JPH08257557A - Treatment method for foamed scum - Google Patents

Treatment method for foamed scum

Info

Publication number
JPH08257557A
JPH08257557A JP9132195A JP9132195A JPH08257557A JP H08257557 A JPH08257557 A JP H08257557A JP 9132195 A JP9132195 A JP 9132195A JP 9132195 A JP9132195 A JP 9132195A JP H08257557 A JPH08257557 A JP H08257557A
Authority
JP
Japan
Prior art keywords
scum
tank
foam
sludge
water
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
JP9132195A
Other languages
Japanese (ja)
Inventor
Hideaki Hamada
英明 浜田
Yoshie Fukuoka
佳江 福岡
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.)
Hitachi Kiden Kogyo Ltd
Original Assignee
Hitachi Kiden Kogyo 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 Hitachi Kiden Kogyo Ltd filed Critical Hitachi Kiden Kogyo Ltd
Priority to JP9132195A priority Critical patent/JPH08257557A/en
Publication of JPH08257557A publication Critical patent/JPH08257557A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To treat foamed scum by a method in which the scum is concentrated in a concentration tank, the concentrated scum is collected on the water surface to be defoamed by water spray, the scum which is restored to a form of sludge is concentrated by gravity to be treated by a sludge dewatering machine. CONSTITUTION: A scum flow obstruction wall 8 is installed radially on the water surface of a circular treatment tank equipped with a scum scraping machine to obstruct the following turn of foamed scum by a scum scraper 72. The operation of the scum scraping machine is periodically stopped for a while to collect the foamed scum efficiently between the scum flow obstruction wall 8 and the scum scraper 72 for defoaming treatment by water spray.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は汚水処理システムにおい
て、沈澱槽または発泡スカムを濃縮するために設けたス
カム処理槽のスカムを集めて、散水にて効率的に沈降さ
せて処理するようにした発泡スカムの処理方法に関する
ものである。
INDUSTRIAL APPLICABILITY The present invention relates to a sewage treatment system in which a scum in a sedimentation tank or a scum treatment tank provided for concentrating foam scum is collected and efficiently settled by sprinkling for treatment. The present invention relates to a method for treating foam scum.

【0002】[0002]

【従来の技術】下水の処理において、下水中の曝気によ
り、処理槽に発泡スカムが多量に発生し、槽水面に浮遊
する。この発泡スカムは土壌細菌(放線菌)が曝気にて
異常増殖し、曝気槽で発泡スカム化するものである。こ
の発泡スカムは最終沈澱池水面上に浮上して、見栄えを
悪くすると共に、処理水と共に越流して水質を悪化させ
る等の問題があった。対策としてスカムスキマーによる
排除方法があるが、発泡スカムの性状が柔らかく、水分
を多量に含むため、固形分として分離しがたく、排除後
はスカム返流水として下水処理場の流入口に戻されてい
る。
2. Description of the Related Art In the treatment of sewage, aeration of sewage causes a large amount of foam scum to be generated in a treatment tank and float on the water surface of the tank. This foamed scum is that soil bacteria (actinomycetes) aerate and abnormally proliferate, and become foamed scum in the aeration tank. The foamed scum floats above the surface of the final settling basin to make it look unattractive and overflow with the treated water to deteriorate the water quality. As a countermeasure, there is a removal method using a scum skimmer, but since the properties of the foam scum are soft and it contains a large amount of water, it is difficult to separate it as a solid content, and after removal it is returned to the inlet of the sewage treatment plant as scum return water. There is.

【0003】[0003]

【発明が解決しようとする課題】しかしこの方法では発
泡スカムを完全に除去しきれず、残留した放線菌が下水
処理系内を循環するため、この放線菌が曝気槽内に流入
すると再び発泡スカム化し、水面に浮遊するものとなっ
ている。
However, in this method, the foam scum cannot be completely removed, and residual actinomycetes circulate in the sewage treatment system. Therefore, when the actinomycete flows into the aeration tank, foam scum is formed again. , It floats on the surface of the water.

【0004】本発明は発泡スカムを濃縮槽内で濃縮し、
これを水面に集めて散水にて消泡し、再度汚泥状態に戻
し、これを重力濃縮して汚泥脱水機にて処理するように
なしたことを目的とする。
The present invention concentrates foam scum in a thickener,
The purpose is to collect this on the surface of the water, defoam it by sprinkling it, return it to the sludge state again, gravity concentrate it, and treat it with a sludge dehydrator.

