JPH06226248A - Aeration element for surfactant separator for household - Google Patents

Aeration element for surfactant separator for household

Info

Publication number
JPH06226248A
JPH06226248A JP5014016A JP1401693A JPH06226248A JP H06226248 A JPH06226248 A JP H06226248A JP 5014016 A JP5014016 A JP 5014016A JP 1401693 A JP1401693 A JP 1401693A JP H06226248 A JPH06226248 A JP H06226248A
Authority
JP
Japan
Prior art keywords
surfactant
exposure
bubbles
air
bubble
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
JP5014016A
Other languages
Japanese (ja)
Inventor
Yoshitoyo Kenjo
好豊 見城
Hiroyuki Fujii
裕幸 藤井
Fumio Ota
文夫 太田
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP5014016A priority Critical patent/JPH06226248A/en
Publication of JPH06226248A publication Critical patent/JPH06226248A/en
Pending 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

  • Detail Structures Of Washing Machines And Dryers (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Physical Water Treatments (AREA)

Abstract

PURPOSE:To enable the effective generation of relatively large bubbles by constituting an aeration element to be used for a device for effectively separating surfactants from the waste water liquid of a washing machine, etc., to a multilayered structure consisting of inside layers having numerous fine pores and outside layers having numerous coarse holes. CONSTITUTION:The surfactant separator for the washing machine has a water storage tank 2 for storing the waste water liquid 3 from the washing machine 1 and generates the air bubbles by operating an aeration means 4 consisting of the aeration element 4a and air pump 4b immersed in this water storage tank 2 and blowing air into the waste water. The surfactants in the waste water liquid are adsorbed on the surfaces of the air bubbles and are floated and after the air bubbles are introduced through an air bubble storage tank 5 to a bubble rupturing means 6, the surfactants are recovered into a treating tank 7 by liquefying the air bubbles. The aeration element 4a is made into the multilayered structure consisting of the inside layers the having numerous fine pores and the outside layers having the numerous coarse holes. The outside layers are so formed that the pore sizes decrease successively along the longitudinal direction of the element and generate the relatively large air bubbles.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、洗濯機等の排水液か
ら、界面活性剤を効率的に分離するための曝氣素子に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exposing element for efficiently separating a surfactant from a drainage liquid of a washing machine or the like.

【0002】[0002]

【従来の技術】従来、一般家庭での衣料の洗濯や食器の
洗浄によって生じる排水液中には、多くの界面活性剤が
含まれており、この中にはまだ活性力を有するものが含
まれている。しかし従来の洗濯機・食器洗い機・システ
ムキッチンにはこの排水液中から界面活性剤を分離回収
する機能は付加されておらず、これらの排水液は、なん
ら処理されることなく外に排出され、水質汚染の要因に
なっていたが、最近になって泡によって分離回収する方
法が提案された。
2. Description of the Related Art Conventionally, a lot of surfactants are contained in the drainage liquid produced by washing clothes and washing dishes in a general household, and some of them still have an activity. ing. However, conventional washing machines, dishwashers, and system kitchens do not have the function of separating and collecting surfactants from this drainage liquid, and these drainage liquids are discharged outside without any treatment. Although it has been a factor of water pollution, recently, a method of separating and collecting by bubbles has been proposed.

【0003】この泡による界面活性剤の分離方法につい
て、洗濯機排水液処理例により、図5,図6,図7,図
8,図9に基づいて説明する。
A method of separating the surfactant by the foam will be described based on an example of washing liquid of a washing machine with reference to FIGS. 5, 6, 7, 8 and 9.

【0004】図5は洗濯機用界面活性剤分離装置の構成
図である。洗濯機1から貯水槽2内に排水液3を供給
し、曝氣素子4aとエアーポンプ4bからなる曝氣手段
4を作動させて排水液中に空気を吹き込むことにより、
気泡を発生させると、気泡はその表面に排水液中の界面
活性剤を吸着して排水液上面へと浮上する。曝氣を継続
することにより排水液上面に浮上した気泡はその上に設
けられた気泡滞留槽5内を上昇して破泡手段6へ導かれ
る。破泡手段6で界面活性剤を吸着した気泡を液化し
て、界面活性剤処理槽7に回収する。従って、貯水槽2
で処理されて排水口8から排水される液の界面活性剤の
濃度は低くなり、河川の汚染は改善される。
FIG. 5 is a block diagram of a surfactant separating device for a washing machine. By supplying the drainage liquid 3 from the washing machine 1 into the water storage tank 2 and operating the exposure means 4 including the exposure element 4a and the air pump 4b to blow air into the drainage liquid,
When air bubbles are generated, the air bubbles adsorb the surfactant in the waste water on the surface thereof and float to the upper surface of the waste water. By continuing the exposure, the bubbles floating on the upper surface of the drainage liquid rise in the bubble retention tank 5 provided thereon and are guided to the bubble breaking means 6. The bubbles adsorbing the surfactant are liquefied by the bubble breaking means 6 and collected in the surfactant treatment tank 7. Therefore, the water tank 2
The concentration of the surface active agent in the liquid treated by the above and discharged from the drain port 8 becomes low, and the pollution of the river is improved.

