JPH05228488A - Microbial column for water treatment - Google Patents

Microbial column for water treatment

Info

Publication number
JPH05228488A
JPH05228488A JP4072263A JP7226392A JPH05228488A JP H05228488 A JPH05228488 A JP H05228488A JP 4072263 A JP4072263 A JP 4072263A JP 7226392 A JP7226392 A JP 7226392A JP H05228488 A JPH05228488 A JP H05228488A
Authority
JP
Japan
Prior art keywords
reaction tank
microbial
partition
column
water
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
JP4072263A
Other languages
Japanese (ja)
Inventor
Koichi Mizuta
耕市 水田
Hideaki Hamada
英明 浜田
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.)
Hitachi Kiden Kogyo Ltd
Original Assignee
Hitachi Kiden Kogyo 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 Hitachi Kiden Kogyo Ltd filed Critical Hitachi Kiden Kogyo Ltd
Priority to JP4072263A priority Critical patent/JPH05228488A/en
Publication of JPH05228488A publication Critical patent/JPH05228488A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PURPOSE:To minimize the use of power and thereby supply the air efficiently to the deepest area so that bacterial treatment can be performed. CONSTITUTION:The interior of a bacterial reaction tank for waste water treatment of a required size is divided at least in more than two sections in a water depth direction using a shelf-like partition screen 4. In addition, an aeration device is provided in the each partitioned chamber divided in the form of a shelf using the partition screen 4. Further, each partition section is filled with a fixing microbe, and a column 11 is installed so that the microbial concentration becomes higher in the water depth direction. After that, a required minimum quantity of air is supplied to the each partitioned section.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は動力を最小限に抑えて高
水深域への空気の供給を効率的に行い、かつ生物処理を
行う水処理用微生物カラムに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a microbial column for water treatment, which minimizes power and efficiently supplies air to a deep water region and performs biological treatment.

【0002】[0002]

【従来の技術】家庭用、産業用、その他の排水中には多
量の有機物質が含有されている。この排水を生物処理を
して無公害化し、これを河川、湖沼等へ排水するように
している。この排水を生物処理する方法として曝気法が
一般的である。この曝気法は汚水中に空気を供給し、撹
拌しつつ曝気するもので、その一例として特公昭55−
29756号公報に開示のものがある。これは槽内に円
筒体を配設し、この円筒体内にスクリューを設け、これ
により円筒体内の汚水に空気を吹き込みつつ、下向流を
発生させ、槽底に達した後、円筒体の外周部を上向流と
して槽内を循環させる方法である。
2. Description of the Related Art A large amount of organic substances are contained in domestic, industrial and other waste water. This wastewater is biologically treated to be pollution-free, and then discharged to rivers, lakes and marshes. The aeration method is generally used as a method for biologically treating this wastewater. In this aeration method, air is supplied to wastewater and aeration is performed while stirring, and as an example, Japanese Patent Publication 55-
There is one disclosed in Japanese Patent Publication No. 29756. This is to arrange a cylindrical body in the tank, and to provide a screw in this cylindrical body, thereby blowing air into the wastewater in the cylindrical body to generate a downward flow, and after reaching the bottom of the tank, the outer circumference of the cylindrical body This is a method of circulating the inside of the tank by making the part upward flow.

【0003】[0003]

【発明が解決しようとする課題】大都市周辺においては
排水処理用の敷地を十分に取得することは近年困難にな
ってきている。それで、限られたスペースで年々増加す
る排水の処理を行うために高水深形の曝気槽が採用され
つつある。しかし高水深部での曝気はその水圧により多
大な動力を必要とし、かつその処理効率は悪いものとな
っている。
In recent years, it has become difficult to obtain sufficient land for wastewater treatment in the vicinity of a large city. Therefore, deep-water aeration tanks are being adopted to treat the increasing amount of wastewater in a limited space each year. However, aeration at high water depth requires a large amount of power due to the water pressure, and its treatment efficiency is poor.

【0004】本発明では投入曝気動力に対して汚水中に
有効な酸素供給を行うことを目的とする。
It is an object of the present invention to effectively supply oxygen into wastewater with respect to input aeration power.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、所要の大きさを有する排水処
理用生物反応槽において、反応槽内部を棚板状に仕切ス
クリーンでもって水深方向に少なくとも2槽以上に仕切
り、この仕切スクリーンにて棚板状に仕切られた各仕切
室内に曝気装置を設けたことを要旨とする。
The present invention has been made to achieve the above object, and in a biological reaction tank for wastewater treatment having a required size, the inside of the reaction tank is divided into a shelf plate by a partition screen. The gist is that at least two tanks are partitioned in the water depth direction, and an aeration device is provided in each partition chamber partitioned into shelf-like shapes by this partition screen.

