JPH0260362B2 - - Google Patents

Info

Publication number
JPH0260362B2
JPH0260362B2 JP6305783A JP6305783A JPH0260362B2 JP H0260362 B2 JPH0260362 B2 JP H0260362B2 JP 6305783 A JP6305783 A JP 6305783A JP 6305783 A JP6305783 A JP 6305783A JP H0260362 B2 JPH0260362 B2 JP H0260362B2
Authority
JP
Japan
Prior art keywords
sedimentation tank
settling tank
tank
partition plates
polluted 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.)
Expired
Application number
JP6305783A
Other languages
Japanese (ja)
Other versions
JPS59189914A (en
Inventor
Hitoshi Hatano
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.)
Nihon Solid Co Ltd
Original Assignee
Nihon Solid 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 Nihon Solid Co Ltd filed Critical Nihon Solid Co Ltd
Priority to JP6305783A priority Critical patent/JPS59189914A/en
Publication of JPS59189914A publication Critical patent/JPS59189914A/en
Publication of JPH0260362B2 publication Critical patent/JPH0260362B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は各種汚濁水を処理するい適した沈澱槽
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sedimentation tank suitable for treating various types of polluted water.

汚濁水中の懸濁粒子を分離する方法としては一
般に浮上法と沈澱法がある。これらの方法におい
ては懸濁粒子の沈降速度が最も重要なポイントと
なる。そして懸濁粒子の沈降は周辺水流が整流お
よび均一流に近くなる程分離効率が高くなる。懸
濁粒子は流速にうちかつた粒子が浮上または沈降
するが、それ以外の軽く、小さい粒子は分離され
ない。これらの浮遊する微細粒子を浮上または沈
降させるためには沈澱槽の流量を小さくしり流速
を遅くして沈澱槽内における滞留時間を長くする
必要がある。したしながらこれらの条件を満足さ
せるためにはおのずから沈澱槽の面積と容積を大
きくしなければならない。
Generally, methods for separating suspended particles in polluted water include a flotation method and a sedimentation method. In these methods, the sedimentation rate of suspended particles is the most important point. Sedimentation of suspended particles becomes more efficient as the surrounding water flow becomes more rectified and more uniform. Suspended particles that are carried away by the flow velocity float or settle, but other light and small particles are not separated. In order to float or settle these floating fine particles, it is necessary to reduce the flow rate of the sedimentation tank to slow the flow rate and increase the residence time in the sedimentation tank. However, in order to satisfy these conditions, it is necessary to increase the area and volume of the settling tank.

本発明者は沈澱槽の規模を可及的に小さくし、
通水流量に対して流速が速く、沈澱槽内の滞留時
間を短くして懸濁粒子の分離効率の高い沈澱槽に
ついて種々研究を重ねた結果本発明を完成するに
至つた。
The present inventor reduced the scale of the settling tank as much as possible,
The present invention was completed as a result of various research into a sedimentation tank that has a high flow rate relative to the water flow rate, shortens the residence time in the sedimentation tank, and has a high separation efficiency for suspended particles.

すなわち本発明は、沈澱槽上部に間隔を置いて
区画板を設け、この各区画板間にさらに複数の仕
切板を設け、前記区画板の下端を仕切板の下端よ
り下方に延長し、且つ沈澱槽の底部に各区画板間
に位置するように空隙を有する遮蔽板を設けたこ
とを特徴とする沈澱槽である。
That is, in the present invention, partition plates are provided at intervals above the sedimentation tank, a plurality of partition plates are further provided between the partition plates, the lower ends of the partition plates are extended downward from the lower ends of the partition plates, and the sedimentation tank is This is a sedimentation tank characterized in that a shielding plate having a gap is provided at the bottom of the tank and is located between each partition plate.

