JPS63294993A - Method for operating malodor preventive device for waste water tank for building or the like - Google Patents

Method for operating malodor preventive device for waste water tank for building or the like

Info

Publication number
JPS63294993A
JPS63294993A JP62133184A JP13318487A JPS63294993A JP S63294993 A JPS63294993 A JP S63294993A JP 62133184 A JP62133184 A JP 62133184A JP 13318487 A JP13318487 A JP 13318487A JP S63294993 A JPS63294993 A JP S63294993A
Authority
JP
Japan
Prior art keywords
aeration
dissolved oxygen
waste water
water tank
tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP62133184A
Other languages
Japanese (ja)
Inventor
Hajime Ito
一 伊藤
Teruhisa Yoshida
輝久 吉田
Hidemi Osagawa
秀実 長川
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 JP62133184A priority Critical patent/JPS63294993A/en
Publication of JPS63294993A publication Critical patent/JPS63294993A/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

Landscapes

  • Sewage (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To efficiently prevent rotting of the sewage in a waste water tank and generation of malodors with less electric power consumption by controlling the air quantity for aeration in such a manner that the dissolved oxygen or oxidation reduction potential in the tank attains a prescribed value. CONSTITUTION:The dissolved oxygen (DO) or oxidation reduction potential (ORP) of the sewage in the miscellaneous waste water tank is detected by a detector 11. This detected value is inputted to a control panel 12 which compares a set value and the detected value. The number of revolutions of a submersible motor 4 for aeration is lowered by a number of revolutions controller 13 to decrease the rate of aeration when the detected value exceeds the set value. The number of revolutions of the motor 4 is conversely returned to the original number to increase the rate of aeration when the detected value lowers below the set value. The air quantity for aeration is controlled by increasing and decreasing the number of revolutions of the motor 4 for aeration in such a manner, by which the dissolved oxygen or oxidation reduction potential is maintained nearly constant and the rotting of the sewage in the miscellaneous waste water tank 1 and the generation of the malodors are prevented.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はビル用排水槽やポンプ場のポンプ井等に悪臭防
止を目的とし設置してた曝気装置の好適な運転方法に間
するものである。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention is directed to a preferred method of operating an aeration device installed in a building drainage tank or a pump well at a pumping station for the purpose of preventing bad odors. be.

〔従来の技術とその問題点〕[Conventional technology and its problems]

ビル内で発生する種々の排水や、し尿は通常自然流下に
よって一旦地下に設けられた排水槽に集められ、排水ポ
ンプにより公共下水道の排水施設に排水される。しかし
従来のビル用排水槽は単なる水槽が設けられているにす
ぎず、滞留している汚水が嫌気腐敗して、悪臭が発生す
る問題が生じることが多かった。このため、ブロアを設
けて曝気を行い、排水の嫌気腐敗を防止する方法が試み
られているが、曝気装置の運転方法が適切でないため、
十分な悪臭防止効果が得られなかったり、効果が得られ
ても電力費がかかるなどの問題があった。
Various types of waste water and human waste generated within a building are usually collected by gravity in a drainage tank installed underground, and then drained to a public sewerage facility by a drainage pump. However, conventional drainage tanks for buildings are simply equipped with a water tank, and the stagnant wastewater often undergoes anaerobic decomposition and generates a bad odor. For this reason, attempts have been made to install a blower to aerate and prevent anaerobic spoilage of the wastewater, but the method of operating the aeration equipment is not appropriate.
There were problems such as not being able to obtain a sufficient odor prevention effect, and even if the effect was obtained, the electricity cost was high.

本発明は排水槽内に空気を供給するとともに槽内を混合
攪拌するために設けた曝気装置の適切な運転方法を提供
することによって、効率的に悪臭の発生を防止すること
を目的とする。
An object of the present invention is to efficiently prevent the occurrence of bad odors by providing an appropriate operating method for an aeration device provided for supplying air into a drainage tank and mixing and agitating the inside of the tank.

