JPH10235386A - Temperature control device for aeration tank - Google Patents
Temperature control device for aeration tankInfo
- Publication number
- JPH10235386A JPH10235386A JP9040744A JP4074497A JPH10235386A JP H10235386 A JPH10235386 A JP H10235386A JP 9040744 A JP9040744 A JP 9040744A JP 4074497 A JP4074497 A JP 4074497A JP H10235386 A JPH10235386 A JP H10235386A
- Authority
- JP
- Japan
- Prior art keywords
- aeration tank
- raw water
- tank
- temperature
- control device
- 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
- Activated Sludge Processes (AREA)
- Control Of Temperature (AREA)
Abstract
(57)【要約】
【課題】 曝気槽の槽内温度を安定化して、槽内の溶存
酸素濃度の変動を少なくし、これによって排水処理設備
の運転及び処理水の水質を安定化することができる制御
装置、及びこれを用いた排水処理設備の制御方法の提
供。
【解決手段】 原水槽、加熱装置を有する中和槽、及び
曝気槽の順に設けられ、中和槽と曝気槽とが冷却用の熱
交換器を有する原水供給配管で接続された活性汚泥法排
水処理設備の曝気槽に、以下の計装機器を備えてなる温
度制御装置。
a)中和槽から曝気槽へ供給される原水の温度を測定す
る原水温度検出器及び原水温度調節器
b)曝気槽内の温度検出器及び曝気槽内温度調節器
c)中和槽の加熱装置用の加熱媒体供給調節弁
d)原水冷却用の熱交換器の冷却媒体供給調節弁
(57) [Summary] [PROBLEMS] To stabilize the temperature in the tank of an aeration tank to reduce fluctuations in the concentration of dissolved oxygen in the tank, thereby stabilizing the operation of wastewater treatment equipment and the quality of treated water. Provided are a control device capable of performing the control and a method for controlling wastewater treatment equipment using the control device. SOLUTION: An activated sludge drainage is provided in the order of a raw water tank, a neutralization tank having a heating device, and an aeration tank, and the neutralization tank and the aeration tank are connected by a raw water supply pipe having a heat exchanger for cooling. A temperature control device comprising the following instrumentation equipment in the aeration tank of a processing facility. a) Raw water temperature detector and raw water temperature controller for measuring the temperature of raw water supplied from the neutralization tank to the aeration tank b) Temperature detector in the aeration tank and temperature controller in the aeration tank c) Heating of the neutralization tank Heating medium supply control valve for equipment d) Cooling medium supply control valve of heat exchanger for cooling raw water
Description
【0001】[0001]
【発明の属する技術分野】本発明は、化学工場等の総合
排水処理場及び下水処理場等で用いられている活性汚泥
法の曝気槽の温度制御装置及びこれを用いる曝気槽の温
度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 a temperature control apparatus for an activated sludge aeration tank used in general wastewater treatment plants and sewage treatment plants such as chemical factories, and a method for controlling the temperature of an aeration tank using the same. Things.
【0002】[0002]
【従来の技術】活性汚泥法による排水処理プロセスにお
いては、排水を原水槽に受入れ、前処理として中和槽に
てpH調整や栄養調整を行った後、曝気槽内に空気又は
酸素を供給し好気性微生物により有機物を酸化・分解さ
せ、必要に応じて汚泥を凝集した後、沈殿槽で沈降分離
を行い、処理水を得る方法が一般的である。2. Description of the Related Art In a wastewater treatment process by the activated sludge method, wastewater is received in a raw water tank, pH and nutrition are adjusted in a neutralization tank as pretreatment, and air or oxygen is supplied into an aeration tank. In general, aerobic microorganisms oxidize and decompose organic matter, aggregate sludge as required, and then separate and settle in a sedimentation tank to obtain treated water.
【0003】このような処理における運転及び排水水質
の安定化のためには、曝気槽内の溶存酸素濃度を一定に
するように制御を行うのが通常であり、そのために曝気
槽内の溶存酸素濃度に応じて槽内に酸素又は空気を供給
するという方法が用いられることが多い。しかしなが
ら、この制御方法だけでは受け入れる排水の温度の変動
や気温の季節変化並びに日変化などの影響により、曝気
槽内の溶存酸素濃度が変動してしまい、設備の運転や処
理水の水質を十分に安定化することは困難であった。In order to stabilize the operation and wastewater quality in such treatment, it is usual to control the concentration of dissolved oxygen in the aeration tank to be constant, and therefore the dissolved oxygen in the aeration tank is controlled. A method of supplying oxygen or air into the tank depending on the concentration is often used. However, with this control method alone, the dissolved oxygen concentration in the aeration tank fluctuates due to fluctuations in the temperature of the wastewater to be received, seasonal changes in temperature, and daily changes. It was difficult to stabilize.
