JPH0316687A - High-speed waste water treating device - Google Patents

High-speed waste water treating device

Info

Publication number
JPH0316687A
JPH0316687A JP15027289A JP15027289A JPH0316687A JP H0316687 A JPH0316687 A JP H0316687A JP 15027289 A JP15027289 A JP 15027289A JP 15027289 A JP15027289 A JP 15027289A JP H0316687 A JPH0316687 A JP H0316687A
Authority
JP
Japan
Prior art keywords
liquid
tank
wastewater
waste water
rapid
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
JP15027289A
Other languages
Japanese (ja)
Inventor
Keiichi Honda
啓一 本田
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.)
HETSUZU KK
Original Assignee
HETSUZU KK
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 HETSUZU KK filed Critical HETSUZU KK
Priority to JP15027289A priority Critical patent/JPH0316687A/en
Publication of JPH0316687A publication Critical patent/JPH0316687A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To stably execute solid-liquid flotation separation by providing a rapid treating machine which adds a flocculating agent to the desorption liquid of a separating chamber and stirs the liquid and a floating tank which stabilizes the waste water from this rapid treating machine. CONSTITUTION:The floatable material and settlable materials in the waste water are subjected to the solid-liquid sepn. in the separating tank 1. The polymer flocculating agent 4 is added by the rapid treating machines 5 to this desorption liquid to form flocculated lumps. The liquid is stirred at a high speed and air is mixed therewith to adsorb the unstable flocculated lumps on the bubble surfaces. The bubbles are released into the floating tank 10. The bubbles are rapidly expanded and are floated together with the flocculated lumps adsorbed on the bubble surfaces in the floating tank 10. After the floated materials are treated with a chemical, the materials are reduced in weight by a dehydrating machine and are incinerated. The treated liquid is discharged from a discharge pipe 11.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、生活排水、雑排水、工場排水などの高速排水
処F■装置に関するもので、とくに小型の処理装置や工
場排水処理における前処理装置として有効に利用できる
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a high-speed wastewater treatment F■ system for domestic wastewater, gray water, industrial wastewater, etc., and is particularly concerned with small-sized treatment equipment and pre-treatment in industrial wastewater treatment. It can be effectively used as a device.

[従来の技術] 一般住宅、集合住宅、高■仕築物などから排出される生
活排水や雑排水あるいは、外食Il業、レストラン、食
品工場などの営業用排水は、有機物質や無機物質が物理
的、化学的に混合または化合されており、また、工場排
水には汀害物質を含んだ特殊排水や高濃度排水がある。
[Conventional technology] Domestic wastewater and gray water discharged from general houses, apartment complexes, high-rise buildings, etc., as well as commercial wastewater from catering industries, restaurants, food factories, etc., contain organic and inorganic substances. In addition, industrial wastewater includes special wastewater and high-concentration wastewater that contain pollutants.

このような排水をそのまま自然界に放出すると、天然浄
化作用だけでは分解汀ト化できず、自然サイクル以上の
重や濃度となって悪影響をおよぼずことが知られており
、これらの排水による汚濁を防止し、環境の浄化をはか
るため8秤の排水処理方法が開発されていろ。
It is known that if such wastewater is released directly into nature, it cannot be decomposed into slag by natural purification alone, and the weight and concentration exceeds the natural cycle, causing no adverse effects. 8 types of wastewater treatment methods have been developed to prevent this and purify the environment.

これらの汚水処理方法を大別すると、物理的処理方式と
生物的処理方式に分かれ、114者は小型、高速、高効
串であるが、装れがM1雅でイニシャルコストやランニ
ングコストが高価であり、その性質上余剰生成物が多く
ランニングコストを高くする一因となっている。
Broadly speaking, these sewage treatment methods can be divided into physical treatment methods and biological treatment methods, and 114 methods are small, high-speed, and highly effective skewers, but they are M1 elegant and have high initial costs and running costs. Due to its nature, there are many surplus products, which is one of the causes of high running costs.

一方、生物的処理方式は、若干滞留時間が長く、設置面
積が大で費用も高くなる。しかし、活性汚泥方式では、
有害物質による不安定性と余剰生成物のmが多くなる問
題があるが、現行基準型の分離接触曝気型は保守点検f
1ミ、経済性、安定虹において(f効で一般的である。
On the other hand, biological treatment methods have a slightly longer residence time, require a larger installation area, and are more expensive. However, with activated sludge method,
Although there are problems with instability due to harmful substances and increased m of surplus products, the current standard separation contact aeration type requires maintenance and inspection f
1 mi, economical, stable rainbow (f effect and common).

