JP2926070B2 - Coagulation sedimentation equipment - Google Patents

Coagulation sedimentation equipment

Info

Publication number
JP2926070B2
JP2926070B2 JP4925295A JP4925295A JP2926070B2 JP 2926070 B2 JP2926070 B2 JP 2926070B2 JP 4925295 A JP4925295 A JP 4925295A JP 4925295 A JP4925295 A JP 4925295A JP 2926070 B2 JP2926070 B2 JP 2926070B2
Authority
JP
Japan
Prior art keywords
inclined bottom
sewage
tank body
coagulation sedimentation
deepest
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
JP4925295A
Other languages
Japanese (ja)
Other versions
JPH08215504A (en
Inventor
清和 佐藤
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.)
MASUZAWA GIKEN JUGEN
Original Assignee
MASUZAWA GIKEN JUGEN
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 MASUZAWA GIKEN JUGEN filed Critical MASUZAWA GIKEN JUGEN
Priority to JP4925295A priority Critical patent/JP2926070B2/en
Publication of JPH08215504A publication Critical patent/JPH08215504A/en
Application granted granted Critical
Publication of JP2926070B2 publication Critical patent/JP2926070B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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、小規模工場等から排出
される各種廃液を含む汚水(以下、「汚水」という。)
の浄化処理に使用する凝集沈でん装置の改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to sewage containing various waste liquids discharged from small-scale factories (hereinafter referred to as "sewage").
The present invention relates to an improvement in a coagulation and sedimentation apparatus used for purification treatment of ash.

【0002】[0002]

【従来の技術】従来、凝集沈でん方式の汚水の浄化処理
は、汚水に空気または酸素を供給する一方、攪拌機構
によりその汚水を攪拌しつつ、薬品の投入やバクテリヤ
の増殖で汚水中の汚染物質を酸化あるいは還元するため
の攪拌槽と、上記攪拌槽で反応が完了し得られた浮遊
懸濁物質や酸化物または還元物を沈でんさせるための沈
でん槽、の2槽で行われていた。
2. Description of the Related Art Conventionally, in the purification treatment of sewage by the coagulation and sedimentation method, while supplying air or oxygen to the sewage, the sewage is stirred by a stirring mechanism, and chemicals and bacteria are multiplied. The reaction is carried out in two tanks: a stirring tank for oxidizing or reducing the water and a sedimentation tank for sedimenting suspended suspended solids, oxides or reduced products obtained by completing the reaction in the stirring tank.

【0003】しかしながら、小規模工場等における例え
ばレンズ研磨汚水、メッキ汚水、窯業汚水、プリント基
板製作の汚水、アルマイト等各種表面処理加工の汚水、
印刷所の洗浄汚水等は、いずれも1回に処理すべき汚水
量が1,000リットル程度であり、上記2体の槽装置
は大規模となり、広い設置面積を必要とするとか日常の
管理が複雑であるとかの問題を有し、小規模工場等では
この装置を容易に設置しがたいものとしていた。
However, in small factories, for example, lens polishing wastewater, plating wastewater, ceramic wastewater, wastewater for printed circuit board production, wastewater for various surface treatments such as alumite,
The amount of sewage to be treated at one time is about 1,000 liters for the washing sewage etc. of the printing shop. The above two tanks are large-scale and require a large installation area or complicated daily management. In a small-scale factory or the like, it is difficult to install this device.

【0004】そして、上記の問題を解決した汚水の攪
拌反応と、反応の完了により生成された浄水の排水
と、浮遊懸濁物等の沈でんおよび排泥を同一槽で行う
ことができる、小型で比較的少量の各種汚水の処理に適
する凝集沈でん装置が特許出願公告昭55ー11885
号により発表され、現在、各所の小規模工場等で使用さ
れている。
[0004] A compact, compact reactor capable of performing the agitation reaction of sewage, which solves the above-mentioned problems, the drainage of purified water generated by the completion of the reaction, and the sedimentation and discharge of suspended solids and the like in the same tank. A coagulation settling apparatus suitable for treating a relatively small amount of various kinds of sewage is disclosed in Japanese Patent Application Publication No. 55-11885.
And is currently used in small factories at various locations.

