JPH064886Y2 - Settling tank - Google Patents

Settling tank

Info

Publication number
JPH064886Y2
JPH064886Y2 JP1989027032U JP2703289U JPH064886Y2 JP H064886 Y2 JPH064886 Y2 JP H064886Y2 JP 1989027032 U JP1989027032 U JP 1989027032U JP 2703289 U JP2703289 U JP 2703289U JP H064886 Y2 JPH064886 Y2 JP H064886Y2
Authority
JP
Japan
Prior art keywords
chamber
settling
sludge
tank
settling tank
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 - Lifetime
Application number
JP1989027032U
Other languages
Japanese (ja)
Other versions
JPH02117006U (en
Inventor
春城 高橋
幹雄 荒牧
国広 池上
好照 今泉
保 塚部
和夫 増田
昭男 榎本
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.)
Japan Sewage Works Agency
Mitsubishi Heavy Industries Ltd
Original Assignee
Japan Sewage Works Agency
Mitsubishi Heavy Industries 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 Japan Sewage Works Agency, Mitsubishi Heavy Industries Ltd filed Critical Japan Sewage Works Agency
Priority to JP1989027032U priority Critical patent/JPH064886Y2/en
Publication of JPH02117006U publication Critical patent/JPH02117006U/ja
Application granted granted Critical
Publication of JPH064886Y2 publication Critical patent/JPH064886Y2/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)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は,下水処理を行う沈殿処理槽,特に,浮体上に
配置される沈殿処理槽の改良に関するものである。
[Detailed Description of the Invention] [Industrial field of application] The present invention relates to an improvement of a sedimentation treatment tank for treating sewage, in particular, a sedimentation treatment tank arranged on a floating body.

〔従来の技術〕 第2図に下水処理の一般的なフローを示してある。[Prior Art] FIG. 2 shows a general flow of sewage treatment.

Aは最初沈殿槽で,下水中の大きな固形物を沈殿除去す
るためのもの。Bは曝気槽で下水中に含まれるBOD成
分を微生物で処理するため,空気を吹き込んでエアレー
ションする所である。Cは最終沈殿槽で,本考案の対象
となる沈殿処理槽が採用されており,曝気された活性汚
泥混合液に含まれる汚泥を静置し沈殿させるものであ
る。Dは滅菌槽で、最終沈殿槽の上澄みを滅菌処理して
排出するものである。
A is a first settling tank for removing large solids in sewage. In the aeration tank B, a BOD component contained in the sewage is treated with microorganisms, so air is blown in for aeration. C is a final settling tank, and the settling tank which is the subject of the present invention is adopted, and sludge contained in the aerated activated sludge mixed solution is allowed to stand and settle. D is a sterilization tank in which the supernatant of the final precipitation tank is sterilized and discharged.

なお、最初沈殿槽A,および,最終沈殿槽Cから得られ
る汚泥は,肥料として再利用したり,焼却炉で焼却処理
したり,あるいは,埋め立て等で処理される。
The sludge obtained from the first settling tank A and the final settling tank C is reused as fertilizer, incinerated in an incinerator, or disposed of in landfill.

第3図には,最終沈殿槽Cで用いる沈殿処理槽の概略を
示してある。
FIG. 3 shows an outline of the precipitation treatment tank used in the final precipitation tank C.

1は沈殿槽で,多くの孔のあいた整流板4によって流入
室2と沈殿室3とに区画されている。流入室2には流入
管5が取り付けられており,通常2000ないし300
0PPmの活性汚泥混合液が供給され,整流板4によっ
て一様流が形成されて沈殿室3に流れ込む。沈殿室3に
は処理水排出用の越流堰(穴明き潜り管でも良い)6が
配置され,滞留時間3時間程度静置された排水の上澄み
は浮遊物質濃度10PPm程度,あるいは,それ以下に
なり,排水管7から排出されるようになっている。
A settling tank 1 is divided into an inflow chamber 2 and a settling chamber 3 by a straightening vane 4 having many holes. An inflow pipe 5 is attached to the inflow chamber 2, and is usually 2000 to 300.
The activated sludge mixed solution of 0PPm is supplied, and a uniform flow is formed by the straightening vanes 4 and flows into the precipitation chamber 3. An overflow weir (a perforated pipe may be used) 6 for discharging treated water is placed in the settling chamber 3, and the supernatant of the wastewater left standing for about 3 hours has a suspended matter concentration of about 10 PPm or less. And is discharged from the drainage pipe 7.