【0004】[0004]
【発明が解決しようとする課題】そこで、曝気槽の温度
を特定の範囲内に制御する運転方法が提案されている
が、この方法でも、曝気槽の温度を制御するため槽内に
熱水や冷水を供給したり、熱交換設備を曝気槽に設置し
たりすると、その際に発生する温度分布によって、微生
物の活性が影響を受け、制御性が悪化する、という問題
があった。Therefore, an operating method for controlling the temperature of the aeration tank within a specific range has been proposed. In this method, too, hot water or the like is contained in the tank to control the temperature of the aeration tank. When cold water is supplied or heat exchange equipment is installed in an aeration tank, there is a problem in that the temperature distribution generated at that time affects the activity of microorganisms, and controllability deteriorates.
【0005】即ち、本発明が解決しようとする課題は、
曝気槽の槽内温度を安定化して、槽内の溶存酸素濃度の
変動を少なくし、これによって排水処理設備の運転及び
処理水の水質を安定化することができる制御装置、及び
これを用いた排水処理設備の制御方法を提供することで
ある。That is, the problem to be solved by the present invention is:
A control device capable of stabilizing the temperature in the tank of the aeration tank and reducing the fluctuation of the dissolved oxygen concentration in the tank, thereby stabilizing the operation of the wastewater treatment equipment and the quality of the treated water, and using the same. An object of the present invention is to provide a method for controlling a wastewater treatment facility.
【0006】[0006]
【課題を解決するための手段】本発明者らは、上記の諸
点について検討を重ねた結果、温度の調節を特定の箇所
で行うことにより、良好な結果が得られることを見出
し、本発明を完成した。即ち、本発明の要旨は、原水槽
(1)、加熱装置を有する中和槽(2)、及び曝気槽
(3)の順に設けられ、中和槽(2)と曝気槽(3)と
が冷却用の熱交換器(16)を有する原水供給配管(1
2)で接続された活性汚泥法排水処理設備の曝気槽の温
度制御装置であって、以下の計装機器を備えてなる制御
装置、に存する。Means for Solving the Problems As a result of repeated studies on the above points, the present inventors have found that good results can be obtained by adjusting the temperature at a specific location. completed. That is, the gist of the present invention is that a raw water tank (1), a neutralization tank (2) having a heating device, and an aeration tank (3) are provided in this order, and the neutralization tank (2) and the aeration tank (3) are provided. Raw water supply pipe (1) having a heat exchanger (16) for cooling
The temperature control device for the aeration tank of the activated sludge wastewater treatment equipment connected in 2) is a control device including the following instrumentation equipment.
【0007】a)中和槽(2)から曝気槽(3)へ供給
される原水の温度を測定する原水温度検出器(4) b)曝気槽内の温度検出器(6)及び曝気槽内温度調節
器(7) c)原水温度検出器(4)の出力と曝気槽内温度調節器
(7)の出力とに基づいて、曝気槽へ供給される原水の
温度を調節する原水温度調節器(5) d)原水温度調節器(5)の加熱用操作端をなす中和槽
の加熱装置用の加熱媒体供給調節弁(8) e)原水温度調節器(5)の冷却用操作端をなす原水冷
却用の熱交換器(16)の冷却媒体供給調節弁(9) また、本発明の要旨は、曝気槽内温度調節器(7)をマ
スター側、原水温度調節器(5)をスレーブ側としたカ
スケード制御ループが形成されてなる上記の制御装置、
及び原水温度調節器(5)としてスプリットレンジ調節
器を用いる上記の制御装置、にも存している。更に、本
発明の要旨は、上述の制御装置を用いる活性汚泥法排水
処理設備の曝気槽の温度制御方法にも存している。A) Raw water temperature detector (4) for measuring the temperature of raw water supplied from neutralization tank (2) to aeration tank (3) b) Temperature detector (6) in the aeration tank and inside the aeration tank Temperature controller (7) c) Raw water temperature controller for adjusting the temperature of raw water supplied to the aeration tank based on the output of the raw water temperature detector (4) and the output of the temperature controller in the aeration tank (7). (5) d) A heating medium supply control valve (8) for the heating device of the neutralization tank, which is a heating operation end of the raw water temperature controller (5) e) A cooling operation end of the raw water temperature controller (5) The cooling medium supply control valve (9) of the heat exchanger (16) for cooling the raw water to be formed The gist of the present invention is that the temperature controller (7) in the aeration tank is on the master side and the raw water temperature controller (5) is the slave. The above-described control device in which a cascade control loop on the side is formed,
And the above control device using a split range adjuster as the raw water temperature adjuster (5). Furthermore, the gist of the present invention resides in a method for controlling the temperature of an aeration tank of an activated sludge wastewater treatment facility using the above-described control device.
