JPH0523664A - Method for automatically controlling backwashing of biological activated-carbon treating tower - Google Patents

Method for automatically controlling backwashing of biological activated-carbon treating tower

Info

Publication number
JPH0523664A
JPH0523664A JP3184278A JP18427891A JPH0523664A JP H0523664 A JPH0523664 A JP H0523664A JP 3184278 A JP3184278 A JP 3184278A JP 18427891 A JP18427891 A JP 18427891A JP H0523664 A JPH0523664 A JP H0523664A
Authority
JP
Japan
Prior art keywords
backwashing
water
activated carbon
air
tower
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.)
Granted
Application number
JP3184278A
Other languages
Japanese (ja)
Other versions
JP3149465B2 (en
Inventor
Masao Fujio
昌男 藤生
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 JP18427891A priority Critical patent/JP3149465B2/en
Publication of JPH0523664A publication Critical patent/JPH0523664A/en
Application granted granted Critical
Publication of JP3149465B2 publication Critical patent/JP3149465B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

Landscapes

  • Water Treatment By Sorption (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To improve a cleaning effect by passing cleaning water backward through an activated-carbon treating tower in accordance with the water level in the tower and supplying air from the lower part of the tower. CONSTITUTION:The backwashing of a downward-flow biological activatedcarbon treating tower is automatically controlled by a controller 24, and the system is formed with a level gage 23 (backwashing is started at a water level L2, air cleaning is started at a level L3, and the backwashing is finished at a level L1), a backwashing pipeline (a backwashing motor-operated valve 17, a backwashing flowmeter 18 and a backwashing pump 19) and an air cleaning pipeline (an air cleaning motor-operated valve 20, an air cleaning flowmeter 21 and a cleaning air pump 22). When backwashing is started, activated carbon- treated water is sent to the tower to raise the water level and to secure the space permitting the fluidization of the mixed part of activated carbon. However, this operation is omitted when the water head is sufficient at the start of backwashing. When a combination of aeration and water backwashing is applied, the activated-carbon tank is fluidized by aeration to increase the water backwashing effect.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は浄水処理装置における生
物活性炭処理塔の逆洗自動制御方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an automatic backwashing control method for a biological activated carbon treatment tower in a water purification treatment device.

【0002】[0002]

【従来の技術】図2は、現在、一般的に行われている浄
水プロセスを示すものである。図2において、1は着水
井、2は混和池、3は撹拌器、4はフロック形成池、5
は撹拌器、6は沈澱池、7はろ過池である。8は浄水処
理システムで、オゾン接触塔9と活性炭処理塔10によ
って構成される。
2. Description of the Related Art FIG. 2 shows a water purification process which is generally performed at present. In FIG. 2, 1 is a landing well, 2 is a mixing pond, 3 is an agitator, 4 is a floc formation pond, 5
Is a stirrer, 6 is a sedimentation tank, and 7 is a filtration tank. Reference numeral 8 is a purified water treatment system, which is composed of an ozone contact tower 9 and an activated carbon treatment tower 10.

【0003】図2の浄水プロセスにおいて、河川・湖沼
から取水した原水が着水井1に入る。つぎに、原水中の
濁質成分(粘度、有機物等)を除去する目的で凝集剤を
注入し混合する混和池2をへてフロック形成池4に入
る。フロック形成池4では、ある時間滞留させ、かつ、
緩やかな撹はんを行うことによりより大きなフロックを
成長させる。その後、フロック形成池で成長したフロッ
クは沈澱池6で分離され、さらに、沈澱6で分離できな
い微フロックをろ過池7で除去する。この浄水工程に於
いて、殺藻処理、除鉄、除マンガン、色度除去を目的と
した塩素を注入する処理が行われる。
In the water purification process of FIG. 2, raw water taken from rivers and lakes enters the landing well 1. Next, the flocculation basin 4 is entered through the mixing basin 2 in which a flocculant is injected and mixed for the purpose of removing turbid components (viscosity, organic matter, etc.) in raw water. In the floc formation pond 4, stay for a certain period of time, and
Grow larger flocs by gentle agitation. After that, the flocs grown in the flocculation basin are separated in the sedimentation basin 6, and fine flocs that cannot be separated in the sedimentation 6 are removed in the filtration basin 7. In this water purification process, algae killing treatment, iron removal, manganese removal, and chlorine injection for the purpose of removing chromaticity are performed.