〔問題点を解決するための手段〕[Means for solving problems]

ビル用排水槽内の溶存酸素または酸化還元電位を検出す
る装置の少なくとも一方と曝気装置を連動し、溶存酸素
または酸化還元電位がほぼ一定となるように曝気空気量
を制御することにより、排水槽の汚水が腐敗し、悪臭が
発生するのを未然に防ぐようになす。
By linking at least one of the devices for detecting dissolved oxygen or redox potential in a building drainage tank with an aeration device, and controlling the amount of aeration air so that the dissolved oxygen or redox potential is approximately constant, To prevent wastewater from decomposing and causing bad odors.

〔実施例〕〔Example〕

以下本発明の一実施例を図により説明する。 An embodiment of the present invention will be described below with reference to the drawings.

第1図において、1はビルの地階部分に所要容積を有す
るように設けた雑排水槽で、この雑排水槽1の槽底2の
所望位置に曝気装置3を設置する。第2図は、この曝気
装置の詳細説明図で、水中モータ4と、攪拌羽根5と、
ドラフトチューブ6と空気吹込管7よりなる。水中モー
タ4は槽底に固定されるとともに、この水中モータ4に
上端6aがラッパ状に拡開し、下部6bが槽底に沿うよ
うにL字形に屈曲したドラフトチューブ6を一体に設け
、このドラフトチューブ内に前記モータにて駆動される
攪拌羽根5を設ける。このドラフトチューブ6にはほぼ
回転中心に、しかも攪拌羽根先端の内径内に空気吹込ロ
アaを挿入するようにして空気吹込管7が設けられる。
In FIG. 1, reference numeral 1 denotes a gray water tank having a required volume installed in the basement of a building, and an aeration device 3 is installed at a desired position on the tank bottom 2 of this gray water tank 1. FIG. 2 is a detailed explanatory diagram of this aeration device, showing the submersible motor 4, stirring blade 5,
It consists of a draft tube 6 and an air blowing pipe 7. The submersible motor 4 is fixed to the bottom of the tank, and is integrally provided with a draft tube 6 whose upper end 6a is expanded in a trumpet shape and whose lower part 6b is bent in an L-shape along the bottom of the tank. A stirring blade 5 driven by the motor is provided inside the draft tube. An air blowing pipe 7 is provided in the draft tube 6 so that the air blowing lower a is inserted approximately at the center of rotation and within the inner diameter of the tip of the stirring blade.

この空気吹込管7の上端は水位が変動しても常に大気中
に開口するようにして、しかも所要の空気量が汚水中に
吹き込まれるようにした径を有するバイブである。
The upper end of the air blowing pipe 7 is a vibrator having a diameter such that it is always open to the atmosphere even when the water level fluctuates, and a required amount of air is blown into the waste water.

以上の如く構成した装置において、水中モータ4を駆動
すると攪拌羽根5が回転し、槽内の汚水を攪拌する。ま
たこれによりこの羽根の先端部分の汚水中に負圧が発生
し、空気吹込管7から大気中の空気が吸引され、空気吹
込ロアaから汚水中に吹き込まれて、ドラフトチューブ
内の汚水と混合され、ドラフトチューブ前方向へと押し
出される。
In the apparatus configured as described above, when the submersible motor 4 is driven, the stirring blades 5 rotate to stir the wastewater in the tank. This also generates negative pressure in the waste water at the tip of this blade, and atmospheric air is sucked through the air blowing pipe 7, blown into the waste water from the air blowing lower a, and mixed with the waste water in the draft tube. and is pushed out toward the front of the draft tube.

水面に浮遊しているスカムは、攪拌羽根5の駆動にて、
ドラフトチューブ内へ流入される汚水とともに、該チュ
ーブ内へ流入され、前記攪拌羽根によって破砕される。
The scum floating on the water surface is removed by the stirring blade 5.
The waste water flows into the draft tube together with the waste water, and is crushed by the stirring blade.