【0005】以下、この発明を図を参照しながら説明す
る。図3は装置の内部構成を示す側面図、図4は図3の
平面図である。この両図において、1は直立円筒形の槽
体、1aは槽体1の一側から他側にかけて配設された傾
斜底、2は、槽体1の上方から傾斜底1aの上面に沿
い、傾斜底1aの最低部付近にまで延引配設され、その
先端に複数の噴気孔2aが穿設された二股分岐部2bを
設けた給気管、3は、槽体1の槽壁1bの最深部側の中
間部に設けられた汚水6から処理された浄水の排水口、
3aは、槽体1の槽壁1bの最深部側の最深部に設けら
れた汚水6の処理された凝集沈でん物の排泥口である。
なお、2dはブロア装置、3bは、排水口3からの残留
浮遊物の排出阻止壁を示す。
Hereinafter, the present invention will be described with reference to the drawings. FIG. 3 is a side view showing the internal configuration of the apparatus, and FIG. 4 is a plan view of FIG. In these figures, 1 is an upright cylindrical tank body, 1a is an inclined bottom disposed from one side of the tank body 1 to the other side, 2 is an upper surface of the tank body 1 along the upper surface of the inclined bottom 1a, An air supply pipe extending to the vicinity of the lowest portion of the inclined bottom 1a and provided with a forked branch portion 2b having a plurality of blowout holes 2a formed at the tip thereof, 3 is the deepest portion of the tank wall 1b of the tank body 1. Outlet of purified water treated from sewage 6 provided in the middle part of the side
Reference numeral 3a denotes a discharge port for the treated coagulated sediment of the sewage 6 provided at the deepest part on the deepest part side of the tank wall 1b of the tank body 1.
Reference numeral 2d denotes a blower device, and 3b denotes a wall for preventing discharge of residual suspended matter from the drain port 3.

【0006】このようにして、槽体1に送られた汚水
6に中和剤、凝集剤等の薬液が加えられ、続いてブロ
ア装置2dからの空気を給気管2を介して、上記の二股
分岐部2bの噴気孔2aから激しく噴出させると、図
中の矢印で示すように、噴出空気は槽体1の最深部から
周囲の汚水6を伴って上昇し、水面に到着すると槽体1
の円筒形に阻まれて自然に槽体1の中心部方向に流動
し、汚水6自体と槽壁1bの抵抗により減速しつつ反対
側の槽壁1b付近に達し、連続する汚水6の上昇による
加力により傾斜底1aの浅部方向に還流する。この還
流の繰り返しにより、攪拌、酸素供給、薬液反応が効果
的に行われる。そして設定時間(約30分)の還流
後、設定時間(約60分)の滞留をさせることにより凝
集物は槽体1の最深部方向に沈でん堆積する。そこで
上方の排水口3を開き処理された浄水を排水し、浄水
の排水後に下方の排泥口3aを開き沈でんした凝集物を
排泥させる。
In this manner, a chemical such as a neutralizing agent and a coagulant is added to the sewage 6 sent to the tank body 1, and the air from the blower device 2 d is supplied through the air supply pipe 2 to the above-mentioned bifurcated water. When violently ejected from the fumarole 2a of the branch portion 2b, the ejected air rises from the deepest part of the tank body 1 with the surrounding sewage 6 as shown by the arrow in the figure.
And naturally flows in the direction of the center of the tank body 1 and decelerates due to the resistance of the sewage 6 itself and the tank wall 1b, and reaches the vicinity of the opposite tank wall 1b while being decelerated. By the applied force, the fluid flows back toward the shallow part of the inclined bottom 1a. By repeating this reflux, stirring, oxygen supply, and chemical reaction are effectively performed. After the reflux for a set time (about 30 minutes), the aggregate is settled and deposited in the deepest part direction of the tank body 1 by being kept for a set time (about 60 minutes). Then, the upper drain port 3 is opened to drain the treated purified water, and after draining the purified water, the lower drain port 3a is opened to drain the settled aggregates.