【0005】[0005]

【課題を解決するための手段】本発明は上記目的を達成
するためになしたもので、スカム掻寄機を備えた円形処
理槽の半径方向で、その水面上にスカム阻流壁を設け
て、スカム掻寄板による発泡スカムの供回りを阻止し、
かつ周回運動するスカム掻寄機を定期的に一時停止せし
め、スカム阻流壁とスカム掻寄板の間に発泡スカムを効
率よく集めて、散水による脱泡処理を行うことを要旨と
する。
The present invention has been made to achieve the above object, and a scum baffle wall is provided on the water surface in the radial direction of a circular processing tank equipped with a scum scraper. , Prevents the foam scum from going around with the scum draw plate,
In addition, the scum crawler that makes an orbital motion is temporarily stopped, and the foam scum is efficiently collected between the scum baffle wall and the scum crawler plate to perform defoaming treatment by watering.

【0006】[0006]

【作用】スカム掻寄機を配備した円形処理槽の半径方向
で、その水面上にスカム阻流壁を設けて、スカム掻寄板
による発泡スカムの供回りを阻止し、かつ周回運動する
スカム掻寄機を定期的に一時停止せしめ、スカム阻流壁
とスカム掻寄板の間に発泡スカムを効率よく集めて濃縮
することができ、そしてこれを散水により消泡して汚泥
状態に戻している。このため、発泡スカムの処理が効率
的に行えるものとなる。
Operation: A scum blocking wall is provided on the water surface in the radial direction of a circular treatment tank equipped with a scum scraper to prevent the foam scum from being circulated by the scum scraper plate and to move around the scum scraper. By periodically suspending the stop machine, the foam scum can be efficiently collected and concentrated between the scum barrier wall and the scum draw plate, and this is defoamed by sprinkling and returned to the sludge state. Therefore, the processing of the foam scum can be efficiently performed.

【0007】[0007]

【実施例】以下本発明発泡スカムの処理方法を図示の実
施例に基づいて説明する。図3は下水処理場に流入する
下水(汚水)を曝気槽を経て濃縮槽で濃縮した後、最終
沈澱池に導き処理する下水処理のフローチャートであっ
て、1は各家庭その他等より廃水された下水を回収し流
入する原水槽、2はこの原水槽1で、予め固液を分離し
た汚泥等をポンプP等を介して供給し曝気処理を施す曝
気槽である。
The method for treating the foamed scum of the present invention will be described below with reference to the illustrated embodiment. Fig. 3 is a flow chart of sewage treatment in which sewage (sewage) flowing into the sewage treatment plant is concentrated in an enrichment tank via an aeration tank and then led to the final settling tank for treatment, where 1 is wastewater from each household or the like. A raw water tank 2 for collecting and inflowing sewage is a raw water tank 1, which is an aeration tank for supplying sludge or the like in which solid-liquid is separated in advance through a pump P or the like to perform aeration treatment.

【0008】この曝気槽2で発生した発泡スカムは、水
面上に浮遊しているため、曝気槽内の撹拌流やブロワー
の空気流等とオイルフェンスの組合せにより曝気槽より
越流させて効率よく、し渣スクリーン6へ導く。このし
渣スクリーン6では、ビニール袋、生理用品など、発泡
スカムと性状を異にするし渣を除去することを目的とし
て、曝気槽及び最終沈澱池から送られた水を前処理し
て、次行程で発泡スカムを確実に処理できるようにす
る。
Since the foamed scum generated in the aeration tank 2 floats on the water surface, it can be efficiently overflowed from the aeration tank by a combination of the stirring flow in the aeration tank, the air flow of the blower and the oil fence. , To the residue screen 6. In this residue screen 6, the water sent from the aeration tank and the final sedimentation tank is pretreated for the purpose of removing the residue that has a property different from that of the foam scum such as a plastic bag and sanitary goods, and then Ensure that foam scum can be treated in the process.

