carbon treatment tower 2, wherein A layer is the nitrifying bacteria layer and B layer is the THM-producing ability removing layer. As described above, when part of the granular activated carbon 3 having nitrifying bacteria adhered to the nitrifying bacteria culture tank 4 is returned from the biological activated carbon treatment tower 2 to the nitrifying bacteria culture tank 4, the thickness of the layer A, which is the nitrifying bacteria layer, becomes small, The amount of raw water that flows in is increased by that amount, and by increasing the thickness of the nitrifying bacteria layer A, the ammonia removal rate is increased by the activity of the nitrifying bacteria as described above. Therefore, in consideration of the state of raw water 1 and the treatment capacity of the biological activated carbon treatment tower 2, the granular activated carbon 2 for the nitrifying bacteria supply device 10
Alternatively, by determining the returned amount of the biological filter medium and the supplied amount of the nitrifying bacteria from the nitrifying bacteria culture tank 4 to the biological activated carbon treatment tower 2, it is possible to cope with the load fluctuation of the ammonia concentration.

【0025】更に図3に示すように、アンモニア除去能
とTHMFP除去能との関係をモニタリングした結果、
主に処理塔の上層にてアンモニアの除去が行われ、主に
処理塔の中層から下層にわたってTHMFPの除去が行
われることが確認された。
Further, as shown in FIG. 3, as a result of monitoring the relationship between the ammonia removing ability and the THMFP removing ability,
It was confirmed that ammonia was mainly removed in the upper layer of the treatment tower, and THMFP was mainly removed from the middle layer to the lower layer of the treatment tower.

【0026】[0026]

【発明の効果】以上説明したように、本発明によれば、
生物活性炭処理塔もしくは生物濾過処理塔から返送系を
介して硝化菌培養槽に硝化菌が付着した粒状活性炭もし
くは生物濾材の一部を返送することにより、硝化菌培養
槽内で硝化菌が増殖するので、供給系を介して硝化菌が
多量に付着した粒状活性炭もしくは生物濾材を生物活性
炭処理塔又は生物濾過処理塔に戻すことにより、生物活
性炭処理塔もしくは生物濾過処理塔内の活性炭表面にお
ける微生物の付着量を増大させて硝化菌の活性度が向上
し、原水のアンモニア除去率を高めることができる。特
に夏期の高水温時に比して水温が下がる冬期には硝化菌
の活性度が低下し易いため、冬期に本発明を適用するこ
とが有効であり、それに伴って水温低下時における硝化
菌による定常的なアンモニア除去処理を達成する時間を
短縮することが出来る。
As described above, according to the present invention,
The nitrifying bacteria grow in the nitrifying bacteria culture tank by returning part of the granular activated carbon or the biological filter material on which the nitrifying bacteria adhere to the nitrifying bacteria culture tank from the biological activated carbon treatment tower or the biological filtration processing tower through the return system. Therefore, by returning the granular activated carbon or biological filter medium with a large amount of nitrifying bacteria attached to the biological activated carbon treatment tower or the biological filtration treatment tower through the supply system, the microorganisms on the activated carbon surface in the biological activated carbon treatment tower or the biological filtration treatment tower are The activity of nitrifying bacteria is improved by increasing the adhered amount, and the ammonia removal rate of raw water can be increased. In particular, the activity of nitrifying bacteria is likely to decrease in the winter when the water temperature is lower than when the water temperature is high in the summer, so it is effective to apply the present invention in the winter, and accordingly, the steady state by the nitrifying bacteria at the time when the water temperature decreases It is possible to shorten the time for achieving the effective ammonia removal treatment.

【0027】又、生物活性炭処理塔もしくは生物濾過処
理塔の逆洗時に、誤操作によって硝化菌の付着した粒状
活性炭又は濾材が流出した場合には、本発明にかかる硝
化菌供給装置をタイムリーに利用することにより、処理
塔に直ちに硝化菌を補充することが可能であり、アンモ
ニア除去率の低下を防止することができる。
Further, when the granular activated carbon or the filter medium to which the nitrifying bacteria adhere is erroneously discharged during backwashing of the biological activated carbon treatment tower or the biological filtration treatment tower, the nitrifying bacteria supply device according to the present invention can be used in a timely manner. By doing so, it is possible to immediately replenish the treatment tower with nitrifying bacteria and prevent a decrease in the ammonia removal rate.