【0008】[0008]
【発明の実施の形態】以下、本発明について更に詳細に
説明する。本発明の対象となる活性汚泥法排水処理設備
は、原水槽(1)、加熱装置を有する中和槽(2)、及
び曝気槽(3)の順に設けられ、中和槽(2)と曝気槽
とが冷却用の熱交換器(16)を有する原水供給配管
(12)で接続された構成の設備である。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in more detail. The activated sludge wastewater treatment equipment to be used in the present invention is provided with a raw water tank (1), a neutralization tank (2) having a heating device, and an aeration tank (3) in this order. The tank is a facility connected to a raw water supply pipe (12) having a heat exchanger (16) for cooling.
【0009】原水槽(1)は、単一又は複数の排水系統
からの排水を受け入れる槽であり、また中和槽(2)
は、この排水を活性汚泥処理するに先立ち、排水のpH
調整及び/又は栄養調整を行うための槽である。処理設
備の規模によっては、この原水槽と中和槽とを一つの槽
にまとめることも可能である。この中和槽には加熱装置
を設ける。加熱装置としては、ジャケット、コイル等の
間接加熱装置や蒸気吹込管のような直接加熱装置のどち
らを用いても良いが、蒸気吹込管が、熱効率及び保守・
点検の簡便さの点で好ましい。The raw water tank (1) is a tank for receiving wastewater from one or a plurality of drainage systems, and a neutralization tank (2).
Before the wastewater is treated with activated sludge,
This is a tank for performing adjustment and / or nutrition adjustment. Depending on the scale of the treatment equipment, the raw water tank and the neutralization tank can be combined into one tank. This neutralization tank is provided with a heating device. As the heating device, any of an indirect heating device such as a jacket and a coil and a direct heating device such as a steam blowing tube may be used.
This is preferable in terms of simplicity of inspection.
【0010】活性汚泥による排水処理を行う曝気槽と中
和槽とは冷却用の熱交換器を有する原水供給配管で接続
される。この熱交換器の形式は特に限定されるものでは
なく、例えば二重管式のものでも多管式のものでもよ
い。また、熱交換器の設置箇所も中和槽と曝気槽との接
続配管の途中であれば特に限定されるものではないが、
温度調節後の原水への外気温の影響を避けて効率的な運
転を行うためには、曝気槽に近い位置に設けるのが好ま
しい。[0010] An aeration tank for performing wastewater treatment with activated sludge and a neutralization tank are connected by a raw water supply pipe having a heat exchanger for cooling. The type of the heat exchanger is not particularly limited, and may be, for example, a double tube type or a multi tube type. The location of the heat exchanger is not particularly limited as long as it is in the middle of the connection pipe between the neutralization tank and the aeration tank.
In order to avoid the influence of the outside air temperature on the raw water after the temperature control and to perform the efficient operation, it is preferable to provide the raw water at a position close to the aeration tank.
【0011】このように、曝気槽の槽内温度を制御する
に当たって、曝気槽に加熱・冷却装置を設置せず、曝気
槽へ供給される原水の温度を調節するという方法を採る
ことにより、曝気槽内の温度分布の発生を少なくし、従
って微生物の失活や活性の低下を引き起こす恐れがなく
なる、という効果が得られる。上記の排水処理設備を効
果的に制御するために、以下の計装機器を備えた制御装
置を使用する。As described above, in controlling the temperature in the tank of the aeration tank, the method of adjusting the temperature of the raw water supplied to the aeration tank without installing a heating / cooling device in the aeration tank is adopted. This has the effect of reducing the occurrence of temperature distribution in the tank and, therefore, eliminating the risk of inactivating or reducing the activity of microorganisms. In order to effectively control the above wastewater treatment equipment, a control device equipped with the following instrumentation is used.