【0005】この時、気泡の大きさ・量が界面活性剤の
分離特性に大きく影響する。図6は泡径と水持ち出し率
・界面活性剤の回収率の関係を示し、図7は曝氣量(泡
の量)と水持ち出し率・界面活性剤の回収率の関係を示
す。例えば、泡径小・泡量大(曝氣量大)の場合は、図
6,図7に示すように泡が水を一緒に持ち出して界面活
性剤の分離が事実上できなくなる。逆に、泡径が大きす
ぎると曝氣量に対する界面活性剤の回収効率が極端に悪
くなる。また、図8は排水液の界面活性剤濃度と水持ち
出し率・界面活性剤回収量の関係を示し、図9は泡滞留
槽体積と水持ち出し率・界面活性剤回収率の関係を示
す。この図8,図9から分かるように、排水液の界面活
性剤の濃度や気泡滞留槽の大きさの影響も大変大きく、
気泡の発生は細かく制御する必要がある。
At this time, the size and amount of bubbles have a great influence on the separation characteristics of the surfactant. FIG. 6 shows the relationship between the bubble diameter and the water carry-out rate / surfactant recovery rate, and FIG. 7 shows the relationship between the exposure amount (foam quantity) and the water carry-out rate / surfactant recovery rate. For example, when the bubble diameter is small and the bubble amount is large (exposure amount is large), the bubbles take out water together as shown in FIGS. 6 and 7, and it becomes practically impossible to separate the surfactant. On the contrary, if the bubble diameter is too large, the efficiency of collecting the surfactant with respect to the exposure amount becomes extremely poor. Further, FIG. 8 shows the relationship between the surfactant concentration of the waste water and the water carry-out ratio / surfactant recovery amount, and FIG. 9 shows the relationship between the foam retention tank volume and the water carry-out ratio / surfactant recovery ratio. As can be seen from FIGS. 8 and 9, the influences of the concentration of the surfactant in the drainage liquid and the size of the bubble retention tank are very large,
The generation of bubbles needs to be finely controlled.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、泡を発
生させるための曝氣素子は、下水処理用のものは色々あ
るが、洗濯機の排水液等から、効率よく界面活性剤を分
離するのに適した特性を有するものは見当たらない。
However, there are various exposure elements for generating bubbles, which are for treating sewage. However, in order to efficiently separate the surfactant from the drainage liquid of the washing machine, etc. No one has suitable properties.

【0007】本発明は上記問題点を解決するもので、比
較的小さな曝氣量で、比較的大きな泡を素子全面に均一
に発生させる曝氣素子を提供することを第1の目的とす
る。また連続的に界面活性剤を分離する時、同一曝氣量
で、より効率的に界面活性剤を分離する曝氣素子を提供
することを第2の目的とする。また連続的界面活性剤分
離で、水持ち出し率をおさえて、かつ効率よく界面活性
剤を分離する曝氣素子を提供することを第3の目的とす
る。さらに低コストで、比較的小さな曝氣量で、比較的
大きな泡を素子全面に均一に発生させる曝氣素子を提供
することを第4の目的とする。
The present invention solves the above problems, and it is a first object of the present invention to provide an exposure element capable of uniformly generating relatively large bubbles over the entire surface of the element with a relatively small exposure amount. A second object is to provide an exposure element that more efficiently separates the surfactant with the same exposure amount when continuously separating the surfactant. A third object of the present invention is to provide an exposure element which suppresses the amount of water taken out and efficiently separates the surfactant by continuous surfactant separation. A fourth object is to provide an exposure element that can generate relatively large bubbles uniformly over the entire surface of the element at a low cost and with a relatively small exposure amount.

【0008】[0008]

【課題を解決するための手段】本発明は上記第1の目的
を達成するために、曝氣素子の内層が細かな孔を均一に
無数に有する素材からなり、外層が荒い孔を均一に無数
に有する素材からなる多層構成にしたことを第1の課題
解決手段としている。
In order to achieve the first object of the present invention, the inner layer of the exposure element is made of a material having a large number of fine holes and the outer layer has a large number of rough holes. The first problem-solving means is to have a multi-layered structure made of the materials described in 1.

