JP2691003B2 - Settling tank - Google Patents

Settling tank

Info

Publication number
JP2691003B2
JP2691003B2 JP5737089A JP5737089A JP2691003B2 JP 2691003 B2 JP2691003 B2 JP 2691003B2 JP 5737089 A JP5737089 A JP 5737089A JP 5737089 A JP5737089 A JP 5737089A JP 2691003 B2 JP2691003 B2 JP 2691003B2
Authority
JP
Japan
Prior art keywords
chamber
settling
tank
inflow
sludge
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
JP5737089A
Other languages
Japanese (ja)
Other versions
JPH02237606A (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 JP5737089A priority Critical patent/JP2691003B2/en
Publication of JPH02237606A publication Critical patent/JPH02237606A/en
Application granted granted Critical
Publication of JP2691003B2 publication Critical patent/JP2691003B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は,下水処理を行う沈殿処理槽,特に,浮体上
に設置される沈殿処理槽の改良に関するものである。
Description: TECHNICAL FIELD The present invention relates to an improvement of a precipitation treatment tank for treating sewage, particularly a precipitation treatment tank installed 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分を沈殿除去
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,本発明の対象
となる沈殿処理槽が採用されており,曝気された下水に
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 the first settling tank for removing large solids in sewage. B is an aeration tank where BOD components contained in the sewage are treated with microorganisms, and air is blown in for aeration. C is a final settling tank, which employs a settling tank which is the subject of the present invention, and is for leaving the sludge contained in the aerated sewage to stand still for settling. D is a sterilization tank for sterilizing and discharging the supernatant of the final precipitation tank.

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3000ppm
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。
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 3000 ppm.
The activated sludge mixed solution is supplied, and a uniform flow is formed by the straightening vanes 4 and flows into the settling chamber 3.

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
れ以下となり,排水管7から排出されるようになってい
る。
In the settling chamber 3, there is an overflow weir (may be a perforated dive pipe) 6 for discharging treated water, and the supernatant of the drainage that has been 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側に掻き寄せれれ,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 is formed on the bottom of the inflow chamber 2 through the gap between the straightening vane 4 and the settling chamber 3. Collected in the sludge chamber 8. The collected sludge of about several thousand to tens of thousands ppm is taken out through the discharge pipe 9.

[発明が解決しようとする問題点] 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。
[Problems to be Solved by the Invention] Conventional sewage treatment equipment is placed on the ground, and when the equipment is installed on a floating body, various problems occur. That is, various effects are brought about by using what is originally used in a stationary state in a swinging state 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 the rocking 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,浮体は少なからず動揺す
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 sewage treatment equipment is installed on the floating body, the floating body will be shaken to a considerable extent due to the effects of tidal waves, 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 tilts, 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凝集によるフロック化が生じ,
凝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。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,やっと凝集した汚泥の撹拌も行われ,十分な沈殿分
離の効果を得ることができない。
The most significant effect on sludge settling is at the inlet from the inflow chamber 2 to the sedimentation chamber 3, that is, near the straightening plate 4, at which the sludge agglomerates due to agglomeration of sludge.
The activated sludge mixed solution containing flocs that have agglomerated is deposited in the sedimentation chamber 3
And sedimentation separation proceeds. Therefore, the sedimentation is inhibited by the activated sludge mixed liquid flowing back and forth through the rectifying plate 4, and the sludge finally aggregated is also stirred, so that the effect of sufficient sedimentation cannot be obtained.

[問題点を解決するための手段] 本発明は,整流板によって流入室と沈殿室とに区画さ
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
準水面以下に保持する天井板とを備え,上記流入室を常
時満水状態となるようにしたものである。
[Means for Solving the Problems] The present invention relates to a settling tank divided into an inflow chamber and a settling chamber by a straightening plate, a means for supplying an activated sludge mixed liquid (raw water) to the inflow chamber, and the above settling. In a precipitation treatment tank having means for draining the supernatant from the chamber, means for scraping sludge settling in the settling chamber of the settling tank, and means for discharging the scraped sludge, A ceiling plate that holds the room below the reference water level is provided so that the inflow room is always filled with water.

[作用] 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液の出入りがない。
[Operation] By providing the ceiling plate in the inflow chamber, the almost 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 whole settling tank is tilted and the liquid level in the settling chamber is tilted, the activated sludge mixed solution does not come in and out through the straightening vanes.

[実施例] 以下,本発明を第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なしい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。
[Embodiment] Hereinafter, the present invention will be described with reference to a precipitation treatment apparatus according to an embodiment shown in FIG. 1. However, since the structural action of those denoted by reference numeral 1 or 9 is the same as that of FIG. Omit it.

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,
An air vent pipe equipped with a check valve or the like is attached to the ceiling plate 10 so that the inflow chamber is always filled with water even when the amount of the activated sludge mixed liquid flowing into the inflow chamber 3 changes.

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は天井板10が取り付けてあり上部の空気のみが空気
抜き管により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, the infill chamber 2 is always full of water, and the activated sludge mixed liquid in the inflow chamber 2 and the sedimentation chamber 3 is always filled. There is no going back and forth.

したがって,沈殿室における汚泥の沈殿は順調に行わ
れ,地上の設置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。
Therefore, sludge settling in the settling chamber is carried out smoothly, and it is possible to improve the settling separation efficiency that is no different from installation on the ground.

[発明の効果] 本発明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。
[Advantages of the Invention] By using the precipitation treatment tank of the present invention, it becomes possible to install a sewage treatment facility on a floating body, which has been considered difficult in the past, and it is extremely useful industrially.

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

第1図は本発明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:整流板,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: Settling tank, 2: Inflow chamber, 3: Settling chamber, 4: Rectifier plate, 5: Inflow pipe, 6: Weir, 7: Drain pipe, 8: Sludge chamber, 9: Discharge pipe, 10: Ceiling plate

───────────────────────────────────────────────────── フロントページの続き (72)発明者 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)発明者 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)発明者 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)発明者 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)発明者 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 the front page (72) Inventor Kunihiro Ikegami 1-1, Atsunoura-machi, Nagasaki-shi, Nagasaki Mitsubishi Heavy Industries, Ltd. Nagasaki Research Center (72) Inventor Yoshiteru Imaizumi 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) Inventor, 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)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】整流板によって流入室と沈殿室とに区画さ
れた沈殿槽と,上記流入室に活性汚泥混合液に供給する
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
下に保持する天井板とを備え,上記流入室を常時満水状
態となるようにしたことを特徴とする沈殿処理槽。
1. A settling tank divided into an inflow chamber and a settling chamber by a straightening plate, a means for supplying the activated sludge mixed solution to the inflow chamber, a means for draining the supernatant from the settling chamber, and the settling tank. In a settling chamber having means for scraping sludge settled in the settling chamber and means for discharging the sludge slid in, a ceiling plate for holding the water surface of the inflow chamber below the reference water surface of the settling chamber. A precipitation treatment tank, characterized in that the inflow chamber is always filled with water.
JP5737089A 1989-03-09 1989-03-09 Settling tank Expired - Lifetime JP2691003B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5737089A JP2691003B2 (en) 1989-03-09 1989-03-09 Settling tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5737089A JP2691003B2 (en) 1989-03-09 1989-03-09 Settling tank

Publications (2)

Publication Number Publication Date
JPH02237606A JPH02237606A (en) 1990-09-20
JP2691003B2 true JP2691003B2 (en) 1997-12-17

Family

ID=13053705

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5737089A Expired - Lifetime JP2691003B2 (en) 1989-03-09 1989-03-09 Settling tank

Country Status (1)

Country Link
JP (1) JP2691003B2 (en)

Also Published As

Publication number Publication date
JPH02237606A (en) 1990-09-20

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