【0004】近年、都市部での水環境の悪化により河
川、湖沼の水質汚濁が進んできており、従来の凝集沈
澱、ろ過処理、および塩素処理との組み合わせだけでは
水道用原水中の色度、臭気の除去には限界があり、ま
た、原水の水質悪化にともなう塩素注入量の増加により
生成される有機塩素化合物で発ガン性物質であるトリハ
ロメタンが増加する懸念が生じている。さらに、微量有
害物質の混入も問題となっている。このような背景から
「安全でおいしい水」を求める動きが強くなってきた。
そこで、これらの効果的な除去或は低減方法として、オ
ゾン処理、活性炭処理等とを複合した高度処理を浄水プ
ロセスに組み込む方式が実施されるようになってきた。
活性炭処理は、活性炭により被処理水中の微量有機物質
を吸着除去するものであり、浄水プロセスによっては活
性炭の表面に微生物を繁殖させ水中のアンモニアを除去
することも可能である(生物活性炭処理と呼ぶ)。活性
炭処理方式の種類は、固定槽式と流動槽式とがあり、活
性炭を固定槽状態か、流動状態で使用するかにより区別
され、各々、被処理水は活性炭処理塔を下向流および上
向流で移動する。固定槽式および流動槽式とは各々長所
・短所がある。下向流(固定槽)式活性炭処理は、流動
槽式に比べて運転操作が簡単で活性炭粒子の流出が少な
い点が長所であるが、浮遊懸濁物質の堆積による損失水
頭を取り除くために、定期的に活性炭槽の洗浄を行う必
要がある。
In recent years, water pollution in rivers and lakes is advancing due to the deterioration of water environment in urban areas, and the chromaticity in raw water for tap water can be improved only by combining conventional coagulation sedimentation, filtration and chlorine treatment. There is a limit to the removal of odors, and there is a concern that trihalomethane, which is a carcinogenic substance, is an organochlorine compound generated due to an increase in chlorine injection amount accompanying the deterioration of water quality of raw water. Furthermore, the inclusion of trace amounts of harmful substances is also a problem. Against this background, there has been a strong demand for “safe and delicious water”.
Therefore, as a method of effectively removing or reducing these, a method of incorporating an advanced treatment combining ozone treatment, activated carbon treatment and the like into a water purification process has come to be implemented.
Activated carbon treatment adsorbs and removes trace organic substances in the water to be treated with activated carbon, and depending on the water purification process, it is also possible to reproduce microorganisms on the surface of activated carbon and remove ammonia in the water (called biological activated carbon treatment). ). There are two types of activated carbon treatment methods: fixed tank type and fluidized tank type, and they are distinguished depending on whether the activated carbon is used in a fixed tank state or in a fluidized state. Move in countercurrent. The fixed tank type and the fluidized tank type each have advantages and disadvantages. The downflow (fixed tank) type activated carbon treatment has the advantage that the operation is simpler and the outflow of activated carbon particles is smaller than the fluidized-bed type, but in order to remove the head loss due to the accumulation of suspended suspended matter, It is necessary to wash the activated carbon tank regularly.