次に本発明を図面を参照しながら説明する。沈
澱槽1の上部に間隔を置いて区画板2を設け、こ
の各区画板2の間にさらに複数の仕切板3を設け
る。この区画板2および仕切板3の下端部はいず
れも沈澱槽の水位より下方に位置していることが
必要である。そして区画板2の下端は仕切板3の
下端より下方に延長して設けられている。また沈
澱槽の底部には前記各区画板2の間に位置するよ
うに遮蔽板4が設けられている。そしてこの遮蔽
板4は多孔状あるいはスリツト状の空隙部5を有
している。
Next, the present invention will be explained with reference to the drawings. Dividing plates 2 are provided at intervals above the settling tank 1, and a plurality of partition plates 3 are further provided between each of the dividing plates 2. It is necessary that the lower ends of the partition plate 2 and the partition plate 3 are both located below the water level of the settling tank. The lower end of the partition plate 2 is provided to extend downward from the lower end of the partition plate 3. Further, a shielding plate 4 is provided at the bottom of the settling tank so as to be located between each of the partition plates 2. This shielding plate 4 has a porous or slit-like cavity 5.

また本発明の沈澱槽1は前記区画板2と仕切板
3の間あるいは仕切板3と仕切板3の間に左右に
可動するスクレーパー6が設けられている。さら
に沈澱槽の汚濁水導入部7には凝集剤注入管8お
よび散気管9を設けると好適である。また本発明
の沈澱槽1は第2図に示すように両サイドにムカ
ムポケツト10が設けられている。
Further, the sedimentation tank 1 of the present invention is provided with a scraper 6 that is movable left and right between the partition plates 2 and 3 or between the partition plates 3 and 3. Furthermore, it is preferable to provide a flocculant injection pipe 8 and an aeration pipe 9 in the polluted water introduction section 7 of the settling tank. Further, the sedimentation tank 1 of the present invention is provided with mucum pockets 10 on both sides, as shown in FIG.

前記のように構成された沈澱槽によれば沈澱槽
1底部に設けらた空隙部5を有する遮蔽板4の該
空隙部5を汚濁水が通過する際噴出された状態を
呈することから、かかる現象により汚濁水中の汚
濁粒子の分離から促進される。また汚濁水導入部
7から流入した汚濁水は沈澱槽1を通過する際、
各区画板2の間に遮蔽板4が設けられていること
から、この間を通過するのに、汚濁水は迂流し沈
澱槽内における滞留時間が長くなり汚濁粒子の分
離効率が高められる。
According to the sedimentation tank configured as described above, when polluted water passes through the gap 5 of the shielding plate 4 provided at the bottom of the sedimentation tank 1, it appears to be blown out. The phenomenon facilitates the separation of pollutant particles in polluted water. In addition, when the polluted water flowing in from the polluted water introduction part 7 passes through the settling tank 1,
Since the shielding plates 4 are provided between the partition plates 2, the polluted water takes a detour to pass between the partition plates 2, and the residence time in the settling tank becomes longer, thereby increasing the separation efficiency of polluted particles.

次に本発明の沈澱槽1を用いた処理方法につき
説明する。
Next, a treatment method using the settling tank 1 of the present invention will be explained.

沈澱槽1の汚濁水導入部7に入つた汚濁水(図
示せず)はここで凝集剤注入管8から凝集剤が注
入され、また散気管9から空気が導入される。こ
のようにして処理された汚濁水は区画板2と遮蔽
板4の間隔部を通過し、あるいは遮蔽板4の空隙
部5を通過する際に汚濁水中の汚濁粒子が分離さ
れ浮上する。また沈澱槽1の水面部が区画板2お
よび仕切板3で区画されていることからこの部分
に静域層が形成され、汚濁粒子の分離効率が高め
られる。分離浮上した汚濁粒子(スカム)は区画
板2と仕切板3あるいは仕切板3の間に集められ
る。集められたスカムは沈澱槽1上部に設けられ
たスクレーパー6の右左運動によつて沈澱槽の両
サイドに設けられたスカムポケツト10に掻き集
められる。集められたスカムは沈澱槽外に除去さ
れる。一方沈澱槽を通過して汚濁粒子を除去され
た処理水はポンプによつて吸い上げられ放流管1
1から沈澱槽外に放流される。
The polluted water (not shown) that has entered the polluted water inlet 7 of the settling tank 1 is injected with a coagulant from a coagulant injection pipe 8, and air is introduced from an aeration pipe 9. When the thus treated polluted water passes through the space between the partition plate 2 and the shielding plate 4, or through the gap 5 of the shielding plate 4, the polluted particles in the polluted water are separated and floated to the surface. Further, since the water surface portion of the settling tank 1 is divided by the partition plates 2 and 3, a static zone layer is formed in this portion, and the efficiency of separating pollutant particles is increased. Separated and floated contaminant particles (scum) are collected between the partition plate 2 and the partition plate 3 or between the partition plate 3. The collected scum is scraped into scum pockets 10 provided on both sides of the sedimentation tank by the left and right movement of a scraper 6 provided at the top of the sedimentation tank 1. The collected scum is removed outside the settling tank. On the other hand, the treated water from which pollutant particles have been removed after passing through the settling tank is sucked up by a pump and sent to the discharge pipe 1.
1 is discharged outside the sedimentation tank.