【0007】[0007]

【発明が解決しようとする課題】上述の凝集沈でん装置
は、槽体内の汚水を上昇させ、分岐させ、槽体の内円周
に沿い、他側で衝突、合流させて減速下降流ならしめ、
短い攪拌時間で攪拌の目的が達成できるようにしたもの
で、小型の装置に構成され設置面積も少くて良く、少量
ずつ排出される汚水の浄化処理に卓越した効果を奏する
ものであり、従来の技術の項で述べたように、現在も多
くの小規模工場等で使用されている。
The above-mentioned coagulation and sedimentation apparatus raises and branches sewage in the tank body, and collides and merges on the other side along the inner circumference of the tank body to form a decelerated downflow.
It is intended to achieve the purpose of stirring in a short stirring time, it is configured in a small device, the installation area may be small, and has an excellent effect on the purification treatment of sewage discharged little by little. As mentioned in the technical section, it is still used in many small factories.

【0008】しかしながら、この装置は低濃度汚水の浄
化処理について最適なものであるが、水性塗料汚水、ア
ルミダイカスト離型剤汚水等の高濃度汚水については低
濃度汚水の場合と異なり、低濃度の場合の設定時間に
よる攪拌では十分な反応が得られず、再攪拌するとか、
攪拌設定時間を変更するとか、従来方法で得られた浄
水、汚泥を再処理するとかを余儀なくされる。加え
て、生成された沈でん凝集物については粘度が高く、傾
斜底部分および沈でん物の排泥口に沈でん物が粘着残留
し、次第に処理能力が低下して装置が使用できなくな
る。という問題を有し、専ら低濃度汚水の浄化処理にの
みに使用されて来た。本発明は、上記の問題に鑑みなさ
れたものであり、高濃度汚水の浄化処理に使用しても全
く支障がない改良された一槽式の凝集沈でん装置の提供
を目的とする。
[0008] However, this apparatus is optimal for the purification treatment of low-concentration sewage. However, unlike high-concentration sewage such as aqueous paint sewage and aluminum die-casting release agent sewage, unlike the low-concentration sewage, this apparatus has a low concentration. In the case of stirring for a set time, a sufficient reaction cannot be obtained,
It is necessary to change the set stirring time or to reprocess the purified water and sludge obtained by the conventional method. In addition, the generated sediment agglomerates have a high viscosity, and the sediment sticks to the slanted bottom portion and the sediment discharge port of the sediment, so that the treatment capacity gradually decreases and the apparatus cannot be used. It has been used exclusively for purification treatment of low-concentration sewage. The present invention has been made in view of the above problems, and an object of the present invention is to provide an improved one-tank type coagulation and sedimentation apparatus which does not cause any problem even when used for purification treatment of high-concentration sewage.

【0009】[0009]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明に係る凝集沈でん装置は、一側から他側に
かけて傾斜底が形成された直立円筒形の槽体と、前記傾
斜底の高位部から低位部にかけての上面に前記槽体の上
方から配設され、前記傾斜底の低位部方向に複数の噴気
孔が穿設された二股分岐部を有する給気管と、からな
り、前記槽体の槽壁の最深部側の中間部に各種廃液を含
む汚水の処理された浄水の排水口が、同最深部側の最深
部に同汚水の処理された凝集沈でん物の排泥口がそれぞ
れ設けられた凝集沈でん装置において、前記傾斜底の低
位部に立設された前記給気管の二股分岐部の揺動防止装
置と、前記傾斜底の下面部に取り付けられた振動発生装
置を備えたものである。
In order to achieve the above object, an apparatus for coagulating and settling according to the present invention comprises: an upright cylindrical tank body having an inclined bottom formed from one side to the other side; An air supply pipe, which is disposed from above the tank body on the upper surface from the higher portion to the lower portion, and has a forked branch portion in which a plurality of blast holes are drilled in the lower portion direction of the inclined bottom, In the middle part of the tank wall at the deepest side of the tank body, there is a drain port for treated purified water containing wastewater, and at the deepest part on the deepest side, there is a drain port for treated flocculated sediment. The coagulation and sedimentation devices provided respectively include a swing prevention device for a bifurcated branch portion of the air supply pipe erected on a lower portion of the inclined bottom, and a vibration generator attached to a lower surface portion of the inclined bottom. Things.