【0006】[0006]

【作用】深い反応槽内を固液分離スクリーンをもって棚
板状にして水深方向に少なくとも2層以上に仕切り、こ
の各仕切室内に曝気装置を備え、かつ必要に応じて固定
化微生物を充填する。そして水深方向に微生物濃度が高
くなるようにし、各仕切室内へ必要最小限の空気を供給
するように制御する。これにより酸素の溶解性は水圧が
大きくなる高濃度域ほど溶け込み易いことが知られてい
ることと前記水深方向に微生物濃度が高くなるように固
定化微生物との使用により各々の深さにおいて微生物量
に見合った空気量を供給する。従ってこれにより大気へ
拡散される未利用空気量を低減することが可能となり、
投入曝気動力当りの微生物利用酸素量が増加し、効果的
な曝気処理が行える。
In the deep reaction tank, a solid-liquid separation screen is used to form a shelf plate, which is partitioned into at least two layers in the depth direction of the water, and each partition chamber is equipped with an aeration device and, if necessary, filled with immobilized microorganisms. Then, the concentration of microorganisms is increased in the water depth direction, and control is performed so that the minimum necessary air is supplied into each partition chamber. As a result, it is known that the solubility of oxygen is more likely to dissolve in a higher concentration range where the water pressure increases, and the amount of microorganisms at each depth is increased by using immobilized microorganisms so that the concentration of microorganisms increases in the depth direction. Supply the amount of air commensurate with. Therefore, it becomes possible to reduce the amount of unused air diffused into the atmosphere.
The amount of microbial oxygen used per input aeration power increases, and effective aeration treatment can be performed.

【0007】[0007]

【実施例】以下本発明水処理用微生物カラムを図示の実
施例にもとづいて説明する。図において11は所要の大
きさと深度を有する曝気反応槽で、この反応槽11内を
その水深方向に少なくとも2段以上に仕切るように仕切
スクリーン4を棚板状に用いて反応槽11内をその上部
より低濃度微生物反応槽1、中濃度微生物反応槽2、高
濃度微生物反応槽3とを順次仕切り、各仕切室の反応槽
1,2,3内に夫々曝気装置12を設ける。
EXAMPLE A microbial column for water treatment of the present invention will be described below with reference to the illustrated example. In the figure, 11 is an aeration reaction tank having a required size and depth, and the inside of the reaction tank 11 is divided by using partition screens 4 in a shelf shape so as to divide the inside of the reaction tank 11 into at least two stages in the depth direction. A low-concentration microbial reaction tank 1, a medium-concentration microbial reaction tank 2, and a high-concentration microbial reaction tank 3 are sequentially partitioned from the upper part, and aeration devices 12 are provided in the reaction tanks 1, 2 and 3 of each partition chamber.

【0008】また曝気反応槽1と別個に受水槽5を配置
し、この受水槽5内に供給された汚水を汚水ポンプ6及
び管13を介して最下段の高濃度微生物反応槽3内へ供
給する。この場合汚水が反応槽3内へその底部より均一
に供給されるように整流板7が設置される。
Further, a water receiving tank 5 is arranged separately from the aeration reaction tank 1, and the sewage supplied into the water receiving tank 5 is supplied into the lowermost high-concentration microbial reaction tank 3 through a sewage pump 6 and a pipe 13. To do. In this case, the current plate 7 is installed so that the sewage is uniformly supplied into the reaction tank 3 from the bottom thereof.

【0009】また各段の反応槽1,2,3に設置された
曝気装置12にはブロワー8より給気管14及び空気調
整バルブ9を介して供給し、各段槽内で曝気するが、こ
の給気量は各段反応槽にて夫々適量となるようバルブ9
にて制御される。
Further, the aeration device 12 installed in the reaction tanks 1, 2 and 3 of each stage is supplied from the blower 8 through the air supply pipe 14 and the air regulating valve 9 to aerate in each stage tank. The amount of air supply should be adjusted to the appropriate value in each stage of the reaction tank.
Controlled by.

