JPS60114398A - Cooling tower for industrial water provided with function for treating activated sludge - Google Patents
Cooling tower for industrial water provided with function for treating activated sludgeInfo
- Publication number
- JPS60114398A JPS60114398A JP58221831A JP22183183A JPS60114398A JP S60114398 A JPS60114398 A JP S60114398A JP 58221831 A JP58221831 A JP 58221831A JP 22183183 A JP22183183 A JP 22183183A JP S60114398 A JPS60114398 A JP S60114398A
- Authority
- JP
- Japan
- Prior art keywords
- water
- activated sludge
- air
- aeration
- layers
- 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
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Activated Sludge Processes (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
この発明は、工業用水の冷却塔において、冷却水の冷却
機能の他に、その排出空気を利用して、活性汚泥処理水
のエアレーションを行う機能を付加した工業用水冷却塔
に関する。[Detailed Description of the Invention] (Industrial Application Field) This invention provides a cooling tower for industrial water, in which, in addition to the cooling function of cooling water, the discharged air is used to aerate activated sludge treated water. This article relates to industrial water cooling towers with additional functions.
(従来技術)
化学工場、食品工場等、生産工程から排出される有機性
汚水を活性汚泥処理する設備を備えた工場では、生産工
程の冷却水として使用される工業用水を冷却塔に通して
循環使用していることが多い。(Prior art) In factories equipped with activated sludge treatment equipment for organic sewage discharged from production processes, such as chemical factories and food factories, industrial water used as cooling water in the production process is circulated through a cooling tower. Often used.
工業用水の冷却塔においては、外部設備の冷却に使用し
て温度が上昇した冷却水(温水)を冷却塔に導入し、冷
却水用充填材層上に散布してこれが層内を流下する間に
、この充填材層に外気空気を誘引通過させることにより
、温水と熱交換を行わせ、この熱交換によって温度上昇
した温風はそのままに大気放出させているものであり、
ここに大量の熱エネルギーの損失がある。In industrial water cooling towers, cooling water (warm water) whose temperature has risen from being used to cool external equipment is introduced into the cooling tower, and is spread over the cooling water packing layer while it flows down inside the layer. In this method, external air is induced to pass through this filler layer to exchange heat with the hot water, and the warm air whose temperature has increased due to this heat exchange is released into the atmosphere as it is.
There is a large loss of thermal energy here.
一方、従来の活性汚泥水処理に当たっての活性汚泥水の
エアレーションの方法は、曝気槽内に散気装置を設け、
空気(酸素)を吹き込んで流入汚水と活性汚泥を混合、
攪拌する空気曝気方式、曝気槽内に充填した濾材に好気
性微生物を付着、増殖させ、これに空気(酸素)を吹き
込んで、流入汚水を循環、接触させることによる接触曝
気方式、また曝気槽水面上に回転翼車を設け、流入汚水
と活性汚泥の混合水を吸い上げて薄い膜状に飛散させ、
空気との接触を図るようにした機械式表面曝気方式等が
あり、これらはいずれも大きな動力を必要とする。On the other hand, the conventional method of aeration of activated sludge water in activated sludge water treatment involves installing an aeration device in the aeration tank.
Blow in air (oxygen) to mix inflow sewage and activated sludge.
Air aeration method with stirring, contact aeration method where aerobic microorganisms are attached to and multiply on the filter material filled in the aeration tank, air (oxygen) is blown into this, and the inflowing wastewater is circulated and brought into contact with it, and the aeration tank water surface A rotary impeller is installed on top to suck up the mixed water of inflowing sewage and activated sludge and scatter it in a thin film.
There are mechanical surface aeration methods that make contact with air, and all of these require a large amount of power.
活性汚泥法におけるエアレーションの目的は、大気中の
酸素を供給しながら流入汚水と活性汚泥を混合、攪拌し
て汚水中の汚染物t(有機物)を微生物が吸着し、酸化
分解、浄化することであり、汚水の浄化に適する温度範
囲は20℃〜30°Cとされている。The purpose of aeration in the activated sludge method is to mix and stir inflowing sewage and activated sludge while supplying oxygen from the atmosphere, allowing microorganisms to adsorb pollutants (organic substances) in the sewage, oxidatively decompose them, and purify them. The temperature range suitable for purifying wastewater is 20°C to 30°C.