このように、本実施例に示した曝気装置は排水槽内の攪
拌と曝気に加えて、浮遊スカムの破砕も同時に行うこと
ができるが、スカム破砕が不可能な曝気装置であっても
よい。ただしスカムも悪臭発生源の1つであるため、ス
カム破砕の機能を有する曝気装置を採用するか、スカム
破砕用の攪拌機を別に設けることが望ましい。
As described above, the aeration apparatus shown in this embodiment can not only agitate and aerate the inside of the drainage tank but also crush floating scum at the same time, but it may be an aeration apparatus that cannot crush scum. However, since scum is also one of the sources of bad odor, it is desirable to employ an aeration device with a scum crushing function or to provide a separate stirrer for scum crushing.

一方、第1図に示した排水ポンプ9はレベルスイッチ1
0と連動させて0N−OFF運転を行い、水位が常に高
水位HWLと低水位LWLO閏になるようにする。この
時のHWLとLWLは、トラフドブチューブの吸込口6
aの上端から水面までの距離がlOO〜200 mm程
度となるように設定すれば、効率的に水面上の浮遊スカ
ムを吸い込むことができる。
On the other hand, the drain pump 9 shown in FIG.
0N-OFF operation is performed in conjunction with 0, so that the water level is always in the range of high water level HWL and low water level LWLO. At this time, HWL and LWL are the suction port 6 of the trough tube.
If the distance from the upper end of a to the water surface is set to about 100 to 200 mm, floating scum on the water surface can be efficiently sucked in.

以上の機能を有する曝気H置を溶存酸素(Do)、また
は酸化還元電位(ORP)の検出器11と連動運転させ
る。すなわち、検出器11からの測定値は演算機能を有
する制御盤12に入力され、設定値と測定値を比較判定
される。
The aeration station having the above functions is operated in conjunction with the dissolved oxygen (Do) or oxidation-reduction potential (ORP) detector 11. That is, the measured value from the detector 11 is input to the control panel 12 having an arithmetic function, and the set value and the measured value are compared and determined.

c4気装置の曝気量を調整するための回転数制御装置1
3は制御盤12からの信号により、曝気用水中モータ4
の回転数が制御される。制御の指標となる溶存酸素また
は酸化還元電位の設定値は溶存酸素の場合3 mg /
 を前後、酸化還元電位の場合は+5(1wV前後が適
切である。たとえば、溶存酸素が一定になるように制御
する場合は、溶存酸素が4 噌g / 1になれば水中
モータの回転数を1/2に低下させて曝気量を減少させ
、それに従って溶存酸素が低下して3 mg / tに
なれば、再び回転数を元に戻して曝気量を増加させ、こ
れを繰り返し行うことによってI1m気空気量を制御す
る。回転数制御の段階は2段階とするのが最も簡単であ
るが、溶存酸素または酸化還元電位が増加するにつれて
数段階に回転数を低下させる方法であってもよい。ただ
し、その場合は溶存酸素または酸化還元電位の下限値が
溶存酸素の場合0.5 mg / L維持用、酸化還元
電位の場合−100mV以上となるように設定しなけれ
ば悪臭防止の効果がない。これは曝気量が少なすぎて、
槽内が還元状態になると汚水中に存在する硫酸還元菌等
の嫌気性微生物の活動が活発になり、硫酸イオン等が分
解されて悪臭成分の大部分を占める硫化水素が生成する
ためである。
Rotation speed control device 1 for adjusting the aeration amount of the c4 air device
3 is a submersible motor 4 for aeration based on a signal from the control panel 12.
The rotation speed is controlled. The set value of dissolved oxygen or redox potential, which is an indicator for control, is 3 mg /
For redox potential, +5 (around 1wV) is appropriate. For example, if you want to control the dissolved oxygen to be constant, the rotation speed of the underwater motor should be adjusted when the dissolved oxygen reaches 4 g/1. The amount of aeration is reduced by 1/2, and when the dissolved oxygen decreases to 3 mg/t, the rotation speed is returned to the original value and the amount of aeration is increased. By repeating this process, I1m is reduced. It is simplest to control the rotational speed in two stages, but it is also possible to reduce the rotational speed in several stages as dissolved oxygen or redox potential increases. However, in that case, the lower limit value of dissolved oxygen or redox potential must be set to maintain 0.5 mg/L for dissolved oxygen, or -100 mV or more for redox potential, or there will be no odor prevention effect. .This is because the amount of aeration is too small.
This is because when the inside of the tank becomes reduced, the activity of anaerobic microorganisms such as sulfate-reducing bacteria present in the wastewater becomes active, decomposing sulfate ions, etc., and producing hydrogen sulfide, which makes up most of the malodorous components.