【0009】曝気槽2には最終沈澱池3を接続し、曝気
槽内で分離して除去する汚泥分を供給し、この最終沈池
3で汚泥中の固形分を分離し、この固形分(汚泥)の一
部を曝気槽2へ返送する返送汚泥とし、他の汚泥はこれ
を濃縮して一時貯留するため、汚泥濃縮貯留槽4へ送
る。そしてここで生じる上澄水は処理水として排水され
る。
A final settling tank 3 is connected to the aeration tank 2 to supply a sludge component to be separated and removed in the aeration tank, the solid content in the sludge is separated in the final sedimentation tank 3, and the solid content ( A part of the sludge is returned to the aeration tank 2 to be returned sludge, and the other sludge is sent to the sludge concentration storage tank 4 to concentrate and temporarily store it. The supernatant water generated here is discharged as treated water.

【0010】汚泥濃縮貯留槽4に汚泥脱水機5を配設
し、濃縮汚泥をさらに脱水して予め定めた含水率となる
ようにして排出し、ここで生じる脱離水を回収して原水
槽1へ戻し、再処理するものである。
A sludge dewatering machine 5 is installed in the sludge thickening storage tank 4, and the concentrated sludge is further dehydrated and discharged so as to have a predetermined water content, and the desorbed water generated here is recovered to collect the raw water tank 1. To reprocess and reprocess.

【0011】し渣スクリーン6には発泡スカム濃縮槽7
を接続する。この発泡スカム濃縮槽7では、し渣スクリ
ーン6にて前処理した発泡スカムを脱泡処理して重力沈
澱、濃縮せしめる。発泡スカムの濃縮物は曝気槽混合液
と、放線菌/汚泥微生物比が同じであり、発泡スカム濃
縮物、すなわち汚泥濃縮物となって最終沈澱池3から引
き抜く余剰汚泥と混合して、後段の汚泥処理が行える。
汚泥脱水処理では放線菌を95〜99%回収できるの
で、脱水ケーキ搬出により系内の放線菌を低減できる。
この発泡スカム中の放線菌数は、発泡スカム1g当たり
1000万個程度含まれており、曝気槽混合液と比べ、
10倍以上の濃度であり、また放線菌と汚泥微生物の比
率は発泡スカムと混合液とも同じである。つまり、発泡
スカムの脱泡物は汚泥そのものであるため、通常の汚泥
脱水処理が可能で、また汚泥脱水機による放線菌の回収
率は95〜99%であり、効率よく処理される。
The residue screen 6 has a foam scum concentrating tank 7
Connect. In the foam scum concentrating tank 7, the foam scum pretreated by the residue screen 6 is defoamed to be gravity precipitated and concentrated. The foam scum concentrate has the same actinomycetes / sludge microbial ratio as the aeration tank mixed solution, and it becomes foam scum concentrate, that is, sludge concentrate, and is mixed with the excess sludge drawn from the final settling tank 3, Sludge treatment is possible.
Since 95 to 99% of the actinomycetes can be recovered in the sludge dehydration treatment, the actinomycetes in the system can be reduced by carrying out the dehydrated cake.
The number of actinomycetes contained in this foamed scum is about 10 million per 1 g of foamed scum, which is higher than that of the aeration tank mixed solution.
The concentration is 10 times or more, and the ratio of actinomycetes and sludge microorganisms is the same in both foam scum and mixed solution. That is, since the defoamed material of the foam scum is the sludge itself, ordinary sludge dewatering treatment is possible, and the recovery rate of actinomycetes by the sludge dewatering machine is 95 to 99%, which is an efficient treatment.

【0012】脱水機5による脱離水の放線菌は、流入下
水と同じレベル1000〜10000個/ml程度に低減
されるので、原水槽1へ返流しても差し支えない。場合
によっては塩素等の手段により殺菌処理して返流しても
かまわない。次に発泡スカム濃縮槽7の上澄水は、槽へ
の流入によりオーバーフローして原水槽へ戻す。この場
合、上澄水は流入下水と同等乃至それ以下の処理である
ため、場内返流が可能である。
Since the actinomycetes of the desorbed water by the dehydrator 5 are reduced to the same level as the inflowing sewage, about 1000 to 10000 / ml, it can be returned to the raw water tank 1. In some cases, it may be sterilized by a means such as chlorine and returned. Next, the supernatant water of the foaming scum concentrating tank 7 overflows upon returning to the tank and is returned to the raw water tank. In this case, since the supernatant water has a treatment equal to or less than that of the inflow sewage, it can be returned to the site.