しかし、エアレーションの過程では、たえず熱の放散が
あるため水温が降下し、特に外気温度が低くなる冬場に
は、微生物の活性度が低下して汚水の浄化に長い時間が
かかるようになる。However, during the aeration process, heat is constantly dissipated, which causes the water temperature to drop, and especially in the winter when the outside air temperature is low, the activity of microorganisms decreases and it takes a long time to purify the wastewater.
(発明の目的)
この発明は上記の点に着目してなされたものであって、
工業用水冷却塔の冷却水用充填材層において、層内を流
下する温水と熱交換を行わせて排出される飽和湿り空気
を、同じ塔内に設けた活性汚泥水エアレーション用充填
層に導き、該充填材層に於いて層上から流下する活性汚
泥水と気液接触させることにより、活性汚泥水のエアレ
ーションと同時にその加温を図り、ここで活性汚泥水と
の熱交換によって冷却された空気をファンによって外気
排出される過程をとり、この排熱エネルギーの有効利用
を図ると共に、汚水中に充分な酸素の供給を図り、微生
物による汚水浄化作用が常に好適な条件下に維持される
ようにして、活性汚泥法による汚水処理設備のコストダ
うンに大きく寄与する工業用水冷却塔を擢供しようとす
るものである。(Object of the invention) This invention has been made focusing on the above points,
In the cooling water filling layer of an industrial water cooling tower, the saturated humid air that is discharged after exchanging heat with the hot water flowing down in the layer is guided to the activated sludge water aeration packed layer installed in the same tower. By bringing the activated sludge water flowing down from above the bed into gas-liquid contact in the filler layer, the activated sludge water is heated at the same time as aeration, and the air cooled by heat exchange with the activated sludge water is heated. The waste heat is discharged to the outside air by a fan, and this waste heat energy is used effectively, and sufficient oxygen is supplied to the waste water so that the sewage purification effect of microorganisms is always maintained under suitable conditions. The aim is to provide an industrial water cooling tower that will greatly contribute to reducing the cost of wastewater treatment equipment using the activated sludge method.
(発明の構成)
この発明は、塔内に設けた水冷却用充填材層の空気通過
後方に活性汚泥水エアレーション用充填材層を併設し、
その空気通過後部に水沫除脱器を設け、水冷却用充填材
層を通過して加温、加湿された飽和湿り空気によって活
性汚泥水エアレーション用充瞑材層において活性汚泥水
のエアレーションを行わしめるように構成したことを要
旨とする。(Structure of the Invention) This invention provides a packing material layer for activated sludge water aeration at the rear of the water cooling packing material layer provided in the tower through which air passes,
A water droplet remover is provided at the rear of the air passage, and the activated sludge water is aerated in the activated sludge water aeration filling material layer using heated and humidified saturated moist air that passes through the water cooling filling material layer. The summary is as follows.
以下、この発明の実施例を図面に基づいて説明する。Embodiments of the present invention will be described below based on the drawings.
図において、1は塔本体、2はこの塔本体内に設けた冷
却水用充填材層で、−L下方向に段階状に区分している
。3は冷却水用充填材層上に配装され、外部設備に接続
された温水供給管4に接続した温水分配槽・で、底面に
は充填材槽2に対して全面的に均一散水可能に多数の散
水用ノズル5を備えている。6は充填材N2の層下に設
けた冷却水受水槽、7は充填材層2の空気通過後部に設
けた水沫除脱器、8は塔本体1の側壁部に冷却水充填層
2に対応して開設され、外気空気が流入する開口部で、
ルーパー9を備えている。10は冷却水充填材層2に隣
接して塔本体内に設けた活性汚泥水エアレーション用充
填材層で、空気抵抗が小さく流下汚水の飛散を防止し得
る棚段式充填材等を採用した形式のもので、各棚段は洗
浄が容易な着脱自在な引き出し方式を採っている。In the figure, 1 is a tower main body, and 2 is a cooling water filling layer provided within this tower main body, which is divided into steps in the downward direction of -L. 3 is a hot water distribution tank arranged on the cooling water filler layer and connected to a hot water supply pipe 4 connected to external equipment, and the bottom surface is capable of uniformly sprinkling water over the entire surface of the filler tank 2. It is equipped with a large number of water spray nozzles 5. Reference numeral 6 indicates a cooling water receiving tank provided under the layer of packing material N2, 7 indicates a water droplet remover provided at the rear part of the packing material layer 2 through which air passes, and 8 corresponds to the cooling water filled layer 2 on the side wall of the tower body 1. This is an opening that is opened to allow outside air to flow in.