【0012】a)中和槽(2)から曝気槽(3)へ供給
される原水の温度を測定する原水温度検出器(4) b)曝気槽内の温度検出器(6)及び曝気槽内温度調節
器(7) c)原水温度検出器(4)の出力と曝気槽内温度調節器
(7)の出力とに基づいて、曝気槽へ供給される原水の
温度を調節する原水温度調節器(5) d)原水温度調節器(5)の加熱用操作端をなす中和槽
の加熱装置用の加熱媒体供給調節弁(8) e)原水温度調節器(5)の冷却用操作端をなす原水冷
却用の熱交換器(16)の冷却媒体供給調節弁(9) これらの温度検出器、温度調節器及び調節弁は、一般に
計装用として用いられるものを使用できる。A) Raw water temperature detector (4) for measuring the temperature of raw water supplied from neutralization tank (2) to aeration tank (3) b) Temperature detector (6) in aeration tank and inside aeration tank Temperature controller (7) c) Raw water temperature controller for adjusting the temperature of raw water supplied to the aeration tank based on the output of the raw water temperature detector (4) and the output of the temperature controller in the aeration tank (7). (5) d) A heating medium supply control valve (8) for the heating device of the neutralization tank, which is a heating operation end of the raw water temperature controller (5) e) A cooling operation end of the raw water temperature controller (5) Cooling medium supply control valve (9) of heat exchanger (16) for cooling raw water to be used As these temperature detector, temperature controller and control valve, those generally used for instrumentation can be used.
【0013】また、加熱媒体としては水蒸気が、また冷
却媒体としては冷却水(再冷水や冷水等)が、入手の容
易さなどの点で好ましい。このような計装機器を、曝気
槽内温度調節器(7)をマスター側、原水温度調節器
(5)をスレーブ側としたカスケード制御ループが形成
されるように結合することにより、変動の少ない、安定
な制御が可能となる。[0013] In addition, steam is preferable as the heating medium, and cooling water (re-cooled water, cold water, or the like) is preferable as the cooling medium from the viewpoint of easy availability. By connecting such instrumentation devices so as to form a cascade control loop in which the temperature controller (7) in the aeration tank is on the master side and the raw water temperature controller (5) is on the slave side, fluctuations are small. , Stable control becomes possible.
【0014】更に、原水温度調節器(5)としてスプリ
ットレンジ調節器を用いると、1台の調節器で加熱時及
び冷却時の操作端の切替ができるので、装置のコンパク
ト化及び設備費用の削減が可能となる。また、本発明の
曝気槽の温度制御方法は、上述の制御装置を用いて活性
汚泥法排水処理設備の曝気槽の槽内温度を制御する、と
いうものである。Further, if a split range controller is used as the raw water temperature controller (5), the operating end can be switched between heating and cooling with one controller, so that the apparatus can be made compact and the equipment cost can be reduced. Becomes possible. Further, the temperature control method of the aeration tank according to the present invention is to control the temperature in the tank of the aeration tank of the activated sludge wastewater treatment equipment by using the above-described control device.
【0015】[0015]
【実施例】以下、実施例を用いて本発明の実施の態様を
より詳細に説明するが、本発明はその要旨を越えない限
り、実施例によって限定されるものではない。図1は、
曝気槽内温度調節器(7)をマスター側調節器、スプリ
ットレンジ型原水温度調節器(5)をスレーブ側調節器
としたカスケード制御ループからなる曝気槽内温度制御
装置を示している。The embodiments of the present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the scope of the present invention. FIG.
The temperature control device in the aeration tank comprises a cascade control loop in which the temperature controller in the aeration tank (7) is a master-side controller and the split-range-type raw water temperature controller (5) is a slave-side controller.