【0010】そして、前記揺動防止装置を、前記傾斜底
の最低位部付近から前記槽体の最深部側の中間部にかけ
て立設され、その下端部分が前記給気管の二股分岐部の
二股部分に介入するように設計された揺動防止板とする
ことが良い。そして、前記振動発生装置を超音波発生装
置とすることが好適である。また、前記振動発生装置を
バイブレータ装置としても良い。
The swing prevention device is erected from the vicinity of the lowest part of the inclined bottom to the middle part on the deepest part side of the tank body, and the lower end part thereof is a forked part of a forked branch part of the air supply pipe. It is preferable to use an anti-swing plate designed to intervene in the vehicle. Preferably, the vibration generator is an ultrasonic generator. Further, the vibration generator may be a vibrator.

【0011】[0011]

【作用】 傾斜底の低位部に給気管の二股分岐部の揺動防止装置
が立設されているので、激しい噴気作用に伴う二股分岐
部の揺動が防止されるとともに、汚水を伴う空気の揺動
を少くしてその上昇流を整流し、汚水の還流速度を著し
く加速する。このようにして従来の攪拌設定時間内にお
ける汚水の還流量が増加し、高濃度汚水の浄化処理に対
応できる。 傾斜底の下面部に振動発生装置が取り付けられている
ので、高濃度汚水の浄化処理における還流攪拌後の滞留
時間に、この装置を作動させることにより凝集沈でん物
の傾斜底への粘着が阻止される。 この装置は一基で低濃度汚水、高濃度汚水の浄化処理
をすることができる。
[Function] Since the swing prevention device for the bifurcated branch of the air supply pipe is provided upright at the lower part of the inclined bottom, the swing of the bifurcated bifurcation due to the violent fumarolic action is prevented, and the air with sewage is removed. By reducing the fluctuation, the upward flow is rectified and the return speed of the wastewater is remarkably accelerated. In this way, the amount of sewage recirculation within the conventional stirring set time is increased, and it is possible to cope with the purification treatment of high-concentration sewage. Since the vibration generating device is attached to the lower surface of the inclined bottom, by operating this device during the residence time after the reflux stirring in the purification treatment of high-concentration sewage, sticking of the coagulated sediment to the inclined bottom is prevented. You. This device can purify low concentration sewage and high concentration sewage by itself.

【0012】[0012]

【実施例】以下、本発明の実施例を図を参照しながら説
明する。図1は、凝集沈でん装置の構成を示す側面図、
図2は図1の平面図である。この両図において、1は直
立円筒形の槽体、1aは槽体1の一側から他側にかけて
配設された傾斜底、2は槽体1の上方から傾斜底1aの
上面に沿い、その最低部付近まで延引配設され、上記最
低部方向に複数の噴気孔2aの穿設された二股分岐部2
bを設けた給気管、3は槽体1の槽壁1bの最深部側の
中間部に設けられた処理済の浄水の排水口、3aは槽体
1の槽壁1bの最深部側の最深部に設けられた凝集沈で
ん物の排泥口であり、4は傾斜底1aの最低位部付近か
ら槽体1の最深部側の中間部にかけて立設され、その下
端部分が給気管2の二股分岐部2bの二股部分2cに介
入するように設計された上記二股分岐部2bの揺動防止
板、5は傾斜底1aの下面部1cに取り付けられた振動
発生装置としての超音波発生装置である。なお、2dは
ブロア送風装置、3bは排水口3からの残留浮遊物の排
出阻止壁、6は汚水を示す。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a side view showing a configuration of a coagulation sedimentation apparatus,
FIG. 2 is a plan view of FIG. In these figures, 1 is an upright cylindrical tank body, 1a is an inclined bottom provided from one side of the tank body 1 to the other side, and 2 is an upper surface of the tank body 1 along the upper surface of the inclined bottom 1a. A forked bifurcation 2 extending to the vicinity of the lowest portion and having a plurality of fumaroles 2a in the direction of the lowest portion.
b, an air supply pipe provided with b, 3 is a drain port of treated purified water provided at an intermediate portion on the deepest part side of the tank wall 1b of the tank body 1, 3a is a deepest part on the deepest part side of the tank wall 1b of the tank body 1. Numeral 4 is a mud port for coagulated sediment provided in the section, and 4 is erected from the vicinity of the lowest part of the inclined bottom 1a to the middle part on the deepest side of the tank body 1, and the lower end part thereof is a fork of the air supply pipe 2. The anti-swing plate 5 of the bifurcated branch 2b designed to intervene in the bifurcated portion 2c of the bifurcation 2b is an ultrasonic generator as a vibration generator attached to the lower surface 1c of the inclined bottom 1a. . In addition, 2d is a blower blower, 3b is a wall for preventing discharge of residual suspended matter from the drain port 3, and 6 is sewage.