【0010】最上段の反応槽1内には固液分離スクリー
ン10を設け、澄清水のみがこのスクリーン10より濾
過され排水されるようになす。
A solid-liquid separation screen 10 is provided in the uppermost reaction tank 1 so that only clear fresh water is filtered and drained from this screen 10.

【0011】上述の如く深層反応槽を水深方向に仕切り
各段仕切室の反応槽1,2,3には水深方向に固定化微
生物を充填して微生物カラムを構成する。微生物カラム
11は、反応槽仕切スクリーン4により深さ方向へ3槽
に区分し、それぞれの反応槽1,2,3に包括固定化活
性汚泥を充填するとともに深い反応槽ほど微生物量が多
くなるよう調整する。
As described above, the deep-layer reaction tank is partitioned in the water depth direction, and the reaction tanks 1, 2 and 3 in the respective compartments are filled with immobilized microorganisms in the water depth direction to form a microorganism column. The microbial column 11 is divided into three tanks in the depth direction by the reaction tank partition screen 4, and the respective reaction tanks 1, 2 and 3 are filled with entrapment-immobilized activated sludge, and the deeper reaction tank has a larger amount of microorganisms. adjust.

【0012】一方、受水槽5へ流入した汚水は汚水ポン
プ6,管13により、微生物カラムの最深部の高濃度微
生物反応槽3へ整流板7を介して均等に分配する。高濃
度微生物反応槽での水処理は、微生物カラムの第1段階
であり、汚水中には多量の有機物が含まれている。
On the other hand, the sewage flowing into the water receiving tank 5 is evenly distributed by the sewage pump 6 and the pipe 13 to the highest concentration microbial reaction tank 3 at the deepest part of the microbial column via the straightening plate 7. Water treatment in the high-concentration microbial reaction tank is the first stage of the microbial column, and the wastewater contains a large amount of organic matter.

【0013】このため第1槽では、高濃度な微生物量で
あることが望ましいが、ここでは有機物分解のために微
生物が多量の酸素を必要とするので酸欠が懸念されるが
最深部では、水圧が大きいため酸素の溶解性が高く、微
生物量を高濃度に保持できる環境条件が備わっている。
For this reason, it is desirable that the concentration of the microorganisms in the first tank is high. However, since the microorganisms require a large amount of oxygen in order to decompose the organic matter, oxygen deficiency is a concern. Since the water pressure is large, the solubility of oxygen is high and the environmental conditions are maintained so that the amount of microorganisms can be maintained at a high concentration.

【0014】しかし同時に、ブロワーの空気押し込み圧
が大きくなるという問題点が生じるため、その投入動力
は高濃度微生物反応槽にだけ必要な空気量を送るものと
し、最小限にコントロールする。
At the same time, however, there is a problem that the air pushing pressure of the blower becomes large. Therefore, the power for feeding the blower is such that the required amount of air is sent only to the high-concentration microbial reaction tank and is controlled to the minimum.

【0015】このようにして第1段階の処理がなされた
汚水は上向流として一つ上段の中濃度微生物反応槽2へ
移行するが、高濃度微生物ペレットは反応槽仕切スクリ
ーンにより遮断され、元の反応槽内へとどまる。第2段
階の中濃度微生物反応槽での処理は、汚水中の有機物が
ある程度分解されているため、最深部のように微生物濃
度を高くしておく必要はなく、従って空気量も中濃度微
生物反応槽に相当分だけを供給すればよい。
The sewage thus treated in the first step is transferred as an upward flow to the upper middle-concentration microbial reaction tank 2, but the high-concentration microbial pellets are blocked by the reaction tank partition screen, Stay in the reaction tank. In the treatment in the second-stage medium-concentration microbial reaction tank, the organic matter in the wastewater is decomposed to some extent, so it is not necessary to increase the microbial concentration as in the deepest part. Only a considerable amount needs to be supplied to the tank.

【0016】第3段階の低濃度微生物反応槽においても
同様の操作、調整を行うが、処理目標水質に応じてこの
処理の段数を増減させることが可能であり、汚水は最終
槽の固液分離スクリーン10を介して上澄水として消毒
槽へ流下して水処理を完結する。
The same operation and adjustment are performed in the third-stage low-concentration microbial reaction tank, but the number of stages of this treatment can be increased or decreased according to the target water quality of the treatment, and sewage is separated into solid-liquid separation in the final tank. The clear water is passed through the screen 10 to the disinfecting tank to complete the water treatment.