【0016】ここでは、加熱媒体として水蒸気(以下
「蒸気」と略記することがある)を、冷却媒体として冷
却水を使用している。蒸気供給調節弁(8)は冬季にお
いて加温が必要な時期に、冷却水供給調節弁(9)は、
夏季において冷却が必要な時期に、それぞれ使い分けら
れる。例えば、冬季においてはマスター側調節器である
曝気槽内温度調節器(7)は、曝気槽内の目標温度と実
際の温度との偏差から、目標温度に近づけるために必要
な蒸気量を算出し、原水温度スプリットレンジ型調節器
(5)に設定値として信号を送る。スレーブ側調節器で
ある原水温度スプリットレンジ型調節器(5)は、その
設定値に追従させるべく蒸気供給調節弁(8)を調節す
る。夏季にはこれと同様にして、冷却水供給調節弁
(9)が使用されて原水が冷却される。Here, steam (hereinafter sometimes abbreviated as "steam") is used as a heating medium, and cooling water is used as a cooling medium. When the steam supply control valve (8) needs to be heated in winter, the cooling water supply control valve (9)
They can be used in summer when cooling is required. For example, in winter, the temperature controller (7) in the aeration tank, which is the master-side regulator, calculates the amount of steam required to approach the target temperature from the deviation between the target temperature in the aeration tank and the actual temperature. , A signal is sent as a set value to the raw water temperature split range controller (5). The raw water temperature split range controller (5), which is a slave controller, adjusts the steam supply control valve (8) so as to follow the set value. In the summer, similarly, the cooling water supply control valve (9) is used to cool the raw water.
【0017】即ち、原水温度の変動をスレーブ側調節器
にて吸収し、主目的である曝気槽内の温度を一定に保つ
ことが可能となる。図2は、図1の制御装置を用いて曝
気槽の槽内温度制御を開始する前後の、槽内温度の時間
変動を測定したグラフである。TT1で示される曝気槽
の槽内温度は、制御開始前は6〜7℃の変動幅があった
にもかかわらず、制御開始後は目標温度である36℃に
対して±0.5℃の範囲内に入っていることが判る。That is, the fluctuation of the raw water temperature is absorbed by the slave-side controller, and the temperature in the aeration tank, which is the main purpose, can be kept constant. FIG. 2 is a graph in which the time variation of the inside temperature of the aeration tank before and after the start of the inside temperature control of the aeration tank using the control device of FIG. 1 is measured. The temperature in the aeration tank indicated by TT1 was ± 0.5 ° C. with respect to the target temperature of 36 ° C. after the control was started, despite the fluctuation range of 6 to 7 ° C. before the control was started. You can see that it is within the range.
【0018】図3は、図2に示される運転を行った際の
曝気槽内の溶存酸素濃度(DO)の時間変動を示す。曝
気槽の温度制御を開始する前は約1ppmの変動幅であ
ったのが、制御開始後は、0.5ppm程度となり、更
に減少して行く傾向にあるのが観察される。FIG. 3 shows the time variation of the dissolved oxygen concentration (DO) in the aeration tank when the operation shown in FIG. 2 is performed. Before the temperature control of the aeration tank was started, the fluctuation range was about 1 ppm, but after the control was started, it was about 0.5 ppm, and it is observed that the temperature tends to further decrease.
【0019】[0019]
【発明の効果】本発明の制御装置を用いることにより、
曝気槽内の微生物の活性に影響を与えることなく、その
温度制御が可能となるので、槽内の溶存酸素濃度の変動
を少なくすることができる。これによって排水処理設備
の運転及び処理水の水質を安定化することが可能とな
る。By using the control device of the present invention,
Since the temperature can be controlled without affecting the activity of the microorganisms in the aeration tank, fluctuations in the dissolved oxygen concentration in the tank can be reduced. This makes it possible to stabilize the operation of the wastewater treatment facility and the quality of the treated water.
【0020】また、曝気槽内の溶存酸素濃度及び温度が
一定に保たれるようになると、曝気槽内の好気性微生物
の生息環境も安定化することから、有機物(COD、B
OD成分)の分解率向上も期待できる。When the concentration of dissolved oxygen and the temperature in the aeration tank are kept constant, the habitat of the aerobic microorganisms in the aeration tank is stabilized, and the organic matter (COD, B
An improvement in the decomposition rate of the OD component can also be expected.
【図1】 本発明の曝気槽の温度制御装置の一例、及び
これを用いた排水処理設備を示す概要図である。FIG. 1 is a schematic diagram showing an example of a temperature control device for an aeration tank of the present invention and a wastewater treatment facility using the same.
