JPH027680Y2 - - Google Patents

Info

Publication number
JPH027680Y2
JPH027680Y2 JP1983121078U JP12107883U JPH027680Y2 JP H027680 Y2 JPH027680 Y2 JP H027680Y2 JP 1983121078 U JP1983121078 U JP 1983121078U JP 12107883 U JP12107883 U JP 12107883U JP H027680 Y2 JPH027680 Y2 JP H027680Y2
Authority
JP
Japan
Prior art keywords
oxidizing liquid
tank
liquid
pipe
compressed air
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.)
Expired
Application number
JP1983121078U
Other languages
Japanese (ja)
Other versions
JPS6028098U (en
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 filed Critical
Priority to JP1983121078U priority Critical patent/JPS6028098U/en
Publication of JPS6028098U publication Critical patent/JPS6028098U/en
Application granted granted Critical
Publication of JPH027680Y2 publication Critical patent/JPH027680Y2/ja
Granted 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

  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Description

【考案の詳細な説明】 〔考案の技術的分野〕 本考案は比較的小規模な水処理において、酸化
液の一部を脱窒槽に戻す装置に関する。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention relates to an apparatus for returning a portion of an oxidizing liquid to a denitrification tank in relatively small-scale water treatment.

〔考案の技術的背景とその問題点〕[Technical background of the invention and its problems]

従来の水処理においては、酸化槽で酸化した処
理液の一部を嫌気性脱窒槽に戻して、酸化処理水
中の硝酸態窒素、亜硝酸態窒素を減少させる手段
として、第1図に示すように、酸化槽2の水中に
垂直管20を挿入し、この垂直管20の途中より
嫌気性脱窒槽1の水面上へ溢流管21を導出し、
さらに垂直管20中に圧縮空気導入管22を挿入
しておき、圧縮空気を導入管22内に送り込み、
この水中に気泡を撹散させて液の比重を軽くして
垂直管20中の水位を上昇させ、液を溢流管21
より脱窒槽1へ送り込んだものであるが、垂直管
20中の水位を上げるためには大量の空気を送り
込む必要があり空気圧縮機の動力を多く必要とし
た。また溢流量を調節することが出来ないから一
度に大量に溢出させるか或は停止させるかであつ
た。
In conventional water treatment, a portion of the treated liquid oxidized in the oxidation tank is returned to the anaerobic denitrification tank to reduce nitrate nitrogen and nitrite nitrogen in the oxidized water, as shown in Figure 1. Then, a vertical pipe 20 is inserted into the water of the oxidation tank 2, and an overflow pipe 21 is led out from the middle of this vertical pipe 20 onto the water surface of the anaerobic denitrification tank 1.
Furthermore, a compressed air introduction pipe 22 is inserted into the vertical pipe 20, and compressed air is sent into the introduction pipe 22.
Air bubbles are dispersed in this water to reduce the specific gravity of the liquid and raise the water level in the vertical pipe 20, causing the liquid to flow into the overflow pipe 20.
However, in order to raise the water level in the vertical pipe 20, it was necessary to send a large amount of air, which required a large amount of power from the air compressor. Furthermore, since the amount of overflow cannot be adjusted, it is necessary to either allow a large amount to overflow at once or to stop the overflow.

〔考案の目的〕[Purpose of invention]

本考案は上述の問題に鑑み、嫌気性処理がなさ
れる脱窒槽と、酸化液が貯留される酸化液槽と、
この酸化液槽に挿入されたポンプ本体とよりな
り、このポンプ本体が、曝気用圧縮空気の一部が
導入されるとともに下端吸入口に圧縮空気の導入
によつて閉じ水圧によつて開く弁を有する吸入筒
と、この吸入筒の前記吸入口近くより分岐して液
面上に立ち上らせ前記脱窒槽に酸化液を吐出する
吐出筒より構成され、曝気用空気の一部を用いて
酸化液の一部を吸い上げてこれを脱窒槽に吐出さ
せ少い動力で酸化液を戻しまたその調節も可能に
しようとするものである。
In view of the above-mentioned problems, the present invention includes a denitrification tank in which anaerobic treatment is performed, an oxidizing liquid tank in which oxidizing liquid is stored,
The main body of the pump is inserted into the oxidizing liquid tank, and the pump main body receives a portion of the compressed air for aeration and has a valve at the lower end inlet that is closed by the introduction of compressed air and opened by water pressure. and a discharge tube that branches from near the suction port of the suction tube and rises above the liquid surface to discharge the oxidizing liquid into the denitrification tank. The purpose is to suck up a portion of the liquid and discharge it into a denitrification tank, thereby returning the oxidizing liquid with a small amount of power and making it possible to adjust the oxidizing liquid.