【0017】[0017]

【発明の効果】本発明水処理用微生物カラムは反応槽内
部を棚板状に仕切スクリーンでもって水深方向に少なく
とも2槽以上に仕切り、この仕切スクリーンにて棚板状
に仕切られた各仕切室内に曝気装置を設けたため、微生
物カラムは竪型構造となり、省スペース化が図られると
ともに高濃度微生物量の保持が酸素溶解性の高い高水深
域で可能となり、処理効率が向上する。さらに微生物量
及び水深に応じた空気量コントロールが可能であり、各
水深で最少必要量の曝気を行うことで投入曝気動力当り
の微生物利用酸素量が増加する等の利点を有する。
INDUSTRIAL APPLICABILITY The microbial column for water treatment of the present invention divides the inside of the reaction tank into at least two tanks in the depth direction with a partition screen into partition plates, and each partition chamber partitioned into shelf plates with this partition screen. Since the aeration device is installed in the column, the microbial column has a vertical structure, space can be saved, and the amount of high-concentration microorganisms can be retained in a high water depth area where oxygen solubility is high, thus improving treatment efficiency. Further, it is possible to control the amount of air according to the amount of microorganisms and the water depth, and by performing the minimum required amount of aeration at each water depth, there is an advantage that the amount of oxygen used by microorganisms per aeration power input increases.

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

【図1】本発明水処理用微生物カラムの説明図である。FIG. 1 is an explanatory view of a microorganism column for water treatment of the present invention.

【符号の説明】[Explanation of symbols]

1 低濃度微生物反応槽 2 中濃度微生物反応槽 3 高濃度微生物反応槽 4 反応槽仕切スクリーン 5 受水槽 6 汚水ポンプ 7 整流板 8 ブロワー 9 空気調整バルブ 10 固液分離スクリーン 11 微生物カラム 1 Low-concentration microbial reaction tank 2 Medium-concentration microbial reaction tank 3 High-concentration microbial reaction tank 4 Reactor partition screen 5 Water receiving tank 6 Sewage pump 7 Rectifier 8 Blower 9 Air regulating valve 10 Solid-liquid separation screen 11 Microbial column

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 所要の大きさを有する排水処理用生物反
応槽において、反応槽内部を棚板状に仕切スクリーンで
もって水深方向に少なくとも2槽以上に仕切り、この仕
切スクリーンにて棚板状に仕切られた各仕切室内に曝気
装置を設けたことを特徴とする水処理用微生物カラム。
1. A bioreaction tank for wastewater treatment having a required size, wherein the inside of the reaction tank is divided into at least two tanks in the depth direction by a partition screen, and the partition screen is used to form a shelf plate. A microbial column for water treatment, wherein an aeration device is provided in each of the partitioned compartments.
【請求項2】 排水処理用生物反応槽の内部を棚板状に
仕切スクリーンでもって水深方向に少なくとも2槽以上
に仕切り、この各仕切室内に曝気装置を設けるとともに
各仕切室内に固定化微生物を充填し、かつ水深方向に微
生物濃度が高くなるようにカラムを設置し、それぞれの
区画室内に必要な最少量の空気を供給するようになした
ことを特徴とする水処理用微生物カラム。
2. The biological reaction tank for wastewater treatment is partitioned into at least two tanks in the depth direction by a partition screen in the form of a shelf plate, and an aeration device is provided in each partition chamber and immobilized microorganisms are provided in each partition chamber. A microbial column for water treatment, characterized in that the column is installed so that the microbial concentration is high in the depth direction of the water, and the minimum amount of air required for each compartment is supplied.
JP4072263A 1992-02-21 1992-02-21 Microbial column for water treatment Pending JPH05228488A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4072263A JPH05228488A (en) 1992-02-21 1992-02-21 Microbial column for water treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4072263A JPH05228488A (en) 1992-02-21 1992-02-21 Microbial column for water treatment

Publications (1)

Publication Number Publication Date
JPH05228488A true JPH05228488A (en) 1993-09-07

Family

ID=13484231

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4072263A Pending JPH05228488A (en) 1992-02-21 1992-02-21 Microbial column for water treatment

Country Status (1)

Country Link
JP (1) JPH05228488A (en)

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