【0013】このように凝集沈でん装置が構成され、汚
水6が槽体1に送水されるとともに必要とする薬液が加
えられ、ブロア送風装置からの空気が給気管2を介して
上記二股分岐部2bの噴気孔2aから噴出されることに
より、従来の技術の項で述べたように汚水6と薬液の混
合液が還流を繰り返し、攪拌および処理反応が効果的に
行われる(設定時間約30分)。そして攪拌を停止し滞
留(設定時間約60分)させることにより、槽体1の最
深部に処理反応された凝集物の沈でん堆積が完了する。
そして処理された浄水が排水口3から排水され、次いで
凝集沈でん物が排泥口3aから排泥される。
The coagulation and sedimentation apparatus is constructed as described above, and the sewage 6 is supplied to the tank body 1 and the required chemical liquid is added thereto, and the air from the blower blower is supplied through the air supply pipe 2 to the bifurcated branch 2b. Is ejected from the fumarole 2a, the mixed liquid of the sewage 6 and the chemical solution repeats reflux as described in the section of the prior art, and the stirring and the treatment reaction are effectively performed (set time: about 30 minutes). . Then, the agitation is stopped and settled (set time: about 60 minutes), thereby completing the sedimentation and accumulation of the aggregate that has been subjected to the processing reaction at the deepest part of the tank body 1.
Then, the treated purified water is drained from the drain port 3, and then the coagulated sediment is discharged from the drain port 3a.

【0014】しかし、本実施例においては、給気管2の
二股分岐部2bの二股部分2cに介入される揺動防止板
4が、傾斜底1aの最低位部付近から槽体1の最深部側
の中間部にかけて立設されているので、作用の項で述べ
たように二股分岐部2bが揺動防止板4により保持さ
れ、激しい噴気作用に伴う二股分岐部2bの揺動を防止
するとともに、汚水を伴う空気の揺動を少くしてその上
昇流を整流し、汚水の還流速度が著しく加速され、還流
量が増加する。このため上記設定時間内で反応処理を困
難ならしめた高濃度汚水の浄化処理が達成するものであ
る。そして、傾斜底1aの下面部に取り付けられた超音
波発生装置5を使用することにより、高濃度凝集物の傾
斜底1aへの粘着が阻止されるので粘着による支障を生
じない。なお、この装置に代えてバイブレータ装置を使
用しても差支えない。この実施例の凝集沈でん装置は、
一基で低濃度汚水、高濃度汚水に対応できるものであ
り、経済的である。
However, in the present embodiment, the swing prevention plate 4 interposed in the forked portion 2c of the forked branch portion 2b of the air supply pipe 2 is arranged such that the rocking prevention plate 4 is located from the vicinity of the lowest portion of the inclined bottom 1a to the deepest portion of the tank body 1. As described in the section of the operation, the forked bifurcation 2b is held by the swing prevention plate 4 to prevent the forked bifurcation 2b from being violently fumed. The swing of the air accompanying the sewage is reduced to rectify the upward flow, so that the return speed of the sewage is remarkably accelerated and the amount of the return increases. For this reason, the purification treatment of the high-concentration sewage which makes the reaction treatment difficult within the set time is achieved. By using the ultrasonic generator 5 attached to the lower surface of the inclined bottom 1a, the adhesion of the high-concentration aggregates to the inclined bottom 1a is prevented, so that no trouble is caused by the adhesion. Note that a vibrator device may be used instead of this device. The coagulating sedimentation apparatus of this embodiment is:
It is economical because it can handle low-concentration sewage and high-concentration sewage by itself.