〔考案の概要〕[Summary of the idea]

本考案は、嫌気性処理がなされる脱窒槽と、酸
化液が貯留される酸化液槽と、この酸化液槽中に
挿入されたポンプ本体とよりなり、このポンプ本
体が、曝気用圧縮空気の一部が導入されるととも
に下端吸入口に圧縮空気の導入によつて閉じ水圧
によつて開く弁を有する吸入筒と、この吸入筒の
前記吸入口近くより分岐して液面上に立ち上らせ
前記脱窒槽に酸化液を吐出する吐出筒とより成
り、曝気用圧縮空気の一部で酸化液の吸上げ作用
をさせるものである。
The present invention consists of a denitrification tank where anaerobic treatment is performed, an oxidizing liquid tank where oxidizing liquid is stored, and a pump body inserted into the oxidizing liquid tank. A part of the suction cylinder is introduced into the lower end, and has a valve that closes when compressed air is introduced into the lower end suction port and opens by water pressure. and a discharge tube for discharging the oxidizing liquid into the denitrification tank, and a portion of the aeration compressed air acts to suck up the oxidizing liquid.

〔考案の実施例〕[Example of idea]

本考案の一実施例を添附図面について説明す
る。
An embodiment of the present invention will be described with reference to the accompanying drawings.

1は原水が導入され嫌気性処理がなされる脱窒
槽、2は酸化液槽で空気圧縮機3より導出された
圧縮空気管5より分岐した曝気管4が導入され、
さらにポンプ本体6が挿入されている。
1 is a denitrification tank into which raw water is introduced and subjected to anaerobic treatment; 2 is an oxidizing liquid tank; an aeration pipe 4 branched from a compressed air pipe 5 led out from an air compressor 3 is introduced;
Furthermore, the pump body 6 is inserted.

ポンプ本体6は酸化液槽2の水面上より垂直に
水中深く挿入された細長管状の吸入筒7とこの吸
入筒7の下端近くより分岐され吸入筒7に沿つて
立ち上らせ上端を水面上に突出させた細長管状の
吐出筒8とより成り、吸入筒7の上端には、通気
管18が連通され、下端に開口した吸入口9の弁
座10に臨ませて板状の弁11が開閉自在に軸着
されている。さらに吸入口9の近くで分岐された
吐出筒8の上端は屈曲されて吐出口12が仕切壁
13より脱窒槽1の水面上に開口されている。ま
た、前記通気管18は三方切換電磁弁14を介し
て圧縮空気管5に連通され通路15の切換によつ
て吸入筒7を圧縮空気管5又は大気と連通させる
ようになつている。さらに三方切換電磁弁14に
はこの電磁弁14の切換時間を設定したタイマー
を有する操作用電源盤16が接続されている。1
7は電源である。
The pump body 6 includes an elongated tubular suction tube 7 that is vertically inserted deep into the water above the water surface of the oxidizing liquid tank 2, and is branched from near the lower end of this suction tube 7 and stands up along the suction tube 7 with the upper end above the water surface. A vent pipe 18 is communicated with the upper end of the suction cylinder 7, and a plate-shaped valve 11 faces the valve seat 10 of the suction port 9 opened at the lower end. It is pivoted so that it can be opened and closed. Furthermore, the upper end of the discharge tube 8 branched near the suction port 9 is bent so that the discharge port 12 is opened above the water surface of the denitrification tank 1 through the partition wall 13 . Further, the vent pipe 18 is communicated with the compressed air pipe 5 through a three-way switching solenoid valve 14, and by switching the passage 15, the suction pipe 7 is communicated with the compressed air pipe 5 or the atmosphere. Further, the three-way switching solenoid valve 14 is connected to an operating power supply board 16 having a timer for setting the switching time of the solenoid valve 14. 1
7 is a power source.

次に上述の実施例の作用を説明する。 Next, the operation of the above embodiment will be explained.