【0028】更に生物活性炭処理塔の運転開始の際とか
活性炭交換後の運転再開の際に、活性炭の表面の微生物
増殖速度を加速することが出来るので、立ち上げ運転時
間を短縮することが可能とし、しかも微量有機物等の除
去性能及びアンモニア態窒素の除去性能ともに優れた処
理を行える装置が提供される。
Further, at the time of starting the operation of the biological activated carbon treatment tower or restarting the operation after exchanging the activated carbon, it is possible to accelerate the growth rate of microorganisms on the surface of the activated carbon, which makes it possible to shorten the startup operation time. In addition, an apparatus is provided that can perform a treatment that is excellent in the removal performance of trace organic substances and the like and the removal performance of ammonia nitrogen.

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

【図1】本発明にかかる生物活性炭処理塔の硝化菌供給
装置の一実施例を示す概略図。
FIG. 1 is a schematic diagram showing an embodiment of a nitrifying bacteria supply device for a biological activated carbon treatment tower according to the present invention.

【図2】粒状活性炭に対する硝化菌の付着状態を示す模
式図。
FIG. 2 is a schematic diagram showing a state of adhesion of nitrifying bacteria to granular activated carbon.

【図3】生物活性炭処理塔内での硝化菌層の厚みの変化
を示す模式図。
FIG. 3 is a schematic diagram showing changes in the thickness of a nitrifying bacteria layer in a biological activated carbon treatment tower.

【符号の説明】[Explanation of symbols]

1…原水、2…生物活性炭処理塔、3…粒状活性炭、4
…硝化菌培養槽、5…恒温槽、6…硝化菌、7…散気
管、8…ブロワ、9…原水供給部、10…硝化菌供給装
置、11…返送系、12…供給系、13…ポンプ、14
…流量調整弁、15…逆洗用排水口、16…処理水流出
口。
1 ... Raw water, 2 ... Biological activated carbon treatment tower, 3 ... Granular activated carbon, 4
... Nitrifying bacteria culture tank, 5 ... Constant temperature tank, 6 ... Nitrifying bacteria, 7 ... Air diffuser, 8 ... Blower, 9 ... Raw water supply unit, 10 ... Nitrifying bacteria supply device, 11 ... Return system, 12 ... Supply system, 13 ... Pump, 14
... Flow rate adjusting valve, 15 ... Backwash drain port, 16 ... Treated water outlet.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 粒状活性炭が充填された生物活性炭処理
塔とは別途に硝化菌培養槽を配設するとともに、該硝化
菌培養槽に、槽内の硝化菌への酸素供給機構及び撹拌機
構を配備し、更に上記生物活性炭処理塔から硝化菌培養
槽へ粒状活性炭の一部を送り込む返送系と、硝化菌培養
槽から生物活性炭処理塔へ培養された硝化菌が付着され
た粒状活性炭を送り込む供給系とを具備して成ることを
特徴とする生物活性炭処理塔の硝化菌供給装置。
1. A nitrifying bacteria culture tank is provided separately from the biological activated carbon treatment tower filled with granular activated carbon, and the nitrifying bacteria culture tank is provided with an oxygen supply mechanism and a stirring mechanism for the nitrifying bacteria in the tank. A supply system that deploys and sends a part of the granular activated carbon from the biological activated carbon treatment tower to the nitrifying bacteria culture tank and a granular activated carbon to which the cultured nitrifying bacteria are attached from the nitrification bacteria culture tank to the biological activated carbon treatment tower A system for supplying nitrifying bacteria to a biological activated carbon treatment tower, comprising:
【請求項2】 上記生物活性炭処理塔に代えて、微生物
活性の高い生物濾材が充填された生物濾過処理塔を用い
た請求項1記載の生物活性炭処理塔の硝化菌供給装置。
2. The nitrifying bacteria supply device for a biological activated carbon treatment tower according to claim 1, wherein a biological filtration treatment tower filled with a biological filter medium having a high microbial activity is used in place of the biological activated carbon treatment tower.
【請求項3】 前記硝化菌培養槽を、20℃〜30℃の
範囲に保持された恒温槽内に配置した請求項1記載の生
物活性炭処理塔の硝化菌供給装置。
3. The nitrifying bacteria supply device for a biological activated carbon treatment tower according to claim 1, wherein the nitrifying bacteria culture tank is arranged in a constant temperature tank maintained in a range of 20 ° C. to 30 ° C.
【請求項4】 前記硝化菌培養槽に、アンモニアを含有
する原水を一定時間毎又は連続的に供給する原水供給部
を配備した請求項1記載の生物活性炭処理塔の硝化菌供
給装置。
4. The nitrifying bacteria supply device for a biological activated carbon treatment tower according to claim 1, wherein the nitrifying bacteria culture tank is provided with a raw water supply unit for supplying raw water containing ammonia at regular intervals or continuously.
JP3340548A 1991-12-24 1991-12-24 Device for supplying nitrification bacteria in biological activated carbon treatment tower Pending JPH05169090A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3340548A JPH05169090A (en) 1991-12-24 1991-12-24 Device for supplying nitrification bacteria in biological activated carbon treatment tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3340548A JPH05169090A (en) 1991-12-24 1991-12-24 Device for supplying nitrification bacteria in biological activated carbon treatment tower