前記構成の曝気装置を約l0II+3のビル用排水槽に
設置し、DO値が3〜3 、5IIIg/ Lとなるよ
うに曝気空気量を制御しながら、溶存酸素制御運転を行
ったところ槽内空気中の硫化水素は設置前に5ppm以
上あったのに対し、本運転期間中は常時0.01ppm
以下の低濃度に保つことができた。
The aeration system with the above configuration was installed in a building drainage tank of about 10 II + 3, and dissolved oxygen control operation was performed while controlling the amount of aeration air so that the DO value was 3 to 3.5 III g/L. The hydrogen sulfide inside was more than 5ppm before installation, but it was always 0.01ppm during the actual operation period.
We were able to maintain the concentration at a low level below.

第3図は、本発明の別の実施例を示したもので、空気吹
込管7に設けた電動弁14の開度を調整することにより
、曝気空気量を制御する方法により、悪臭の発生を防止
する。電動弁14の開度は第1図の場合と同様に、溶存
酸素または酸化還元電位の検出器11の測定値を演算機
能を有する制御盤12に人力して、予め人力した設定値
と比較判定させ、測定値が上限設定値になれば電動弁の
開度な小さくして曝気量を減少させ、それに伴って測定
値が低下して、下限設定値になれば再び電動弁を全開す
るという動作を繰り返す、溶存酸素または酸化還元電位
の設定値は前記実施例と同程度とする。
FIG. 3 shows another embodiment of the present invention, in which the amount of aeration air is controlled by adjusting the opening degree of the electric valve 14 provided in the air blowing pipe 7, thereby preventing the occurrence of bad odors. To prevent. As in the case of FIG. 1, the opening degree of the electric valve 14 is determined by manually inputting the measured value of the dissolved oxygen or oxidation-reduction potential detector 11 to the control panel 12 having arithmetic functions, and comparing it with a previously manually inputted set value. When the measured value reaches the upper limit set value, the opening of the electric valve is reduced to reduce the aeration amount, and when the measured value decreases accordingly and reaches the lower limit set value, the electric valve is fully opened again. The set values for dissolved oxygen or redox potential are the same as in the previous example.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、ビル用排水槽等に曝気装置と溶存酸素
または酸化還元電位の少なくとも一方を検出する装置を
設け、溶存酸素または酸化還元電位がほぼ一定となるよ
うに、曝気装置の駆動回転数または空気吹込管のパルプ
開度を調整しながら曝気空気量を制御することにより、
排水槽内の汚水が腐敗して悪臭が発生するのを少ない消
費電力で効率的に防止することができる。
According to the present invention, an aeration device and a device for detecting at least one of dissolved oxygen and oxidation-reduction potential are provided in a building drainage tank, etc., and the driving rotation of the aeration device is adjusted so that the dissolved oxygen or the oxidation-reduction potential is approximately constant. By controlling the amount of aeration air while adjusting the number or pulp opening of the air blowing pipe,
To efficiently prevent wastewater in a drainage tank from decomposing and producing a bad odor with less power consumption.