前記したように本発明の沈澱槽によれば効率よ
く汚濁水を処理することができる。
As described above, according to the settling tank of the present invention, polluted water can be efficiently treated.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の沈澱槽の概略断面図であり、
第2図はそのたて概略断面図である。
FIG. 1 is a schematic cross-sectional view of the settling tank of the present invention,
FIG. 2 is a schematic vertical sectional view thereof.

Claims (1)

【特許請求の範囲】[Claims] 1 沈澱槽上部に間隔を置いて区画板を設け、こ
の各区画板間にさらに複数の仕切板を設け、前記
区画板の下端を仕切板の下端より下方に延長し、
且つ沈澱槽の底部に各区画板間に位置するように
空隙部を有する遮蔽板を設けたことを特徴とする
沈澱槽。
1. Partition plates are provided at intervals in the upper part of the sedimentation tank, and a plurality of partition plates are further provided between each partition plate, and the lower end of the partition plate is extended downward from the lower end of the partition plate,
A sedimentation tank characterized in that a shielding plate having a gap is provided at the bottom of the sedimentation tank and is located between each partition plate.
JP6305783A 1983-04-12 1983-04-12 Precipitation tank Granted JPS59189914A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6305783A JPS59189914A (en) 1983-04-12 1983-04-12 Precipitation tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6305783A JPS59189914A (en) 1983-04-12 1983-04-12 Precipitation tank

Publications (2)

Publication Number Publication Date
JPS59189914A JPS59189914A (en) 1984-10-27
JPH0260362B2 true JPH0260362B2 (en) 1990-12-17

Family

ID=13218325

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6305783A Granted JPS59189914A (en) 1983-04-12 1983-04-12 Precipitation tank

Country Status (1)

Country Link
JP (1) JPS59189914A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005288425A (en) * 2004-04-02 2005-10-20 Jikkan Engineering:Kk Solid-liquid separator provided with rectangular horizontal multistage plate-type scraper

Also Published As

Publication number Publication date
JPS59189914A (en) 1984-10-27

Similar Documents

Publication Publication Date Title
US4022696A (en) Apparatus for clarification of waste water operating on dissolved air flotation process
US3925205A (en) Method of separating solids suspended in a liquid
US3479281A (en) Method and apparatus for the separation of phases by gaseous flotation
MX156978A (en) APPARATUS AND METHOD FOR REMOVING SUSPENSION PARTICLES
US2565343A (en) Liquid separation
CN1179113A (en) Method and apparatus for separatin non-soluble particles from liquid
US2509933A (en) Clarification of liquids
RU1836301C (en) Installation for waste-water-cleaning
EP0074342B1 (en) Filtering apparatus
JPH0663321A (en) Inclined plate type precipitation tank
CA1117439A (en) Stripping equipment for removal of contaminations floating in liquids, especially having lower specific weight than that of the liquid, expediently for purification of oil-containing sewages
JPH0378121B2 (en)
SU1212962A1 (en) Floating machine
SU1237637A1 (en) Device for purifying sewage
JPH0450842B2 (en)
GB1511458A (en) Apparatus and method for separating foreign solid particles from a liquid
JPH0734903U (en) Water purification promotion device
US6149827A (en) Device for separating particles from a particle containing liquid and a method for cleaning such a device
JPH0838927A (en) Purifying device for sand having gas introduction part in lower range and purification method using this purifying device
US3305092A (en) Pressure-fluid actuated skimmer and method
JPH0128879Y2 (en)
EP0128234A1 (en) Sand filtration apparatus
JPS59189914A (en) Precipitation tank
SU1446114A1 (en) Structure for purifying waste water from petroleum products and suspended matter
SU1139709A1 (en) Flotation classifier