【0013】図1は発泡スカム濃縮槽7の平面図、図2
は同縦断面図で、以下発泡スカム濃縮槽7での作用を図
1,図2に基づいて説明する。所要面積を有する発泡ス
カム濃縮槽7には、その中心にモータ70にて駆動され
る駆動軸71を回動自在に配設し、この駆動軸71には
水面位置にスカム掻寄板72、槽底部に汚泥掻寄板73
をそれぞれ設け、共に回動するようにする。
FIG. 1 is a plan view of the foam scum concentrating tank 7, FIG.
Is a vertical sectional view of the same, and the operation of the foam scum concentrating tank 7 will be described below with reference to FIGS. A drive shaft 71 driven by a motor 70 is rotatably disposed at the center of the foamed scum concentrating tank 7 having a required area, and a scum draw plate 72, a tank are provided at the water surface position on the drive shaft 71. Sludge drawing plate 73 on the bottom
Are provided so that they can rotate together.

【0014】また発泡スカム濃縮槽7の中央部には、セ
ンターウェル74を水没するようにして配設し、これに
スカム流入管75を設けると共に、槽底中央部には集泥
ピット76を設けて汚泥引抜管77にて排泥する。
Further, a center well 74 is disposed in the center of the foam scum concentrating tank 7 so as to be submerged in water, and a scum inflow pipe 75 is provided therein, and a mud collecting pit 76 is provided in the center of the bottom of the tank. The sludge drawing pipe 77 discharges the sludge.

【0015】発泡スカム濃縮槽7の水面位置外周部には
上澄水排水トラフ8を配置し、処理された上澄水をこれ
に接続した上澄水排水管79を経て排水すると共に、槽
中心より内周壁まで半径方向にスカム阻流壁8を水面位
置に配設し、かつこのスカム阻流壁8の外端を槽内周壁
面に沿って円形に配設したスカム越流防止板81の内周
面と当接する。
A supernatant water drainage trough 8 is arranged on the outer peripheral portion of the water surface position of the foam scum concentrating tank 7, and the treated supernatant water is drained through a supernatant water drainage pipe 79 connected thereto, and the inner peripheral wall from the center of the tank. The inner peripheral surface of the scum overflow prevention plate 81 in which the scum baffle wall 8 is arranged at the water surface position in the radial direction and the outer end of the scum baffle wall 8 is circularly arranged along the inner wall surface of the tank. Abut.

【0016】またスカム阻流壁8の上流側には散水管9
を複数本半径方向に配設し、この散水管9に消泡用の散
水を供給するが、この散水管下方位置までスカム掻寄板
72が侵入しないよう散水管の前方位にスカム掻寄板停
止装置91を設ける。
A water sprinkling pipe 9 is provided upstream of the scum baffle wall 8.
Are provided in the radial direction, and sprinkling water for defoaming is supplied to the sprinkler pipe 9. However, the scum attractor plate 72 is provided in the front direction of the sprinkler pipe so that the scum attractor plate 72 does not enter the position below the sprinkler pipe. A stop device 91 is provided.

【0017】従って発泡スカム濃縮槽7への流入は発泡
スカム以外に混合液が多く含まれる。従って汚泥部分は
センターウェル74により汚泥が拡散しないように装置
中央下の汚泥ピット76へ直下させる。一方発泡スカム
は比重が小さく、水面に浮上するが、センターウェル7
4が水没しているため、水面の全域に広がる。この発泡
スカムを中心駆動のスカム掻寄板72にて掻き寄せる
が、池の半径方向にスカム阻流壁8を設けているので、
発泡スカムの供回りを阻止する。スカム掻寄板はスカム
掻寄板停止装置位置でリミットスイッチ等の手段で回転
を一時休止させる。発泡スカムはスカム掻寄板とスカム
阻流壁の間で高密度に掻き寄せられ、滞留する。この滞
留位置の上部には脱泡のための散水管が数多く配管され
ており、回転休止時間中にシャワリングして、十分脱泡
処理を行う。
Therefore, the inflow into the foam scum concentrating tank 7 contains a large amount of mixed liquid in addition to the foam scum. Therefore, the sludge part is directly moved to the sludge pit 76 under the center of the apparatus so that the sludge is not diffused by the center well 74. On the other hand, the foam scum has a small specific gravity and floats above the water surface, but the center well 7
Since 4 is submerged, it spreads over the entire water surface. This foamed scum is scraped by the scum scraping plate 72 of the center drive, but since the scum blocking wall 8 is provided in the radial direction of the pond,
Prevents foam scum from going around. The scum crawler plate temporarily stops its rotation by means such as a limit switch at the scum crawler plate stop device position. The foamed scum is raked at a high density between the scum draw plate and the scum baffle and stays there. A large number of sprinkling pipes for defoaming are installed above the retention position, and showering is performed during the rotation suspension time to sufficiently perform defoaming treatment.

