JPH0717398U - Sludge activation device in sewage treatment system - Google Patents

Sludge activation device in sewage treatment system

Info

Publication number
JPH0717398U
JPH0717398U JP071024U JP7102493U JPH0717398U JP H0717398 U JPH0717398 U JP H0717398U JP 071024 U JP071024 U JP 071024U JP 7102493 U JP7102493 U JP 7102493U JP H0717398 U JPH0717398 U JP H0717398U
Authority
JP
Japan
Prior art keywords
pipe
sludge
aeration tank
treatment system
sewage treatment
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
JP071024U
Other languages
Japanese (ja)
Other versions
JPH081039Y2 (en
Inventor
充弘 藤原
Original Assignee
充弘 藤原
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 充弘 藤原 filed Critical 充弘 藤原
Priority to JP1993071024U priority Critical patent/JPH081039Y2/en
Publication of JPH0717398U publication Critical patent/JPH0717398U/en
Application granted granted Critical
Publication of JPH081039Y2 publication Critical patent/JPH081039Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

  • Activated Sludge Processes (AREA)

Abstract

(57)【要約】 【目的】 汚泥と浄化水の分離作用が曝気槽に入る前の
段階からすでに進行して、曝気槽に入った時にはかなり
分離が進んでいるようにし、これにより、前記分離がよ
り効果的に進み、かつ、曝気槽の容量(面積)や施工コ
ストさらに電力消費が大幅に削減されるようにするこ
と。 【構成】 下水処理システムにおける曝気槽よりも上流
に配置される前後のパイプ間に連通して接続される汚泥
活性化装置であって、前記両パイプ間に配置される同パ
イプより数倍太径のパイプと、同パイプに設けられてエ
アー供給手段、微生物供給手段および攬拌手段のうち少
なくとも1つの手段が備わっていることを特徴とする。
(57) [Summary] [Purpose] The separation action of sludge and purified water has already progressed from the stage before entering the aeration tank, and the separation has progressed considerably when entering the aeration tank. Will be more effective, and the aeration tank capacity (area), construction cost, and power consumption will be significantly reduced. [Structure] A sludge activation device, which is connected to and communicates between pipes before and after arranged upstream of an aeration tank in a sewage treatment system, and has a diameter several times larger than that of the pipe arranged between the pipes. And at least one of an air supply means, a microorganism supply means, and an agitation means provided on the pipe.

Description

【考案の詳細な説明】 〔技術分野〕 この考案は、下水処理システムにおける汚泥活性化装置に関する。TECHNICAL FIELD The present invention relates to a sludge activating device in a sewage treatment system.

〔技術背景〕 下水処理システムには、第1図に示すように、雨水1や生活汚水2が第1パイ プ3を通じて抽水所(ポンプ場)4に流れ込むようになっている。 [Technical background] In the sewage treatment system, as shown in FIG. 1, rainwater 1 and domestic sewage 2 flow into a water extraction station (pump station) 4 through a first pipe 3.

抽水所4からの汚水は第2パイプ5を通じて沈砂池・スクリーン6を経由して予 備曝気槽7・沈澱池8に流れ込む。これらを通る間に汚水は砂や大きなゴミが取 り除かれる。つぎに、(本)曝気槽9で微生物(つりがね虫等)の入ったドロ水 (活性汚泥)が加えられるとともに、空気が吹き込まれて攪拌される。前記微生 物は、下水の中の汚れを吸着して沈みやすくなり、汚泥として濃縮槽10に導か れてのち、消化槽11・脱水機12・焼却炉13を通じて埋立地14に廃棄され る。前記曝気槽9からの下水は沈澄池(最終沈澱池)15に導かれ、ここで汚れ を吸着した微生物は池の底に沈んでゆき、上方には、浄化された水が残る。The sewage from the extraction station 4 flows into the preliminary aeration tank 7 / settling basin 8 through the second pipe 5 and the sand basin / screen 6. While passing through these, sewage is cleared of sand and large debris. Next, in the (main) aeration tank 9, the drooled water (activated sludge) containing microorganisms (such as a worm) is added, and the air is blown in and stirred. The micro-organisms adsorb the dirt in the sewage and are prone to sink, and are guided to the concentration tank 10 as sludge and then disposed of in the landfill 14 through the digestion tank 11, the dehydrator 12 and the incinerator 13. The sewage from the aeration tank 9 is led to a sedimentation pond (final sedimentation pond) 15, where microorganisms adsorbing dirt sink to the bottom of the pond, and purified water remains above.

この浄化水は、滅菌室16で消毒されて河川17に流される。The purified water is sterilized in the sterilization chamber 16 and then flowed into the river 17.

〔考案が解決決しようとする課題〕 前記下水処理システムにおいては、予備曝気槽7ならびに曝気槽9の段階に入 ってから曝気がなされるようになっているが、このようにすると、汚水が曝気な くして長い経路を経てのち、急激に曝気がなされる結果、これら曝気槽7,9に おける負荷が非常に大きくなる。これにより、これら曝気槽7,9はかなり大き な容量になって施工が大変でありかつコスト高になるとともに、急激な曝気であ るので、汚泥と浄化水との効果的な分離に多くの電力が必要になる不都合がある 。 [Problems to be resolved by the invention] In the sewage treatment system, aeration is performed after the preliminary aeration tank 7 and the aeration tank 9 are entered. After a long route without aeration, rapid aeration results in a very large load on these aeration tanks 7 and 9. As a result, these aeration tanks 7 and 9 have a considerably large capacity, which makes the construction difficult and costly, and because of the rapid aeration, it is often used for effective separation of sludge and purified water. It has the disadvantage of requiring power.

前記問題を解決するため、この考案の課題は、汚泥と浄化水の分離作用が曝気 槽に入る前の段階からすでに進行して、曝気槽に入った時にはかなり分離が進ん でいるようにし、これにより、前記分離がより効果的に進み、かつ、曝気槽の容 量(面積)や施工コストさらに電力消費が大幅に削減されるようにすることにあ る。 In order to solve the above-mentioned problem, the problem of this invention is that the separation action of sludge and purified water has already progressed from the stage before entering the aeration tank, and the separation has progressed considerably when entering the aeration tank. This will enable the separation to proceed more effectively and to significantly reduce the capacity (area) of the aeration tank, construction costs, and power consumption.

〔課題を解決するための手段〕 前記課題を解決するため、この考案は、下水処理システムにおける曝気槽より も上流に配置される前後のパイプ間に連通して接続される汚泥活性化装置であっ て、前記両パイプ間に配置される同パイプより数倍太径のパイプと、同パイプに 設けられてエアー供給手段、微生物供給手段および攪拌手段のうち少なくとも1 つの手段が備わっていることを特徴とする。 [Means for Solving the Problems] In order to solve the above problems, the present invention provides a sludge activating device which is connected to and communicates between front and rear pipes arranged upstream of an aeration tank in a sewage treatment system. And a pipe having a diameter several times larger than the pipe arranged between the two pipes, and at least one of an air supply unit, a microorganism supply unit, and a stirring unit provided on the pipe. And

〔実施例〕 以下、この考案を図示した実施例を参照しつつ詳細に説明する。 Embodiment Hereinafter, the present invention will be described in detail with reference to the illustrated embodiments.

第1図は、前記した下水処理システムであるが、その丸印を付した個所Aにこ の考案にかかる汚泥活性化装置が組み込まれる。同個所Aは、抽水所4よりも上 流と、同抽水所4・沈砂池6間の2個所であるが、実際の配置個所はこれらの両 者あるいはそのうちの一方である。その他の個所に設けられることもある。 FIG. 1 shows the sewage treatment system described above, and the sludge activating device according to the present invention is incorporated in the circled portion A. The location A is two locations upstream of the water extraction station 4 and between the water extraction station 4 and the sand basin 6, but the actual location is either or both of them. It may be provided at other locations.

第2図は、たとえば、抽水所4前に装置が組み込まれる場合を例示している。 FIG. 2 illustrates the case where the device is installed in front of the water extraction station 4, for example.

第1パイプ3,3は土中において互いに離間して埋め込まれている。これら両パ イプ3,3間に汚泥活性化装置が組み込まれて接続され、かつ、埋め込まれるよ うになっている。第1パイプ3,3間に、同パイプ3の数倍(実施例では3倍程 度)太径のパイプ25が接続され、同パイプ25の上部にエアレーションを引き 起こす攪拌手段26を備えてなるものである。The first pipes 3 are embedded in the soil while being separated from each other. A sludge activation device is installed between these pipes 3 and 3, and is connected and embedded. A pipe 25 having a diameter several times as large as that of the pipe 3 (about three times in the embodiment) is connected between the first pipes 3 and 3, and a stirring means 26 for causing aeration is provided on the upper portion of the pipe 25. It is a thing.

前記パイプ25の下部には汚泥排出口27が開口している。同実施例の装置に よる場合、第1パイプ3からの汚水がパイプ25内に入ると、同パイプ25が充 分に太径であるので急激に流速を下げ、これにより、前記分離が流れを保ちなが ら効果的になされるとともに、パイプ25の下部に汚泥が溜まりやすくなって前 記汚泥排出口27を通して排出される。 A sludge discharge port 27 is opened at the bottom of the pipe 25. According to the apparatus of the embodiment, when the dirty water from the first pipe 3 enters the pipe 25, the pipe 25 has a sufficiently large diameter so that the flow velocity is rapidly reduced, whereby the separation causes the flow. While being effectively maintained, sludge easily accumulates in the lower part of the pipe 25 and is discharged through the sludge discharge port 27.

この汚泥は、第1図の脱水機12の前段階あるいは図示されていないホッパー に導入される。前記パイプ25は配管の1つであるティー(T字形のもの)を利 用することができる。前記パイプ25には空気導入パイプおよび/または微生物 導入手段が設けられることがある。 This sludge is introduced into the hopper (not shown) before the dehydrator 12 shown in FIG. As the pipe 25, a tee (T-shaped one) which is one of the pipes can be used. The pipe 25 may be provided with an air introduction pipe and / or a microorganism introduction means.

第3図に示す実施例は、前記実施例同様に、第1パイプ3,3間に、太い径を したパイプ30を接続したものであるが、同パイプ30には、空気導入手段31 の他に微生物循環供給手段32が設けられている。同手段32は、内部に微生物 が入れられていてポンプで供給されるようになっている。 The embodiment shown in FIG. 3 is similar to the above-mentioned embodiment in that a pipe 30 having a large diameter is connected between the first pipes 3 and 3. Is provided with a microbial circulation supply means 32. The means 32 has a microorganism inside and is supplied by a pump.

同手段32は、バルブ35を有する導出パイプ33の他に循環導入パイプ34 も備えているとともに、バルブ36により開閉自在な微生物補給手段37も備え ている。前記第1パイプ3から流れてくるものは殆ど汚泥であることが多く、同 汚泥は通常活性化していない場合が殆どである。 The means 32 is provided with a circulation introduction pipe 34 in addition to the outlet pipe 33 having a valve 35, and is also provided with a microorganism supply means 37 which can be opened and closed by a valve 36. Most of what flows from the first pipe 3 is sludge, and the sludge is usually not activated in most cases.

そこで、前記微生物循環供給手段32により微生物が供給されると共に空気導 入手段31から空気が供給される。 Therefore, the microorganisms are supplied by the microorganism circulation supply means 32 and the air is supplied from the air introduction means 31.

これにより、図示のように、汚泥に空気および微生物が混入して汚泥が活性化 して分解効率が良くなって流れる。パイプ30の下部からは汚泥が排出されるよ うにしてもよい。 As a result, as shown in the figure, air and microorganisms are mixed into the sludge, the sludge is activated, the decomposition efficiency is improved, and the sludge flows. Sludge may be discharged from the lower part of the pipe 30.

〔考案の効果〕 この考案は以上のように構成されているので、汚泥と浄化水の分離作用が曝気 槽に入る前の段階からすでに進行して、曝気槽に入った時にはかなり分離が進ん でいるようになるので、前記装置を設けるだけで曝気槽の容量(面積)や施工コ ストさらに電力消費が削減されるようになる。 [Effect of the device] Since this device is constructed as described above, the separation action of sludge and purified water has already progressed from the stage before entering the aeration tank, and when it enters the aeration tank, the separation proceeds considerably. Therefore, the capacity (area) of the aeration tank, the construction cost, and the power consumption can be reduced simply by providing the above device.