It is equipped with a looper 9. 10 is a packing material layer for activated sludge water aeration provided in the tower body adjacent to the cooling water filling material layer 2, and is of a type that adopts a tiered packing material etc. that has low air resistance and can prevent scattering of flowing sewage. Each shelf has a removable drawer system for easy cleaning.
11はこの充填材N10最上段層に開口して配装され、
外部汚水処理設備に連結した活性汚泥水供給管、12は
充填材層10の層下に設けた活性汚泥水受水槽、13は
充填材層10の空気通過後部に設けた水沫除脱器、14
は冷却水用充填材層2と活性汚泥水エアレーション用充
填材層10との間に設けた空間、15は活性汚泥水エア
レーション用充填材層10の空気通過後方に設けた空間
、16はこの空間15の上部に開口した排気口で、該排
気口16にモータ17に連結した排気ファン18を配装
している。11 is opened and arranged in the uppermost layer of this filler N10,
Activated sludge water supply pipe connected to external sewage treatment equipment, 12 an activated sludge water receiving tank provided under the filler layer 10, 13 a water droplet remover provided at the rear of the filler layer 10 through which air passes, 14
15 is a space provided between the cooling water filler layer 2 and the activated sludge aeration filler layer 10, 15 is a space provided behind the air passage of the activated sludge aeration filler layer 10, and 16 is this space. An exhaust port 15 is opened at the top, and an exhaust fan 18 connected to a motor 17 is disposed at the exhaust port 16 .
尚、図中、19は空間14.15に対してそれぞれ出入
可能に設けた点検扉である。In addition, in the figure, reference numeral 19 is an inspection door provided to allow access to and exit from the spaces 14 and 15, respectively.
(作 用)
上記構成において、モータ17の起動によって排気ファ
ン1日が作動して塔本体l内に開口部8を介して誘引さ
れる外気空気は、まづ冷却水用充填材層2内を通過する
間に、該層を流下する温水との熱交換が行われて温風と
なって水沫脱除器7を通過する。この水沫脱除器7を通
過することによって温風中の水沫が除去され、飽和湿り
空気として空間14を経て活性汚泥水エアレーション用
充填材層10に入り、該層内において活性汚泥水のエア
レーションを行わしめるものである。(Function) In the above configuration, the exhaust fan is activated by starting the motor 17, and the outside air that is drawn into the tower body l through the opening 8 first passes through the cooling water filling layer 2. While passing through, heat exchange is performed with the hot water flowing down the layer, and the air becomes warm air, which passes through the water droplet remover 7. Water droplets in the warm air are removed by passing through the water droplet remover 7, and enter the activated sludge water aeration filler layer 10 as saturated moist air through the space 14, where the activated sludge water is aerated. It is something that will be carried out.
然して、この活性汚泥水エアレーション用充填材層10
に入ってくる空気は、加温、加湿された大量の飽和湿り
空気であり、これが冷たい活性汚泥水と接触することに
より、活性汚泥水には充分な酸素が供給されると同時に
微生物の活性を維持するための充分な熱が供給され、汚
水中のBOD成分の効率的な酸化分解を助ける役目を果
たすことになる。However, this activated sludge water aeration filler layer 10
The incoming air is a large amount of saturated moist air that has been heated and humidified, and when this comes into contact with the cold activated sludge water, sufficient oxygen is supplied to the activated sludge water and at the same time it stimulates the activity of microorganisms. Sufficient heat is supplied for maintenance, which serves to support efficient oxidative decomposition of BOD components in wastewater.
尚、エアレーション用充填剤層10としては、活性汚泥
水が順次流下する水滴飛散の少ない形式を採用すること
で、活性汚泥水の工業用水への混入や汚泥付着による塔
内汚染が防止され、また冷却水用充填材層2からの空気
流に同伴して飛来する水滴を捕捉することもできるので
、冷却水用充填材層2後方の水沫除去器7を省略して空
気抵抗の増大を防止することもできる。In addition, by adopting a format for the aeration filler layer 10 in which the activated sludge water flows down sequentially with less water droplet scattering, it is possible to prevent the activated sludge water from mixing with industrial water and contaminating the inside of the tower due to sludge adhesion. Since water droplets flying along with the air flow from the cooling water filling layer 2 can be captured, the water droplet remover 7 behind the cooling water filling layer 2 can be omitted to prevent an increase in air resistance. You can also do that.
(発明の効果)
この発明は、上記の如き構成作用によって次のような効
果を奏する。(Effects of the Invention) The present invention has the following effects due to the above-described structural action.
(1)活性汚泥水中に含まれる有機物質を生物学的に分
解、除去するのに必要な酸素の供給機能については、冷
却塔より排出される空気量が膨大な量であり、通常の散
気方式の空気量に比べて数十倍もの空気量となり、充分
な酸素供給機能を持っている。(1) Regarding the function of supplying oxygen necessary for biologically decomposing and removing organic substances contained in activated sludge water, the amount of air discharged from the cooling tower is enormous, and ordinary aeration is not sufficient. The amount of air is several tens of times higher than that of the conventional method, and it has a sufficient oxygen supply function.
(2)活性汚泥水中の有機物質とそれを分解除去する生
物群との効果的な接触を行わせるための、気液接触機能
は活性汚泥水を上部より充填材層に散水し、自然落下さ
せる過程における混合、攪拌作用により充分に発揮され
る。(2) The gas-liquid contact function sprays activated sludge water onto the filler layer from above and allows it to fall naturally, in order to bring about effective contact between organic substances in activated sludge water and the group of organisms that decompose and remove them. It is fully demonstrated by the mixing and stirring action during the process.
(3)従来の活性汚泥法では、水温が4℃〜9℃となる
冬場では、10時間以上もエアレーション時間をかけて
、BOD除去率90%をやっと達成できたものであるが
、この発明では冷却塔の排熱が有効に利用され、活性汚
泥水と加温された温風との気液接触によって水温を常に
20℃以上に保持できるので、4〜6時間にて目的のB
OD除去率が得られる。(3) With the conventional activated sludge method, in winter when the water temperature is between 4°C and 9°C, it takes more than 10 hours of aeration time to achieve a BOD removal rate of 90%, but with this invention, The exhaust heat from the cooling tower is effectively used, and the water temperature can be maintained at 20°C or higher through gas-liquid contact between the activated sludge water and the heated hot air.
OD removal rate is obtained.
(4)活性汚泥法の設計基準は、従来は冬期においての
処理能力が基準にされているが、この発明の装置を採用
することにより、冬場においての処理能力は例えば上記
のように約倍増して設計条件が四季変わらずの状態とな
り、安定した運転管理が得られることになる。(4) Conventionally, the design criteria for the activated sludge method was based on the treatment capacity in winter, but by adopting the device of this invention, the treatment capacity in winter can be approximately doubled, for example, as mentioned above. This means that the design conditions remain the same throughout the seasons, resulting in stable operation management.
(5)冬場における汚水処理能力の増大により、曝気槽
の容量縮小が可能となるばかりでなく、この発明の冷却
塔を汚水処理設備に近接配置することにより、設備全体
をコンパクトにまとめることができるので、設備建設費
の大幅なコストダウンを図れることになる。(5) By increasing the sewage treatment capacity in winter, it is not only possible to reduce the capacity of the aeration tank, but also by placing the cooling tower of this invention close to the sewage treatment equipment, the entire equipment can be made compact. Therefore, it is possible to significantly reduce equipment construction costs.
(6)冷却塔本来の機能、並びに保守については万全を
期しており、活性汚泥水エアレーション用充填材層にも
棚段的充虜材等の採用で水滴飛散防止を充分に考慮に入
れた構造とするとか、活性汚泥水の有機物質の付着に対
する処置についても、充填材を着脱可能な引き出し方式
とし、容易に洗浄可能な構造として問題がない。(6) The original functions and maintenance of the cooling tower are well-maintained, and the structure takes into account the prevention of water droplet scattering by adopting tiered filling material for the activated sludge water aeration filling layer. In addition, there is no problem in dealing with the adhesion of organic substances in activated sludge water as the filler is removably drawn out and has a structure that allows easy cleaning.