【0018】脱泡後、発泡スカムは通常の汚泥として濃
縮し、汚泥掻寄板にて槽中央下部分に収集し、汚泥引抜
管より汚泥処理工程へ移送する。一方スカム掻寄板は所
定の時間休止後、タイマーにより再起動して円形槽軌道
上を動作し、掻き寄せ・休止のサイクルを繰り返して所
定位置に発泡スカムを効率よく集められるものである。
After defoaming, the foamed scum is concentrated as ordinary sludge, collected in the lower part of the center of the tank by a sludge attracting plate, and transferred to a sludge treatment process through a sludge drawing pipe. On the other hand, the scum scraping plate is restarted by a timer after operating for a predetermined time to operate on the circular tank orbit, and the scraping / pausing cycle is repeated to efficiently collect the foamed scum at a predetermined position.

【0019】以下説明の濃縮槽は、同等の機能を最終沈
澱池に付与することが可能である。この場合は濃縮槽を
廃し、かつ沈澱槽3Aを円形とし、図4にそのフローチ
ャートを示す。
The concentration tank described below can provide the same function to the final settling basin. In this case, the concentration tank is abolished, and the precipitation tank 3A is circular, and its flow chart is shown in FIG.

【0020】この実施例では図4に示すように流入する
下水を原水槽1より曝気槽2、し渣スクリーン6を経て
沈澱槽3Aへ導入し、その後沈澱槽3A内で回収した汚
泥を汚泥濃縮貯留槽4へ導き、脱水機5にて脱水する。
In this embodiment, as shown in FIG. 4, the inflowing sewage is introduced from the raw water tank 1 to the settling tank 3A through the aeration tank 2 and the residue screen 6, and then the sludge collected in the settling tank 3A is concentrated into sludge. It is led to the storage tank 4 and dehydrated by the dehydrator 5.

【0021】またこの沈澱槽3Aには、第1実施例と同
様図1、図2に示すように槽内にて回動するスカム掻寄
機、汚泥掻寄機を設けると共に、この槽3Aの半径方向
の水面上に、スカム阻流壁8及び散水管9を設けて構成
し、第1実施例と同じ作用を行うものである。
Further, as in the first embodiment, the settling tank 3A is provided with a scum scraper and a sludge scraper that rotate in the tank as shown in FIGS. The scum baffle wall 8 and the sprinkler pipe 9 are provided on the water surface in the radial direction, and the same operation as that of the first embodiment is performed.

【0022】[0022]

【発明の効果】本発明の発泡スカムの処理方法はスカム
掻寄機を備えた円形処理槽の半径方向で、その水面上に
スカム阻流壁を設けて、スカム掻寄板による発泡スカム
の供回りを阻止し、かつ周回運動するスカム掻寄機を定
期的に一時停止せしめ、スカム阻流壁とスカム掻寄板の
間に発泡スカムを効率よく集めて、散水による脱泡処理
を行うようにしているため、発泡スカムの原因生物であ
る放線菌を脱水ケーキ中へ効率よく回収して排出できる
ため、系内の放線菌数を減らすことができ、発泡スカム
による見栄えや処理水質の悪化を防止できる利点があ
る。
According to the method for treating foam scum of the present invention, the scum blocking wall is provided on the water surface in the radial direction of the circular treatment tank equipped with the scum scraper, and the scum scooping plate serves to provide the foam scum. The scum scraper that blocks the rotation and moves in a circular motion is temporarily stopped, and the foamed scum is efficiently collected between the scum barrier wall and the scum scraper plate to perform defoaming treatment by sprinkling water. Therefore, the actinomycetes that are the causative organism of the foaming scum can be efficiently collected and discharged into the dehydrated cake, so the number of actinomycetes in the system can be reduced, and the appearance and the quality of treated water can be prevented from being deteriorated due to the foaming scum. There is.