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

第1図は下水処理システムと同システムに組み込まれる
本装置の配置を示すフローシート、第2図は本装置の第
1実施例を示す模式図、第3図は本装置の第2実施例を
示す模式図である。 7,9…曝気槽 3…第1パイプ 25,30…パイプ
31…空気導入手段 32…微生物導入手段 26…攪拌手段
FIG. 1 is a flow sheet showing the arrangement of a sewage treatment system and this device incorporated in the same system, FIG. 2 is a schematic diagram showing a first embodiment of this device, and FIG. 3 is a second embodiment of this device. It is a schematic diagram which shows. 7, 9 ... Aeration tank 3 ... 1st pipe 25, 30 ... Pipe 31 ... Air introduction means 32 ... Microbe introduction means 26 ... Stirring means

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 1 下水処理システムにおける曝気槽よりも上流に配置
される前後のパイプ間に連通して接続される汚泥活性化
装置であって、前記両パイプ間に配置される同パイプよ
り数倍太径のパイプと、同パイプに設けられてエアー供
給手段、微生物供給手段および攪拌手段のうち少なくと
も1つの手段が備わっていることを特徴とする下水処理
システムにおける汚泥活性化装置。
1 A sludge activating device that is connected to and communicates between the front and rear pipes arranged upstream of the aeration tank in the sewage treatment system, and has a diameter several times larger than the pipe arranged between the pipes. And a sludge activation device in a sewage treatment system, which is provided in the pipe and is provided with at least one of an air supply unit, a microorganism supply unit, and a stirring unit.
JP1993071024U 1993-11-22 1993-11-22 Sludge activation device in sewage treatment system Expired - Lifetime JPH081039Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1993071024U JPH081039Y2 (en) 1993-11-22 1993-11-22 Sludge activation device in sewage treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1993071024U JPH081039Y2 (en) 1993-11-22 1993-11-22 Sludge activation device in sewage treatment system

Publications (2)

Publication Number Publication Date
JPH0717398U true JPH0717398U (en) 1995-03-28
JPH081039Y2 JPH081039Y2 (en) 1996-01-17

Family

ID=13448550

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1993071024U Expired - Lifetime JPH081039Y2 (en) 1993-11-22 1993-11-22 Sludge activation device in sewage treatment system

Country Status (1)

Country Link
JP (1) JPH081039Y2 (en)

Also Published As

Publication number Publication date
JPH081039Y2 (en) 1996-01-17

Similar Documents

Publication Publication Date Title
CN102775025B (en) Municipal life wastewater treatment system with high efficiency and low energy consumption
CN103449658B (en) Sewage treatment method
CN101323494A (en) Carwash circulating water processing system
CN107082540A (en) A kind of integrated sewage treating apparatus and its handling process
CN101591118A (en) Multifunctional general sewage treatment system
CN107555600A (en) A kind of sewage disposal system
CN106865905A (en) It is a kind of to meet the sewage disposal system for being directly discharged into the class water body standard of II class of earth's surface III
CN202945124U (en) Urban sewage treatment system with high efficiency and low energy consumption
CN2659883Y (en) Domestic sewage treatment plant
JPH0646556Y2 (en) Sludge activation device in sewage treatment system
JPH081039Y2 (en) Sludge activation device in sewage treatment system
CN206590953U (en) A kind of plate membrane bioreactor sewage-treatment plant
CN201268648Y (en) Multifunctional universal sewage treatment system
CN101293724A (en) Miniature general use sewage treatment system
CN206244583U (en) Integrated water treatment facilities
JPH081040Y2 (en) Sludge activation device in sewage treatment system
CN109437492A (en) Sewage disposal system for town domestic sewage purified treatment
CN1234626C (en) Process for comprehensively treating high-concentration water organic water
JP3125265B2 (en) Sludge treatment function enhancement system for septic tank
CN108529824A (en) A kind of ship shipping sewage treatment unit
CN209442733U (en) A kind of submerged MBRs phosphating solution processing equipment
CN106167336A (en) Integrated water treatment facilities
CN208182783U (en) A kind of integrated purification of waste water waste gas recovery equipment
CN207877382U (en) A kind of biological carbon and phosphorous removal system and a kind of intelligent zero-emission bio-toilet
CN206783409U (en) Administer the gravity biological selector of continuous flow biological reaction device filamentous bulking of activated sludge