【0005】[0005]

【発明が解決しようとする課題】下向流式生物活性炭処
理塔において、通水を継続して行うと活性炭槽に蓄積す
る懸濁物質あるいは活性炭槽内に繁殖する微生物の影響
により通水抵抗が増加し水頭(活性炭上端部の水位)が
上昇する。このため、定期的に活性炭槽を洗浄し、通水
の抵抗となる懸濁物質等を除去しなければならない。洗
浄の方式としては、水逆洗洗浄、空気洗浄等がある。水
逆洗洗浄は、被処理水の通水を止めて、処理塔の下部か
ら、活性炭処理水を逆洗用水として使用し活性炭槽の槽
膨張率を通常30〜40%程度になるように流量調節し
一定時間逆洗操作を継続するものであり、逆洗排水は処
理塔上部よりオーバーフローにより流出し浄水場原水へ
返送する。また、空気洗浄は、水逆洗洗浄と同様に被処
理水の通水を止めて、処理塔の下部から空気を送り活性
炭槽全体を激しく混合するため活性炭粒子相互間に与え
るせん断力が大きく水逆洗洗浄だけでは不十分な場合に
は有効であり洗浄効果が大きいが、活性炭粒子の摩耗や
生物活性炭処理を行っている場合には微生物の剥離する
問題がある。通常、空気洗浄は、単独には実施せず水逆
洗洗浄の補助として使用する。したがって、下向流式生
物活性炭処理塔を効率よく運転するためには、逆洗洗浄
の組合せ方法、および、逆洗をいかに適切に行うかが重
要であり、逆洗洗浄の自動化の必要性が生ずる。
In the downward flow type biological activated carbon treatment tower, when water is continuously supplied, the water resistance is increased due to the influence of suspended substances accumulated in the activated carbon tank or microorganisms propagating in the activated carbon tank. The water head (water level at the upper end of activated carbon) rises. For this reason, it is necessary to regularly wash the activated carbon tank to remove suspended substances and the like that cause resistance to water flow. Examples of the cleaning method include backwashing with water and air cleaning. In backwashing with water, stop the passage of water to be treated, and use the activated carbon-treated water as water for backwashing from the bottom of the treatment tower so that the tank expansion rate of the activated carbon tank is usually about 30-40%. It is adjusted and the backwashing operation is continued for a certain period of time. The backwash drainage flows out from the upper part of the treatment tower due to overflow and is returned to the raw water of the water treatment plant. Further, in the air cleaning, like the backwashing with water, the flow of the water to be treated is stopped, and air is sent from the lower part of the processing tower to vigorously mix the entire activated carbon tank. When only backwashing is insufficient, it is effective and has a large cleaning effect, but there is a problem that abrasion of activated carbon particles and separation of microorganisms occur when biological activated carbon treatment is performed. Normally, air washing is not carried out alone, but is used as an aid for backwashing with water. Therefore, in order to operate the downflow type biological activated carbon treatment tower efficiently, it is important to combine backwashing and how to properly perform the backwashing, and it is necessary to automate backwashing. Occurs.

【0006】本発明は上述の問題点に鑑みてなされたも
ので、その目的は、水逆洗洗浄と空気逆洗洗浄を効率的
に組合せ制御することにより高性能な洗浄作用を得るこ
とである。
The present invention has been made in view of the above-mentioned problems, and an object thereof is to obtain a high-performance cleaning action by efficiently controlling the combination of water backwashing and air backwashing. ..

【0007】[0007]

【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、活性炭処理塔に処理すべき原水を通流さ
せた後に処理槽に導びき、該原水を処理するものにおい
て、前記活性炭処理塔の水位レベルに対応して該活性炭
処理塔に、洗浄水を逆流させると共に、前記活性炭処理
塔の下方から空気を供給する。
In order to achieve the above object, the present invention relates to a method of treating raw water by passing the raw water to be treated through an activated carbon treatment tower and then introducing the raw water into a treatment tank. Washing water is caused to flow backward to the activated carbon treatment tower corresponding to the water level of the activated carbon treatment tower, and air is supplied from below the activated carbon treatment tower.