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

【図1】本発明の発泡スカムの処理方法の一実施例を示
すフローチャートである。
FIG. 1 is a flowchart showing an embodiment of a method for treating foam scum according to the present invention.

【図2】発泡スカム濃縮槽の縦断面図である。FIG. 2 is a vertical sectional view of a foam scum concentrating tank.

【図3】同平面図である。FIG. 3 is a plan view of the same.

【図4】異なる実施例の発泡スカムの処理方法のフロー
チャートである。
FIG. 4 is a flow chart of a method of treating foam scum according to another embodiment.

【符号の説明】[Explanation of symbols]

1 原水槽 2 曝気槽 3 最終沈澱池 4 汚泥濃縮貯留槽 5 脱水機 6 し渣スクリーン 7 濃縮槽 72 スカム掻寄板 73 汚泥掻き寄せ板 74 センターウェル 78 上澄水排水トラフ 8 スカム阻流壁 81 越流防止板 9 散水管 1 Raw water tank 2 Aeration tank 3 Final settling tank 4 Sludge concentration storage tank 5 Dewatering machine 6 Silt screen 7 Concentration tank 72 Scum draw plate 73 Sludge draw plate 74 Center well 78 Clear water drainage trough 8 Scum barrier wall 81 Overfill Flow prevention plate 9 Sprinkling pipe

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 スカム掻寄機を備えた円形処理槽の半径
方向で、その水面上にスカム阻流壁を設けて、スカム掻
寄板による発泡スカムの供回りを阻止し、かつ周回運動
するスカム掻寄機を定期的に一時停止せしめ、スカム阻
流壁とスカム掻寄板の間に発泡スカムを効率よく集め
て、散水による脱泡処理を行うことを特徴とする発泡ス
カムの処理方法。
1. A scum baffle wall is provided on the water surface in the radial direction of a circular processing tank equipped with a scum scraper to prevent the foam scum from being circulated by a scum scraper plate and to make a circular motion. A method for treating foam scum, which comprises periodically suspending the scum scraper, efficiently collecting the foam scum between the scum barrier wall and the scum draw plate, and performing defoaming treatment by sprinkling water.
【請求項2】 下水処理場に流入する下水を濃縮槽及び
最終沈澱槽を用いて処理する工程において、円形処理槽
を濃縮槽とした請求項1記載の発泡スカムの処理方法。
2. The method for treating foam scum according to claim 1, wherein in the step of treating the sewage flowing into the sewage treatment plant using the concentrating tank and the final settling tank, the circular treating tank is a concentrating tank.
【請求項3】 下水処理場に流入する下水を沈澱槽を用
いて処理する工程において、円形処理槽を沈澱槽とした
請求項1記載の発泡スカムの処理方法。
3. The method for treating foam scum according to claim 1, wherein in the step of treating the sewage flowing into the sewage treatment plant by using the precipitation tank, the circular treatment tank is a precipitation tank.
JP9132195A 1995-03-24 1995-03-24 Treatment method for foamed scum Pending JPH08257557A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9132195A JPH08257557A (en) 1995-03-24 1995-03-24 Treatment method for foamed scum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9132195A JPH08257557A (en) 1995-03-24 1995-03-24 Treatment method for foamed scum

Publications (1)

Publication Number Publication Date
JPH08257557A true JPH08257557A (en) 1996-10-08

Family

ID=14023199

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9132195A Pending JPH08257557A (en) 1995-03-24 1995-03-24 Treatment method for foamed scum

Country Status (1)

Country Link
JP (1) JPH08257557A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113336362A (en) * 2021-06-16 2021-09-03 新疆生产建设兵团建设工程(集团)环境工程有限公司 Environment-friendly industrial wastewater treatment pond
CN115594245A (en) * 2022-07-13 2023-01-13 钱广燕(Cn) Air floatation purification device for industrial wastewater treatment

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113336362A (en) * 2021-06-16 2021-09-03 新疆生产建设兵团建设工程(集团)环境工程有限公司 Environment-friendly industrial wastewater treatment pond
CN113336362B (en) * 2021-06-16 2023-01-20 新疆生产建设兵团建设工程(集团)环境工程有限公司 Environment-friendly industrial wastewater treatment tank
CN115594245A (en) * 2022-07-13 2023-01-13 钱广燕(Cn) Air floatation purification device for industrial wastewater treatment

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