【図2】 図1の温度制御装置を用いて曝気槽の温度制
御を開始する前後の曝気槽の槽内温度の時間的変動状況
を示すグラフである。FIG. 2 is a graph showing temporal fluctuations in the temperature inside the aeration tank before and after starting the temperature control of the aeration tank using the temperature control device of FIG. 1;
【図3】 図1の温度制御装置を用いて曝気槽の温度制
御を開始する前後の曝気槽の溶存酸素濃度の時間的変動
状況を示すグラフである。FIG. 3 is a graph showing the temporal variation of the dissolved oxygen concentration in the aeration tank before and after starting the temperature control of the aeration tank using the temperature control device of FIG.
1・・・原水槽 2・・・中和槽 3・・・曝気槽 4・・・原水温度検出器 5・・・原水温度スプリットレンジ調節器(TC2) 6・・・曝気槽内温度検出器 7・・・曝気槽内温度調節器(TC1) 8・・・加熱媒体(蒸気)供給調節弁 9・・・冷却媒体(冷却水)供給調節弁 10・・・蒸気供給配管 11・・・冷却水供給配管 12・・・原水供給配管 13・・・酸素供給配管 14・・・排ガス排出配管 15・・・排水受入配管 16・・・冷却用熱交換器 TT1・・曝気槽の槽内温度 TT2・・原水温度 DO・・・溶存酸素濃度計 DESCRIPTION OF SYMBOLS 1 ... Raw water tank 2 ... Neutralization tank 3 ... Aeration tank 4 ... Raw water temperature detector 5 ... Raw water temperature split range controller (TC2) 6 ... Temperature detector in aeration tank 7 ... Temperature controller in aeration tank (TC1) 8 ... Heating medium (steam) supply control valve 9 ... Cooling medium (cooling water) supply control valve 10 ... Steam supply pipe 11 ... Cooling Water supply pipe 12 Raw water supply pipe 13 Oxygen supply pipe 14 Exhaust gas discharge pipe 15 Drainage receiving pipe 16 Cooling heat exchanger TT1 Temperature inside aeration tank TT2 ..Raw water temperature DO: dissolved oxygen concentration meter
───────────────────────────────────────────────────── フロントページの続き (72)発明者 山本 義章 岡山県倉敷市潮通三丁目10番地 三菱化学 株式会社水島事業所内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yoshiaki Yamamoto 3-10, Utsudori, Kurashiki-shi, Okayama Pref.
Claims (4)
(2)、及び曝気槽(3)の順に設けられ、中和槽
(2)と曝気槽(3)とが冷却用の熱交換器(16)を
有する原水供給配管(12)で接続された活性汚泥法排
水処理設備の曝気槽の温度制御装置であって、以下の計
装機器を備えてなる制御装置。 a)中和槽(2)から曝気槽(3)へ供給される原水の
温度を測定する原水温度検出器(4) b)曝気槽内の温度検出器(6)及び曝気槽内温度調節
器(7) c)原水温度検出器(4)の出力と曝気槽内温度調節器
(7)の出力とに基づいて、曝気槽へ供給される原水の
温度を調節する原水温度調節器(5) d)原水温度調節器(5)の加熱用操作端をなす中和槽
の加熱装置用の加熱媒体供給調節弁(8) e)原水温度調節器(5)の冷却用操作端をなす原水冷
却用の熱交換器(16)の冷却媒体供給調節弁(9)1. A raw water tank (1), a neutralization tank (2) having a heating device, and an aeration tank (3) are provided in this order, and the neutralization tank (2) and the aeration tank (3) are provided for cooling. A temperature control device for an aeration tank of an activated sludge wastewater treatment facility connected by a raw water supply pipe (12) having a heat exchanger (16), the control device including the following instrumentation equipment. a) Raw water temperature detector (4) for measuring the temperature of raw water supplied from neutralization tank (2) to aeration tank (3) b) Temperature detector in aeration tank (6) and temperature controller in aeration tank (7) c) Raw water temperature controller (5) for adjusting the temperature of raw water supplied to the aeration tank based on the output of the raw water temperature detector (4) and the output of the temperature controller in the aeration tank (7). d) A heating medium supply control valve (8) for the heating device of the neutralization tank, which forms a heating operation end of the raw water temperature controller (5). e) Raw water cooling, which forms a cooling operation end of the raw water temperature controller (5). Medium supply control valve (9) for heat exchanger (16)
側、原水温度調節器(5)をスレーブ側としたカスケー
ド制御ループが形成されてなる請求項1に記載の曝気槽
の温度制御装置。2. A temperature control device for an aeration tank according to claim 1, wherein a cascade control loop is formed in which the temperature controller in the aeration tank is on the master side and the raw water temperature controller is on the slave side. .