【0015】[0015]

【発明の効果】本発明は、上述のように構成されたこと
により、以下のような効果を奏する。 給気管の二股分岐部の二股部分が揺動防止板により、
傾斜底上の所定位置に保持されているので、激しい噴気
作用に伴う二股分岐部の揺動が防止されるとともに、汚
水を伴う空気の揺動を少くして上昇流を整流し、還流速
度が著しく加速され設定時間内の還流量が増加し、設定
時間内で浄化処理し得なかった高濃度汚水の浄化処理に
対応することができる。 傾斜底の下面部に振動発生装置が取り付けられている
ので、高濃度汚水の浄化処理に際し駆動することによ
り、凝集沈でん物の傾斜底への粘着による支障が無い。 一基の装置で、低濃度汚水および高濃度汚水の併用処
理ができるので、経済的である。 構成が簡単で製作が容易で、廉価に提供できる。
The present invention has the following effects due to the above-mentioned structure. The bifurcated part of the bifurcated branch of the air supply pipe is made by the swing prevention plate,
Since it is held at a predetermined position on the inclined bottom, the swing of the forked branch due to the violent fumarolic action is prevented, the swing of the air accompanying the sewage is reduced, the upward flow is rectified, and the reflux speed is reduced. It is remarkably accelerated, the amount of recirculation within the set time increases, and it is possible to cope with the purification process of high-concentration sewage that could not be purified within the set time. Since the vibration generating device is attached to the lower surface of the inclined bottom, it is driven during the purification treatment of the high-concentration sewage, so that there is no trouble due to the adhesion of the coagulated sediment to the inclined bottom. It is economical because low-concentration sewage and high-concentration sewage can be used together with a single device. It has a simple configuration, is easy to manufacture, and can be provided at low cost.

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

【図1】本発明の凝集沈でん装置の構成を示す側面図で
ある。
FIG. 1 is a side view showing a configuration of a coagulation sedimentation apparatus of the present invention.

【図2】図1の平面図である。FIG. 2 is a plan view of FIG.

【図3】従来の凝集沈でん装置の構成を示す側面図であ
る。
FIG. 3 is a side view showing a configuration of a conventional coagulation and sedimentation apparatus.

【図4】図3の平面図である。FIG. 4 is a plan view of FIG. 3;

【符号の説明】[Explanation of symbols]

1 槽体 1a 傾斜底 1b 槽壁 1c 下面部 2 給気管 2a 噴気孔 2b 二股分岐部 2c 二股部分 3 排水口 3a 排泥口 4 揺動防止装置 5 振動発生装置 6 汚水 DESCRIPTION OF SYMBOLS 1 Tank body 1a Slant bottom 1b Tank wall 1c Lower surface part 2 Air supply pipe 2a Spray hole 2b Bifurcated branch part 2c Bifurcated part 3 Drain outlet 3a Drainage outlet 4 Swing prevention device 5 Vibration generator 6 Sewage

