JP3051500B2 - Sedimentation concentrator - Google Patents

Sedimentation concentrator

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Publication number
JP3051500B2
JP3051500B2 JP3147595A JP14759591A JP3051500B2 JP 3051500 B2 JP3051500 B2 JP 3051500B2 JP 3147595 A JP3147595 A JP 3147595A JP 14759591 A JP14759591 A JP 14759591A JP 3051500 B2 JP3051500 B2 JP 3051500B2
Authority
JP
Japan
Prior art keywords
scum
pipe
sedimentation
cylinder
lid plate
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.)
Expired - Fee Related
Application number
JP3147595A
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Japanese (ja)
Other versions
JPH0564707A (en
Inventor
静夫 竹田
Original Assignee
静夫 竹田
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Application filed by 静夫 竹田 filed Critical 静夫 竹田
Priority to JP3147595A priority Critical patent/JP3051500B2/en
Publication of JPH0564707A publication Critical patent/JPH0564707A/en
Application granted granted Critical
Publication of JP3051500B2 publication Critical patent/JP3051500B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、産業廃水等の懸濁水
を清澄化処理するための装置、特に、沈殿性粒子を沈降
させて濃縮する機能と、浮上スカムを除去する機能とを
兼備した沈降濃縮装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for clarifying suspended water such as industrial wastewater, and in particular, has both a function of settling sedimentable particles and concentrating the same and a function of removing floating scum. The present invention relates to a sedimentation and concentration device.

【0002】[0002]

【従来の技術】一般に、沈殿性粒子の比率が高い懸濁水
は沈降濃縮装置により処理され、浮上スカムの比率が高
い懸濁水は加圧浮上装置によって処理されている。とこ
ろが、沈殿性粒子及び浮上スカムの両方を含む懸濁水の
場合、特に、比較的少量の原水を二台の装置で処理して
いてはコストが高くつき大変不経済である。そこで、従
来、沈殿性粒子を沈降濃縮して取出し、浮上スカムを浮
かせて除去するように構成した沈降濃縮装置が提案され
ている。
2. Description of the Related Art Generally, suspended water having a high ratio of sedimentable particles is treated by a sedimentation / concentration device, and suspended water having a high ratio of floating scum is treated by a pressure flotation device. However, in the case of a suspension containing both sedimentable particles and floating scum, it is expensive and very uneconomical, especially if a relatively small amount of raw water is treated with two units. Therefore, conventionally, a sedimentation / concentration device configured to take out sedimentable particles by sedimentation / concentration and remove the floating scum by floating is proposed.

【0003】図2に示すように、従来の沈殿濃縮装置に
おいては、タンク本体1の上部に供給筒2が設置され、
その供給筒2には導入管3を介して凝集タンク4が接続
されている。凝集タンク4では原水と高分子凝集剤とが
撹拌機5により撹拌されて懸濁物のフロック化が促進さ
れる。供給筒2の下側には裾広がりの傾斜面を備えた沈
降促進筒6が配設され、ここで懸濁水中の沈殿性粒子P
が急速に沈降し、浮上スカムSは液面に浮上する。沈殿
性粒子Pはタンク本体1の底部で濃縮され、モータ7で
駆動されるスクレーパ8の回転に伴い掻寄せられてスラ
リー取出管9から外部に取出される。清澄水は沈降促進
筒6の内部に流入し、そこから上昇管10及び流出管1
1を通って外部へ流出する。液面に浮んだ浮上スカムS
は作業員により定期的に汲取られる。
As shown in FIG. 2, in a conventional sedimentation / concentration apparatus, a supply cylinder 2 is provided above a tank body 1,
A coagulation tank 4 is connected to the supply tube 2 via an introduction pipe 3. In the flocculation tank 4, the raw water and the polymer flocculant are stirred by the stirrer 5 to promote flocculation of the suspension. A sedimentation promoting cylinder 6 having a flared slope is disposed below the supply cylinder 2, where the sedimentation particles P in the suspension water are provided.
Sinks rapidly, and the floating scum S floats on the liquid surface. The sedimentable particles P are concentrated at the bottom of the tank main body 1, are scraped by the rotation of the scraper 8 driven by the motor 7, and are discharged from the slurry discharge pipe 9 to the outside. The clarified water flows into the settling accelerating cylinder 6, from which the riser pipe 10 and the outlet pipe 1
It flows out through 1. Floating scum S floating on the liquid surface
Is regularly sampled by workers.