【0009】また、上記第2の目的を達成するために、
曝氣素子の外層の孔径を素子の長手方向に沿って順に小
さくなるように構成したことを第2の課題解決手段とし
ている。
In order to achieve the second object,
A second problem solving means is that the hole diameter of the outer layer of the exposure element is configured to be gradually reduced along the longitudinal direction of the element.

【0010】また、上記第3の目的を達成するために、
曝氣素子の内層および外層の孔の開口率が、素子の長手
方向に沿って順に大きくなるように構成したことを第3
の課題解決手段としている。
Further, in order to achieve the third object,
The third aspect is that the aperture ratio of the holes in the inner layer and the outer layer of the exposure element is sequentially increased along the longitudinal direction of the element.
Is used as a means for solving the problem.

【0011】また、上記第4の目的を達成するために、
曝氣素子の上面約半分を空気的にマスキングしたことを
第4の課題解決手段としている。
In order to achieve the above-mentioned fourth object,
The fourth problem solving means is that about half of the upper surface of the exposure element is masked pneumatically.

【0012】[0012]

【作用】曝氣素子により発生する泡は次のような性質を
持っている。その泡径は、曝氣素子の孔径・素子材料の
親水性・孔出口の空気の吐出圧により決まる。この3要
因のうち、特に孔径の影響が大きい。また、発生する泡
の量は、孔を通過する空気の量(曝氣量)にほぼ比例
し、空気量は孔の出口までの空気抵抗に逆比例する。
[Function] The bubbles generated by the exposure element have the following properties. The bubble diameter is determined by the hole diameter of the exposing element, the hydrophilicity of the element material, and the discharge pressure of air at the hole outlet. Among these three factors, the influence of the hole diameter is particularly large. Further, the amount of bubbles generated is almost proportional to the amount of air (exposure amount) passing through the hole, and the amount of air is inversely proportional to the air resistance to the outlet of the hole.

【0013】本発明は上記した第1の課題解決手段によ
り、曝氣素子の内層の細かな孔で一定の空気抵抗をもた
せ、素子の各部分への空気量を一定にしたうえで、外層
の孔径を大きくすることで、比較的大きな泡を素子全面
にわたって均一に発生させることができる。
According to the first means for solving the problems described above, the present invention provides a constant air resistance by the fine holes in the inner layer of the exposure element to make the amount of air to each part of the element constant, and then the outer layer of the element. By increasing the pore size, relatively large bubbles can be uniformly generated over the entire surface of the element.

【0014】また、第2の課題解決手段により、曝氣素
子の長手方向に沿って順に小さな泡を発生させることが
できる。
Further, the second problem solving means makes it possible to generate small bubbles in sequence along the longitudinal direction of the exposure element.

【0015】また、第3の課題解決手段により、曝氣素
子の長手方向に沿って順に泡の量を多く発生させること
ができる。
Further, by the third problem solving means, it is possible to generate a large amount of bubbles in sequence along the longitudinal direction of the exposure element.

【0016】また、第4の課題解決手段により、簡単な
構造で泡を素子全面にわたって均一に発生させることが
できる。
Further, according to the fourth problem solving means, bubbles can be uniformly generated over the entire surface of the element with a simple structure.

【0017】[0017]

【実施例】以下本発明の第1の実施例について、図面を
参照しながら説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described below with reference to the drawings.

【0018】図1において、ポリプロピレンの比較的大
きな粉末を焼結成型し、比較的大きな連続孔を有する外
層11の内側に、ポリプロピレンの比較的小さな粉末を
焼結成型して小さな連続孔を有しかつ中空の内層12を
密接して配し、中空の一方を蓋13で締め切り、反対側
に空気導入用のパイプ14を設けて、曝氣素子を構成し
ている。
In FIG. 1, a relatively large powder of polypropylene is sinter-molded, and a relatively small powder of polypropylene is sinter-molded to have a small continuous hole inside the outer layer 11 having a relatively large continuous hole. In addition, the hollow inner layer 12 is arranged in close contact, one of the hollows is closed with a lid 13, and a pipe 14 for introducing air is provided on the opposite side to form an exposure element.

【0019】上記構成において、図1,図5を参照しな
がら動作を説明する。貯水槽2の底面に設置された曝氣
素子4aの空気導入パイプ14に、エアーポンプ4bか
ら空気が送り込まれると、その空気は内層12の小さな
孔を通って外層11に達し、外層11の比較的大きな孔
を通って外層11の外面すなわち排水液に達する。この
空気はエアーポンプ4bから次々に送られてくる空気に
よって排水液中に押し出され、外層11の孔の大きさと
排水液の表面張力(≒界面活性剤濃度)によってほぼ決
まる径の気泡を排水液面上に発生させる。この泡は気泡
滞留槽5を上昇する間に水分を引力によって下方に落と
し、界面活性剤濃度の高い気泡となり破泡手段6に導か
れ、液化されて界面活性剤処理槽7に溜められる。
The operation of the above structure will be described with reference to FIGS. When air is sent from the air pump 4b to the air introduction pipe 14 of the exposure element 4a installed on the bottom surface of the water tank 2, the air reaches the outer layer 11 through the small holes of the inner layer 12, and the comparison of the outer layer 11 is made. The outer surface of the outer layer 11, that is, the drainage liquid is reached through the large holes. This air is pushed into the drainage liquid by the air sent from the air pump 4b one after another, and bubbles having a diameter substantially determined by the size of the pores of the outer layer 11 and the surface tension of the drainage liquid (≈surfactant concentration) are discharged. Generate on the surface. While the bubbles are rising in the bubble retention tank 5, moisture is dropped downward by attractive force to form bubbles having a high surfactant concentration, which are guided to the bubble breaking means 6, liquefied and stored in the surfactant treatment tank 7.

【0020】ところで、曝氣素子の各孔から押し出され
る空気量:A1は、エアーポンプ4bの空気吐出圧をV
o、エアーポンプ4bから曝氣素子の内層12の中空部
までの空気抵抗をRa、内層12の空孔1つ当たりの空
気抵抗をRb1、外層11の孔1つ当たりの空気抵抗を
Rc1、外層11の表面から排水液の表面までの水圧に
よる空気抵抗をRd1とすると A1=Vo÷(Ra+Rb1+Rc1+Rd1) ここで、外層の空孔径は、要求される泡径によって決ま
り、機能上あまり小さくできず、Rc1はどうしても小
さな値になり、もしRb1がないと Rc1≦(Ra+Rd1) となり、A1はRd1の影響を大きく受ける。すなわち、
曝氣素子が排水液中で傾いて設置されると、高い方から
のみ泡が発生し、低い方からは泡が出ないとか、曝氣素
子の上面からは泡が出るが下面からは泡が出ないという
現象がおこる。本実施例の内層12を設け、Rb1を大
きくとると Rb1≫(Ra+Rc1+Rd1) となり、A1はRd1の影響をほとんど受けず、またRc
1のバラツキの影響も小さくなり、VoとRb1の関数と
なる。従って内層の各孔の空気抵抗(Rb1,Rb2,…
Rbn)が均一になるように焼結成型すれば曝氣素子か
ら均一に泡が出せるようになる。
By the way, the amount of air pushed out from each hole of the exposure element: A1 is the air discharge pressure of the air pump 4b is V
o, the air resistance from the air pump 4b to the hollow portion of the inner layer 12 of the exposure element is Ra, the air resistance per hole of the inner layer 12 is Rb1, the air resistance per hole of the outer layer 11 is Rc1, the outer layer Let Rd1 be the air resistance due to the water pressure from the surface of 11 to the surface of the drainage liquid. Becomes a small value, and if Rb1 does not exist, Rc1≤ (Ra + Rd1), and A1 is greatly affected by Rd1. That is,
When the exposure element is installed tilted in the drainage liquid, bubbles are generated only from the higher side and bubbles are not emitted from the lower side, or bubbles are emitted from the upper surface of the exposure element but bubbles are generated from the lower surface. The phenomenon that it does not appear occurs. When the inner layer 12 of the present embodiment is provided and Rb1 is made large, Rb1 >> (Ra + Rc1 + Rd1), and A1 is hardly affected by Rd1 and Rc
The influence of the variation of 1 also becomes small and becomes a function of Vo and Rb1. Therefore, the air resistance (Rb1, Rb2, ...
If sinter molding is performed so that Rbn) becomes uniform, bubbles can be uniformly emitted from the exposure element.

【0021】このように、曝氣素子を2層にし、内層に
空気抵抗をもたせることにより、比較的小さな曝氣量
で、比較的大きな泡を、曝氣素子全面にわたって均一に
発生させることができる。なお本実施例では、素子を2
層構成にしたが、3層にしてもよく、また焼結成型にポ
リプロピレンを用いたが、ポリエチレンやポリ弗化ビニ
リデン等でもよい。
By thus forming the exposure element in two layers and providing the inner layer with air resistance, relatively large bubbles can be uniformly generated over the entire surface of the exposure element with a relatively small exposure amount. . In this embodiment, the element is 2
Although it has a layered structure, it may have three layers, and although polypropylene is used for the sintering molding, polyethylene, polyvinylidene fluoride, or the like may be used.

