JPS63294994A - 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
JPS63294994A
JPS63294994A JP62133185A JP13318587A JPS63294994A JP S63294994 A JPS63294994 A JP S63294994A JP 62133185 A JP62133185 A JP 62133185A JP 13318587 A JP13318587 A JP 13318587A JP S63294994 A JPS63294994 A JP S63294994A
Authority
JP
Japan
Prior art keywords
aeration
tank
waste water
water tank
building
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
JP62133185A
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 JP62133185A priority Critical patent/JPS63294994A/en
Publication of JPS63294994A publication Critical patent/JPS63294994A/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 intermittently operating an aeration device 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 1 is detected by a detector 11. The operation of the aeration device 3 is stopped when the detected value attains the upper limit value set in an upper and lower limit setter 12. The operation of the aeration device 3 is restarted when the measured value attains the lower limit value. The rotting of the sewage in the miscellaneous waste water tank 1 and the generation of the malodors are prevented by intermittently operating the aeration device 3 in such a manner.

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
止を目的として設置した曝気装置の好適な運転方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a preferred method of operating an aeration device installed in a building drainage tank, a pump well at a pump station, etc. for the purpose of preventing bad odors.

〔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雑排水や、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’x*敗して、悪臭が発
生するという問題が生じることが多かった。このため、
ブロアを設けて111i′X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!!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 kinds of gray 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 water tanks, and the problem often arises in that the stagnant sewage gets stale and generates a bad odor. For this reason,
Attempts have been made to install a blower and perform 111i'X to prevent anaerobic decay of wastewater, but aeration! ! Because the operating method of the equipment was not appropriate, there were problems such as not being able to obtain sufficient odor prevention effects, and even if the effects were obtained, the electricity costs were 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。
The present invention aims to efficiently prevent the occurrence of bad odors by supplying air into a drainage tank and providing an appropriate operating method for an aeration device installed to mix and stir the tank. .

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

ビル用排水槽に設置した曝気装置を、Do計、ORP計
またはタイマーの少なくとも一つと連動させて間欠曝気
運転することにより、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 intermittent aeration operation of the aeration device installed in the building drainage tank in conjunction with at least one of the Do meter, ORP meter, or timer, it is possible to prevent the sewage in the drainage tank from rotting and causing bad odors. Eggplant.

〔実施例〕〔Example〕

以下本発明を−の実施例を図により説明する。 Embodiments 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】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がラッパ状に拡関し、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、
このト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 with a required volume installed in the basement of a building, and an aeration device 3 is installed at a desired position on the bottom 2 of this gray water tank. FIG. 2 is a detailed explanatory diagram of this aeration device, which is composed of a submersible motor 4, a stirring blade 5, a draft tube 6, and an air blowing pipe 7. The submersible motor 4 is fixed to the tank bottom, and is integrally provided with a draft tube 6 having an upper end 6a extending in a trumpet shape and a lower part 6b bent in an L-shape along the tank bottom.
A stirring blade 5 driven by the motor is provided inside this traft 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、しが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パイプである。
The upper end of this air blowing pipe 7 is a pipe having a diameter such that it is always open to the atmosphere even if the water level fluctuates, so that the required amount of air can be 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v7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 wastewater at the tip of this blade, and air from the atmosphere is sucked in from the air blower v7, blown into the wastewater from the air blower lower a, and mixed with the wastewater in the draft tube. , 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LWLの間になるようにする。この
時のHWLとLWLは、ドラフトチューブの吸込口6a
の上端から水面までの距離が100〜200nws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 between the high water level HWL and the low water level LWL. At this time, HWL and LWL are the suction port 6a of the draft tube.
If the distance from the upper end of the tank to the water surface is set to about 100 to 200 nws, floating scum on the water surface can be efficiently sucked in.

以上の機能を有する曝気装置を間欠運転するために、溶
存酸素(Do)または酸化還元電位(ORP)の検出器
11と上下限設定器12を設ける。上下限設定器12は
溶存酸素または酸化還元電位の測定値が上限設定値にな
れば曝気装置が停止し、つ嘴いて該測定値が下限設定値
まで低下すれば、曝気装置が再起動するという簡単な制
御装置で曝気装置の0N−OFF繰り返し運転により、
槽内の溶存酸素または酸化還元電位を上下限設定値の範
囲内に保つことができる。
In order to intermittently operate the aeration system having the above functions, a detector 11 and an upper and lower limit setter 12 for dissolved oxygen (Do) or oxidation-reduction potential (ORP) are provided. The upper and lower limit setter 12 stops the aeration device when the measured value of dissolved oxygen or redox potential reaches the upper limit set value, and restarts the aeration device when the measured value drops to the lower limit set value. By repeating ON-OFF operation of the aeration equipment with a simple control device,
Dissolved oxygen or redox potential in the tank can be maintained within the upper and lower set values.

