JPS6119835Y2 - - Google Patents

Info

Publication number
JPS6119835Y2
JPS6119835Y2 JP1982003110U JP311082U JPS6119835Y2 JP S6119835 Y2 JPS6119835 Y2 JP S6119835Y2 JP 1982003110 U JP1982003110 U JP 1982003110U JP 311082 U JP311082 U JP 311082U JP S6119835 Y2 JPS6119835 Y2 JP S6119835Y2
Authority
JP
Japan
Prior art keywords
pipe
tank
return
water
aeration
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
JP1982003110U
Other languages
Japanese (ja)
Other versions
JPS57145593U (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 JP1982003110U priority Critical patent/JPS6119835Y2/ja
Publication of JPS57145593U publication Critical patent/JPS57145593U/ja
Application granted granted Critical
Publication of JPS6119835Y2 publication Critical patent/JPS6119835Y2/ja
Expired 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

Description

【考案の詳細な説明】 本考案は、有機性汚水を曝気処理して浄化する
とともに、処理中に生成する汚泥を、外部に排出
することなく、閉回路式に自己消化させるように
した装置に関するもので、以下添付の図面に基い
て具体的に説明する。
[Detailed description of the invention] The present invention relates to a device that purifies organic sewage through aeration treatment, and that self-extinguishes the sludge generated during the treatment in a closed-circuit manner without discharging it to the outside. This will be specifically explained below based on the attached drawings.

1は汚濁物質分解槽で、その内部には、多数の
網板状の好気性菌増殖板2が、所定間隔をもつ
て、かつ一定方向に向けて斜設され、同じく底部
には、多数の上向噴水孔3が穿設された水平の散
水管4が固設されている。
Reference numeral 1 denotes a pollutant decomposition tank, inside which a large number of mesh plate-like aerobic bacteria growth plates 2 are installed obliquely at predetermined intervals and in a certain direction; A horizontal sprinkler pipe 4 in which an upward water fountain hole 3 is bored is fixedly installed.

分解槽1の上部は、中間に弁5を備える連通管
6をもつて、次段の曝気槽7に接続されている。
The upper part of the decomposition tank 1 is connected to the next stage aeration tank 7 through a communication pipe 6 having a valve 5 in the middle.

分解槽1及び曝気槽7は、それぞれ頂板1a,
7aをもつて、実質的に密閉されている。
The decomposition tank 1 and the aeration tank 7 each have a top plate 1a,
7a, and is substantially sealed.

曝気槽7内における連通管6が接続されている
前側壁7aより、後側壁7b近くまでの間には、
網板または平板よりなる多数の垂直の汚泥付着板
8が、所定間隔をもつて、上端は水面より若干低
く、下端は付着曝気槽7の底面より若干上方に位
置するように固設され、最後位の付着板8′と後
側壁7bの間は、上昇路9となつている。
In the aeration tank 7, from the front wall 7a to which the communication pipe 6 is connected to the rear wall 7b,
A large number of vertical sludge adhesion plates 8 made of mesh plates or flat plates are fixedly installed at predetermined intervals so that the upper ends are slightly lower than the water surface and the lower ends are located slightly above the bottom of the adhesion aeration tank 7. A rising path 9 is formed between the second attachment plate 8' and the rear wall 7b.

上昇路9の下部には、多数の噴気孔10が穿設
された垂直の噴気管11が配設され、噴気管11
の上端は、送気管12をもつて、曝気槽7の外部
に設置されたブロアー13に接続されている。
A vertical fumarole pipe 11 with a large number of fumarole holes 10 is disposed at the bottom of the ascending passage 9.
The upper end of the aeration tank 7 is connected to a blower 13 installed outside the aeration tank 7 through an air supply pipe 12 .

上昇路9の上部は、中間に弁14を備える浄水
管15をもつて、次段の消毒槽16に接続され、
消毒槽16には排水管17が接続されている。
The upper part of the ascending path 9 is connected to the next stage disinfection tank 16 with a water purification pipe 15 having a valve 14 in the middle.
A drain pipe 17 is connected to the disinfection tank 16.

上昇路9の下端は、返送管18をもつて返送ポ
ンプ19の吸水口に接続され、返送ポンプ19の
吐出口は、中間に弁20を備える吐出管21をも
つて、酸素溶解槽22に接続されている。
The lower end of the ascending path 9 is connected to the water intake port of a return pump 19 through a return pipe 18, and the discharge port of the return pump 19 is connected to an oxygen dissolution tank 22 through a discharge pipe 21 having a valve 20 in the middle. has been done.

吐出管21より分岐する逆送管23は、弁24
とインジエクター式空気混入装置25を経て、前
記返送管18に接続されている。
A reverse feed pipe 23 branching from the discharge pipe 21 has a valve 24.
It is connected to the return pipe 18 via an injector type aeration device 25.

酸素溶解槽22は、空気混入装置25により吸
入された空気を、返送水に溶解させるためのもの
で、その下部から導出された送水管27は、弁2
6及び混合器28を経て、上記散水管4の中央部
に接続されている。
The oxygen dissolving tank 22 is for dissolving the air taken in by the aeration device 25 into return water, and the water pipe 27 led out from the bottom of the tank 22 is connected to the valve 2.
6 and a mixer 28, it is connected to the center of the water sprinkler pipe 4.

また混合器28には、中間に弁29を備える汚
水管30が接続されている。
Further, a waste water pipe 30 having a valve 29 in the middle is connected to the mixer 28 .

なお、31,32は、それぞれ分解槽1と曝気
槽7の頂板1a,7aに貫設された排気管であ
る。
In addition, 31 and 32 are exhaust pipes installed through the top plates 1a and 7a of the decomposition tank 1 and the aeration tank 7, respectively.

次に、上記構成の本案装置の作用について説明
する。
Next, the operation of the present device having the above configuration will be explained.

汚水管30より送られた汚水は、混合器28に
おいて、後述するように送水管27より返送され
る溶存酸素と微細な気泡を多量に含む返送水と混
合され、散水管4を介して、分解槽1の底部へ、
概ね均一に送り込まれる。
The sewage sent from the sewage pipe 30 is mixed in the mixer 28 with return water returned from the water pipe 27 containing a large amount of dissolved oxygen and fine bubbles as described later, and is decomposed via the water sprinkler pipe 4. To the bottom of tank 1,
It is fed almost uniformly.

すると、汚水および返送水中の有機性汚濁物質
は、気泡と共に、一定方向に傾斜している多数の
網状の各増殖板2を順次通過する間に、増殖板2
に効果的に付着して、好気性菌が繁殖し、増殖板
2面には、好気性菌の集団が形成される。
Then, the organic pollutants in the sewage and returned water, together with air bubbles, sequentially pass through each of the many reticular growth plates 2 that are inclined in a certain direction.
The aerobic bacteria effectively adhere to the substrate and propagate, and a population of aerobic bacteria is formed on the two surfaces of the growth plate.

この集団は、送水管27より供給された多量の
溶存酸素の助けにより、汚水中の有機性汚濁物質
を急速に酸化分解して浄化するとともに、好気性
菌の共食い現象により、余剰汚泥は自己消化され
る。
With the help of a large amount of dissolved oxygen supplied from the water pipe 27, this group rapidly oxidizes and decomposes organic pollutants in the wastewater to purify it, and the surplus sludge is self-digested by the cannibalism phenomenon of aerobic bacteria. be done.

このようにして1次処理の終つた汚水は、連通
管6を経て、曝気槽7に流入する。
The wastewater that has undergone the primary treatment in this manner flows into the aeration tank 7 via the communication pipe 6.

曝気槽7の上昇路9においては、噴気管11よ
り噴出する空気により、汚水にさらに酸素が供給
されるとともに、上昇水流が発生する。
In the ascending path 9 of the aeration tank 7, oxygen is further supplied to the wastewater by the air ejected from the fumarole pipe 11, and an ascending water flow is generated.

酸素が補給されて上昇した汚水は、連通管6よ
り流入する汚水とともに、多数の付着板8の間を
下降する。
The sewage that has risen after being supplemented with oxygen descends between a large number of attachment plates 8 together with the sewage that flows in from the communication pipe 6.

その間に、汚水中の汚濁物質は、付着板8に付
着し、一方、噴気管11より吹き込まれた空気に
より、好気性菌が付着板8面上に繁殖するため、
汚水の2次浄化が行われるとともに、余剰汚泥の
自己消化が行われる。
During this time, the pollutants in the wastewater adhere to the adhesion plate 8, and on the other hand, aerobic bacteria breed on the adhesion plate 8 due to the air blown from the fumarole pipe 11.
Secondary purification of sewage is performed, and excess sludge is self-extinguished.

処理された汚水は、浄水管15を経て消毒槽1
6に導かれ、消毒されて排水管17より放出され
る。
The treated wastewater passes through a water purification pipe 15 to a disinfection tank 1.
6, sterilized, and discharged from a drain pipe 17.

曝気槽7において処理された汚水の一部は、返
送管18を経て、返送ポンプ19により、酸素溶
解槽22に送り込まれる。
A part of the wastewater treated in the aeration tank 7 is sent to the oxygen dissolution tank 22 by a return pump 19 via a return pipe 18 .

返送ポンプ19の吐出口は、また空気混入装置
25を経て吸水口に接続されているので、酸素溶
解槽22には返送汚水とともに、空気混入装置2
5より吸引された空気も共に送り込まれる。
The discharge port of the return pump 19 is also connected to the water inlet via the aeration device 25, so that the oxygen dissolution tank 22 receives the returned wastewater as well as the aeration device 2.
The air sucked from 5 is also sent together.

酸素溶解槽22において、返送汚水は空気中の
酸素を十分に溶解するとともに、空気は微細な気
泡となり、上記したように、混合器28において
汚水と混合して、分解槽1に送り込まれる。
In the oxygen dissolution tank 22, the returned sewage sufficiently dissolves oxygen in the air, and the air becomes fine bubbles, which are mixed with the sewage in the mixer 28 and sent to the decomposition tank 1, as described above.

上述のようにして、汚水管30より流入した汚
水は、急速に浄化されるとともに、生成する余剰
汚泥は、装置内において、自己消化され、装置内
に溜つたり、装置外へ排出されたりすることはな
く、好都合である。
As described above, the sewage flowing in from the sewage pipe 30 is rapidly purified, and the generated surplus sludge is self-extinguished within the device, and either accumulates within the device or is discharged outside the device. That's not a problem, it's convenient.

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

第1図は、本案装置の一例を概示する配置図、
第2図は、第1図のA−A線における縦断面図で
ある。 1……汚濁物質分解槽、2……増殖板、3……
噴水孔、4……散水管、5……弁、6……連通
管、7……曝気槽、7a……前側壁、7b……後
側壁、8……汚泥付着板、9……上昇路、10…
…噴気孔、11……噴気管、12……送気管、1
3……ブロアー、14……弁、15……浄水管、
16……消毒槽、17……排水管、18……返送
管、19……返送ポンプ、20……弁、21……
吐出管、22……酸素溶解槽、23……逆送管、
24……弁、25……空気混入装置、26……
弁、27……送水管、28……混合器、29……
弁、30……汚水管、31,32……排気管。
FIG. 1 is a layout diagram schematically illustrating an example of the proposed device;
FIG. 2 is a longitudinal sectional view taken along line A-A in FIG. 1. 1... Pollutant decomposition tank, 2... Growth plate, 3...
Fountain hole, 4...Water pipe, 5...Valve, 6...Communication pipe, 7...Aeration tank, 7a...Front side wall, 7b...Rear side wall, 8...Sludge adhesion plate, 9...Rising path , 10...
... Fumarole, 11... Fumarole pipe, 12... Air pipe, 1
3...Blower, 14...Valve, 15...Water purification pipe,
16...Disinfection tank, 17...Drain pipe, 18...Return pipe, 19...Return pump, 20...Valve, 21...
Discharge pipe, 22...oxygen dissolution tank, 23...reverse feed pipe,
24... Valve, 25... Air mixing device, 26...
Valve, 27... Water pipe, 28... Mixer, 29...
Valve, 30...Sewage pipe, 31, 32...Exhaust pipe.

Claims (1)

【実用新案登録請求の範囲】 (a) 内部に、一定方向に斜設した多数の網板状の
増殖板2を、相互に間隔をあけて配設するとと
もに、底部に散水管4を設けた汚濁物質分解槽
1と、 (b) 前部が前記汚濁物質分解槽1の上部に連な
り、内部に、多数の上下方向をなす汚泥付着板
8を、相互に間隔をあけて、かつその上端が水
面より若干下方に位置し、同じく下端が底面よ
り若干上方に位置するようにして配設するとと
もに、後側壁7bと最後位の汚泥付着板8′と
の間に、上下方向を向く汚水の上昇路を形成さ
せ、この上昇路の下部に、ブロアー13に連な
る噴気管11を設けてなる曝気槽7と、 (c) 曝気槽7における汚水上昇路の上部に連な
り、かつ排水管17を備える消毒槽16と、 (d) 曝気槽7内における処理水の一部を、返送ポ
ンプ19の入口側に導く返送管18と、 (e) 返送ポンプ19の出口側に接続されている酸
素溶解槽22と、 (f) 返送ポンプ19の出口側より分岐して、返送
管18の途中に接続され、かつ中間にインジエ
クター式空気混入装置25を備える逆送管23
と、 (g) 酸素溶解槽22内において、前記空気混入装
置25により吸入された空気が溶解されて、微
細な気泡を含有している返送水と、汚水管30
により導かれた未処理汚水とを混合して、上記
分解槽1内の散水管4に送り込むべく案内する
混合器28 とを備えることを特徴とする自己消化式汚水浄化
装置。
[Claims for Utility Model Registration] (a) A large number of net plate-like growth plates 2 are arranged diagonally in a certain direction, spaced apart from each other, and a water sprinkler pipe 4 is provided at the bottom. (b) The front part of the pollutant decomposition tank 1 is connected to the upper part of the pollutant decomposition tank 1, and inside thereof, there are a number of sludge adhesion plates 8 arranged in the vertical direction, spaced apart from each other, and whose upper ends are It is located slightly below the water surface, and the lower end is also located slightly above the bottom surface, and between the rear wall 7b and the rearmost sludge adhesion plate 8', the sewage rises vertically. (c) an aeration tank 7 which is provided with a fumarole pipe 11 connected to a blower 13 in the lower part of the ascending channel; (d) a return pipe 18 that guides a portion of the treated water in the aeration tank 7 to the inlet side of the return pump 19; and (e) an oxygen dissolution tank 22 connected to the outlet side of the return pump 19. (f) A return pipe 23 that branches from the outlet side of the return pump 19, is connected to the middle of the return pipe 18, and is provided with an injector type air mixing device 25 in the middle.
(g) In the oxygen dissolving tank 22, the air taken in by the aeration device 25 is dissolved to produce return water containing fine air bubbles and the waste water pipe 30.
A self-extinguishing type sewage purification device characterized by comprising a mixer 28 for mixing the untreated sewage introduced by the decomposition tank 1 and guiding it to the sprinkler pipe 4 in the decomposition tank 1.
JP1982003110U 1982-01-13 1982-01-13 Expired JPS6119835Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1982003110U JPS6119835Y2 (en) 1982-01-13 1982-01-13

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1982003110U JPS6119835Y2 (en) 1982-01-13 1982-01-13

Publications (2)

Publication Number Publication Date
JPS57145593U JPS57145593U (en) 1982-09-13
JPS6119835Y2 true JPS6119835Y2 (en) 1986-06-14

Family

ID=29801542

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1982003110U Expired JPS6119835Y2 (en) 1982-01-13 1982-01-13

Country Status (1)

Country Link
JP (1) JPS6119835Y2 (en)

Also Published As

Publication number Publication date
JPS57145593U (en) 1982-09-13

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