【0004】なお、従来、液面に浮んだ浮上スカムSを
供給筒2の周囲からオーバフローさせて除去する技術も
知られている。また、前記沈降促進筒6及びスクレーパ
8を備えた沈降濃縮装置としては、特公昭57−432
84号公報、特公平2−62282号公報に開示された
技術が公知である。
[0004] Conventionally, there is also known a technique of removing the floating scum S floating on the liquid surface from the periphery of the supply cylinder 2 by overflowing. Further, as a sedimentation-concentration device provided with the sedimentation promoting cylinder 6 and the scraper 8, there is Japanese Patent Publication No. 57-432.
The technology disclosed in Japanese Patent Publication No. 84 and Japanese Patent Publication No. 2-62282 is known.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、従来の
沈降濃縮装置によると、浮上スカムSを液面に浮かせて
除去するため、汲取りに人手を要したり、或いは、浮上
スカムSと共に多量の懸濁水がオーバフローしてしまう
などの問題点があった。また、濃縮層から発生した浮上
スカムSが沈降促進筒6の内部に入り、清澄水と共に流
出するという不具合もあった。そこで、この発明の課題
は、浮上スカムを自動的かつ効率よく除去できる沈降濃
縮装置を提供することにある。
However, according to the conventional sedimentation / concentration apparatus, the floating scum S is floated on the surface of the liquid and removed, so that it takes a lot of labor to pump the scum S or a large amount of suspended scum S together with the floating scum S. There were problems such as turbid water overflowing. Further, there is also a problem that the floating scum S generated from the concentrated layer enters the settling promoting cylinder 6 and flows out together with the clarified water. Therefore, an object of the present invention is to provide a sedimentation / concentration device capable of automatically and efficiently removing a floating scum.

【0006】[0006]

【課題を解決するための手段】上記の課題を解決するた
めに、この発明の沈降濃縮装置は、タンク本体の上端部
に蓋板を設け、蓋板の略中央部に供給筒を設置し、供給
筒に懸濁水の導入管を蓋板より上方の位置で接続し、供
給筒の下側に裾広がりの傾斜面を備えた沈降促進筒を配
設し、タンク本体の底部にスラリー取出管を接続し、沈
降促進筒の内部には懸濁水中の浮上スカムを捕集する上
広がりの傾斜面を備えたスカム捕集筒を収容し、スカム
捕集筒の下端に清澄水の通過口を形成し、沈降促進筒の
上端に上昇管を立設し、上昇管に流出管を蓋板より上方
の位置で接続し、沈降促進筒にスカム捕集筒の上部外周
に連通するスカム導出管を立設し、スカム導出管の上端
を蓋板の下面近傍にて開口し、スカム導出管の上端と対
応する高さのタンク本体にスカム排出口を設けて構成さ
れる。
In order to solve the above-mentioned problems, a sedimentation-concentration apparatus according to the present invention includes a cover plate provided at an upper end portion of a tank body, and a supply cylinder provided at a substantially central portion of the cover plate. The suspension pipe is connected to the supply pipe at a position above the lid plate, a settling-promoting pipe with a flared slope is provided below the supply pipe, and a slurry discharge pipe is provided at the bottom of the tank body. A scum collection tube with a scum collection tube that has an upwardly expanding inclined surface that collects floating scum in suspended water is housed inside the sedimentation promotion tube, and a clear water passage port is formed at the lower end of the scum collection tube A riser pipe is erected at the upper end of the sedimentation promotion cylinder, an outflow pipe is connected to the riser pipe at a position above the lid plate, and a scum discharge pipe communicating with the upper periphery of the scum collection cylinder is set up on the sedimentation promotion cylinder. The upper end of the scum outlet pipe is opened near the lower surface of the lid plate, and a tank having a height corresponding to the upper end of the scum outlet pipe is provided. Configured scum outlet provided in the body.