【0022】なお、曝氣素子全体からの空気量Aoは、
当然のことながら次のように表される。A1+A2+……
Anは各空孔空気量である。
The air amount Ao from the entire exposure element is
Naturally, it is expressed as follows. A1 + A2 + ……
An is the amount of air in each hole.

【0023】Ao=A1+A2+……An 次に第2の実施例について、図2,図5,図6,図8に
基づいて説明する。
Ao = A1 + A2 + ... An Next, a second embodiment will be described with reference to FIGS. 2, 5, 6 and 8.

【0024】図2において、外層を3つに分け、荒い孔
をもつ11aと、中くらいの孔をもつ11bと、細かな
孔をもつ11cによりなり、曝氣時の泡径が順に小さく
なるように構成する。内層12は細かな孔を有する焼結
成型された樹脂からなり、大きな空気抵抗をもたせて、
素子全体から均一に曝氣できるように構成する。その他
は、図1と同じなので、同じ番号を付して説明を省略す
る。
In FIG. 2, the outer layer is divided into three parts, that is, 11a having a rough hole, 11b having a medium hole, and 11c having a fine hole so that the bubble diameter at the time of exposure becomes smaller. To configure. The inner layer 12 is made of a sinter-molded resin having fine pores, and has a large air resistance,
It is configured so that the entire element can be exposed uniformly. Others are the same as those in FIG.

【0025】上記構成において、動作を説明する。図5
において、貯水槽2の底に設けられた曝氣素子4bに
は、洗濯機1側からは、濃度の高い界面活性剤を含んだ
液が供給されるが、排水口8側では、洗濯機1側から泡
により順に界面活性剤が分離されるので、界面活性剤の
低い液が供給される。従って、排水口8の近くでは、図
8に示す特性より、界面活性剤濃度が下がり水持ち出し
率は下がるが、界面活性剤の回収量も下がり、処理能力
も下がってしまう。これを防ぐために図6に示す特性よ
り、水持ち出し率が妥協できるところまで泡径を小さく
することにより、界面活性剤の回収率を上げることがで
きる。このように曝氣素子の泡径を順に小さくすること
で、限られたスペース内での処理能力を高めることがで
きる。
The operation of the above configuration will be described. Figure 5
In the above, the liquid containing the high-concentration surfactant is supplied from the washing machine 1 side to the exposure element 4b provided at the bottom of the water storage tank 2, but the washing machine 1 side is provided on the drain port 8 side. Since the surfactants are sequentially separated from the side by bubbles, a liquid having a low surfactant is supplied. Therefore, in the vicinity of the drainage port 8, the concentration of the surfactant is lower and the water carry-out rate is lower than the characteristics shown in FIG. 8, but the recovery amount of the surfactant is also low and the treatment capacity is also low. In order to prevent this, from the characteristics shown in FIG. 6, the recovery rate of the surfactant can be increased by reducing the bubble diameter to a point where the water removal rate can be compromised. By decreasing the bubble diameter of the exposure element in this way, it is possible to increase the processing capacity in a limited space.

【0026】具体的には、図2の構成で説明したように
外層の孔径を11a,11b,11cのごとく順に小さ
くし、曝氣素子4aの11aを洗濯機1側に、11cを
排水口8側に向けて設置することにより、上記目的を達
成することができる。
Specifically, as described with reference to the configuration of FIG. 2, the hole diameters of the outer layers are reduced in the order of 11a, 11b and 11c, 11a of the exposing element 4a is on the washing machine 1 side, and 11c is the drain port 8. The above-mentioned object can be achieved by installing it toward the side.

【0027】以上のように、本実施例によれば、曝氣素
子全面にわたり均一に発泡しかつ泡径を順に小さくでき
るので、スペースファクターの良い界面活性剤分離装置
を提供できる。
As described above, according to this embodiment, since the foaming can be performed uniformly over the entire surface of the exposure element and the diameter of the foam can be reduced in order, it is possible to provide the surfactant separating apparatus having a good space factor.