Publications (1)

Publication Number Publication Date
JPH05169090A true JPH05169090A (en) 1993-07-09

Family

ID=18338045

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3340548A Pending JPH05169090A (en) 1991-12-24 1991-12-24 Device for supplying nitrification bacteria in biological activated carbon treatment tower

Country Status (1)

Country Link
JP (1) JPH05169090A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002028693A (en) * 2000-07-14 2002-01-29 Kurabo Ind Ltd Method for treating alkaline wastewater
JP2005512770A (en) * 2001-12-13 2005-05-12 インバイロンメンタル オペレイティング ソリューションズ インコーポレイテッド Wastewater treatment process and equipment
JP2006116376A (en) * 2004-10-19 2006-05-11 Chubu Electric Power Co Inc Waste water treatment system
JP2006212484A (en) * 2005-02-01 2006-08-17 Kurita Water Ind Ltd Pure water production method and apparatus
JP2010119937A (en) * 2008-11-18 2010-06-03 Shizunai Eiseisha:Kk Efficient nitrifying bacterium and purification process of urea and ammonia using the bacterium
JP2010194541A (en) * 2010-05-14 2010-09-09 Chubu Electric Power Co Inc Waste water treatment system
JP2011020059A (en) * 2009-07-16 2011-02-03 Kanaiwa:Kk Water treatment apparatus and water treatment method
JP2012055827A (en) * 2010-09-08 2012-03-22 Nippon Mizushori Giken:Kk Culture device and culture system
CN102701436A (en) * 2012-06-13 2012-10-03 哈尔滨工业大学宜兴环保研究院 Biological activated carbon filtering pond and method for advanced wastewater treatment by using biological activated carbon filtering pond
WO2014017429A1 (en) * 2012-07-26 2014-01-30 学校法人 東洋大学 Method and device for treating ammonia nitrogen-containing water at low temperature
JP2017104818A (en) * 2015-12-11 2017-06-15 水ing株式会社 Operation control method of water treatment installation

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002028693A (en) * 2000-07-14 2002-01-29 Kurabo Ind Ltd Method for treating alkaline wastewater
JP2005512770A (en) * 2001-12-13 2005-05-12 インバイロンメンタル オペレイティング ソリューションズ インコーポレイテッド Wastewater treatment process and equipment
JP4563134B2 (en) * 2004-10-19 2010-10-13 中部電力株式会社 Wastewater treatment system
JP2006116376A (en) * 2004-10-19 2006-05-11 Chubu Electric Power Co Inc Waste water treatment system
JP2006212484A (en) * 2005-02-01 2006-08-17 Kurita Water Ind Ltd Pure water production method and apparatus
JP2010119937A (en) * 2008-11-18 2010-06-03 Shizunai Eiseisha:Kk Efficient nitrifying bacterium and purification process of urea and ammonia using the bacterium
JP2011020059A (en) * 2009-07-16 2011-02-03 Kanaiwa:Kk Water treatment apparatus and water treatment method
JP2010194541A (en) * 2010-05-14 2010-09-09 Chubu Electric Power Co Inc Waste water treatment system
JP2012055827A (en) * 2010-09-08 2012-03-22 Nippon Mizushori Giken:Kk Culture device and culture system
CN102701436A (en) * 2012-06-13 2012-10-03 哈尔滨工业大学宜兴环保研究院 Biological activated carbon filtering pond and method for advanced wastewater treatment by using biological activated carbon filtering pond
WO2014017429A1 (en) * 2012-07-26 2014-01-30 学校法人 東洋大学 Method and device for treating ammonia nitrogen-containing water at low temperature
JPWO2014017429A1 (en) * 2012-07-26 2016-07-11 学校法人 東洋大学 Method and apparatus for low temperature treatment of ammonia nitrogen containing water
JP2017104818A (en) * 2015-12-11 2017-06-15 水ing株式会社 Operation control method of water treatment installation

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