JPH0378121B2 - - Google Patents
Info
- Publication number
- JPH0378121B2 JPH0378121B2 JP5277683A JP5277683A JPH0378121B2 JP H0378121 B2 JPH0378121 B2 JP H0378121B2 JP 5277683 A JP5277683 A JP 5277683A JP 5277683 A JP5277683 A JP 5277683A JP H0378121 B2 JPH0378121 B2 JP H0378121B2
- Authority
- JP
- Japan
- Prior art keywords
- settling tank
- partition
- partition plates
- partition plate
- sedimentation
- 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
Links
- 238000005192 partition Methods 0.000 claims description 31
- 238000004062 sedimentation Methods 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 239000002245 particle Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 5
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 239000013049 sediment Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000005273 aeration Methods 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
Description
【発明の詳細な説明】
本発明は各種汚濁水を処理するに適した沈澱槽
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たり流
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。しか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 or slow down the flow rate to 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、該
区画板の下部と前記遮蔽板の上部が互にオーバー
ラツプするように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 A sedimentation tank characterized in that a shielding plate having a gap is provided at the bottom of the tank between the partition plates, and a lower part of the partition plate and an upper part of the shielding plate overlap with each other.
次に本発明を図面を参照しながら説明する。 Next, the present invention will be explained with reference to the drawings.
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。この遮蔽
板4は図面からも明らかなように、区画板2の下
端部と該遮蔽板4の上端部とがhで示すようにオ
ーバーラツプしていることが必要である。このオ
ーバーラツプさせる程度は処理する汚濁水の性質
等により適宜選択すればよい。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。 Partition plates 2 are provided at intervals on the upper part of the settling tank 1, and a plurality of partition plates 3 are further provided between each partition plate 2.
will be established. 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. As is clear from the drawings, it is necessary that the lower end of the partition plate 2 and the upper end of the shield plate 4 overlap as shown by h. The degree of overlap may be appropriately selected depending on the nature of the polluted water to be treated. 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
可動するスクレーバー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スカ
ムポケツト10が設けられている。 Further, the settling tank 1 of the present invention is provided with a scraper 6 that can be moved from side to side 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 settling tank 1 of the present invention is provided with scum 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底部に設けられた空隙部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
汚濁粒子の分離が促進される。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、
区画板2の下端部と遮蔽板4の上端部とがオーバ
ーラツプしていることからこの間を通過するのに
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 lower end of the partition plate 2 and the upper end of the shielding plate 4 overlap, the residence time in the sedimentation tank is increased due to the detour flowing between them, thereby increasing the separation efficiency of the pollutant 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
たスクレーバー6の左右運動によつて沈澱層の両
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層外に除去さ
れる。一方沈澱層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から沈澱層外に放流される。 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 sediment layer 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 sediment layer. On the other hand, the treated water from which pollutant particles have been removed after passing through the sedimentation layer is sucked up by a pump and sent to the discharge pipe 1.
1 is discharged to the outside of the sediment layer.
前記したように本発明の沈澱層によれば効率よ
く汚濁水を処理することができる。 As described above, the sedimentation layer of the present invention allows efficient treatment of polluted water.
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)
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、該区画板の下部と
前記遮蔽板の上部が互にオーバーラツプするよう
に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 settling tank characterized in that a shielding plate having a gap is provided at the bottom of the settling tank between the partition plates, and a lower part of the partition plate and an upper part of the shielding plate overlap each other. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5277683A JPS59179115A (en) | 1983-03-30 | 1983-03-30 | Settling tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5277683A JPS59179115A (en) | 1983-03-30 | 1983-03-30 | Settling tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59179115A JPS59179115A (en) | 1984-10-11 |
| JPH0378121B2 true JPH0378121B2 (en) | 1991-12-12 |
Family
ID=12924257
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5277683A Granted JPS59179115A (en) | 1983-03-30 | 1983-03-30 | Settling tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59179115A (en) |
-
1983
- 1983-03-30 JP JP5277683A patent/JPS59179115A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59179115A (en) | 1984-10-11 |
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