【0007】[0007]

【作用】この発明の沈降濃縮装置によれば、懸濁水中の
浮上スカムは懸濁水が沈降促進筒を流下する過程で浮上
して蓋板の下面に収集される。清澄水中に残留する浮上
スカム及び濃縮層から発生した浮上スカムは、沈降促進
筒の内部においてスカム捕集筒により捕集されたのち、
スカム導出管を通って蓋板の下面に収集される。懸濁液
の導入管は蓋板より上方に位置し、供給筒の水位がスカ
ム収集層より高いため、この水位差によって蓋板下面に
高密度で凝集された浮上スカムがスカム排出口から外部
へ強制的に排出される。したがって、人手またはポンプ
等の排出手段を用いなくても、浮上スカムを自動的かつ
効率よく除去することができる。
According to the sedimentation / concentration device of the present invention, the floating scum in the suspension water floats in the process of the suspension water flowing down the settling accelerating cylinder and is collected on the lower surface of the lid plate. The floating scum remaining in the clear water and the floating scum generated from the concentrated layer are collected by the scum collecting cylinder inside the settling accelerating cylinder,
It is collected on the lower surface of the lid plate through the scum outlet pipe. The suspension inlet pipe is located above the lid plate, and the water level of the supply cylinder is higher than the scum collection layer, so the floating scum that has been densely aggregated on the lower surface of the lid plate due to this water level difference goes outside from the scum discharge port. Emitted forcibly. Therefore, the floating scum can be automatically and efficiently removed without using manual means or a discharging means such as a pump.

【0008】[0008]

【実施例】以下、この発明を具体化した一実施例を図面
に基づいて説明する。図1に示すように、この実施例の
沈殿濃縮装置においては、タンク本体1が円筒状に形成
され、その上端部には蓋板13が固設されている。蓋板
13の中央部には供給筒2が設置され、その上端はタン
ク本体1の上端と同じ高さに、また、下端は蓋板13よ
り下方に位置している。供給筒2には導入管3が蓋板1
3より上方の位置で接続され、その導入管3は従来と同
様の凝集タンク4に結合されている。なお、蓋板13に
はエアー抜き管12が立設されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below with reference to the drawings. As shown in FIG. 1, in the sedimentation and concentration apparatus of this embodiment, a tank body 1 is formed in a cylindrical shape, and a lid plate 13 is fixed to an upper end thereof. The supply tube 2 is installed at the center of the cover plate 13, the upper end of which is located at the same height as the upper end of the tank body 1, and the lower end thereof is located below the cover plate 13. The supply tube 2 has an inlet tube 3 and a cover plate 1
3 and is connected to a coagulation tank 4 similar to the conventional one. The cover plate 13 is provided with the air vent tube 12 provided upright.

【0009】供給筒2の下側には、裾広がりの円錐傾斜
面を備えた沈降促進筒6が配設され、その上端が供給筒
2の内部に挿入されるとともに、下端は支持片14によ
りタンク本体1の内壁面に支持されている。沈降促進筒
6の上端には上昇管10が接続され、その上昇管10に
は流出管11が前記導入管3と同じ高さで接続されてい
る。上昇管10と沈降促進筒6の内部にはロッド15が
挿通され、その下端にはスクレーパ8が固設され、上端
にはスクレーパ8を回転させるモータ7が連結されてい
る。タンク本体1の底部にはスラリー溜り16が形成さ
れ、そこにはスラリー取出管9が接続されている。な
お、スラリー取出管9は電磁バルブを介し汚泥タンク
(いずれも図示略)に接続されている。
On the lower side of the supply cylinder 2, a sedimentation promoting cylinder 6 having a flared conical inclined surface is disposed, the upper end of which is inserted into the supply cylinder 2, and the lower end of which is supported by a support piece 14. It is supported on the inner wall surface of the tank body 1. A rising pipe 10 is connected to the upper end of the settling promoting cylinder 6, and an outflow pipe 11 is connected to the rising pipe 10 at the same height as the introduction pipe 3. A rod 15 is inserted into the inside of the riser pipe 10 and the settling promoting cylinder 6, and a scraper 8 is fixedly provided at a lower end thereof, and a motor 7 for rotating the scraper 8 is connected to an upper end thereof. A slurry reservoir 16 is formed at the bottom of the tank body 1, and a slurry discharge pipe 9 is connected thereto. The slurry discharge pipe 9 is connected to a sludge tank (both not shown) via an electromagnetic valve.

【0010】沈降促進筒6の内部には、懸濁水中の浮上
スカムSを捕集する上広がりの円錐傾斜面を備えたスカ
ム捕集筒17が収容固定され、その下端には清澄水が上
方へ通過する通過口18が形成されている。また、沈降
促進筒6の外面にはスカム導出管19が立設され、その
下端はスカム捕集筒17の上部外周の位置にに連通され
るとともに、上端は蓋板13の下面近傍に開口されてい
る。そして、このスカム導出管19の上端と対応する高
さにおいてタンク本体1にはスカム排出口20が設けら
れている。なお、スカム排出口20も電磁バルブ(図示
略)を介し前記汚泥タンクに接続されている。
Inside the sedimentation promoting cylinder 6, a scum collecting cylinder 17 having an upwardly expanding conical inclined surface for collecting the floating scum S in the suspension water is accommodated and fixed, and at the lower end thereof, clear water is provided upward. Is formed. A scum outlet pipe 19 is provided upright on the outer surface of the sedimentation promoting cylinder 6, and the lower end thereof communicates with the upper outer periphery of the scum collecting cylinder 17, and the upper end is opened near the lower surface of the cover plate 13. ing. A scum discharge port 20 is provided in the tank body 1 at a height corresponding to the upper end of the scum outlet pipe 19. The scum discharge port 20 is also connected to the sludge tank via an electromagnetic valve (not shown).

【0011】上記のように構成したこの実施例の沈降濃
縮装置においては、凝縮タンク4で原水と高分子凝集剤
とが撹拌機5により急速に撹拌されて、懸濁物のフロッ
ク化が促進され、フロック生成物を含んだ懸濁水が導入
管3を介して供給筒2に導入される。供給筒2では懸濁
水が旋回水流により緩速で撹拌されて、フロック化がさ
らに促進され、その状態で懸濁水が供給筒2の下端開口
から沈降促進筒6の周囲に供給される。沈降促進筒6で
はその傾斜面の作用により懸濁水中の沈殿性粒子Pが急
速に沈降されるとともに、浮上スカムSが浮上して蓋板
13の下面に収集される。沈降促進筒6の下方へ沈降し
た沈殿性粒子Pはタンク本体1の底部で濃縮され、スク
レーパ8の回転に伴いスラリー溜り16に掻寄せられ
る。そして、スラリー取出管9に接続した電磁バルブが
例えば一日に数回開放されると、スラリー溜り16の濃
縮スラリーがスラリー取出管9を通って汚泥タンクに排
出される。
In the settling and concentrating apparatus of this embodiment constructed as described above, the raw water and the polymer flocculant are rapidly stirred in the condensing tank 4 by the stirrer 5 to promote flocculation of the suspension. The suspension water containing the floc product is introduced into the supply tube 2 through the introduction pipe 3. In the supply tube 2, the suspended water is stirred at a slow speed by the swirling water flow, and flocculation is further promoted. In this state, the suspended water is supplied from the lower end opening of the supply tube 2 to the periphery of the settling promoting tube 6. In the sedimentation promoting cylinder 6, the sedimentary particles P in the suspension water are rapidly settled by the action of the inclined surface, and the floating scum S floats and is collected on the lower surface of the cover plate 13. The sedimentable particles P that have settled below the sedimentation promoting cylinder 6 are concentrated at the bottom of the tank body 1 and are scraped by the slurry reservoir 16 as the scraper 8 rotates. When the electromagnetic valve connected to the slurry discharge pipe 9 is opened, for example, several times a day, the concentrated slurry in the slurry reservoir 16 is discharged to the sludge tank through the slurry discharge pipe 9.