脱窒槽1に導入された原水は、ここで嫌気性条
件で分解処理された液が酸化液槽2に導入され挿
入された曝気管4によつて酸化され一部は放流さ
れる。さらに酸化液槽2に挿入されたポンプ本体
6の吸入筒7内には図示の状態では酸化液が槽2
の水位の高さまで導入されている。このとき電磁
弁14の通路15はa位置で圧縮空気管5と連通
され曝気管4へ送られる1000mma.q〜2000mma.qの
圧縮空気の一部が通気管18を介して吸入筒7に
圧入され、導入されていた液が押下げられて弁1
1を閉じ、液は吐出筒8に押し上げられ、先端の
吐出口12より脱窒槽1中に吐出される。このよ
うに曝気管4に送られる空気の一部は吸入筒7に
導入されるが、曝気管4からは引続き散気がされ
ている。次にタイマーが設定時間に動作し、電磁
弁14の通路15がb位置に切換えられると、通
路15は圧縮空気の導入が遮断され大気と連通す
る。そして通気管18を介して吸入筒7内が大気
と連通されるから、水圧によつて弁11が押し開
かれ液が吸入筒7内に槽2の水位の高さまで導入
される。このとき圧縮空気は全量が曝気管4へ送
られる。
The raw water introduced into the denitrification tank 1 is decomposed under anaerobic conditions, and the liquid is introduced into the oxidizing liquid tank 2, where it is oxidized by the inserted aeration pipe 4, and a portion is discharged. Further, in the illustrated state, the oxidizing liquid is inside the suction tube 7 of the pump body 6 inserted into the oxidizing liquid tank 2.
It has been introduced up to the water level of . At this time, the passage 15 of the solenoid valve 14 is in communication with the compressed air pipe 5 at position a, and a part of the compressed air of 1000 mma.q to 2000 mma.q sent to the aeration pipe 4 is forced into the suction cylinder 7 via the ventilation pipe 18. The liquid that had been introduced is pushed down and valve 1
1 is closed, the liquid is pushed up into the discharge cylinder 8, and is discharged into the denitrification tank 1 from the discharge port 12 at the tip. A part of the air sent to the aeration pipe 4 in this way is introduced into the suction cylinder 7, but air is still being diffused from the aeration pipe 4. Next, when the timer operates at a set time and the passage 15 of the solenoid valve 14 is switched to position b, the introduction of compressed air is cut off and the passage 15 communicates with the atmosphere. Since the inside of the suction cylinder 7 is communicated with the atmosphere through the ventilation pipe 18, the valve 11 is pushed open by the water pressure, and the liquid is introduced into the suction cylinder 7 up to the water level of the tank 2. At this time, the entire amount of compressed air is sent to the aeration pipe 4.

以上のような動作が繰り返されて酸化液槽2の
酸化液の一部が脱窒槽1に間歇的に戻される。
The above operations are repeated, and a portion of the oxidizing liquid in the oxidizing liquid tank 2 is intermittently returned to the denitrification tank 1.

尚以上の実施例は、脱窒槽1に隣接して酸化槽
としての酸化液槽2が設けられた場合について説
明したが、酸化液槽2が例えば酸化槽からの処理
液を更に貯留する槽である場合等脱窒槽1と酸化
液槽2間に他の槽が介在する場合は、図の鎖線に
示すように樋19を用いて酸化液を脱窒槽1に案
内することも出来る。
In the above embodiments, the oxidizing liquid tank 2 as an oxidizing tank is provided adjacent to the denitrification tank 1. In some cases, when another tank is interposed between the denitrification tank 1 and the oxidizing liquid tank 2, the oxidizing liquid can be guided to the denitrifying tank 1 using the gutter 19 as shown by the chain line in the figure.