レンジ調節器を用いる請求項1又は2に記載の曝気槽の
温度制御装置。3. A temperature control device for an aeration tank according to claim 1, wherein a split range adjuster is used as the raw water temperature adjuster (5).
御装置を用いる活性汚泥法排水処理設備の曝気槽の温度
制御方法。4. A method for controlling the temperature of an aeration tank of an activated sludge wastewater treatment facility using the control device according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9040744A JPH10235386A (en) | 1997-02-25 | 1997-02-25 | Temperature control device for aeration tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9040744A JPH10235386A (en) | 1997-02-25 | 1997-02-25 | Temperature control device for aeration tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10235386A true JPH10235386A (en) | 1998-09-08 |
Family
ID=12589150
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9040744A Pending JPH10235386A (en) | 1997-02-25 | 1997-02-25 | Temperature control device for aeration tank |
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JP (1) | JPH10235386A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
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KR20020092853A (en) * | 2002-09-25 | 2002-12-12 | 윤필주 | The method of temperature control for aeration tank |
JP2006263642A (en) * | 2005-03-25 | 2006-10-05 | Sumitomo Chemical Co Ltd | Microbial acclimatization method and organic wastewater treatment method with acclimatized microorganisms |
JP2008080281A (en) * | 2006-09-28 | 2008-04-10 | Sumitomo Chemical Co Ltd | Microbial acclimatization apparatus, wastewater treatment apparatus, microorganism acclimatization method and wastewater treatment method |
JP2009045512A (en) * | 2007-08-14 | 2009-03-05 | Mitsubishi Paper Mills Ltd | Waste heat recovery method for activated sludge treatment tank inflow wastewater |
JP2010184211A (en) * | 2009-02-13 | 2010-08-26 | Sumitomo Chemical Co Ltd | Wastewater treatment method |
US7956138B2 (en) | 2007-05-16 | 2011-06-07 | Exxonmobil Chemical Patents Inc. | Catalyst system for olefin polymerization and polymers produced therefrom |
CN113651417A (en) * | 2021-08-27 | 2021-11-16 | 艾萍 | Sewage treatment system and method for environmental engineering |
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1997
- 1997-02-25 JP JP9040744A patent/JPH10235386A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20020092853A (en) * | 2002-09-25 | 2002-12-12 | 윤필주 | The method of temperature control for aeration tank |
JP2006263642A (en) * | 2005-03-25 | 2006-10-05 | Sumitomo Chemical Co Ltd | Microbial acclimatization method and organic wastewater treatment method with acclimatized microorganisms |
JP2008080281A (en) * | 2006-09-28 | 2008-04-10 | Sumitomo Chemical Co Ltd | Microbial acclimatization apparatus, wastewater treatment apparatus, microorganism acclimatization method and wastewater treatment method |
US7956138B2 (en) | 2007-05-16 | 2011-06-07 | Exxonmobil Chemical Patents Inc. | Catalyst system for olefin polymerization and polymers produced therefrom |
JP2009045512A (en) * | 2007-08-14 | 2009-03-05 | Mitsubishi Paper Mills Ltd | Waste heat recovery method for activated sludge treatment tank inflow wastewater |
JP2010184211A (en) * | 2009-02-13 | 2010-08-26 | Sumitomo Chemical Co Ltd | Wastewater treatment method |
CN113651417A (en) * | 2021-08-27 | 2021-11-16 | 艾萍 | Sewage treatment system and method for environmental engineering |
CN113651417B (en) * | 2021-08-27 | 2022-07-15 | 昆山皖源环境技术有限公司 | Sewage treatment system and method for environmental engineering |
KR102696664B1 (en) * | 2023-07-06 | 2024-08-20 | 아세아제지(주) | mehtod for industrial waste water of a paper mill |
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