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 一側から他側にかけて傾斜底1aが形成
された直立円筒形の槽体1と、前記傾斜底1aの高位部
から低位部にかけての上面に前記槽体1の上方から配設
され、前記傾斜底1aの低位部方向に複数の噴気孔2a
が穿設された二股分岐部2bを有する給気管2と、から
なり、前記槽体1の槽壁1bの最深部側の中間部に各種
廃液を含む汚水6から処理された浄水の排水口3が、同
最深部側の最深部に同汚水から処理された凝集沈でん物
の排泥口3aがそれぞれ設けられた凝集沈でん装置にお
いて、 前記傾斜底1aの低位部に立設された前記給気管2の二
股分岐部2bの揺動防止装置4と、前記傾斜底1aの下
面部1cに取り付けられた振動発生装置5を備えた凝集
沈でん装置。
1. An upright cylindrical tank body 1 having an inclined bottom 1a formed from one side to the other side, and an upper surface of the inclined bottom 1a from a higher portion to a lower portion thereof, which is disposed from above the tank body 1. And a plurality of blast holes 2a in the lower part direction of the inclined bottom 1a.
And a supply pipe 2 having a bifurcated branch portion 2b with a hole formed therein. A drain port 3 for purified water treated from sewage 6 containing various waste liquids in an intermediate portion on the deepest side of the tank wall 1b of the tank body 1 However, in the coagulation sedimentation apparatus provided with a discharge port 3a for coagulation sediment treated from the sewage in the deepest part on the deepest part side, the air supply pipe 2 erected at a lower part of the inclined bottom 1a A coagulation sedimentation device comprising a swing prevention device 4 for the forked branch portion 2b and a vibration generator 5 attached to the lower surface portion 1c of the inclined bottom 1a.
【請求項2】 前記揺動防止装置4を、前記傾斜底1a
の最低位部付近から前記槽体1の最深部側の中間部にか
けて立設され、その下端部分が前記給気管2の二股分岐
部2bの二股部分2cに介入するように設計された揺動
防止板とする請求項1記載の凝集沈でん装置。
2. The swing preventing device 4 is mounted on the inclined bottom 1a.
Is formed so as to extend from the vicinity of the lowest part to the middle part on the deepest part side of the tank body 1 and its lower end part is designed to intervene in the forked part 2c of the forked branch part 2b of the air supply pipe 2. The coagulation sedimentation apparatus according to claim 1, which is a plate.
【請求項3】 前記振動発生装置5を超音波発生装置と
する請求項1記載の凝集沈でん装置。
3. The coagulation sedimentation apparatus according to claim 1, wherein said vibration generator 5 is an ultrasonic generator.
【請求項4】 前記振動発生装置5をバイブレータ装置
とする請求項1記載の凝集沈でん装置。
4. The coagulation sedimentation apparatus according to claim 1, wherein the vibration generator 5 is a vibrator.
JP4925295A 1995-02-15 1995-02-15 Coagulation sedimentation equipment Expired - Fee Related JP2926070B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4925295A JP2926070B2 (en) 1995-02-15 1995-02-15 Coagulation sedimentation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4925295A JP2926070B2 (en) 1995-02-15 1995-02-15 Coagulation sedimentation equipment

Publications (2)

Publication Number Publication Date
JPH08215504A JPH08215504A (en) 1996-08-27
JP2926070B2 true JP2926070B2 (en) 1999-07-28

Family

ID=12825659

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4925295A Expired - Fee Related JP2926070B2 (en) 1995-02-15 1995-02-15 Coagulation sedimentation equipment

Country Status (1)

Country Link
JP (1) JP2926070B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19928600C1 (en) * 1999-06-22 2001-05-03 Thermoselect Ag Vaduz Separation device and its use
JO3758B1 (en) * 2008-12-24 2021-01-31 Crystal Lagoons Tech Inc Suctioning device
JP5863166B2 (en) * 2011-10-05 2016-02-16 宇都宮工業株式会社 Sediment transfer equipment
CN111773872B (en) * 2020-08-17 2022-02-22 朱文霞 Ultrasonic filtering device for severe dust pollution

Also Published As

Publication number Publication date
JPH08215504A (en) 1996-08-27

Similar Documents

Publication Publication Date Title
KR100723337B1 (en) An oxidizing Pressurized Uprising Apparatus
CA2307188A1 (en) Process and apparatus for electrocoagulative treatment of industrial waste water
US6620317B2 (en) Waste water treatment system
JP2926070B2 (en) Coagulation sedimentation equipment
JP2005211822A (en) Waste liquid treatment system
KR101026768B1 (en) Cavitation uprising apparatus and wastewater treatment apparatus using the same
JPH1128312A (en) Flocculator
JPS6233564A (en) Method and apparatus for treating contaminated grit
JP2002186962A (en) Pressurized whirl type floatation and separation wastewater treatment equipment
KR100209938B1 (en) Method for treating waste water by sludge flotation
JP2001038105A (en) Reaction settling tank for waste water treatment
JPH04952Y2 (en)
JP3200810B2 (en) Float type supernatant water collecting device
KR200366205Y1 (en) Coagulating sedimentation processing apparatus
JPH0549812A (en) Waste water treating device
JPS631408A (en) Washing appratus for slanted part in settling apparatus
JPS6337118Y2 (en)
JP2582038Y2 (en) Coagulation settling equipment
CN220265436U (en) Pork pig plant waste liquid treatment device
JP2558150B2 (en) Wastewater treatment equipment
KR200288463Y1 (en) agitator equipment for waste water
KR20010055004A (en) Apparatus for removing sludge by floating of sludge in a settling tank
JPS6246472Y2 (en)
KR100350688B1 (en) Cement waste water treatment system
KR200214758Y1 (en) Waste water treatment by induced air

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees