JPS60143887A - Apparatus for purifying filthy water - Google Patents

Apparatus for purifying filthy water

Info

Publication number
JPS60143887A
JPS60143887A JP24584483A JP24584483A JPS60143887A JP S60143887 A JPS60143887 A JP S60143887A JP 24584483 A JP24584483 A JP 24584483A JP 24584483 A JP24584483 A JP 24584483A JP S60143887 A JPS60143887 A JP S60143887A
Authority
JP
Japan
Prior art keywords
water
tank
sewage
sludge
air
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.)
Pending
Application number
JP24584483A
Other languages
Japanese (ja)
Inventor
Eiichi Sugiura
杉浦 栄市
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP24584483A priority Critical patent/JPS60143887A/en
Priority to CN85101250A priority patent/CN1015169B/en
Publication of JPS60143887A publication Critical patent/JPS60143887A/en
Pending legal-status Critical Current

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  • Physical Water Treatments (AREA)

Abstract

PURPOSE:To separate impurities from water surely and to improve recovering efficiency of impurities by providing many nozzles for ejecting aqueous liquid contg. atomized air toward the bottom of a duct tank to the inside bottom of a duct tank for the filthy water. CONSTITUTION:Aqueous liquid contg. atomized air is passed through a main pipe 7 and is ejected from nozzles 6 of each ejection pipe 5 into a duct tank 1 for filthy water. Since the water contg. atomized air is ejected toward the inside bottom of the duct tank 1 for the filthy water, relatively heavy sludge which is liable to settle to the inside bottom of the duct tank 1 for the filthy water is also floated, and the atomized air is adsorbed to the sludge to float all sludge to the surface of the water in the duct tank 1 for the filthy water. The floated sludge moves toward a conveyor 15 in accompany with water stream moving toward a discharge port 2 of water, and is recovered successively by the driving of the conveyor 15.

Description

【発明の詳細な説明】 本発明は、渦巻ポンプを使用して、スラッジ等を含む汚
水を清浄化する汚水浄化装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sewage purification device that uses a centrifugal pump to purify sewage containing sludge and the like.

スラッジ等の固形汚物を含む汚水において、当該汚水に
含まれる固形汚物を分離して汚水を清浄化するための手
段としては、多種多様の装置が提案されているが、従来
一般的に採用されている固形汚物と水分との分離手段と
しては、フィルタを使用しているものと、加圧曝気浮上
等が用いられているのが現状である。しかしながら、か
がるフィルターでは、固形物による目詰りが生じやすい
ことから、該フィルターを一定期間毎に清掃するか某換
するといった作業が必要となり、長期に亘って汚水処理
を継続することができない不便があり、加圧曝気浮上は
加圧に要する費用が大きく、かつ大量連続処理が困難と
されている。
A wide variety of devices have been proposed as means for separating the solid waste contained in wastewater such as sludge and purifying the wastewater, but none of them have been generally adopted in the past. At present, the means for separating solid waste from water are those that use filters, pressurized aeration flotation, and the like. However, because filters are easily clogged with solid matter, it is necessary to clean or replace the filters at regular intervals, making it impossible to continue treating wastewater over a long period of time. Pressurized aeration flotation is inconvenient, requires high costs for pressurization, and is difficult to process continuously in large quantities.

また、比較的比重め重い固形汚物にあっては、汚水槽の
内底部に沈澱されるために、この汚水槽を定期的に清掃
して、沈澱物を除去する作業が必要となる等の問題点が
あった。
In addition, solid waste that is relatively heavy in specific gravity settles at the inner bottom of the sewage tank, making it necessary to periodically clean the sewage tank to remove the sediment. There was a point.

本発明は、かかる問題点を解消するためになされたもの
で、汚水槽の内底部より微粒子化した空気混入水を噴射
せしめて、汚水に含まれるスラッジ等の不純物に微粒子
化したエアを吸着せしめて不純物を浮上させ、次いでこ
の浮上不純物を回収して、汚水を清浄化するようにした
汚水浄化装置を提供することを目的とするものである。
The present invention has been made to solve this problem, and it injects aerated water that is atomized from the inner bottom of a sewage tank, and causes the atomized air to be adsorbed to impurities such as sludge contained in the sewage. It is an object of the present invention to provide a sewage purification device that purifies sewage by floating impurities and then recovering the floating impurities.

