JPH0226689A - Sewage treatment apparatus - Google Patents
Sewage treatment apparatusInfo
- Publication number
- JPH0226689A JPH0226689A JP17773588A JP17773588A JPH0226689A JP H0226689 A JPH0226689 A JP H0226689A JP 17773588 A JP17773588 A JP 17773588A JP 17773588 A JP17773588 A JP 17773588A JP H0226689 A JPH0226689 A JP H0226689A
- Authority
- JP
- Japan
- Prior art keywords
- waste water
- tank
- flocs
- water
- bubbles
- 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
Links
- 239000010865 sewage Substances 0.000 title claims description 7
- 239000002351 wastewater Substances 0.000 claims abstract description 44
- 239000000126 substance Substances 0.000 claims abstract description 10
- 239000006260 foam Substances 0.000 claims description 22
- 238000005273 aeration Methods 0.000 claims description 5
- 238000005187 foaming Methods 0.000 claims description 5
- 230000003311 flocculating effect Effects 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 3
- 238000003756 stirring Methods 0.000 abstract description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 abstract description 2
- 239000003945 anionic surfactant Substances 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract description 2
- 229920000642 polymer Polymers 0.000 abstract description 2
- 239000004094 surface-active agent Substances 0.000 abstract description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 abstract 2
- 238000005189 flocculation Methods 0.000 abstract 2
- 230000016615 flocculation Effects 0.000 abstract 2
- 238000005406 washing Methods 0.000 abstract 2
- 101150054854 POU1F1 gene Proteins 0.000 abstract 1
- 238000009792 diffusion process Methods 0.000 abstract 1
- 239000002736 nonionic surfactant Substances 0.000 abstract 1
- 239000008399 tap water Substances 0.000 abstract 1
- 235000020679 tap water Nutrition 0.000 abstract 1
- 239000003599 detergent Substances 0.000 description 9
- 238000000746 purification Methods 0.000 description 9
- 239000000243 solution Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003657 drainage water Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000001055 chewing effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N hexane Substances CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000002563 ionic surfactant Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野1
本発明は主に洗車場から出る洗車排水を、再利用可能な
状態まで浄化する汚水処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field 1] The present invention mainly relates to a sewage treatment device that purifies car wash wastewater discharged from a car wash to a state where it can be reused.
[従来の問題点1
近年水質汚染や水資源節約を呼びかける声から、フィン
洗車場あるいはサービスステーションの洗車コーナーか
ら排出される洗車排水を浄化して再利用する考えが提案
されている。[Conventional Problem 1] In recent years, in response to calls for water pollution and conservation of water resources, the idea of purifying and reusing car wash wastewater discharged from Finn car washes or car wash corners of service stations has been proposed.
洗車排水は一般に砂・塵埃にはじまり、ワックス・洗剤
といった各種懸濁質を含んでおり、これら懸濁質を取り
除いて排水を浄化するには、発泡性をもつ洗剤成分とそ
の他の懸濁質を同時に除去しなければならず、従来の装
置では洗剤による泡の処理が問題となっていた。しかも
常に洗車排水に洗剤成分が含まれているとは限らず、洗
剤成分を含む排水と含まない排水によって処理方法を変
えなければならない等の問題点があった。Car wash wastewater generally contains various suspended solids, including sand and dust, as well as wax and detergent.In order to remove these suspended solids and purify the wastewater, it is necessary to add foaming detergent ingredients and other suspended solids. It has to be removed at the same time, and with conventional equipment, the treatment of foam with detergents has been a problem. Furthermore, car wash wastewater does not always contain detergent components, and there are problems such as the need to change the treatment method depending on whether the wastewater contains detergent components or not.
[発明の目的1
本発明は上記問題点に対処し成されたもので、浄化処理
時に発生する泡を利用しあらゆる条件の洗車排水に対し
ても、十分な浄化作用の得られる汚水浄化装置を提供す
ることを目的としている。[Objective of the Invention 1] The present invention has been made to address the above-mentioned problems, and provides a sewage purification device that utilizes the foam generated during purification treatment to obtain a sufficient purification effect for car wash wastewater under any conditions. is intended to provide.
[発明の実施例1 以下図面を基に本発明実施例について詳細に説明する。[Embodiment 1 of the invention Embodiments of the present invention will be described in detail below based on the drawings.