汚水から発生する悪臭成分の大部分は硫化水素で、汚水
の流入及び滞留に伴って槽内が還元状態になり、汚水中
に存在する@酸還元菌等の嫌気性微生物の活動が活発に
なった時、汚水中の硫酸イオンやイオウ分を含むタンパ
ク質等が分解されて多量の硫化水素が発生する。従って
適切な曝気を行って汚水を好気状態に保つことにより硫
化水素等悪臭の発生を防止することができる。ただし、
悪臭防止効果を発揮するためには少なくとも溶存酸素は
0.5 mg / を以上、酸化還元電位は一100m
V以上に保つ必要がある。曝気量の増加に伴って溶存酸
素及び酸化還元電位が上昇し悪臭の発生量も減少するが
、ある程度以上になるとほとんど悪臭が発生しなくなる
ことから、それ以上曝気を行う必要はなく、また省エネ
の観点からも曝気を停止する方が好ましい。この時の汚
水のDO値は3 mg / を程度、ORP値は+50
 mV程度であることから、前記上下限値をこの値の近
傍に設置することにより、少ない消費電力で効率的に悪
臭を防止することができる。
Most of the malodorous components generated from sewage are hydrogen sulfide, and as the sewage flows in and accumulates, the inside of the tank becomes reduced, and the activity of anaerobic microorganisms such as @ acid-reducing bacteria present in the sewage becomes active. When this occurs, proteins containing sulfate ions and sulfur in the wastewater are decomposed and a large amount of hydrogen sulfide is generated. Therefore, by maintaining wastewater in an aerobic state through appropriate aeration, it is possible to prevent the generation of bad odors such as hydrogen sulfide. however,
In order to exhibit the odor prevention effect, the dissolved oxygen must be at least 0.5 mg / or more, and the redox potential must be -100 m
It is necessary to maintain the voltage above V. As the amount of aeration increases, dissolved oxygen and oxidation-reduction potential rise, and the amount of bad odor generated decreases, but beyond a certain point, almost no bad odor is generated, so there is no need to carry out further aeration, and this is an energy-saving measure. From this point of view as well, it is preferable to stop aeration. At this time, the DO value of the sewage was about 3 mg/, and the ORP value was +50.
Since it is approximately mV, by setting the upper and lower limits near this value, it is possible to efficiently prevent bad odors with less power consumption.

次に前記構成の曝気装置を約15a3のビル用排水槽に
設置し、槽内のORP値が単に±OmV〜+100w+
Vとなるように酸化還元電位の上下限値を設定して、曝
気装置の間欠曝気運転を行った。
Next, the aeration device with the above configuration was installed in a building drainage tank of about 15a3, and the ORP value in the tank was only ±OmV ~ +100w+
The upper and lower limits of the oxidation-reduction potential were set to be V, and intermittent aeration operation of the aeration device was performed.

槽内空気中の硫化水素濃度は曝気装置設置前は最大10
 ppmLu上であったのに対し、本運転期閏中は常時
0.01 ppm以下の低濃度に保持することができた
。また、この時の曝気装置の運転時間は連続運転の場合
の40%程度であったことから、消費電力の面からも5
0%以上の省エネ効果が得られた。
The hydrogen sulfide concentration in the air inside the tank was up to 10 before the aeration equipment was installed.
ppmLu, but during the actual operating period, the concentration could be maintained at a low level of 0.01 ppm or less. In addition, since the operating time of the aeration equipment at this time was approximately 40% of that in continuous operation, it was also
An energy saving effect of 0% or more was obtained.