即ち本発明は、汚水中に、微粒子化したエアを送り込ん
で、汚水中のスラッジ等の不純物にエアを付着させて不
純物を浮上させ、この浮上した不純物を回収するように
したものであるから、不純物と水分どの分離が確実であ
って、不純物の回収効率が高めら゛れ、さらに、噴射角
度の適宜設定により噴射流で不純物は浮上されることか
ら、沈澱物が少なく、汚水槽内の清掃が簡素化できる等
の特長がある。
That is, the present invention is configured to send atomized air into wastewater, cause the air to adhere to impurities such as sludge in the wastewater, float the impurities, and recover the floated impurities. Separation of impurities and water is reliable, improving the collection efficiency of impurities.Furthermore, since the impurities are floated by the jet flow by setting the spray angle appropriately, there is less sediment, making it easier to clean inside the sewage tank. It has the advantage that it can be simplified.

以下に本発明を肉面に示す実施例に基いて詳細に説明す
る。
The present invention will be described in detail below based on examples shown on the meat side.

1は汚水処理槽であって、この汚水処理槽1の一側上部
には流水口2と、その下部に吸水口6が夫々設けられて
いる。またその流水口2と最も離れている他側部には汚
水流入口4が設けられている。5は汚水流路槽1の内底
部に多数配設されているエア混合水噴射管であって、こ
の各噴射管5には、エア混合水を、略45度の角度で下
向きに、即汚水流路槽1の内底面に向けて噴射させるこ
とができるノズル6が形成されているものである。
Reference numeral 1 denotes a sewage treatment tank, and the sewage treatment tank 1 is provided with a water inlet 2 at the upper part of one side, and a water inlet 6 at the lower part thereof. Further, a waste water inlet 4 is provided on the other side farthest from the water inlet 2. Reference numeral 5 denotes a large number of air-mixed water injection pipes arranged at the inner bottom of the sewage flow path tank 1, and each injection pipe 5 is used to direct air-mixed water downward at an angle of approximately 45 degrees and immediately spray the sewage water. A nozzle 6 is formed that can spray water toward the inner bottom surface of the channel tank 1.

7は汚水流路槽1の外側に配設されている主管であって
、この主管7に、前記の各噴射管5が接続され、またこ
の主管7の広幅は、気液混合用の渦巻ポンプ8の吐出口
9に接続されている。この渦巻ポンプ8の吸入口10に
は、エア吸入口11を有する自動エア吸入弁12と、前
記の吸水0乙に接続される吸水管16が接続されている
ものである。14は、渦巻ポンプ8を駆動するためのモ
ータ、15は汚水流路槽1内で浮遊するスラッジ16等
を回収するためのコンベヤである。
Reference numeral 7 denotes a main pipe disposed outside the sewage channel tank 1, to which each of the injection pipes 5 described above is connected, and the wide width of the main pipe 7 is connected to a vortex pump for mixing gas and liquid. It is connected to the discharge port 9 of 8. An automatic air suction valve 12 having an air suction port 11 and a water suction pipe 16 connected to the water suction port 11 are connected to the suction port 10 of the centrifugal pump 8. 14 is a motor for driving the centrifugal pump 8, and 15 is a conveyor for collecting sludge 16 and the like floating in the wastewater channel tank 1.

以上が本実施例の構成であるが、次にその作用について
述べると、汚水流路槽1内に、汚水流入口4より汚水を
供給しながら、渦巻ポンプ8を駆動すると、この渦巻ポ
ンプ8内では、汚水流路槽1内から吸水口6及び吸水管
13を経て供給された水液と、自動エア吸入弁12から
吸入されたエアとが混合され、さらにこの渦巻ポンプ8
内のインペラーによって、そのエアと水液とがミキシン
グされて微粒子化されたエアが水液中に混和される。(
このエアの混合率は10〜20%となるように自動エア
吸入弁12のエア吸入口11を調整することが望ましい
)かくして、微粒子化されたエアが混和された水液は主
管7を経て、各噴射管5のノズル6から、汚水流路4t
11内に噴射されるが、このエア混合水は汚水流路槽1
の内底部に向けて噴射されるために、汚水流路槽1の内
底部に沈澱しようとする比較的比重の重いスラッジ等も
浮上し、さらにその微粒子化エアはスラッジの表面に吸
着(付着)されて、全べてのスラッジを、汚水流路槽1
内の水面上に浮遊させることができる。かくして浮遊さ
れているスラッジ等は、流水02方向へ流動する水流に
伴なってコンベア15方向に移動し、そのコンベア15
の回動によって順次回収され、またベルトコンベヤを使
用せず、上部のスラッジ浮遊部流路を分離誘導し、フィ
ルタープレス等で脱水することも可能である。がくして
、スラッジ等の不純物が除去された水分は順次流水口2
から流出されるが、この流出水は廃水として排出又は再
利用することができ、必要に応じては、この流出水を二
次的に薬物処理、生物処理してもよい。なお、本発明に
よれば、水中に混和されるエアの粒子は極めて微粒子化
され、水中に滞在される時間が永いことがら、そのエア
の浮上時間を考慮して汚水流路槽1の深さ、長さを設定
する必要がある。また、ノズル6からの噴射圧力は高い
方が望ましいので渦巻ポンプはなるべく大型のものを使
用した方がよい。
The above is the configuration of this embodiment.Next, its operation will be described.When the volute pump 8 is driven while supplying sewage water into the sewage channel tank 1 from the sewage inlet 4, the inside of the vortex pump 8 is In this case, the water liquid supplied from inside the sewage channel tank 1 through the water inlet 6 and the water suction pipe 13 is mixed with the air sucked in from the automatic air intake valve 12, and then this centrifugal pump 8
The air and the water are mixed by the impeller inside, and the finely divided air is mixed into the water. (
(It is desirable to adjust the air intake port 11 of the automatic air intake valve 12 so that the mixing ratio of this air is 10 to 20%.) Thus, the water liquid mixed with the atomized air passes through the main pipe 7. From the nozzle 6 of each injection pipe 5, the wastewater flow path 4t
This air-mixed water is injected into the wastewater channel tank 1.
Because it is injected toward the inner bottom of the sewage channel tank 1, relatively heavy sludge, etc. that would have settled at the inner bottom of the wastewater channel tank 1 also floats to the surface, and the atomized air is adsorbed (attached) to the surface of the sludge. All the sludge is transferred to wastewater channel tank 1.
Can be floated on the surface of the water. The sludge etc. thus suspended moves in the direction of the conveyor 15 along with the water flow flowing in the direction of the flowing water 02.
It is also possible to separate and guide the flow path of the upper sludge floating part and dewater it using a filter press or the like without using a belt conveyor. The water from which impurities such as sludge have been removed is sequentially passed through the water outlet 2.
However, this effluent water can be discharged or reused as wastewater, and if necessary, this effluent water may be subjected to secondary drug treatment or biological treatment. According to the present invention, the air particles mixed into the water are extremely fine particles and stay in the water for a long time, so the depth of the sewage channel tank 1 is determined by taking into consideration the floating time of the air. , you need to set the length. Further, since it is desirable that the injection pressure from the nozzle 6 be high, it is better to use a centrifugal pump as large as possible.

以上のように本発明は、スラッジ等の不純物が混入され
る汚水が流入される汚水流路槽の内底部に、その流路槽
の底面に向けて、微粒子化エアを混和する水液な噴射す
る多数のノズルを配設セしめたものであるから、そのノ
ズルから噴射する微粒子化エアが汚水中の不純物に付着
されて、この不純物を浮遊化させることができるので、
汚水中に含まれる不純物を有効に分離浮上し、これによ
って、その不純物の分離回収が容易にできる効果がある
。さらに本発明によれば、エア混合水が汚水流路槽1の
内底面に向けて噴射させるようにしたものであるから、
その噴射力によって汚水流路槽1内に沈澱物が生じるこ
ともなく、汚水流路槽1内の清掃作業が省ける効果もあ
る。
As described above, the present invention provides an aqueous jet that mixes atomized air toward the inner bottom of a wastewater channel tank into which wastewater mixed with impurities such as sludge flows. Because it is equipped with a large number of nozzles, the atomized air ejected from the nozzles adheres to impurities in the wastewater and can float these impurities.
The impurities contained in the wastewater are effectively separated and floated, thereby facilitating the separation and recovery of the impurities. Furthermore, according to the present invention, since the air-mixed water is injected toward the inner bottom surface of the wastewater channel tank 1,
Due to the jetting force, no sediment is generated in the sewage channel tank 1, and the cleaning work inside the sewage channel tank 1 can be saved.

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

図面はいずれも本発明よりなる汚水浄化装置の実施例を
示し、第1図はその全体を示す構造説明図、第2図はそ
の要部拡大断面図である。 1・・・汚水流路N 2・・・流水口 6・・・吸水0 4−・・汚水流入口 5・・・エア混合水噴射管 6・・・ノズル7・・・主
管 8・・・渦巻ポンプ 9・・・吐出口 10・・・吸入口 11・・・エア吸入口 12・・・自動エア吸入弁16
・・・吸水管 14・・・モータ
The drawings all show embodiments of the sewage purification apparatus according to the present invention, with FIG. 1 being an explanatory structural view showing the entire structure, and FIG. 2 being an enlarged sectional view of the main parts thereof. 1... Sewage flow path N 2... Water inlet 6... Water absorption 0 4-... Sewage inlet 5... Air mixed water injection pipe 6... Nozzle 7... Main pipe 8... Centrifugal pump 9...Discharge port 10...Suction port 11...Air suction port 12...Automatic air suction valve 16
... Water suction pipe 14 ... Motor

Claims (1)

【特許請求の範囲】[Claims] 汚水流路槽1の内底部に配設され、かつエア混合水を、
その汚水流路槽1の内面に向けて噴射できるノズル6を
設けた多数のエア混合水噴射管5と、汚水流路槽1から
取水した水液にエアを混和し、微粒子化エアを混入させ
てなる水液な、前記ノズル6より噴射させる渦巻ポンプ
8と、前記汚水流路槽1内の汚水上に浮遊する不純物を
回収除去するコンベア15、またはスラッジ浮遊上部の
み分離誘専して脱水装置で脱水可能とすることを特徴と
する汚水浄化装置。
It is arranged at the inner bottom of the sewage flow path tank 1, and the air-mixed water is
A large number of air mixing water injection pipes 5 are provided with nozzles 6 that can inject toward the inner surface of the sewage flow path tank 1, and air is mixed with the water taken from the sewage flow path tank 1, and atomized air is mixed. A whirlpool pump 8 that injects water from the nozzle 6, a conveyor 15 that collects and removes impurities floating on the sewage in the sewage channel tank 1, or a dewatering device that separates only the floating upper part of the sludge. A sewage purification device characterized by being capable of dewatering.
JP24584483A 1983-12-29 1983-12-29 Apparatus for purifying filthy water Pending JPS60143887A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP24584483A JPS60143887A (en) 1983-12-29 1983-12-29 Apparatus for purifying filthy water
CN85101250A CN1015169B (en) 1983-12-29 1985-04-01 Prodn. equipment for mixed fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24584483A JPS60143887A (en) 1983-12-29 1983-12-29 Apparatus for purifying filthy water

Publications (1)

Publication Number Publication Date
JPS60143887A true JPS60143887A (en) 1985-07-30

Family

ID=17139689

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24584483A Pending JPS60143887A (en) 1983-12-29 1983-12-29 Apparatus for purifying filthy water

Country Status (1)

Country Link
JP (1) JPS60143887A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62186985A (en) * 1986-02-13 1987-08-15 Sando Iron Works Co Ltd Treatment of waste water
JPS62156398U (en) * 1986-03-24 1987-10-05

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5715956A (en) * 1981-05-29 1982-01-27 Meisei Shiyoukai Kk Plastic composite material using textile having conductive property

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5715956A (en) * 1981-05-29 1982-01-27 Meisei Shiyoukai Kk Plastic composite material using textile having conductive property

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62186985A (en) * 1986-02-13 1987-08-15 Sando Iron Works Co Ltd Treatment of waste water
JPS62156398U (en) * 1986-03-24 1987-10-05

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