第1図は本発明実施例に関わる汚水処理装置のシステム
説明図である。1は洗車場などから排水される洗車排水
を一箇所に集め一時貯留する排水ビット、2は該排水を
ポンプで汲み上げ更に貯留する二次貯留槽である。該二
次貯留槽は互いに連通する複数槽から成り、排水中に含
まれる砂・塵埃といった不純物質を沈澱させ、排水をあ
る程度浄化する役割りを持つ。3は散気管4を備え、底
部を漏斗形状とする汚水浄化槽である。前記散気管4は
コンプレッサ5に接続され、微細気泡を槽内に供給する
。6は浄化処理時に排水に凝集薬液を添加する7a集薬
液添加装置で、7は浄化槽3を包囲する泡沫集収槽であ
る。従って浄化処理時には排水中に形成されるフロック
を、散気W4より噴出する泡沫で浮上させ、排水水面に
滞積するフロックと共に泡沫集収槽にオーバーフローさ
せる。FIG. 1 is a system explanatory diagram of a sewage treatment apparatus according to an embodiment of the present invention. Reference numeral 1 designates a drainage bit that collects and temporarily stores car wash wastewater discharged from a car wash, etc., and 2 designates a secondary storage tank that pumps up the wastewater with a pump and further stores it. The secondary storage tank is composed of a plurality of tanks communicating with each other, and has the role of precipitating impurities such as sand and dust contained in the wastewater and purifying the wastewater to some extent. 3 is a sewage septic tank equipped with an aeration pipe 4 and having a funnel-shaped bottom. The air diffuser pipe 4 is connected to a compressor 5 and supplies fine bubbles into the tank. Reference numeral 6 denotes a drug collecting liquid addition device 7a that adds a flocculating chemical liquid to wastewater during purification treatment, and 7 is a foam collection tank that surrounds the septic tank 3. Therefore, during the purification process, the flocs formed in the waste water are floated by the foam ejected from the air diffuser W4, and are caused to overflow into the foam collection tank together with the flocs accumulated on the water surface of the waste water.
8は浄化槽より圧送される浄化水中に含まれる残留フロ
ックを濾過するフィルター装置で、9は処理水給口、1
0は清水給口、11は処理水及び清水を貯える貯水槽で
ある。12は前記二次貯留槽2底部に沈殿する不純物質
や、浄化処理時に泡沫集収槽7で受けるフロック、及び
浄化槽底部に堆積する不純物質を受けるフロック脱水槽
で、ここで摘出する水分は前記排水ピットに戻される。8 is a filter device that filters residual flocs contained in purified water pumped from the septic tank; 9 is a treated water inlet; 1
0 is a fresh water supply port, and 11 is a water tank for storing treated water and fresh water. Reference numeral 12 denotes a floc dewatering tank which receives impurities precipitated at the bottom of the secondary storage tank 2, flocs received in the foam collection tank 7 during purification treatment, and impurities deposited at the bottom of the septic tank. Returned to the pit.
なお、以上のシステム構成による汚水浄化処理は、連続
的に行なわれるものではなく、浄化槽3を満水にしたら
一度排水の注水を止め、浄化を行なった後再び排水を注
水するというように、浄化槽の容量単位で不連続的にバ
ッチ処理し、その都度処理水を貯水槽に送水するもので
ある。The sewage purification process using the above system configuration is not performed continuously, but once the septic tank 3 is full, the injection of wastewater is stopped, and after purification, the wastewater is injected again. Batch processing is performed discontinuously in units of capacity, and the treated water is sent to a water storage tank each time.
次に以上の構成において、処理槽内にて行なわれる排水
の凝集処理行程について説明する。この行程では、凝集
薬液添加装置6による薬液添加と、前記散気管4から噴
出する微細泡沫による攪拌及び泡沫処理が行なわれる。Next, a description will be given of the coagulation treatment process of wastewater carried out in the treatment tank in the above configuration. In this process, the chemical solution is added by the flocculating chemical solution addition device 6, and the agitation and foam treatment using the fine bubbles ejected from the aeration pipe 4 are performed.
その際に添加される薬液および添加量を以下に示す、な
お、カッコ内の数字は添加順番を表し、添加量について
は全て排水2001に対しての量を表す。The chemical solution added at that time and the amount added are shown below. The numbers in parentheses indicate the order of addition, and all amounts added are based on the amount of wastewater 2001.