【0012】沈殿性粒子Pが分離された一次清澄水は上
昇流となって沈降促進筒6の内部に流入し、スカム捕集
筒17の通過口18を通る過程で減速され、これによ
り、なお残留する微細な沈殿性粒子Pの沈降を促して一
次清澄水の清澄度が向上される。通過口18を通過した
二次清澄水は上昇管10を上昇し、流出管11からオー
バフローして外部の清澄水タンク(図示略)に流出す
る。
The primary clarified water from which the sedimentable particles P have been separated flows upward into the sedimentation promoting cylinder 6 and is decelerated in the course of passing through the passage 18 of the scum collecting cylinder 17. The sedimentation of the remaining fine sedimentable particles P is promoted, and the clarity of the primary clarified water is improved. The secondary clarified water that has passed through the passage port 18 rises in the riser pipe 10, overflows from the outflow pipe 11, and flows out to an external clarified water tank (not shown).

【0013】一方、一次清澄水中に残留している浮上ス
カムS、及び、沈殿性粒子Pの濃縮層から発生した浮上
スカムSは、スカム捕集筒17の傾斜面の作用によって
その上部外周に捕集され、そこからスカム導出管19を
通って蓋板13の下面に収集される。そして、スカム排
出口20に接続した電磁バルブが例えば一日に数回開放
されると、蓋板13の下面に高密度で凝集されたスカム
がスカム排出口20を通って汚泥タンクに排出される。
このとき、導入管3が蓋板13より上方に位置して、供
給筒2内の水位がスカム収集層よりはるかに高いため、
この水位差によって浮上スカムSが強制的に排出され
る。したがって、人手またはポンプ等の排出手段を用い
なくても、浮上スカムSを自動的かつ効率よく除去する
ことができる。
On the other hand, the floating scum S remaining in the primary clarified water and the floating scum S generated from the concentrated layer of the sedimentary particles P are trapped on the outer periphery of the upper part by the action of the inclined surface of the scum collecting cylinder 17. From the scum outlet pipe 19 to the lower surface of the cover plate 13. When the electromagnetic valve connected to the scum outlet 20 is opened, for example, several times a day, scum agglomerated at a high density on the lower surface of the cover plate 13 is discharged to the sludge tank through the scum outlet 20. .
At this time, since the introduction pipe 3 is located above the cover plate 13 and the water level in the supply cylinder 2 is much higher than the scum collection layer,
The floating scum S is forcibly discharged by this water level difference. Therefore, the floating scum S can be automatically and efficiently removed without using manual means or a discharging means such as a pump.

【0014】なお、この発明は上記実施例に限定される
ものではなく、例えば、沈降促進筒6及びスカム捕集筒
17を角錐形状に形成したり、スカム導出管19及びス
カム排出口20をそれぞれ複数個設けたり、スクレーパ
8を省略したりするなど、本発明の趣旨を逸脱しない範
囲で各部の形状並びに構成を適宜に変更して具体化する
ことも可能である。
The present invention is not limited to the above embodiment. For example, the sedimentation promoting cylinder 6 and the scum collecting cylinder 17 may be formed in a pyramid shape, and the scum outlet pipe 19 and the scum discharge port 20 may be respectively formed. The shape and configuration of each part may be appropriately changed and embodied without departing from the spirit of the present invention, such as by providing a plurality of pieces or omitting the scraper 8.

【0015】[0015]

【発明の効果】以上に詳述したように、この発明によれ
ば、浮上スカムをスカム捕集筒により捕集して蓋板の下
面に収集し、水位差を利用して強制的に排出するように
構成したので、人手またはポンプ等の排出手段を用いな
くても、浮上スカムを自動的且つ能率よく除去できると
いう優れた効果を奏する。
As described above in detail, according to the present invention, the floating scum is collected by the scum collecting cylinder, collected on the lower surface of the cover plate, and forcibly discharged using the difference in water level. With such a configuration, there is an excellent effect that the floating scum can be automatically and efficiently removed without using any manual or discharge means such as a pump.

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

【図1】この発明の一実施例を示す沈降濃縮装置の断面
図である。
FIG. 1 is a sectional view of a sedimentation / concentration apparatus showing an embodiment of the present invention.

【図2】従来の沈降濃縮装置を示す断面図である。FIG. 2 is a sectional view showing a conventional sedimentation / concentration device.