【0008】[0008]

【作用】下向流式生物活性炭処理塔の逆洗自動制御をコ
ントローラーにより行い、そのシステム構成はレベル計
(逆洗開始水位レベル、空気洗浄開始水位レベル、逆洗
終了時水位レベル)と水逆洗配管系(逆洗用電動弁、逆
洗用流量計、逆洗用ポンプ)と空気洗浄配管系(空気洗
浄用電動弁、空気洗浄用風量計、空気洗浄用エアーポン
プ)からなる。逆洗操作開始には活性炭混合部分の流動
スペースを確保するために活性炭処理水を処理塔に送り
水位レベルを上げる。ただし、逆洗開始時の水頭が十分
あればこの操作は省略できる。逆洗洗浄方法は、空気曝
気と水逆洗洗浄とを組み合わせ活性炭粒子表面の微生物
膜の剥離を極力抑えた方法と空気洗浄と水逆洗洗浄とを
組み合わせて逆洗効果を向上させる方法の選択が可能で
ある。空気曝気と水逆洗洗浄とを組み合わせた通常の逆
洗方法では、水逆洗洗浄効果をあげるために空気曝気に
より活性炭槽の流動化をはかる。空気洗浄開始水位レベ
ルはオーバフローレベルよりも低い位置に設定し、空気
曝気及び空気洗浄時に活性炭粒子が塔上部から流出しな
いようにしている。
[Function] The controller automatically controls the backwashing of the downward flow type biological activated carbon treatment tower, and the system configuration consists of a level meter (backwash start water level, air wash start water level, backwash end water level) and water backwash. It consists of a washing pipe system (motor valve for backwashing, flow meter for backwashing, pump for backwashing) and an air washing pipe system (motorized valve for air washing, air flow meter for air washing, air pump for air washing). At the start of the backwash operation, the activated carbon treated water is sent to the treatment tower to raise the water level in order to secure a flow space for the activated carbon mixed portion. However, this operation can be omitted if there is sufficient head at the start of backwashing. The backwashing method is a method that combines air aeration and water backwashing to minimize the separation of the microbial film on the surface of the activated carbon particles, and a method that improves the backwashing effect by combining air washing and water backwashing. Is possible. In the usual backwashing method that combines air aeration and water backwashing, the activated carbon tank is fluidized by air aeration in order to improve the water backwashing effect. The water level for starting air cleaning is set to a position lower than the overflow level so that activated carbon particles do not flow out from the upper part of the tower during air aeration and air cleaning.

【0009】[0009]

【実施例】以下に本発明の実施例を図1を参照しながら
説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG.

【0010】図1は本発明の生物活性炭処理塔の逆洗自
動制御方法を実施するためのシステムを示すもので、活
性炭処理塔10は粒状活性炭層11,フィルタ12,処
理水集水部13および逆洗水集水部14からなる。すな
わち、塔最下部に処理水集水部13があり、その上部に
活性炭11を保持し処理水のみを通過させるフィルタ1
2がある。また、塔最上部には水逆洗浄時にオーバーフ
ローした逆洗排水を集水する逆洗水集水部14があり、
ここでオーバーフローした逆洗排水は逆洗水15として
排出される。
FIG. 1 shows a system for carrying out an automatic backwashing control method for a biological activated carbon treatment tower according to the present invention. The activated carbon treatment tower 10 includes a granular activated carbon layer 11, a filter 12, a treated water collecting portion 13 and The backwash water collecting section 14 is provided. That is, there is a treated water collecting portion 13 at the bottom of the tower, and a filter 1 that holds the activated carbon 11 at the upper portion thereof and allows only treated water to pass therethrough.
There are two. In addition, at the top of the tower, there is a backwash water collecting section 14 that collects the backwash drainage that overflows during water backwashing.
The backwash drainage that overflows here is discharged as backwash water 15.

【0011】また、図1において、16は処理水用電動
弁、17は逆洗用電動弁、18は逆洗用流量計、19は
逆洗用ポンプである。20は空気洗浄用電動弁、21は
空気洗浄用風量計、22は空気洗浄用エアポンプ、23
は逆洗制御用レベル計であり、24はシステム制御用コ
ントローラである。
In FIG. 1, 16 is an electric valve for treated water, 17 is an electric valve for backwashing, 18 is a flowmeter for backwashing, and 19 is a pump for backwashing. 20 is an electric valve for cleaning air, 21 is an air flow meter for cleaning air, 22 is an air pump for cleaning air, and 23
Is a backwash control level meter, and 24 is a system control controller.