また、工場排水処理の一例どして、加圧浮上方式が知ら
れている。これは調整摺、加圧タンク、浮上借から構成
され、付属装置として圧縮機、反応剤注入装置等があり
、これらが一連の処理工程により浮上分離作用を生ずる
ものである。そして浮上物質は薬剤処理されて脱水機で
減量後、焼却または狸め尭て等により処分される。
Further, a pressurized flotation method is known as an example of factory wastewater treatment. This system is composed of a regulating slide, a pressurized tank, and a flotation device, and has attached equipment such as a compressor and a reactant injection device, which produce a flotation separation effect through a series of processing steps. The floating material is then treated with chemicals to reduce its weight in a dehydrator, and then disposed of by incineration, slicing, etc.

[本発明が解決しようとする課題] このように一般的な排水処理装置は多槽構造および多種
構造によって構戊され、複雑で大きな設置スペースを必
要とし、専門の技術者によるメンテナンスを要するなど
、設備費や処理費、維持費が高くなり、敗種の薬剤の使
用により余剰生成物が増大するなどの問題がある。
[Problems to be Solved by the Present Invention] As described above, general wastewater treatment equipment has a multi-tank structure and various types of structures, is complex, requires a large installation space, and requires maintenance by specialized engineers. There are problems such as increased equipment costs, processing costs, and maintenance costs, and an increase in surplus products due to the use of chemicals for defeated species.

[課題を解決するための手段] 本発明は、排水中の浮上社物質と沈降性物質をそれぞれ
浮上沈澱させる分離梼で前処理を行い、この分fl&槽
からの脱離液に凝集剤を加えて撹拌したのち空気を混合
さU・る急速処理機を設け、急速処理機からの排水を安
定化させる浮上槽で構成されており、17j記急速処理
機として電よ脱離液を凝集剤とともに吸引してインベラ
で撹拌するポンプと、H!ンプ吐出口において外気を混
合するエジエクタをそなえている。
[Means for Solving the Problems] The present invention pre-treats floating substances and settling substances in wastewater using a separation basin that floats and settles them, and adds a flocculant to the separated liquid from the fl& tank. It is equipped with a rapid treatment machine that mixes air after stirring, and consists of a flotation tank that stabilizes the waste water from the rapid treatment machine. A pump that suctions and stirs with an invera, and H! The pump is equipped with an ejector that mixes outside air at the pump discharge port.

[作川] したがって、排水中の浮J:rk物質と沈降性物質を分
離槽で固液分離し、その脱離液に高分子凝集に、これに
空気を混合さU”不安定な凝集塊を気泡表面に吸着させ
て浮上槽内に放出し、気泡の膨張により浮上分離させる
[Sakukawa] Therefore, floating substances and settling substances in wastewater are separated into solid and liquid in a separation tank, and the separated liquid is mixed with polymer flocculation and air is mixed with it to form unstable flocs. is adsorbed onto the surface of the bubbles and released into the flotation tank, whereupon the bubbles expand and separate by flotation.

[実施例] これを図に示す実施例について説明する。[Example] This will be explained with reference to an embodiment shown in the drawings.

1は分離槽、2は分離槽から脱離液を取り出す排出管、
3(よ取り出された脱離液に凝集剤4を添加する凝集槽
、5は急速処理機で、ボンプ6とエジェクタ7で構成し
ている。8はエジェクタ7内のボンプGの吐出口に設け
たノズル、9は空気吸入管、10は浮上槽、Itは排水
口である。
1 is a separation tank, 2 is a discharge pipe for taking out the desorbed liquid from the separation tank,
3 (a flocculating tank in which a flocculant 4 is added to the removed separated liquid; 5 is a rapid processing machine, which is composed of a pump 6 and an ejector 7; 8 is installed at the discharge port of the pump G in the ejector 7); 9 is an air suction pipe, 10 is a flotation tank, and It is a drain port.

分離槽lに流入した排水は、浮上性物質と沈降性物質を
浮上沈澱させ、脱離液を排出管2から凝集槽3に送る。
The waste water that has flowed into the separation tank 1 causes floating substances and sedimentation substances to float and settle, and the desorbed liquid is sent from the discharge pipe 2 to the flocculation tank 3.

この凝集槽内で脱離液に0.1%濃度の高分子凝集剤4
を1%の注入率で添加し、急速処理機5のポンプ6で吸
い込みインベラの回転により急速に混合撹拌して十分に
脱離液と凝集剤を溶解した後、ノズル8からジェット水
流状態で吹き出させる。ノズル8から吹き出された溶解
液Cよエジェクタ7内で減圧現象(ペンチェリー効果)
により空気吸入管9からの外気が高速、高圧状態で接触
し、溶解液中の不安定な凝集塊が外気気泡の表面に瞬間
的に吸青されて浮上槽10内に放出される。
In this flocculation tank, a polymer flocculant 4 with a concentration of 0.1% is added to the desorbed liquid.
is added at an injection rate of 1%, sucked in by the pump 6 of the rapid treatment machine 5, rapidly mixed and stirred by the rotation of the inflator to sufficiently dissolve the desorbed liquid and the flocculant, and then blown out from the nozzle 8 in the form of a jet water stream. let A decompression phenomenon occurs in the ejector 7 of the solution C blown out from the nozzle 8 (Penchery effect)
As a result, the outside air from the air suction pipe 9 comes into contact with the solution at high speed and high pressure, and unstable aggregates in the solution are instantaneously absorbed by the surface of the outside air bubbles and released into the flotation tank 10.

加圧して放出された気泡凝集塊は、ポンプ内で加圧され
ているため浮上槽内で相対的に減圧状態となり、気泡体
積が急激に膨張して浮力を増し、気泡表面の吸若凝集塊
とともに浮上する。
Since the bubble aggregates released under pressure are pressurized in the pump, they become relatively depressurized in the flotation tank, and the bubble volume expands rapidly, increasing buoyancy and causing the bubbles to absorb and absorb young aggregates on the surface of the bubbles. surface with.

浮上物質は薬剤処理され脱水機で減量後、焼却または狸
め立てなどによって処理され、処理液は排出口l2から
排出されろ。
The floating substances are treated with chemicals to reduce their weight in a dehydrator, and then are treated by incineration or taming, and the treated liquid is discharged from the discharge port 12.

凝集槽3と急速処理機5は、浮上槽の外に設置してもよ
いが、図に示すように浮上槽10内に設置すれば設近ス
ペースをさらに減少できる。なお、凝集剤(よ排水の状
態に合わ仕て選択使用ずることにより排水秤植ごとの処
F1!が可能である。
The flocculation tank 3 and the rapid treatment device 5 may be installed outside the flotation tank, but if they are installed inside the flotation tank 10 as shown in the figure, the space around them can be further reduced. In addition, by selectively using a flocculant (according to the condition of the drainage), it is possible to use a flocculant (F1) for each drainage scale.

[本発明の効果] このように、本発明はnQ処理として排水中の浮上rl
i物質と沈降性物質をそれぞれ洋上沈澱させろ分lII
l摺をそなえ、前記分lllII摺の脱離液に凝集剤を
加えて撹拌するとともに空気を混合する急速処理機によ
り、不安定な凝集塊を気泡表面に吸着させて浮上槽に吹
き出させるようにしてあるので、従来の加圧浮上方式に
おける混合撹拌、加圧タンク、浮上からなる一連の工程
をポンプとエジェクタによる急速処理機で短時間に行う
二とができ、小型、ffll″Aで安定した固液浮上分
離がT!能になり、設備費および処理コストを低下させ
る効果が得られ、下水道の放流基準が強化されても有効
に適用することができる。なお、浮上生成物は凝集処理
がなされているので、そのまま薬品処理をせずに脱水機
に搬送できる利点がある。
[Effects of the present invention] As described above, the present invention provides floating rl in wastewater as nQ treatment.
Sediment i substance and sedimentable substance respectively on the ocean.
A rapid processing machine equipped with a 1 slide, which adds a flocculant to the liquid removed from the 1 II slide, stirs it, and mixes air, adsorbs unstable agglomerates onto the bubble surface and blows them out into the flotation tank. As a result, a series of processes consisting of mixing, stirring, pressurized tank, and flotation in the conventional pressurized flotation system can be performed in a short time using a rapid processing machine using a pump and ejector. Solid-liquid flotation separation has become T!, which has the effect of reducing equipment costs and treatment costs, and can be effectively applied even if sewer discharge standards are strengthened. This has the advantage that it can be transported directly to the dehydrator without chemical treatment.

また、生物処理が可能な排水では、簡単な沈澱分離槽の
後段に、活性汚泥の生理作用に影響の低い凝集剤を用い
た急速処川!機をI1ク処理装置として設置ずろことに
より、110+)負荷、ノルヘキE′J?:i(特にレ
ストラン排水)が軽減でき、良質の排水効果が可能にな
り、前処理装置の浮上生成物と汚水処理装置の余剰汚泥
とを併せて硝化貯留槽で減量することにより物理的処裡
方式と生物的処理方式の両者の利点をそなえた排水処理
装置を得ることができろ。
In addition, for wastewater that can be treated biologically, we use a flocculant that has a low impact on the physiological effects of activated sludge after a simple sedimentation tank. By installing the machine as an I1 processing device, 110+) load, Norheki E'J? :I (especially restaurant wastewater) can be reduced, a high-quality drainage effect is possible, and physical treatment is achieved by reducing the floating products of the pre-treatment equipment and surplus sludge of the sewage treatment equipment together in the nitrification storage tank. It is possible to obtain a wastewater treatment system that has the advantages of both conventional and biological treatment methods.

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

図(1本発明の実施例の構成を示す側断面図である。 lは分離摺、2は排出管、3は凝集槽、5は急速処理機
、6ポンプ、7はエジエクタ、8はノズル、9は空気吸
入管、 10は浮上槽、 口である。 特許出頼人 株式会社 !は排水
Figure (1) is a side sectional view showing the configuration of an embodiment of the present invention. 1 is a separation slide, 2 is a discharge pipe, 3 is a coagulation tank, 5 is a rapid treatment machine, 6 is a pump, 7 is an ejector, 8 is a nozzle, 9 is the air intake pipe, 10 is the flotation tank, and the mouth.

Claims (1)

【特許請求の範囲】 1 排水中の浮上性物質と沈降性物質をそれぞれ浮上沈
澱させる分離槽と、前記分離槽の脱離液に凝集剤を加え
て撹拌するとともに空気を混合する急速処理機と、急速
処理機からの排水を安定化させる浮上槽をそなえたこと
を特徴とする高速排水処理装置。 2 前記急速処理機が、分離槽からの脱離液に凝集剤を
加えて吸水するポンプと、ポンプ吐出口に設け外気を混
合させるエジェクタとで構成されている特許請求の範囲
第1項記載の高速排水処理装置。
[Scope of Claims] 1. A separation tank that floats and settles floating substances and settling substances in wastewater, and a rapid treatment machine that adds a flocculant to the separated liquid in the separation tank, stirs it, and mixes air. , a high-speed wastewater treatment device characterized by being equipped with a flotation tank that stabilizes the wastewater from the rapid treatment device. 2. The rapid treatment device according to claim 1, wherein the rapid treatment device is comprised of a pump that adds a flocculant to the desorbed liquid from the separation tank and absorbs water, and an ejector that is installed at the pump discharge port and mixes outside air. High-speed wastewater treatment equipment.
JP15027289A 1989-06-12 1989-06-12 High-speed waste water treating device Pending JPH0316687A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15027289A JPH0316687A (en) 1989-06-12 1989-06-12 High-speed waste water treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15027289A JPH0316687A (en) 1989-06-12 1989-06-12 High-speed waste water treating device

Publications (1)

Publication Number Publication Date
JPH0316687A true JPH0316687A (en) 1991-01-24

Family

ID=15493327

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15027289A Pending JPH0316687A (en) 1989-06-12 1989-06-12 High-speed waste water treating device

Country Status (1)

Country Link
JP (1) JPH0316687A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100408484B1 (en) * 2000-12-20 2003-12-06 주식회사 앤바이오 Treatment Equipment of Wastewater
JP2007111609A (en) * 2005-10-19 2007-05-10 Toyota Motor Corp Separation method and apparatus
JP4598143B1 (en) * 2009-12-03 2010-12-15 株式会社東横イン環境エネルギー研究所 Domestic water reuse system
JP2011521780A (en) * 2008-05-28 2011-07-28 ブイダブリュエス・ウエストガース・リミテッド Fluid processing apparatus and fluid processing method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100408484B1 (en) * 2000-12-20 2003-12-06 주식회사 앤바이오 Treatment Equipment of Wastewater
JP2007111609A (en) * 2005-10-19 2007-05-10 Toyota Motor Corp Separation method and apparatus
JP4518001B2 (en) * 2005-10-19 2010-08-04 トヨタ自動車株式会社 Separation method and separation apparatus
JP2011521780A (en) * 2008-05-28 2011-07-28 ブイダブリュエス・ウエストガース・リミテッド Fluid processing apparatus and fluid processing method
JP4598143B1 (en) * 2009-12-03 2010-12-15 株式会社東横イン環境エネルギー研究所 Domestic water reuse system
JP2011117184A (en) * 2009-12-03 2011-06-16 Toyoko Inn Kankyo Energy Kenkyusho:Kk System for reusing domestic water

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