【符号の説明】[Explanation of symbols]

1…タンク本体、2…供給筒、3…導入管、6…沈降促
進筒、9…スラリー取出管、10…上昇管、11…流出
管、13…蓋板、17…スカム捕集筒、18…通過口、
19…スカム導出管、20…スカム排出口、P…沈殿性
粒子、S…浮上スカム。
DESCRIPTION OF SYMBOLS 1 ... Tank main body, 2 ... Supply cylinder, 3 ... Introduction pipe, 6 ... Settling promotion cylinder, 9 ... Slurry removal pipe, 10 ... Rise pipe, 11 ... Outflow pipe, 13 ... Cover plate, 17 ... Scum collection cylinder, 18 … Passage,
19: scum discharge pipe, 20: scum discharge port, P: precipitated particles, S: floating scum.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 タンク本体(1)の上端部に蓋板(1
3)を設け、蓋板(13)の略中央部に供給筒(2)を
設置し、供給筒(2)に懸濁水の導入管(3)を蓋板
(13)より上方の位置で接続し、供給筒(2)の下側
に裾広がりの傾斜面を備えた沈降促進筒(6)を配設
し、タンク本体(1)の底部にスラリー取出管(9)を
接続し、沈降促進筒(6)の内部には懸濁水中の浮上ス
カムを捕集する上広がりの傾斜面を備えたスカム捕集筒
(17)を収容し、スカム捕集筒(17)の下端に清澄
水の通過口(18)を形成し、沈降促進筒(6)の上端
に上昇管(10)を立設し、上昇管(10)に流出管
(11)を蓋板(13)より上方の位置で接続し、沈降
促進筒(6)にスカム捕集筒(17)の上部外周に連通
するスカム導出管(19)を立設し、スカム導出管(1
9)の上端を蓋板(13)の下面近傍にて開口し、スカ
ム導出管(19)の上端と対応する高さのタンク本体
(1)にスカム排出口(20)を設けてなることを特徴
とする沈降濃縮装置。
1. A cover plate (1) is provided on an upper end of a tank body (1).
3) is provided, and a supply tube (2) is installed substantially at the center of the lid plate (13), and a suspension pipe (3) is connected to the supply tube (2) at a position above the lid plate (13). A sedimentation promoting cylinder (6) having a flared slope is disposed below the supply cylinder (2), and a slurry discharge pipe (9) is connected to the bottom of the tank body (1) to promote sedimentation. Inside the tube (6), a scum collecting tube (17) having an upwardly-spreading inclined surface for collecting floating scum in the suspension water is accommodated, and clear water is provided at the lower end of the scum collecting tube (17). A passage (18) is formed, and a riser (10) is erected at the upper end of the settling promoting cylinder (6), and an outflow pipe (11) is placed on the riser (10) at a position above the lid plate (13). The scum discharge pipe (1) is connected to the scum discharge pipe (1), and a scum discharge pipe (19) communicating with the upper periphery of the scum collection pipe (17) is erected on the settling promotion pipe (6).
The upper end of 9) is opened near the lower surface of the lid plate (13), and the scum discharge port (20) is provided in the tank body (1) having a height corresponding to the upper end of the scum outlet pipe (19). Characterized sedimentation and concentration equipment.
JP3147595A 1991-06-19 1991-06-19 Sedimentation concentrator Expired - Fee Related JP3051500B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3147595A JP3051500B2 (en) 1991-06-19 1991-06-19 Sedimentation concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3147595A JP3051500B2 (en) 1991-06-19 1991-06-19 Sedimentation concentrator

Publications (2)

Publication Number Publication Date
JPH0564707A JPH0564707A (en) 1993-03-19
JP3051500B2 true JP3051500B2 (en) 2000-06-12

Family

ID=15433906

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3147595A Expired - Fee Related JP3051500B2 (en) 1991-06-19 1991-06-19 Sedimentation concentrator

Country Status (1)

Country Link
JP (1) JP3051500B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100378135B1 (en) * 2000-12-29 2003-04-07 중앙종합기계 주식회사 A high efficiency settling tank
WO2019187355A1 (en) * 2018-03-28 2019-10-03 隆 玉城 Device for removing sediment/floating matter in water and on water surface

Also Published As

Publication number Publication date
JPH0564707A (en) 1993-03-19

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