【0012】図1のシステムにおいて、通常の活性炭処
理では、活性炭処理用原水を活性炭処理塔10の上部よ
り供給し、この原水中の微量有機物・濁質成分等を活性
炭により吸着させ、処理水を処理水集水部13に集め処
理水用電動弁16を開状態にし処理水槽へ送る。通水を
継続すると、活性炭層11への濁質成分等による吸着に
より除々に水頭が増加する。L1は逆洗終了時水位レベ
ル、L2は逆洗開始水位レベル、L3は空気洗浄開始水
位レベルである。この水頭の位置を逆洗制御用レベル計
23により検出し、予め設定しておいた逆洗開始レベル
L2に達したら逆洗自動洗浄が開始される。
In the system of FIG. 1, in the normal activated carbon treatment, raw water for activated carbon treatment is supplied from the upper part of the activated carbon treatment tower 10 to adsorb a trace amount of organic substances, suspended matter components, etc. in the raw water by the activated carbon to treat the treated water. The treated water is collected in the treated water collecting section 13, the treated water electric valve 16 is opened, and the treated water is sent to the treated water tank. When water flow is continued, the water head gradually increases due to adsorption of suspended matter components and the like to the activated carbon layer 11. L1 is the water level at the end of backwash, L2 is the backwash start water level, and L3 is the air wash start water level. The position of this head is detected by the backwash control level meter 23, and when the preset backwash start level L2 is reached, the backwash automatic wash is started.

【0013】自動化逆洗洗浄では、システム洗浄用コン
トローラ24により次のシーケンスで各機器の操作が行
われる。
In the automated backwash cleaning, the system cleaning controller 24 operates each device in the following sequence.

【0014】すなわち、(ステップ1)レベル計23が
逆洗開始水位レベルL2を検出すると、(ステップ2)
活性炭処理用原水を停止し、コントローラ24は処理水
用電動弁16を閉にすると共に、(ステップ3)逆洗用
電動弁17を開、逆洗用ポンプ19を運転して活性炭処
理層11を逆洗浄する。この逆洗浄作用により活性炭処
理塔10の水位が上昇してレベルL3(空気洗浄逆洗開
始水位レベル)まで達すると、レベル計23の検出信号
を基にコントローラ24は、逆洗用電動弁17を閉、逆
洗用ポンプ19を停止させると共に、(ステップ4)空
気洗浄用電動弁20を開、空気洗浄用ポンプ22を運転
して空気曝気を行う。空気曝気操作継続時間は予め操作
員が設定しておく。
That is, (step 1) When the level meter 23 detects the backwash start water level L2, (step 2)
The activated carbon treatment raw water is stopped, and the controller 24 closes the treated water electric valve 16 and (step 3) opens the backwash electric valve 17 and operates the backwash pump 19 to operate the activated carbon treatment layer 11. Back wash. When the water level of the activated carbon treatment tower 10 rises to reach the level L3 (air cleaning backwash start water level level) by this backwashing action, the controller 24 controls the backwash motor-operated valve 17 based on the detection signal of the level meter 23. At the same time as closing and stopping the backwashing pump 19, (step 4) the air washing motor-operated valve 20 is opened and the air washing pump 22 is operated to perform air aeration. The operator sets the duration of the air aeration operation in advance.

【0015】また、(ステップ5)逆洗用電動弁17を
開、逆流用ポンプ10を運転し、逆洗用流量計18の流
量信号が予め設定された設定値になるように逆洗用電動
弁17の開度を調節して流量制御を実行する。水逆洗洗
浄継続時間は予め操作員が設定しておく。逆洗排水は活
性炭処理塔10の上部よりオーバーフローし逆洗水集水
部14へ流入し逆洗水15として排出される。逆洗設定
時間経過後、逆洗用電動弁17を閉、逆洗用ポンプを停
止させる。
(Step 5) The backwash motor-operated valve 17 is opened, the backflow pump 10 is operated, and the backwash motor 18 is operated so that the flow signal of the backwash flow meter 18 becomes a preset value. The opening degree of the valve 17 is adjusted to control the flow rate. The operator sets the duration of backwashing with water in advance. The backwash waste water overflows from the upper part of the activated carbon treatment tower 10, flows into the backwash water collecting portion 14, and is discharged as backwash water 15. After the backwash set time has elapsed, the backwash electric valve 17 is closed and the backwash pump is stopped.