〔考案の効果〕[Effect of idea]

本考案によれば、嫌気性処理がなされる脱窒槽
と、酸化液が貯留される酸化液槽と、この酸化液
槽中に挿入されたポンプ本体とよりなり、このポ
ンプ本体が、曝気用圧縮空気の一部が間けつ的に
導入されるとともに下端吸入口に圧縮空気の導入
によつて閉じ水圧によつて開く弁を有する吸入筒
と、この吸入筒の吸入口近くより分岐して液面上
に立ち上らせ前記脱窒槽に酸化液を吐出する吐出
筒とよりなるため、ポンプ本体は他の動力源を用
いることなく曝気用圧縮空気の圧力を利用して酸
化液を汲み上げてこれを脱窒槽に移すことが出
来、またポンプ本体で用いられる圧縮空気は曝気
用のそれの一部のみで充分であるから曝気作用に
支障を来すこともなく、ポンプ本体は吸入筒と吐
出筒よりなる簡単な構造であるから故障も少く保
守管理も容易である。さらに圧縮空気の導入管を
調節することによつて弁の開閉が調節されるから
酸化液の移送量を任意に調節することも可能とな
るものである。
According to the present invention, the pump body is composed of a denitrification tank in which anaerobic treatment is performed, an oxidizing liquid tank in which oxidizing liquid is stored, and a pump body inserted into the oxidizing liquid tank. A part of the air is introduced intermittently, and a suction cylinder has a valve that closes by introducing compressed air into the lower end suction port and opens by water pressure. Since it consists of a discharge tube that rises upward and discharges the oxidizing liquid into the denitrification tank, the pump body uses the pressure of compressed air for aeration to pump up the oxidizing liquid without using any other power source. It can be transferred to the denitrification tank, and since only a portion of the compressed air used in the pump body is sufficient for aeration, there is no problem with aeration, and the pump body is Because of its simple structure, there are few breakdowns and maintenance is easy. Furthermore, since the opening and closing of the valve is controlled by adjusting the compressed air introduction pipe, it is also possible to arbitrarily adjust the amount of oxidizing liquid transferred.

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

第1図は従来の装置の縦断側面図、第2図は本
考案の実施の一例を示す酸化液戻し装置の縦断側
面図である。 1……脱窒槽、2……酸化液槽、6……ポンプ
本体、7……吸入筒、8……吐出筒、9……吸入
口、11……弁。
FIG. 1 is a vertical side view of a conventional device, and FIG. 2 is a vertical side view of an oxidizing liquid return device showing an example of the implementation of the present invention. DESCRIPTION OF SYMBOLS 1... Denitrification tank, 2... Oxidizing liquid tank, 6... Pump body, 7... Suction cylinder, 8... Discharge cylinder, 9... Suction port, 11... Valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 嫌気性処理がなされる脱窒槽と、酸化液が貯留
される酸化液槽と、この酸化液槽中に挿入された
ポンプ本体とよりなり、このポンプ本体が、曝気
用圧縮空気の一部が間けつ的に導入されるととも
に下端吸入口に圧縮空気の導入によつて閉じ水圧
によつて開く弁を有する吸入筒と、この吸入筒の
吸入口近くより分岐して液面上に立ち上らせ前記
脱窒槽に酸化液を吐出する吐出筒とより成ること
を特徴とする水処理における酸化液戻し装置。
It consists of a denitrification tank in which anaerobic treatment is performed, an oxidizing liquid tank in which oxidizing liquid is stored, and a pump body inserted into this oxidizing liquid tank. A suction cylinder has a valve that is introduced into the lower end suction port by introducing compressed air and opens by water pressure, and the suction cylinder has a valve that branches near the suction port and rises above the liquid surface. An oxidizing liquid return device for water treatment, comprising a discharge tube for discharging the oxidizing liquid to the denitrification tank.
JP1983121078U 1983-08-03 1983-08-03 Oxidized liquid return device in water treatment Granted JPS6028098U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1983121078U JPS6028098U (en) 1983-08-03 1983-08-03 Oxidized liquid return device in water treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1983121078U JPS6028098U (en) 1983-08-03 1983-08-03 Oxidized liquid return device in water treatment

Publications (2)

Publication Number Publication Date
JPS6028098U JPS6028098U (en) 1985-02-25
JPH027680Y2 true JPH027680Y2 (en) 1990-02-23

Family

ID=30277247

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1983121078U Granted JPS6028098U (en) 1983-08-03 1983-08-03 Oxidized liquid return device in water treatment

Country Status (1)

Country Link
JP (1) JPS6028098U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9210340B2 (en) 1998-07-17 2015-12-08 Sony Corporation Imaging apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9210340B2 (en) 1998-07-17 2015-12-08 Sony Corporation Imaging apparatus

Also Published As

Publication number Publication date
JPS6028098U (en) 1985-02-25

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