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

第1図は本発明曝気装置を備えた地下に設置される雑排
水槽の縦断面図、第2図は曝気装置の詳細説明図、第3
図は異なりたる実施例図である。 1は雑排水槽、2は槽底、3は曝気装置、4は水中モー
タ、5は攪拌羽根、6はドラフトチューブ、7は空気吹
込管、9は排水ポンプ、10はレベルスイッチ、11は
検出器、12は制御盤、13は回転数制御i置。 第3図
Figure 1 is a vertical cross-sectional view of a gray water tank installed underground equipped with the aeration system of the present invention, Figure 2 is a detailed explanatory diagram of the aeration system, and Figure 3 is a detailed illustration of the aeration system.
The figure shows different embodiments. 1 is a gray water tank, 2 is a tank bottom, 3 is an aeration device, 4 is a submersible motor, 5 is a stirring blade, 6 is a draft tube, 7 is an air blowing pipe, 9 is a drainage pump, 10 is a level switch, 11 is a detection 12 is a control panel, 13 is a rotation speed control unit. Figure 3

Claims (3)

【特許請求の範囲】[Claims] (1)汚水からの悪臭発生を防止するために、曝気装置
を設けたビル用排水槽や、ポンプ場 のポンプ井等において、槽内の溶存酸素ま たは酸化還元電位の少なくとも一方を検出 し、槽内の溶存酸素または酸化還元電位が 所定の値となるように、曝気空気容量を制 御することを特徴とするビル用排水等にお ける悪臭防止装置の運転方法。
(1) In order to prevent the generation of bad odors from wastewater, at least one of dissolved oxygen or redox potential in the tank is detected in building drainage tanks equipped with aeration equipment, pump wells at pumping stations, etc. 1. A method for operating an odor prevention device for building wastewater, etc., comprising controlling the aeration air volume so that the dissolved oxygen or redox potential in the water reaches a predetermined value.
(2)曝気空気量の制御手段が曝気装置の駆動回転数を
増減させることを特徴とする特許請 求の範囲第1項記載のビル用排水槽等にお ける悪臭防止装置の運転方法。
(2) The method for operating a malodor prevention device in a building drainage tank or the like as set forth in claim 1, wherein the aeration air amount control means increases or decreases the driving rotation speed of the aeration device.
(3)曝気空気量の制御手段が空気吸込管のバルブ開度
を調整することを特徴とする特許請 求の範囲第1項記載のビル用排水槽等にお ける悪臭防止装置の運転方法。
(3) The method for operating an odor prevention device in a building drainage tank or the like as set forth in claim 1, wherein the aeration air amount control means adjusts the valve opening of the air suction pipe.
JP62133184A 1987-05-27 1987-05-27 Method for operating malodor preventive device for waste water tank for building or the like Pending JPS63294993A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62133184A JPS63294993A (en) 1987-05-27 1987-05-27 Method for operating malodor preventive device for waste water tank for building or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62133184A JPS63294993A (en) 1987-05-27 1987-05-27 Method for operating malodor preventive device for waste water tank for building or the like

Publications (1)

Publication Number Publication Date
JPS63294993A true JPS63294993A (en) 1988-12-01

Family

ID=15098655

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62133184A Pending JPS63294993A (en) 1987-05-27 1987-05-27 Method for operating malodor preventive device for waste water tank for building or the like

Country Status (1)

Country Link
JP (1) JPS63294993A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001524876A (en) * 1997-05-12 2001-12-04 ディーシーヴィー インコーポレイテッド Methods for reducing hydrogen sulfide levels in wastewater systems.

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001524876A (en) * 1997-05-12 2001-12-04 ディーシーヴィー インコーポレイテッド Methods for reducing hydrogen sulfide levels in wastewater systems.

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