【0028】第3の実施例を図3,図7に基づいて説明
する。図3において、ポリプロピレンの比較的大きな粉
末を焼結成型し、比較的大きな連続孔を有する外層21
の内側に、ポリプロピレンの比較的小さな粉末を焼結成
型して小さな連続孔を有した円筒状の内層22を密接し
て配し、かつ、外層21・内層22は、21a,21
b,21cのごとく順に孔の数を増して開口率を大きく
し、内層に大きな空気抵抗をもたせ、外層で泡径を調整
するように構成する。また内層22の中空の一方を蓋2
3で締め切り、反対側に空気導入用のパイプ24を設け
て、曝氣素子を構成している。
A third embodiment will be described with reference to FIGS. In FIG. 3, an outer layer 21 having a relatively large continuous hole formed by sintering a relatively large powder of polypropylene.
A relatively small powder of polypropylene is sinter-molded on the inner side of the cylindrical inner layer 22 having small continuous holes, and the outer layer 21 and the inner layer 22 are 21a, 21a.
As shown in b and 21c, the number of holes is increased in order to increase the aperture ratio, the inner layer has a large air resistance, and the outer layer adjusts the bubble diameter. In addition, the hollow one of the inner layer 22 is attached to the lid 2
The deadline is 3, and a pipe 24 for introducing air is provided on the opposite side to form an exposure element.

【0029】上記構成において動作を説明する。図7に
示すように、界面活性剤分離特性は、曝氣量を増すと水
持ち出し率・界面活性剤回収率ともに上昇する特性があ
るので、実施例2で説明したような界面活性剤を含んだ
液が連続的に流れていき、界面活性剤濃度が順に薄くな
る環境に曝氣素子が置かれた場合、界面活性剤濃度に応
じて曝氣量が順に大きくなるように曝氣素子を構成する
ことにより、スペースファクター及び総曝氣量に対する
分離効率の高い界面活性剤分離装置を提供できる。
The operation of the above configuration will be described. As shown in FIG. 7, the surfactant separation characteristics include the characteristics that both the water carry-out rate and the surfactant recovery rate increase with increasing exposure amount, and thus the surfactant as described in Example 2 is included. When the exposure element is placed in an environment in which the saliva flows continuously and the concentration of the surfactant gradually decreases, the exposure element is configured so that the exposure amount increases in order according to the concentration of the surfactant. By doing so, it is possible to provide a surfactant separation device having a high separation efficiency with respect to the space factor and the total exposure amount.

【0030】第4の実施例について図4に基づいて説明
する。ポリプロピレンの粉末を焼結成型し、連続空孔を
有する円筒状の曝氣用樹脂31と、その上半面をマスキ
ングするマスキング樹脂32と、曝氣用樹脂31の中空
部の一方を蓋33で締め切り、反対側に空気導入用のパ
イプ34を設けて、曝氣素子を構成している。
The fourth embodiment will be described with reference to FIG. The polypropylene powder is sintered and molded, and the cylindrical exposure resin 31 having continuous pores, the masking resin 32 for masking the upper half surface thereof, and one of the hollow portions of the exposure resin 31 are closed with a lid 33. A pipe 34 for introducing air is provided on the opposite side to form an exposure element.

【0031】上記構成において、前記曝氣素子を液中に
おいてパイプ34から空気を送りこむと、空気は曝氣用
樹脂31の孔から液中に押し出され気泡を発生する。こ
の時曝氣用樹脂31の上半分がマスキング樹脂32で覆
われているため、曝氣用樹脂31の各部の水圧による空
気抵抗の差が小さくなり、泡が素子の長手方向に沿って
均一に発生しやすくなる。
In the above structure, when air is sent through the pipe 34 while the aforesaid exposure element is in the liquid, the air is extruded into the liquid through the holes of the exposure resin 31 to generate bubbles. At this time, since the upper half of the exposure resin 31 is covered with the masking resin 32, the difference in the air resistance due to the water pressure in each part of the exposure resin 31 becomes small, and the bubbles are evenly distributed along the longitudinal direction of the element. It tends to occur.

【0032】以上のように本実施例によれば、簡単な構
成で素子の長手方向に沿って均一に泡を発生させること
ができる。
As described above, according to this embodiment, it is possible to uniformly generate bubbles along the longitudinal direction of the element with a simple structure.

【0033】[0033]

【発明の効果】以上のように本発明は、曝氣素子の内層
が細かな孔を均一に無数に有する素材からなり、外層が
荒い孔を均一に無数に有する素材からなる多層構成にし
たことにより、比較的大きな泡を素子全面にわたって均
一に発生させることができ、効率よく界面活性剤の分離
ができる。
INDUSTRIAL APPLICABILITY As described above, according to the present invention, the inner layer of the exposure element is made of a material having an infinite number of fine holes, and the outer layer is made of a multi-layer structure made of a material having an infinite number of rough holes. As a result, relatively large bubbles can be uniformly generated over the entire surface of the device, and the surfactant can be efficiently separated.

【0034】また外層の孔径が素子の長手方向に沿って
順に小さくなるように構成したことによって、曝氣素子
全面にわたり均一に発泡しかつ素子の長手方向に沿って
泡径を順に小さくできるので、スペースファクターの良
い界面活性剤分離装置を提供できる。
Further, since the pore diameter of the outer layer is made smaller in order along the longitudinal direction of the element, the exposure element can be uniformly foamed over the entire surface and the bubble diameter can be successively decreased along the longitudinal direction of the element. It is possible to provide a surfactant separation device having a good space factor.

【0035】また内層および外層の孔の開口率が、素子
の長手方向に沿って順に大きくなるように構成すること
によって、曝氣素子の長手方向に沿って順に泡の量を多
く発生させることができるので、界面活性剤濃度が順に
大きくなる環境に曝氣素子が置かれた場合、界面活性剤
濃度に応じて曝氣量が順に大きくなるように曝氣素子を
構成することにより、スペースファクター及び総曝氣量
に対する分離効率の高い界面活性剤分離装置を提供でき
る。
Further, by forming the aperture ratios of the holes of the inner layer and the outer layer to increase sequentially along the longitudinal direction of the element, a large amount of bubbles can be generated sequentially along the longitudinal direction of the exposing element. Therefore, when the exposure element is placed in an environment in which the surfactant concentration increases in order, by configuring the exposure element so that the exposure amount increases in accordance with the surfactant concentration, the space factor and It is possible to provide a surfactant separation device having high separation efficiency with respect to the total exposure amount.

【0036】また素子の上面約半分を空気的にマスキン
グしたことで、簡単な構造で泡を素子全面にわたって均
一に発生させることができる。
By air-masking approximately half of the upper surface of the element, bubbles can be uniformly generated over the entire surface of the element with a simple structure.

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

【図1】本発明の第1の実施例の図FIG. 1 is a diagram of a first embodiment of the present invention.

【図2】本発明の第2の実施例の図FIG. 2 is a diagram of a second embodiment of the present invention.

【図3】本発明の第3の実施例の図FIG. 3 is a diagram of a third embodiment of the present invention.

【図4】本発明の第4の実施例の図FIG. 4 is a diagram of a fourth embodiment of the present invention.

【図5】界面活性剤分離装置の図FIG. 5: Diagram of surfactant separation device

【図6】泡径と界面活性剤回収率の特性図[Figure 6] Characteristic diagram of bubble diameter and surfactant recovery rate

【図7】曝氣量と界面活性剤回収率の特性図[Figure 7] Characteristic diagram of exposure dose and surfactant recovery rate

【図8】界面活性剤濃度と界面活性剤回収率の特性図FIG. 8: Characteristic diagram of surfactant concentration and surfactant recovery rate

【図9】気泡滞留槽体積と界面活性剤回収率の特性図FIG. 9: Characteristic diagram of bubble retention tank volume and surfactant recovery rate

【符号の説明】[Explanation of symbols]

1 洗濯機 2 貯水層 4 曝氣手段 4a 曝氣素子 5 気泡滞留槽 6 破泡手段 DESCRIPTION OF SYMBOLS 1 Washing machine 2 Water storage layer 4 Exposing means 4a Exposing element 5 Bubble retention tank 6 Bubble breaking means

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 界面活性剤を含んだ液の排水経路中に設
けた貯水槽と、この貯水槽に設けた曝氣手段と、この手
段によって生じる気泡の気泡滞留槽と、この気泡滞留槽
を通過してきた気泡を液化する破泡手段とを備えた界面
活性剤分離装置において、内層が細かな孔を均一に無数
に有する素材からなり、外層が荒い孔を均一に無数に有
する素材からなる多層構成にしたことを特徴とする曝氣
手段の曝氣素子。
1. A water storage tank provided in a drainage path of a liquid containing a surfactant, an exposure means provided in this water storage tank, a bubble retention tank for bubbles generated by this means, and this bubble retention tank. In a surfactant separation device equipped with a bubble breaking means for liquefying bubbles that have passed through, an inner layer is made of a material having a large number of fine pores, and an outer layer is a multilayer made of a material having a large number of rough pores. The exposure element of the exposure means characterized by having the structure.
【請求項2】 外層の孔径が素子の長手方向に沿って順
に小さくなるように構成した請求項1記載の曝氣素子。
2. The exposure element according to claim 1, wherein the hole diameter of the outer layer is arranged to become smaller along the longitudinal direction of the element.
【請求項3】 内層および外層の孔の開口率が、素子の
長手方向に沿って順に大きくなるように構成された請求
項1記載の曝氣素子。
3. The exposure element according to claim 1, wherein the aperture ratios of the holes in the inner layer and the outer layer increase in order along the longitudinal direction of the element.
【請求項4】 界面活性剤を含んだ液の排水経路中に設
けた貯水槽と、この貯水槽に設けた曝氣手段と、この手
段によって生じる気泡の気泡滞留槽と、この気泡滞留槽
を通過してきた気泡を液化する破泡手段とを備えた界面
活性剤分離装置において、素子の上面約半分を空気的に
マスキングしたことを特徴とする曝氣手段の曝氣素子。
4. A water storage tank provided in a drainage path of a liquid containing a surfactant, an exposure means provided in this water storage tank, a bubble retention tank for bubbles generated by this means, and this bubble retention tank. In a surfactant separation device comprising a bubble breaking means for liquefying passing bubbles, about half the upper surface of the element is masked pneumatically, and the exposing element of the exposing means.
JP5014016A 1993-01-29 1993-01-29 Aeration element for surfactant separator for household Pending JPH06226248A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5014016A JPH06226248A (en) 1993-01-29 1993-01-29 Aeration element for surfactant separator for household

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5014016A JPH06226248A (en) 1993-01-29 1993-01-29 Aeration element for surfactant separator for household

Publications (1)

Publication Number Publication Date
JPH06226248A true JPH06226248A (en) 1994-08-16

Family

ID=11849402

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5014016A Pending JPH06226248A (en) 1993-01-29 1993-01-29 Aeration element for surfactant separator for household

Country Status (1)

Country Link
JP (1) JPH06226248A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0965674A1 (en) * 1998-06-15 1999-12-22 Samsung Electronics Co., Ltd. Washing machine
JP2004330066A (en) * 2003-05-07 2004-11-25 Mie Prefecture Water cleaning block and method for manufacturing the same, and water cleaning equipment using the water cleaning block
JP2005523808A (en) * 2002-04-23 2005-08-11 フレデレール インフラストラクチュルテクニック ゲーエムベーハー アンド シーオー.カーゲー Aerator
WO2011160185A1 (en) * 2010-06-25 2011-12-29 Nexus Ewater Pty Ltd Λ process and apparatus for purifying watfr
JP2012170946A (en) * 2011-02-24 2012-09-10 Sumitomo Heavy Industries Environment Co Ltd Air diffusion cylinder, and aerobic tank provided therewith
CN105236556A (en) * 2015-10-13 2016-01-13 浙江水利水电学院 Aeration device for gravel contact technology and implementation method thereof
WO2018188935A1 (en) 2017-04-13 2018-10-18 Unilever N.V. Apparatus and method for recovery of surfactants
JP2019166489A (en) * 2018-03-23 2019-10-03 大同メタル工業株式会社 Fine bubble generation nozzle
US10710904B2 (en) 2013-10-08 2020-07-14 Conopco, Inc. Device and a process for purification of grey water

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0965674A1 (en) * 1998-06-15 1999-12-22 Samsung Electronics Co., Ltd. Washing machine
US6148649A (en) * 1998-06-15 2000-11-21 Samsung Electronics Co., Ltd. Washing machine with a device for eliminating hydrophobic substances contained in washing water
JP2005523808A (en) * 2002-04-23 2005-08-11 フレデレール インフラストラクチュルテクニック ゲーエムベーハー アンド シーオー.カーゲー Aerator
JP2004330066A (en) * 2003-05-07 2004-11-25 Mie Prefecture Water cleaning block and method for manufacturing the same, and water cleaning equipment using the water cleaning block
US9868649B2 (en) 2010-06-25 2018-01-16 Nexus Ewater Pty Ltd. Process and apparatus for purifying water
AU2011269658C1 (en) * 2010-06-25 2017-03-23 Fluence Corporation Limited A process and apparatus for purifying water
WO2011160185A1 (en) * 2010-06-25 2011-12-29 Nexus Ewater Pty Ltd Λ process and apparatus for purifying watfr
JP2012170946A (en) * 2011-02-24 2012-09-10 Sumitomo Heavy Industries Environment Co Ltd Air diffusion cylinder, and aerobic tank provided therewith
US10710904B2 (en) 2013-10-08 2020-07-14 Conopco, Inc. Device and a process for purification of grey water
CN105236556A (en) * 2015-10-13 2016-01-13 浙江水利水电学院 Aeration device for gravel contact technology and implementation method thereof
CN105236556B (en) * 2015-10-13 2017-06-20 浙江水利水电学院 A kind of aerator and implementation for contact technique between gravel
WO2018188935A1 (en) 2017-04-13 2018-10-18 Unilever N.V. Apparatus and method for recovery of surfactants
JP2019166489A (en) * 2018-03-23 2019-10-03 大同メタル工業株式会社 Fine bubble generation nozzle

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