(7)運転維持費については、冷却塔のファンで大気に
放出している風量と排熱エネルギーとを有効利用し、そ
してエアレーション用充填材層としては棚段式等、空気
抵抗の小さい形式の充填材層を採用することで、わずか
なファン動力増で済み、従来の散気方式の空気吹き込み
用ブロアーや、機械曝気方式の回転動力に比べ、大きく
減少することになる。更に寒冷地等の冬場に於いては、
曝気槽内の水温を上げるため、蒸気を吹き込んでいる例
もあるがこれらも不用となる。(7) Regarding operation and maintenance costs, the air volume and waste heat energy released into the atmosphere by cooling tower fans should be effectively used, and the aeration filler layer should be of a type with low air resistance, such as a tray type. By using the filler layer, only a slight increase in fan power is required, which is significantly less than the rotational power of conventional air diffusion blowers or mechanical aeration systems. Furthermore, in winter in cold regions,
In some cases, steam is blown into the aeration tank to raise the water temperature, but this is no longer necessary.
図面はこの発明の実施例を示す構成図である。
■・・・塔本体、2・・・冷却水用充填材層、3・・・
温水分配槽、4・・・温水供給管、5・・・散水ノズル
、6・・・冷却水受水槽、7・・・水沫除脱器、8・・
・開口0
部、9・・・ルーバー、10・・・活性汚泥水エアレー
ション用充填材層、11・・・活性汚泥水供給管、12
・・・活性汚泥水受水槽、13・・・水沫除脱器、14
.15・・・空間、16・・・排気口、17・・・モー
タ、18・・・排気ファン、19・・・点検扉。
1The drawings are configuration diagrams showing embodiments of the present invention. ■...Tower body, 2...Cooling water filling layer, 3...
Hot water distribution tank, 4... Hot water supply pipe, 5... Water nozzle, 6... Cooling water receiving tank, 7... Water droplet remover, 8...
・Opening 0 part, 9... Louver, 10... Filler layer for activated sludge water aeration, 11... Activated sludge water supply pipe, 12
...Activated sludge water receiving tank, 13... Water droplet remover, 14
.. 15...Space, 16...Exhaust port, 17...Motor, 18...Exhaust fan, 19...Inspection door. 1
Claims (1)
泥水エアレーション用充填材層を併設し、その空気通過
後部に水沫除脱器を設け、水冷却用充填材層を通過して
加温、加湿された飽和湿り空気によって活性汚泥水エア
レーション用充填材層において活性汚泥水のエアレーシ
ョンを行なわしめるように構成したことを特徴とする活
性汚泥処理機能を備えた工業用水冷却塔。A packing material layer for activated sludge water aeration is installed behind the water cooling packing material layer provided in the tower, and a water droplet remover is installed at the rear of the air passing through. An industrial water cooling tower equipped with an activated sludge processing function, characterized in that it is configured to aerate activated sludge water in a packing material layer for activated sludge water aeration using heated and humidified saturated moist air.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58221831A JPS60114398A (en) | 1983-11-24 | 1983-11-24 | Cooling tower for industrial water provided with function for treating activated sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58221831A JPS60114398A (en) | 1983-11-24 | 1983-11-24 | Cooling tower for industrial water provided with function for treating activated sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60114398A true JPS60114398A (en) | 1985-06-20 |
Family
ID=16772870
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58221831A Pending JPS60114398A (en) | 1983-11-24 | 1983-11-24 | Cooling tower for industrial water provided with function for treating activated sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60114398A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015040672A (en) * | 2013-08-23 | 2015-03-02 | Jfeスチール株式会社 | Cooling tower, installation method of gas-liquid contact part of cooling tower, and maintenance method of cooling tower |
JP2015040656A (en) * | 2013-08-21 | 2015-03-02 | 株式会社Ihi | Cooling tower system |
-
1983
- 1983-11-24 JP JP58221831A patent/JPS60114398A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015040656A (en) * | 2013-08-21 | 2015-03-02 | 株式会社Ihi | Cooling tower system |
JP2015040672A (en) * | 2013-08-23 | 2015-03-02 | Jfeスチール株式会社 | Cooling tower, installation method of gas-liquid contact part of cooling tower, and maintenance method of cooling tower |
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