沈殿室3の底部に沈殿した汚泥は,図示を省略したスク
レーパなどにより流入室2側に掻き寄せられ,整流板4
と沈殿室3との間の隙間を通って流入室2の底部に形成
された汚泥室8に集められる。集められた数千ないし数
万PPm程度の沈殿汚泥は,排出管9より外部に取り出
される。
The sludge settled on the bottom of the settling chamber 3 is scraped to the inflow chamber 2 side by a scraper (not shown) or the like, and the straightening plate 4
It is collected in the sludge chamber 8 formed at the bottom of the inflow chamber 2 through the gap between the sludge chamber 3 and the sedimentation chamber 3. The collected sludge of about several thousand to tens of thousands of PPm is taken out through the discharge pipe 9.

〔考案が解決しようとする問題点〕[Problems to be solved by the invention]

従来の下水処理設備は地上に配置されており,その設備
を浮体上に設置しようとすると,様々な不具合が生じて
くる。すなわち,静置した状態で本来使用するものを,
浮体と言う揺動するところで使用すると種々の影響が出
てくる。
Conventional sewage treatment equipment is located on the ground, and if you try to install the equipment on a floating body, various problems will occur. In other words, what is originally used in a stationary state,
There are various effects when used in a rocking place called a floating body.

最初沈殿槽Aは下水中の大きな固形分を沈殿させるもの
であり,槽が揺動することに対してそれほど敏感ではな
い。また,曝気槽Bは積極的に掻き回すことが必要であ
り、槽の揺動は寧ろ好ましいものとなっている。
Initially, the settling tank A precipitates large solids in the sewage and is not very sensitive to rocking of the tank. Further, the aeration tank B needs to be actively stirred, and swinging of the tank is rather preferable.

しかし,最終沈殿槽Cでは,この揺動が大きな問題とな
る。すなわち,最終沈殿槽Cの沈殿室3で沈殿させるも
のは水とほぼ比重の等しい活性汚泥であるため,出来る
だけ静かに沈殿させることが望ましいからである。
However, in the final settling tank C, this swing becomes a big problem. That is, it is desirable that the sedimentation in the sedimentation chamber 3 of the final sedimentation tank C is activated sludge having a specific gravity almost equal to that of water, so that the sedimentation should be performed as gently as possible.

ところが,浮体上に下水処理設備を設置すると,潮の満
ち干,波,風の影響を受け,浮体は少なからず揺動す
る。浮体,すなわち沈殿槽1が僅か数度傾いただけであ
っても槽内の液面は傾斜し,その都度活性汚泥混合液が
整流板4を通って流入室2内と沈殿室3内の間を行き来
することになる。
However, if the sewage treatment equipment is installed on the floating body, the floating body will not be shaken to a large extent due to the influence of the tide, waves and wind. Even if the floating body, that is, the settling tank 1 is tilted only a few degrees, the liquid level in the tank is tilted, and the activated sludge mixed liquid passes between the inflow chamber 2 and the settling chamber 3 through the straightening plate 4 each time. You will come and go.

汚泥の沈降に最も影響を与えるのは,流入室2から沈殿
室3に入る入口部,つまり,整流板4の付近であって、
この入口部で汚泥の擬集によるフロック化が生じ、擬集
したフロックを含有する活性汚泥混合液が沈殿室3に流
入して沈降分離が進行する。
It is the inlet part from the inflow chamber 2 into the settling chamber 3, that is, the vicinity of the straightening plate 4, that has the greatest effect on the sludge settling.
Flocking occurs due to the pseudo-collection of sludge at this inlet portion, and the activated sludge mixed liquid containing the pseudo-collected flocs flows into the settling chamber 3 and the settling separation proceeds.

従って,整流板4を行き来する活性汚泥混合液によって
沈殿が阻害され,また,やっと擬集した汚泥の攪拌も行
われ、十分な沈殿分離の効果を得ることができない。
Therefore, the sedimentation is inhibited by the activated sludge mixed liquid flowing back and forth through the flow regulating plate 4, and the sludge finally collected is also stirred, so that the effect of sufficient sedimentation separation cannot be obtained.

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

本考案は、流入室と沈殿室とが形成された沈殿槽と,上
記流入室に活性汚泥混合液(原水)を供給する手段と,
上記沈殿室から上澄みを排水する手段と,上記沈殿槽の
沈殿室に沈殿した汚泥を掻き寄せる手段と,掻き寄せら
れた汚泥を排出する手段とを有する沈殿処理槽におい
て、上記流入室の水面を上記沈殿室の基準水面以下で,
かつ満水状態に保持する天井板を配置すると共に,整流
板によって形成される上記流入室の底部を上記沈殿室の
底部より上昇させたものである。
The present invention comprises a settling tank having an inflow chamber and a settling chamber, means for supplying an activated sludge mixture (raw water) to the inflow chamber,
In the settling tank having means for draining the supernatant from the settling chamber, means for scraping sludge settling in the settling chamber of the settling tank, and means for discharging the sludge slid up, Below the standard water level of the sedimentation chamber,
In addition, a ceiling plate that keeps the water in a full state is arranged, and the bottom of the inflow chamber formed by the current plate is raised above the bottom of the settling chamber.

〔作用〕[Action]

流入室に天井板を設けることにより,整流板,天井板で
囲まれた流入室のほぼ密閉された空間が満水の状態とな
り,液面が傾斜することが無い。したがって,沈殿槽全
体が傾き,沈殿室内の液面が傾斜したとしても,整流板
を通しての活性汚泥混合体の出入りがない。
By providing the ceiling plate in the inflow chamber, the nearly enclosed space of the inflow chamber surrounded by the current plate and the ceiling plate is filled with water, and the liquid surface does not tilt. Therefore, even if the entire settling tank is tilted and the liquid level in the settling chamber is tilted, the activated sludge mixture does not come in and out through the straightening vane.

また,整流板で形成した流入室の底部を沈殿室の底部よ
り上昇させたので,沈殿室に堆積した汚泥を攪拌する事
がない。
Moreover, since the bottom of the inflow chamber formed by the straightening plate is raised above the bottom of the settling chamber, the sludge accumulated in the settling chamber is not stirred.

〔実施例〕〔Example〕

以下,本考案を第1図に示す一実施例の沈殿処理装置に
ついて説明するが,符号1ないし9を付したものの構造
作用は第3図のものと同一であるので説明を省略する。
Hereinafter, the present invention will be described with reference to a sedimentation treatment apparatus of one embodiment shown in FIG. 1. However, the structural actions of those denoted by reference numerals 1 to 9 are the same as those in FIG.

図において10は天井板で,流入室2の全面を覆うよう
に取り付けられており,その位置は沈殿室3内の基準水
面L以下になっている。なお,図示は省略してあるが,
天井板10に逆止弁等を備えた空気抜き管を取り付け,
流入室3内に流入する活性汚泥混合液の量が変動した場
合でも流入室が常に満水状態になるようにしてある。
In the figure, 10 is a ceiling plate, which is attached so as to cover the entire surface of the inflow chamber 2, and its position is below the reference water level L in the settling chamber 3. Although not shown,
Attach an air vent pipe equipped with a check valve etc. to the ceiling board 10,
Even when the amount of the activated sludge mixed liquid flowing into the inflow chamber 3 changes, the inflow chamber is always filled with water.

なお,整流板4により流入室2の底部を形成している
が,その高さは沈殿槽3の底部に沈殿した汚泥が揺動浮
体の揺動により隠れたり,あるいは,左右前後に行き来
したとしても整流板4による剪断,攪拌が無いように沈
殿室3の底部から充分離れた高い位置に形成してある。
Although the bottom of the inflow chamber 2 is formed by the straightening vane 4, the height of sludge settled at the bottom of the settling tank 3 is hidden by the swing of the swinging floating body or moves back and forth from side to side. Is also formed at a high position sufficiently separated from the bottom of the settling chamber 3 so that the flow straightening plate 4 does not shear or stir.

このような沈殿処理槽を浮体上に乗せると,浮体の動揺
に応じて沈殿室3内の水面は傾斜する。しかし,流入室
2には天井板10が取り付けてあって,天井板10に取
付けた空気抜き管で上部の空気のみが外部へ排出されて
いるので常に満水状態となっており,活性汚泥混合液が
流入室2と沈殿室3の間を行き来する事がない。
When such a settling tank is placed on the floating body, the water surface in the settling chamber 3 is inclined according to the shaking of the floating body. However, since the ceiling plate 10 is attached to the inflow chamber 2 and only the upper air is discharged to the outside by the air vent pipe attached to the ceiling plate 10, it is always full of water, and the activated sludge mixed liquid is There is no going back and forth between the inflow chamber 2 and the sedimentation chamber 3.

また,浮体の揺動によって生じる沈殿室3底部の沈殿汚
泥の揺動は,上記手段によっても避けることは出来ない
が,整流板4で形成する流入室2の整流板は,沈殿汚泥
層に接触しない充分高い場合に形成してあるので,揺動
する沈殿汚泥を剪断・攪拌することがなく,沈殿汚泥か
らの余分な粒子の浮遊が抑制される。
Moreover, the rocking of the settled sludge at the bottom of the settling chamber 3 caused by the rocking of the floating body cannot be avoided by the above means, but the straightening plate of the inflow chamber 2 formed by the straightening plate 4 contacts the settling sludge layer. Since it is formed when the sludge is sufficiently high, there is no need to shear or agitate the rocking sedimentation sludge, and the floating of extra particles from the sedimentation sludge is suppressed.

以上の総合的な効果によって,沈殿室3における汚泥の
沈殿は順調に行われ,地上の設備となんら変わることの
ない程度の沈殿分離効率をあげることが可能となる。
Due to the above-mentioned overall effect, the sludge can be settled smoothly in the settling chamber 3, and it is possible to improve the settling separation efficiency that is no different from the above-ground equipment.

なお,上記実施例では,水平な整流板4で流入室2の底
部を形成した例を示したが,整流板4上に汚泥の局部的
な体積が生じないように,かつ,整流効果を加味して傾
斜型,あるいはV型などを含めて状況に応じた形状とす
ることが可能である。
In addition, in the above-described embodiment, an example in which the bottom portion of the inflow chamber 2 is formed by the horizontal straightening vane 4 is shown, but a local volume of sludge is not generated on the straightening vane 4 and a straightening effect is added. Then, it is possible to make the shape suitable for the situation, including the inclined type or the V type.

〔考案の効果〕[Effect of device]

本考案の沈殿処理槽を用いることにより,従来困難とさ
れていた浮体上への下水処理設備の設置が可能となり,
産業上極めて有用である。
By using the settling tank of the present invention, it becomes possible to install sewage treatment equipment on a floating body, which has been considered difficult in the past.
It is extremely useful in industry.

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

第1図は本考案の一実施例を示す沈殿処理槽の図,第2
図は下水処理の流れを示す図,第3図は従来の沈殿処理
槽の図である。 1:沈殿槽,2:流入室,3:沈殿室, 4:整流室,5:流入管,6:堰, 7:排水管,8:汚泥室,9:排出管, 10:天井板
FIG. 1 is a diagram of a precipitation treatment tank showing an embodiment of the present invention, and FIG.
The figure shows the flow of sewage treatment, and Fig. 3 shows the conventional settling tank. 1: sedimentation tank, 2: inflow chamber, 3: sedimentation chamber, 4: rectification chamber, 5: inflow pipe, 6: weir, 7: drainage pipe, 8: sludge chamber, 9: discharge pipe, 10: ceiling plate

───────────────────────────────────────────────────── フロントページの続き (72)考案者 池上 国広 長崎県長崎市飽の浦町1番1号 三菱重工 業株式会社長崎研究所内 (72)考案者 今泉 好照 長崎県長崎市飽の浦町1番1号 三菱重工 業株式会社長崎研究所内 (72)考案者 塚部 保 長崎県長崎市飽の浦町1番1号 三菱重工 業株式会社長崎造船所内 (72)考案者 増田 和夫 長崎県長崎市飽の浦町1番1号 三菱重工 業株式会社長崎造船所内 (72)考案者 榎本 昭男 長崎県長崎市飽の浦町1番1号 三菱重工 業株式会社長崎造船所内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Kunihiro Ikegami 1-1 1-1 Atsunoura-machi, Nagasaki-shi, Nagasaki Mitsubishi Heavy Industries, Ltd. Nagasaki Research Institute (72) Yoshiteru Imaizumi 1-1-1 Atsunoura-cho, Nagasaki-shi, Nagasaki Mitsubishi Heavy Industries, Ltd. Nagasaki Research Institute (72) Inventor Tamotsu Tsukabe 1-1, Atsunoura-machi, Nagasaki, Nagasaki Prefecture Mitsubishi Heavy Industries Ltd. Nagasaki Shipyard (72) Kazuo Masuda 1-1, Atsunoura-cho, Nagasaki, Nagasaki Prefecture Mitsubishi Heavy Industries Ltd. Nagasaki Shipyard (72) Inventor Akio Enomoto 1-1, Atsunoura-cho, Nagasaki-shi, Nagasaki Mitsubishi Heavy Industries Ltd. Nagasaki Shipyard

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】流入室と沈殿室とが形成された沈殿槽と,
上記流入室に活性汚泥混合液を供給する手段と,上記沈
殿室から上澄みを排水する手段と,上記沈殿槽の沈殿室
に沈殿した汚泥を掻き寄せる手段と,掻き寄せられた汚
泥を排出する手段とを有する沈殿処理槽において,上記
流入室の水面を上記沈殿室の基準水面以下で,かつ満水
状態に保持する天井板を配置すると共に,整流板で形成
される上記流入室の底部を上記沈殿室の底部より上昇さ
せたことを特徴とする沈殿処理槽。
1. A settling tank having an inflow chamber and a settling chamber,
Means for supplying the activated sludge mixture to the inflow chamber, means for draining the supernatant from the settling chamber, means for scraping the sludge settled in the settling chamber of the settling tank, and means for discharging the scraped sludge And a ceiling plate for keeping the water level of the inflow chamber below the reference water level of the settling chamber and filled with water, and the bottom part of the inflow chamber formed by a straightening vane A settling tank characterized by being raised from the bottom of the chamber.
JP1989027032U 1989-03-09 1989-03-09 Settling tank Expired - Lifetime JPH064886Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1989027032U JPH064886Y2 (en) 1989-03-09 1989-03-09 Settling tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1989027032U JPH064886Y2 (en) 1989-03-09 1989-03-09 Settling tank

Publications (2)

Publication Number Publication Date
JPH02117006U JPH02117006U (en) 1990-09-19
JPH064886Y2 true JPH064886Y2 (en) 1994-02-09

Family

ID=31249187

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1989027032U Expired - Lifetime JPH064886Y2 (en) 1989-03-09 1989-03-09 Settling tank

Country Status (1)

Country Link
JP (1) JPH064886Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5756945B2 (en) * 2010-09-16 2015-07-29 日本ソリッド株式会社 Raw water treatment method

Also Published As

Publication number Publication date
JPH02117006U (en) 1990-09-19

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