【0016】(ステップ6)通水開始操作として、処理
水電動弁16を開状態にし、水逆洗洗浄後の活性炭塔1
0の水頭が減少し水位レベルL1(逆洗終了時水位レベ
ル)に達した時点で活性炭処理用原水の供給を開始す
る。
(Step 6) As an operation for starting water flow, the treated water motor valve 16 is opened, and the activated carbon tower 1 after backwashing with water is washed.
When the water head of 0 decreases and reaches the water level L1 (water level at the end of backwashing), the supply of raw water for activated carbon treatment is started.

【0017】逆洗洗浄による効果を上げるために、ステ
ップ4において「空気洗浄」を行う。この場合、空気洗
浄用電動弁20を開にしてその後洗浄用エアポンプ22
を運転する。空気洗浄用風量計21の流量値信号が予め
設定された設定値になるように空気洗浄用電動弁17の
開度を調節して流量制御を行う。空気逆洗洗浄継続時間
は予め操作員が設定しておく。
In order to enhance the effect of the backwash cleaning, "air cleaning" is performed in step 4. In this case, the air cleaning electric valve 20 is opened and then the cleaning air pump 22 is opened.
To drive. The flow rate is controlled by adjusting the opening degree of the air cleaning electric valve 17 so that the flow rate signal of the air cleaning air flow meter 21 becomes a preset value. The operator sets beforehand the duration of backwashing with air.

【0018】ステップの意味及び留意点は次の通りであ
る。
The meanings of the steps and points to note are as follows.

【0019】(1)ステップ3[処理水送水]は、ステ
ップ4で[空気曝気]、[空気洗浄]を行う際に活性炭
混合部分の流動スペースを確保するための操作であり、
逆洗開始時の水頭が十分あれば水位レベルL2,L3を
共通化しステップ3を省略することも可能である。
(1) Step 3 [Treatment of treated water] is an operation for securing a flow space for the activated carbon mixed portion when performing [air aeration] and [air cleaning] in step 4,
If the water head at the start of backwashing is sufficient, the water level levels L2 and L3 can be made common and step 3 can be omitted.

【0020】(2)ステップ4[空気曝気]の継続時間
は、活性炭が流動状態となるような最小の時間設定を行
い、活性炭粒子の摩耗と表面の微生物剥離を最小限に抑
える。
(2) The duration of step 4 [air aeration] is set to a minimum time such that the activated carbon is in a fluidized state, and wear of activated carbon particles and microbial detachment on the surface are minimized.

【0021】(3)ステップ5[水逆洗洗浄]時の逆洗
流量は、活性炭層の層膨張率を通常30〜40%程度に
なるように流量設定・調節し、活性炭粒子が流出しなし
ようにする。
(3) The backwash flow rate in step 5 [backwashing with water] is set and adjusted so that the layer expansion coefficient of the activated carbon layer is usually about 30 to 40%, and activated carbon particles do not flow out. To try

【0022】(4)ステップ4にて[空気洗浄]を実施
するかの判断として、数回の逆洗操作ごとに[空気洗
浄]を設定する事も可能であるし、通常の逆洗浄操作の
時間間隔が短縮し、ある設定時間以下になった時点[空
気洗浄]を実施することも可能である。
(4) It is possible to set [air cleaning] every several backwashing operations as a judgment as to whether or not to carry out [airwashing] in step 4. It is also possible to carry out the [air cleaning] when the time interval is shortened and becomes less than a certain set time.