第1表
前記二次貯水槽2の排水を処理槽3に規定量溝たしたら
、まず凝集助剤を添加し攪拌を行なう。Table 1 After a specified amount of wastewater from the secondary water storage tank 2 is poured into the treatment tank 3, a coagulation aid is first added and stirred.
こ、の凝集助剤はアニオン界面活性剤と、凝集保促剤と
炭酸塩とから成り、そのうちの7ニオン界面活性剤は発
泡性を備える。この時攪拌時間が短いこともあり、排水
はわずかに発泡する程度で、特に目立った変化は認めら
れない、その後所定時間をおいて、凝集剤を添加し攪拌
を行なうと排水は白濁する。そして再び所定時間放置し
た後、高分子凝集剤を添加し攪拌すると、排水中の@濁
粒子はフロックとして析出し始める。そこで70ツクの
完全な析出を待って今度はそれまでの放置時間と比較し
て、比較的長めの放置時間(ここでは15分)をとる、
すると、排水中に析出したフロックは、そのほとんどが
自然浮上して水面に滞積し、水中にはわずかが浮遊する
のみとなる。This aggregation aid consists of an anionic surfactant, an aggregation promoter, and a carbonate, of which the 7-ionic surfactant has foaming properties. At this time, since the stirring time is short, the waste water only foams slightly and no noticeable change is observed. After a predetermined period of time, when a flocculant is added and stirred, the waste water becomes cloudy. After leaving the mixture for a predetermined time again, a polymer flocculant is added and stirred, and the turbid particles in the wastewater begin to precipitate as flocs. So, after waiting for 70 tsuku to completely precipitate, this time, compared to the previous leaving time, let it stand for a relatively long time (here, 15 minutes).
As a result, most of the flocs deposited in the wastewater float to the surface and accumulate on the water surface, with only a small amount floating in the water.
そこで、処理槽底部に備えられる散気管4から微細泡沫
を噴出して泡沫処理を行なう。その微細泡沫は浮遊フロ
ックに付着してそれを水面に浮上させると共に、排水を
激しく攪拌する。すると初めに添加した発泡性をもつ凝
集剤が作用して、排水が泡立ちはじめ、泡沫処理を行な
っている間予量の泡を発生する。この泡は、水面に浮い
て滞積しているフロックを押し上げて槽外に排出すると
共に、泡が槽外にオーバーフローすることで発泡性を持
つ界面活性剤自身も排水中から取り除くものである。こ
の時に、排水中に洗剤成分が含まれていれば、−緒に除
去されるのはもちろんである。Therefore, foam treatment is performed by ejecting fine foam from an aeration tube 4 provided at the bottom of the treatment tank. The fine bubbles adhere to the floating flocs, causing them to rise to the surface of the water, and also violently agitating the wastewater. Then, the initially added flocculant with foaming properties acts and the wastewater begins to foam, generating a predetermined amount of foam during foam treatment. These bubbles push up the flocs floating on the water surface and discharge them out of the tank, and when the bubbles overflow to the outside of the tank, the foaming surfactant itself is also removed from the waste water. At this time, if detergent components are contained in the wastewater, they will of course be removed at the same time.
このように本発明によると、洗剤成分を含まない洗車排
水も泡沫浮上方式で浄化処理できるようになる。その結
果を第2表に示す。As described above, according to the present invention, car wash wastewater that does not contain detergent components can also be purified using the foam flotation method. The results are shown in Table 2.
tjS2表
透視度 N−ヘキサン
洗車排水(未処理) 4度 28pp噛従米
法 10〜18度 17p、論本発明
30度以上 5 ppeeシステム
説明図。tjS2 surface visibility N-hexane car wash wastewater (untreated) 4 degrees 28 pp chewing rice method 10 to 18 degrees 17 pages, theoretical invention 30 degrees or more 5 Ppee system explanatory diagram.
1は排水ビット、4は散気管、3は浄化槽、7は泡沫集
収槽、6は薬液添加装置。1 is a drainage bit, 4 is an aeration pipe, 3 is a septic tank, 7 is a foam collection tank, and 6 is a chemical solution addition device.
[発明の効果1
以上説明したよ)に、本発明によれば洗剤成分を含まな
い(あるいは含有洗剤濃度の低い)洗車排水でも、泡沫
処理することによって泡を発生させ該泡を利用して、処
理槽よりオーバーフローできず排水水面に滞積していた
フロックを、排水中の浮′Rフロックと共に槽外の泡沫
集収槽に除去することが可能になる。しかもこのことに
よって、従来の装置にあったような、処理槽内の排水水
面に滞積するフロックの塊をかき集めるスクレーパを必
要とすることなく、簡単な装置で浄化処理が可能になる
等の効果が得られる。[Effects of the Invention 1 As explained above], according to the present invention, even car wash wastewater that does not contain detergent components (or has a low detergent concentration) is treated with foam to generate foam, and the foam is utilized. The flocs that could not overflow from the treatment tank and were accumulated on the surface of the drainage water can be removed together with the floating flocs in the drainage water into the foam collection tank outside the tank. Furthermore, this has the effect of making purification treatment possible with a simple device, without the need for a scraper to scrape up lumps of floc accumulated on the surface of the waste water in the treatment tank, which was required with conventional devices. is obtained.
Claims (1)
と、該浄化槽を包囲するよう構成し浄化槽よりオーバー
フローする泡沫を受ける泡沫集収槽と、浄化槽内に発泡
性を有する凝集薬液を添加する薬液添加装置とを備え凝
集薬液により形成されたフロックを泡と共に浮上させ、
泡沫集収槽においてオーバーフロー処理することを特徴
とする汚水処理装置。A drainage pit for storing car wash wastewater, a septic tank equipped with an aeration pipe, a foam collection tank configured to surround the septic tank and receive foam that overflows from the septic tank, and a chemical solution addition device that adds a flocculating chemical solution with foaming properties into the septic tank. and float the flocs formed by the flocculating chemical solution together with bubbles,
A sewage treatment device characterized in that overflow is treated in a foam collection tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17773588A JPH0226689A (en) | 1988-07-15 | 1988-07-15 | Sewage treatment apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17773588A JPH0226689A (en) | 1988-07-15 | 1988-07-15 | Sewage treatment apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0226689A true JPH0226689A (en) | 1990-01-29 |
Family
ID=16036208
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17773588A Pending JPH0226689A (en) | 1988-07-15 | 1988-07-15 | Sewage treatment apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0226689A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20000037345A (en) * | 2000-04-19 | 2000-07-05 | 정효현 | Solid separation method and apparatus using minuteness bubble |
KR20020089762A (en) * | 2001-05-24 | 2002-11-30 | 주식회사 맑은물 | a waste water disposal plant |
KR100427594B1 (en) * | 2001-09-18 | 2004-04-30 | 정인 | Apparatus and method for eliminateing dissolved solids and suspended solids of wastewater by microbubble |
JP2011512127A (en) * | 2008-02-08 | 2011-04-21 | ベーリンガー インゲルハイム エルツェーファウ ゲゼルシャフト ミット ベシュレンクテル ハフツング ウント コンパニー コマンディトゲゼルシャフト | Biomolecule generation method and apparatus |
CN106673104B (en) * | 2017-01-09 | 2020-09-22 | 同济大学 | Preparation method and preparation device of coagulated colloid bubbles |
-
1988
- 1988-07-15 JP JP17773588A patent/JPH0226689A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20000037345A (en) * | 2000-04-19 | 2000-07-05 | 정효현 | Solid separation method and apparatus using minuteness bubble |
KR20020089762A (en) * | 2001-05-24 | 2002-11-30 | 주식회사 맑은물 | a waste water disposal plant |
KR100427594B1 (en) * | 2001-09-18 | 2004-04-30 | 정인 | Apparatus and method for eliminateing dissolved solids and suspended solids of wastewater by microbubble |
JP2011512127A (en) * | 2008-02-08 | 2011-04-21 | ベーリンガー インゲルハイム エルツェーファウ ゲゼルシャフト ミット ベシュレンクテル ハフツング ウント コンパニー コマンディトゲゼルシャフト | Biomolecule generation method and apparatus |
CN106673104B (en) * | 2017-01-09 | 2020-09-22 | 同济大学 | Preparation method and preparation device of coagulated colloid bubbles |
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