JPS588392Y2 - Sewage septic tank - Google Patents

Sewage septic tank

Info

Publication number
JPS588392Y2
JPS588392Y2 JP1980090997U JP9099780U JPS588392Y2 JP S588392 Y2 JPS588392 Y2 JP S588392Y2 JP 1980090997 U JP1980090997 U JP 1980090997U JP 9099780 U JP9099780 U JP 9099780U JP S588392 Y2 JPS588392 Y2 JP S588392Y2
Authority
JP
Japan
Prior art keywords
chamber
partition plate
septic tank
aeration
sedimentation
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
JP1980090997U
Other languages
Japanese (ja)
Other versions
JPS5712298U (en
Inventor
佐々木正明
大岡進
Original Assignee
株式会社 西原環境衛生研究所
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 株式会社 西原環境衛生研究所 filed Critical 株式会社 西原環境衛生研究所
Priority to JP1980090997U priority Critical patent/JPS588392Y2/en
Publication of JPS5712298U publication Critical patent/JPS5712298U/ja
Application granted granted Critical
Publication of JPS588392Y2 publication Critical patent/JPS588392Y2/en
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

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

【考案の詳細な説明】 この考案は汚水浄化槽4体内の沈澱分離室とばり気室間
の仕切板の移流口構造に関するものである。
[Detailed description of the invention] This invention relates to an advection port structure of a partition plate between a sedimentation separation chamber and a flash chamber in a sewage septic tank 4.

浄化槽の槽体内に流入した汚水を沈澱分離、ばつ気、沈
澱処理する浄化槽において沈澱分離室の上澄液をばつ気
室に移流させる移流口の位置としては、第1図に示す如
く■−イの位置に構成するもの、■−口の位置に構成す
るもの、更には■−ハの位置に構成するもの等が知られ
ている。
In a septic tank where sewage that has flowed into the tank body of the septic tank is subjected to sedimentation separation, aeration, and sedimentation treatment, the position of the advection port that advects the supernatant liquid from the sedimentation separation chamber to the aeration chamber is as shown in Figure 1. There are known devices that are configured in the position , those that are configured in the ■-mouth position, and those that are configured in the ■-C position, etc.

即ち、■−イの構成では仕切板8の水面より上方に移流
ロイな形成したので、沈澱分離室2からばつ気室3への
汚水の流入は水位の上昇により行われるが逆流しない構
造となっている。
That is, in the configuration of (1)-(a), since the partition plate 8 is formed with an advection flow above the water surface, the sewage flows from the sedimentation separation chamber 2 to the aeration chamber 3 as the water level rises, but the structure is such that it does not flow back. ing.

従って汚水の流尺放流の水位差が大きく、仕切板への水
圧が大きくなり、又はつ気室内の汚泥の引き抜きが行わ
れないので清掃頻度を多くしなげれば、汚泥が放流され
易く、良好な水質を維持できない又■−口の構成では、
前述の仕切板8の水面近傍に移流口口を形成したので汚
水の流尺がない時はエアリフト効果等ばつ気室3内の攪
拌操作の影響で、ばつ気室内の汚水の一部が沈澱分離室
2に逆流し、それに伴い汚泥を沈澱分離室2に返送でき
るようになっている。
Therefore, if the difference in water level between the sewage scale discharge is large, the water pressure on the partition plate becomes large, or the sludge in the aeration chamber is not drawn out, cleaning may not be done frequently, and the sludge will be easily discharged, resulting in a good condition. In addition, the composition of the mouth cannot maintain a good water quality.
Since the advection port is formed near the water surface of the partition plate 8 mentioned above, when there is no flow rate of sewage, there is an air lift effect, etc. Due to the influence of the stirring operation in the air chamber 3, a part of the sewage in the air chamber is sedimented and separated. The sludge flows back into the chamber 2, and the sludge can be returned to the sedimentation separation chamber 2 accordingly.

しかし汚泥の引き抜き量は微量でよくこの構成ではかえ
って引き抜き過ぎてしまい、ばつ気室3内に浮遊する汚
泥が無くなってしまいMLSS(混合液浮遊物濃度)の
値が低下し良好な処理機能を保つことができない。
However, the amount of sludge drawn out is only a small amount, but with this configuration, too much sludge is drawn out, and there is no sludge floating in the aeration chamber 3, and the value of MLSS (mixed liquid suspended solids concentration) decreases, maintaining a good treatment function. I can't.

更に■−ハの構成では前述の第1の仕切板Iと水面下に
移流ロバを形成したので、ばつ気室3内での攪拌操作の
影響により常にばつ気室3と沈澱分離室2との汚水の入
れ替わりが生じ、汚泥が抜は過ぎてしまう。
Furthermore, in the configuration of ■-C, since an advection donkey is formed below the water surface with the first partition plate I described above, the flow between the aeration chamber 3 and the sedimentation separation chamber 2 is always maintained due to the influence of the stirring operation in the aeration chamber 3. The sewage is replaced and the sludge is drained too much.

このようにこの汚水浄化槽では汚泥の引き抜き量を適正
でなく、長期間ばつ気室3内の活性汚泥の濃度を適正に
維持できず浄化効率が低下する。
As described above, in this sewage purification tank, the amount of sludge drawn out is not appropriate, and the concentration of activated sludge in the aeration chamber 3 cannot be maintained appropriately for a long period of time, resulting in a decrease in purification efficiency.

この考案は上記の欠点を解消し、ばつ気室内の活性汚泥
の濃度を適正に維持するためのもので、最適の汚泥を引
き抜くことができるよう汚水の移流を適当にする移流口
を形成する仕切板構造を提供せんとするものである。
This idea eliminates the above-mentioned drawbacks and maintains the concentration of activated sludge in the aeration chamber at an appropriate level.The purpose of this idea is to eliminate the above-mentioned drawbacks and maintain an appropriate concentration of activated sludge in the aeration chamber. It is intended to provide a plate structure.

以下この考案を第2図及び第3図の実施例に基づき説明
する。
This invention will be explained below based on the embodiments shown in FIGS. 2 and 3.

第2図、第3図は汚水浄化槽で槽体1の内部を沈澱分離
室2とばつ気室3と沈澱室4消毒室5とに区分するため
ばつ気室3と沈澱室4とはセパレータ6で分割され、沈
澱室4と消毒室5とは消毒槽1で分割されており、沈澱
分離室2とばつ気室3とは仕切板8で分割されている。
Figures 2 and 3 show a sewage septic tank in which the interior of the tank body 1 is divided into a sedimentation separation chamber 2, an aeration chamber 3, a sedimentation chamber 4 and a disinfection chamber 5.The aeration chamber 3 and the sedimentation chamber 4 are separated by a separator 6 The sedimentation chamber 4 and the disinfection chamber 5 are divided by a disinfection tank 1, and the sedimentation separation chamber 2 and the aeration chamber 3 are divided by a partition plate 8.

仕切板8は水面下中央部分に連通口8aを、開口量調整
自在に穿設されると共に沈澱分離室のスカムの流入防止
のためほぼ中央より上方に、沈澱分離室2gIIjに張
り出した横断面コ状の貫通する突出部8bを形成した第
1の仕切板8と、前記連通口8aの下端より突出され前
記突出部8blllに上端の水面位置(通常時の水位よ
りや呈上方)迄に伸びを横断面コ状の第2の仕切板9と
、から構成されている。
The partition plate 8 is provided with a communication port 8a in the central part below the water surface, which can be freely adjusted in opening size, and has a cross-sectional co-portion projecting above the center into the sedimentation separation chamber 2gIIj to prevent scum from flowing into the sedimentation separation chamber. The first partition plate 8 has a penetrating protrusion 8b formed thereon, and the protrusion 8b protrudes from the lower end of the communication port 8a and extends to the water surface position at the upper end (slightly above the normal water level). and a second partition plate 9 having a U-shaped cross section.

流入管10かも流入された汚水は沈澱分離室2内で汚水
中の固形物を分離され上澄液が第2仕切板9の上端部か
ら流入し第1の仕切板8の移流口である連通口8aより
ばつ気室に移送される。
The wastewater that has flowed into the inflow pipe 10 is separated from solid matter in the sedimentation separation chamber 2, and the supernatant liquid flows from the upper end of the second partition plate 9 to the communication port which is the advection port of the first partition plate 8. It is transferred to the air chamber through the port 8a.

ばつ気室3内は散気管12かもの空気によりばつ気され
ているので汚水に混入した気泡のエアリフト効果や、攪
拌の影響により微量ずつばつ気室内液が、沈澱分離室へ
逆流しんれ替りを生ずる。
Since the inside of the aeration chamber 3 is aerated with air from the aeration pipe 12, the air lift effect of air bubbles mixed in the wastewater and the influence of stirring cause the liquid in the aeration chamber to be dispersed little by little, backflowing to the sedimentation separation chamber and being replaced. arise.

又汚水が沈澱分離室2に流入した際、沈澱分離室2から
ばつ気室3に向けて強い流れが生じ、目づまり等は起ら
ない。
Furthermore, when wastewater flows into the sedimentation separation chamber 2, a strong flow is generated from the sedimentation separation chamber 2 toward the aeration chamber 3, so that no clogging or the like occurs.

従って従来のようにばつ気室内の攪拌を直接利用して返
送するのではないため、微量ずつ最適量の汚泥を引き抜
くことができる。
Therefore, since the sludge is not returned by directly utilizing agitation in the aeration chamber as in the conventional case, the optimum amount of sludge can be drawn out minute by minute.

液体はばつ気室3かも更にセパレータ6の下方を経て沈
澱室4に移流し汚泥は重力返送され再びばつ気室3に返
送され活性汚泥により酸化分解された上澄液は消毒槽7
の消毒室5に入り消毒された後、槽体1外に流出管13
より放出される。
The liquid is advected into the settling chamber 4 via the aeration chamber 3 and further below the separator 6, and the sludge is returned by gravity and returned to the aeration chamber 3 again.
After entering the disinfection chamber 5 and being disinfected, the outflow pipe 13 is discharged outside the tank body 1.
more released.

同第2の仕切板9は第4図に示すように上端部の水位線
よりやや上方から水面下に向けてV字状の切欠部9aを
形成すれば沈澱分離室2とばつ気室3の液体の入れ替り
の量を最適に調整でき一層効果的であり又この上端部の
位置に調整自在な調整板を枢着して汚水の流通量を調整
するようにすれば前述の連通口8aの調整と合まって汚
水の4n替り量つまりばつ気室3内のMLSS(混合液
浮遊物濃度)が調整できる。
As shown in FIG. 4, the second partition plate 9 has a V-shaped notch 9a extending slightly above the water level at the upper end and downward from the water surface to separate the sedimentation separation chamber 2 and the aeration chamber 3. The amount of liquid exchange can be optimally adjusted, making it even more effective, and if an adjustable adjustment plate is pivotally mounted at the upper end of the plate to adjust the flow rate of wastewater, the above-mentioned adjustment of the communication port 8a can be achieved. Together with this, the 4N replacement amount of wastewater, that is, the MLSS (mixed liquid suspended solids concentration) in the aeration chamber 3 can be adjusted.

又このばつ気室は第2図および第3図に点線で示したよ
うに炉材11を充てんした接触ばつ気でもよい。
Alternatively, this aeration chamber may be a contact aeration chamber filled with furnace material 11 as shown by dotted lines in FIGS. 2 and 3.

以上の如くこの考案によれば沈澱分離室からばつ気室へ
移流する汚水の移流口を構成する仕切板を、連通口を穿
設した第1の仕切板と、この第1の仕切板から突出する
第2の仕切板を水位面近傍上に伸長して配置したため、
ばつ気室内の混合液浮遊物濃度を容易に調整でき長期間
の運転に適した汚水浄化槽が得られる。
As described above, according to this invention, the partition plate constituting the advection port for sewage flowing from the sedimentation separation chamber to the aeration chamber includes a first partition plate in which a communication port is formed and a partition plate that protrudes from the first partition plate. Because the second partition plate was placed extending above the water level,
A sewage septic tank that can easily adjust the concentration of suspended solids in the mixed liquid in the aeration chamber and is suitable for long-term operation can be obtained.

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

第1図は従来の汚水浄化槽の概略部分断面図、第2図は
この考案の実施例を示す浄化槽の要部断面図、第3図は
槽体内部を示す第2図のA−A横断面図、第4図は仕切
板の他の実施例を示す斜視図である。 1・・・・・・槽体、2・・・・・・沈澱分離室、3・
・・・・・ばつ気室、4・・・・・・沈澱室、6・・・
・・・セパレータ、8・・・・・・第1の仕切板、8a
・・・・・・連通口、8b・・・・・・突出部、9・・
・・・・第2の仕切板、11・・・・・・p材、12・
・・・・・散気管。
Fig. 1 is a schematic partial sectional view of a conventional sewage septic tank, Fig. 2 is a sectional view of a main part of a septic tank showing an embodiment of this invention, and Fig. 3 is a cross section taken along line A-A in Fig. 2 showing the inside of the tank body. 4 are perspective views showing other embodiments of the partition plate. 1... Tank body, 2... Sedimentation separation chamber, 3.
...Air chamber, 4...Sedimentation chamber, 6...
...Separator, 8...First partition plate, 8a
...Communication port, 8b...Protrusion, 9...
...Second partition plate, 11...P material, 12.
・・・・・・Diffuser pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 槽体内を沈澱分離室とはり気室とを仕切板で、ばつ気室
と沈澱室とをセパレータでそれぞれ区分された汚水浄化
槽にあって、前記仕切板は水面下中央部分に連通口を穿
設される第1の仕切板と、前記連通口の下方より沈澱分
離室側に突出され上端が水面付近まで伸びた横断面コ状
の第2の仕切板とからなる汚水浄化槽。
A sewage septic tank in which the sedimentation separation chamber and the sedimentation chamber are separated by a partition plate, and the aeration chamber and the sedimentation chamber are separated by a separator, and the partition plate has a communication port in the central part below the water surface. A sewage septic tank comprising: a first partition plate that projects from below the communication port toward the sedimentation separation chamber and has a U-shaped cross section with an upper end extending to near the water surface.
JP1980090997U 1980-06-27 1980-06-27 Sewage septic tank Expired JPS588392Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1980090997U JPS588392Y2 (en) 1980-06-27 1980-06-27 Sewage septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1980090997U JPS588392Y2 (en) 1980-06-27 1980-06-27 Sewage septic tank

Publications (2)

Publication Number Publication Date
JPS5712298U JPS5712298U (en) 1982-01-22
JPS588392Y2 true JPS588392Y2 (en) 1983-02-15

Family

ID=29452992

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1980090997U Expired JPS588392Y2 (en) 1980-06-27 1980-06-27 Sewage septic tank

Country Status (1)

Country Link
JP (1) JPS588392Y2 (en)

Also Published As

Publication number Publication date
JPS5712298U (en) 1982-01-22

Similar Documents

Publication Publication Date Title
JPH07155758A (en) Waste water treating device
CN208250006U (en) A kind of high efficient aeration sedimentation integrated device
JPS588392Y2 (en) Sewage septic tank
JPH0634665B2 (en) Constant water level water supply / drainage device and open type constant water level water circulation device using the same
JPH07275877A (en) Small-scaled combined purifying tank
JP2561317B2 (en) Septic tank
JPH04134594U (en) grease strap
JPH0350969Y2 (en)
JPH064885Y2 (en) Supernatant discharge device
JPS6246474Y2 (en)
JPS5839836Y2 (en) septic tank
JPS586555B2 (en) human waste septic tank
JPS5826074Y2 (en) human waste septic tank
JPS625275Y2 (en)
JPS6221354Y2 (en)
JPS5843989Y2 (en) septic tank
JPH0515890A (en) Sanitary sewage treating tank
JP2004237156A (en) Sewage treatment unit
JP3164138B2 (en) Purification equipment for pond water, etc.
JPS6038199B2 (en) Sewage treatment equipment
JPH02118B2 (en)
JPS6125920Y2 (en)
JP2000246245A (en) Sewage treatment equipment
JPS5851999Y2 (en) purification potion
JPH0728958Y2 (en) Septic tank with flow rate adjustment tank