第3図は、本発明の別の実施例を示したもので、曝気装
置をタイマー13によって単純な0N−OFF運転を行
ったものである。この場合の運転時間及び停止時間の設
定値は各時間帯におけるDO値またはORP値を予め測
定して、前述したように常時溶存酸素は0.5+wg/
を以上、酸化還元電位は一100mV以上となるように
時間設定する必要がある。設定値は曝気時間20分、停
止時間40分というように固定してもよいが、24時間
タイマーやビンボードタイマーを用いて一日の流入負荷
変動を考慮しながら曝気時間と停止時間の各々の値を別
々に設定してもよい。
FIG. 3 shows another embodiment of the present invention, in which the aeration device is operated in a simple ON-OFF state using a timer 13. In this case, the set values for the operating time and stop time are determined by measuring the DO value or ORP value in each time period in advance, and as mentioned above, the dissolved oxygen at all times is 0.5 + wg/
It is necessary to set the time so that the redox potential becomes -100 mV or more. The set values may be fixed such as aeration time of 20 minutes and stop time of 40 minutes, but the aeration time and stop time can be adjusted using a 24-hour timer or bin board timer, taking into account daily inflow load fluctuations. Values may be set separately.

〔発明の効果ゴ 本発明によれば、ビル用排水槽等に悪臭の発生防止を目
的として設置したFr!i気装置を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ながら、予め設定し
た溶存rII!素または酸化還元電位の上限値で曝気を
停止し、下限値で曝気を再開し、これを繰り返し行う間
欠運転するか、またはタイマーにより間欠運転すること
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。
[Effects of the Invention] According to the present invention, Fr! While detecting at least one of dissolved oxygen and redox potential, the preset dissolved rII! By intermittent operation in which aeration is stopped at the upper limit of the element or oxidation-reduction potential and restarted at the lower limit, or by intermittent operation using a timer, the sewage in the drainage tank will rot and odor will be reduced. This can be efficiently prevented with low power consumption.

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

第1図はビルの地階等に設けた雑排水槽の断面図、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。 l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。 Gま 77’  1  壱 第1II)
Figure 1 is a cross-sectional view of a gray water tank installed in the basement of a building, etc.
The figure is a detailed explanatory diagram of the aeration device, and FIG. 3 is a diagram of a different embodiment. 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, and 7 is an air blowing pipe. Gma 77' 1 1st II)

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、槽内用溶存酸素ま たは酸化還元電位が所定の範囲となるよう に、曝気装置を間欠運転することを特徴と するビル用排水槽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 sewage, in building drainage tanks equipped with aeration equipment, pump wells at pump stations, etc., ensure that the dissolved oxygen or oxidation-reduction potential in the tank is within the specified range. , a method for operating an odor prevention device in a building drainage tank, etc., characterized by intermittent operation of an aeration device.
(2)間欠曝気の方法が溶存酸素または酸化還元電位の
上限値で曝気停止、下限値で曝気再 開とし、これを繰り返すことを特徴とする 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) A drainage tank for a building according to claim 1, wherein the method of intermittent aeration is to stop aeration at the upper limit of dissolved oxygen or redox potential, restart aeration at the lower limit, and repeat this process. How to operate a malodor prevention device.
(3)間欠曝気の方法がタイマーによることを特徴とす
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 a malodor prevention device in a building drainage tank or the like as set forth in claim 1, wherein the intermittent aeration is performed using a timer.
JP62133185A 1987-05-27 1987-05-27 Method for operating malodor preventive device for waste water tank for building or the like Pending JPS63294994A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62133185A JPS63294994A (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
JP62133185A JPS63294994A (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
JPS63294994A true JPS63294994A (en) 1988-12-01

Family

ID=15098680

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62133185A Pending JPS63294994A (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) JPS63294994A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007196208A (en) * 2005-12-28 2007-08-09 Sumitomo Heavy Ind Ltd Wastewater treatment apparatus and wastewater treatment method
JP2007196207A (en) * 2005-12-28 2007-08-09 Sumitomo Heavy Ind Ltd Wastewater treatment apparatus and wastewater treatment method
JP2007275847A (en) * 2006-04-11 2007-10-25 Sumitomo Heavy Industries Environment Co Ltd Wastewater treating apparatus and wastewater treating method
JP2007275846A (en) * 2006-04-11 2007-10-25 Sumitomo Heavy Industries Environment Co Ltd Wastewater treatment system and wastewater treatment method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007196208A (en) * 2005-12-28 2007-08-09 Sumitomo Heavy Ind Ltd Wastewater treatment apparatus and wastewater treatment method
JP2007196207A (en) * 2005-12-28 2007-08-09 Sumitomo Heavy Ind Ltd Wastewater treatment apparatus and wastewater treatment method
JP2007275847A (en) * 2006-04-11 2007-10-25 Sumitomo Heavy Industries Environment Co Ltd Wastewater treating apparatus and wastewater treating method
JP2007275846A (en) * 2006-04-11 2007-10-25 Sumitomo Heavy Industries Environment Co Ltd Wastewater treatment system and wastewater treatment method

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