【0023】[0023]

【発明の効果】本発明は上述の如くであって、操作員が
あらかじめ必要な設定値(レベル計水位、流量、風量、
時間設定)を定めておけば、自動で逆洗操作を行うこと
ができる。また、水逆洗洗浄と空気曝気とを組み合わせ
ることにより、活性炭粒子表面の微生物膜の剥離を極力
抑えた逆洗操作が可能であり、また、活性炭層の汚濁物
質の蓄積程度に応じて空気洗浄を組み込むことができ洗
浄効果を上げることができる。さらに、高度浄水処理に
おいて下向流式生物活性炭処理塔の逆洗自動制御を行う
ことにより、活性炭処理操作の信頼性向上、ひいては浄
水工程全体の信頼性向上につながる。
The present invention is as described above, and set values (level meter water level, flow rate, air volume,
If the time setting is set, the backwash operation can be performed automatically. In addition, by combining backwashing with water and air aeration, backwashing can be performed with minimal separation of the microbial membrane on the surface of activated carbon particles, and air washing can be performed according to the degree of accumulation of pollutants in the activated carbon layer. Can be incorporated to improve the cleaning effect. Furthermore, by performing automatic backwash control of the downward flow type biological activated carbon treatment tower in the advanced water purification treatment, the reliability of the activated carbon treatment operation and the reliability of the entire water purification process can be improved.

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

【図1】本発明の実施例による生物活性炭処理塔の逆洗
自動制御方法を実施するための逆洗自動制御システムの
ブロック図。
FIG. 1 is a block diagram of an automatic backwash control system for carrying out an automatic backwash control method for a biological activated carbon treatment tower according to an embodiment of the present invention.

【図2】一般の浄水プロセスのブロック図。FIG. 2 is a block diagram of a general water purification process.

【符号の説明】[Explanation of symbols]

10…活性炭処理塔、11…粒状活性炭、12…フィル
タ、13…処理水集水部、14…逆洗水集水部、15…
逆洗水、16…処理水用電動弁、17…逆洗用電動弁、
18…逆洗用流量計、19…逆洗用ポンプ、20…空気
洗浄用電弁、21…空気洗浄用風量計、22…エアポン
プ、23…逆洗制御用レベル計、24…システム制御用
コントローラ。
10 ... Activated carbon treatment tower, 11 ... Granular activated carbon, 12 ... Filter, 13 ... Treated water collecting part, 14 ... Backwash water collecting part, 15 ...
Backwash water, 16 ... Electric valve for treated water, 17 ... Electric valve for backwash,
18 ... Flowmeter for backwashing, 19 ... Pump for backwashing, 20 ... Electric valve for air washing, 21 ... Air meter for air washing, 22 ... Air pump, 23 ... Level meter for backwashing control, 24 ... Controller for system control ..

Claims (1)

【特許請求の範囲】 【請求項1】 活性炭処理塔に処理すべき原水を通流さ
せた後に処理槽に導びき、該原水を処理するものにおい
て、前記活性炭処理塔の水位レベルに対応して該活性炭
処理塔に、洗浄水を逆流させると共に、前記活性炭処理
塔の下方から空気を供給することを特徴とする生物活性
炭処理塔の逆洗自動制御方法。
Claim: What is claimed is: 1. A raw water to be treated is passed through an activated carbon treatment tower, which is then introduced into a treatment tank to treat the raw water, which corresponds to the water level of the activated carbon treatment tower. A method for automatically controlling backwashing of a biological activated carbon treatment tower, characterized in that washing water is allowed to flow back into the activated carbon treatment tower and air is supplied from below the activated carbon treatment tower.
JP18427891A 1991-07-24 1991-07-24 Automatic backwash control method for biological activated carbon treatment tower Expired - Fee Related JP3149465B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18427891A JP3149465B2 (en) 1991-07-24 1991-07-24 Automatic backwash control method for biological activated carbon treatment tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18427891A JP3149465B2 (en) 1991-07-24 1991-07-24 Automatic backwash control method for biological activated carbon treatment tower

Publications (2)

Publication Number Publication Date
JPH0523664A true JPH0523664A (en) 1993-02-02
JP3149465B2 JP3149465B2 (en) 2001-03-26

Family

ID=16150521

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18427891A Expired - Fee Related JP3149465B2 (en) 1991-07-24 1991-07-24 Automatic backwash control method for biological activated carbon treatment tower

Country Status (1)

Country Link
JP (1) JP3149465B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100358167B1 (en) * 1999-02-09 2002-10-25 엘지건설 주식회사 An equipment and method for the automatic backwashing of activated carbon process
KR20030021022A (en) * 2001-09-05 2003-03-12 주식회사 유니테크 A sewage water treatment system and method, using activated carbon fiber
KR100378924B1 (en) * 2000-05-03 2003-04-07 윤복현 The treatment device for sewage
JP2016097370A (en) * 2014-11-25 2016-05-30 水ing株式会社 Washing method of filter basin and water treatment device
CN107938742A (en) * 2017-11-21 2018-04-20 谢安鹏 A kind of stream cleaner
JP2023139591A (en) * 2022-03-22 2023-10-04 株式会社フジタ Biological filtration device and its cleaning method
CN118702197A (en) * 2024-06-11 2024-09-27 赢特环保科技(无锡)有限公司 An activated carbon adsorption tower with ultra-thick carbon layer and its gas backwashing method and application

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100358167B1 (en) * 1999-02-09 2002-10-25 엘지건설 주식회사 An equipment and method for the automatic backwashing of activated carbon process
KR100378924B1 (en) * 2000-05-03 2003-04-07 윤복현 The treatment device for sewage
KR20030021022A (en) * 2001-09-05 2003-03-12 주식회사 유니테크 A sewage water treatment system and method, using activated carbon fiber
JP2016097370A (en) * 2014-11-25 2016-05-30 水ing株式会社 Washing method of filter basin and water treatment device
CN107938742A (en) * 2017-11-21 2018-04-20 谢安鹏 A kind of stream cleaner
JP2023139591A (en) * 2022-03-22 2023-10-04 株式会社フジタ Biological filtration device and its cleaning method
CN118702197A (en) * 2024-06-11 2024-09-27 赢特环保科技(无锡)有限公司 An activated carbon adsorption tower with ultra-thick carbon layer and its gas backwashing method and application

Also Published As

Publication number Publication date
JP3149465B2 (en) 2001-03-26

Similar Documents

Publication Publication Date Title
CA1335519C (en) Method for enhancing the separation capacity of a multi-bed filtration system
JPH089037B2 (en) Biological contactor for water purification and its control method for drinking water production
Farooq et al. Slow sand filtration of secondary effluent
US20050077247A1 (en) Automated water treatment system and method of use
CN111285505A (en) Reservoir water treatment process
US4028241A (en) Apparatus for and method of recovering water used to backwash and rinse a filter
JP3149465B2 (en) Automatic backwash control method for biological activated carbon treatment tower
CN210261204U (en) Water defluorination device used in water pollution prevention and control process
JP2003200007A (en) Water treatment equipment
ZA200201560B (en) Method and device for purifying and treating waste water in order to obtain drinking water.
JP2520206B2 (en) Activated carbon treatment method for water
JP3473132B2 (en) Upflow filtration method
JPH07232196A (en) Advanced water treatment method and apparatus
JP7269148B2 (en) Filtration treatment method and filtration device
JP2882045B2 (en) Backwash control method for downflow type biological activated carbon treatment tower
JPH03188993A (en) Sewage treating device
CN106861257A (en) Continuous raw streaming active sand filtration treatment device and filter method
CN201501817U (en) Small car wash car wash wastewater treatment equipment
JP3268876B2 (en) How to purify river or lake water
JP3874635B2 (en) Sewage treatment method and treatment apparatus
JP3666065B2 (en) Biological filtration type nitrogen removal method
JPH0487688A (en) Method for washing biologically activated carbon treating tower
CN108238650A (en) Using up-flow thermopnore continuous filter unit and filter method
JP3889254B2 (en) Solid-liquid separation method and apparatus for biological treatment liquid of organic wastewater
JPS60193514A (en) Cleaning apparatus of filter pond in water purifying plant

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees