JPH05192519A - Solid-liquid separation device - Google Patents
Solid-liquid separation deviceInfo
- Publication number
- JPH05192519A JPH05192519A JP4006992A JP699292A JPH05192519A JP H05192519 A JPH05192519 A JP H05192519A JP 4006992 A JP4006992 A JP 4006992A JP 699292 A JP699292 A JP 699292A JP H05192519 A JPH05192519 A JP H05192519A
- Authority
- JP
- Japan
- Prior art keywords
- filter medium
- tank
- sewage
- solid
- medium filling
- 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.)
- Granted
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 10
- 238000000926 separation method Methods 0.000 title abstract description 9
- 239000010865 sewage Substances 0.000 claims abstract description 32
- 230000005484 gravity Effects 0.000 claims abstract description 8
- 238000005192 partition Methods 0.000 claims abstract description 8
- 238000004140 cleaning Methods 0.000 claims description 10
- 238000011282 treatment Methods 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 238000011221 initial treatment Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
(57)【要約】
【目的】 下水中のSSを効率よく除去することがで
き、大規模の下水処理に適用でき、しかも既存の下水処
理場の設備の活用が容易な固液分離装置を提供するこ
と。
【構成】 固液分離装置の下水が水平方向に流れる横向
流槽1の流出側に、仕切壁4を隔てて好ましくは複数個
のろ材充填槽5を設ける。各ろ材充填槽5には比重が1
以下のプラスチック等よりなるろ材を充填し、横向流槽
1において沈降し易いSSを沈降させた下水を下向流ま
たは上向流で流し、細かいSSを捕捉させる。またこの
ろ材充填槽5aの下部に空気導入管7を配置し、ろ材洗浄
を行う。
(57) [Summary] [Purpose] Providing a solid-liquid separation device that can efficiently remove SS in sewage, can be applied to large-scale sewage treatment, and can easily utilize existing sewage treatment plant equipment. To do. [Structure] On the outflow side of a lateral flow tank 1 in which sewage of a solid-liquid separator flows horizontally, preferably a plurality of filter medium filling tanks 5 are provided with a partition wall 4 interposed therebetween. Each filter medium filling tank 5 has a specific gravity of 1
A filter medium made of plastic or the like below is filled, and the sewage in which the SS that is likely to settle in the lateral flow tank 1 is allowed to flow in a downward flow or an upward flow to capture fine SS. Further, the air introducing pipe 7 is arranged below the filter medium filling tank 5a to wash the filter medium.
Description
【0001】[0001]
【産業上の利用分野】本発明は下水の一次処理等に使用
される固液分離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 a solid-liquid separation device used for primary treatment of sewage.
【0002】[0002]
【従来の技術】従来、下水処理場における下水の一次処
理設備としては最初沈殿池が用いられている。この最初
沈殿池は長さが数10mに及ぶ縦長の沈殿池であり、下水
はこの内部をゆっくりと横向きに流れる間にSSを沈殿
させ、沈殿したSSは池の底部に設置されたかき寄せ機
により外部へ排出されるようになっている。2. Description of the Related Art Conventionally, a primary settling tank has been used as a primary treatment facility for sewage in a sewage treatment plant. This first settling basin is a vertically long settling basin with a length of several tens of meters, and the sewage settles SS while slowly flowing sideways in the inside, and the settled SS is set by a scraper installed at the bottom of the pond. It is designed to be discharged to the outside.
【0003】ところがこのような従来の最初沈殿池は、
広い設置スペースを要するにもかかわらずSSの分離を
重力によってのみ行わせているため、単位面積当りの処
理水量が35m3/m2/day 程度であり、またSS分除去率が
40%程度で分離効率が悪いという問題がある。そこで最
近では特開平1-7920号公報に示されるように、比重が1
以下のろ材が充填された処理槽の内部に下水を上向流で
流し、下水中のSSをろ材により除去させるようにした
一次処理設備が提案されている。However, such a conventional first settling tank is
Despite the large installation space, SS is separated only by gravity, so the amount of treated water per unit area is about 35 m 3 / m 2 / day, and the removal rate of SS is
There is a problem that the separation efficiency is poor at about 40%. Therefore, recently, as shown in Japanese Patent Laid-Open No. 1-7920, the specific gravity is 1
A primary treatment facility has been proposed in which sewage is allowed to flow upward in a treatment tank filled with the following filter medium to remove SS in the sewage by the filter medium.
【0004】この設備は従来の最初沈殿池と比較して、
SS分除去能力が優れている。しかしその反面、上向流
であるために本来は自然沈降するはずのSSまで巻き上
げてろ材に捕捉させることとなり、頻繁にろ材の洗浄が
必要となるので運転時間に対する洗浄のための運転停止
時間が長くなり、また洗浄のための動力も多大となる欠
点がある。更にまた、小規模でない下水処理への適用が
困難でしかも既存の下水処理場の最初沈殿池の活用がで
きないという欠点もある。This equipment, compared to the conventional first settling tank,
Excellent SS removal capability. On the other hand, however, since it is an upward flow, it will be wound up to SS, which should naturally settle, and be trapped in the filter medium, and it is necessary to wash the filter medium frequently, so the operation stop time for cleaning relative to the operating time It has the drawback of being long and consuming much power for cleaning. Furthermore, there is a drawback that it is difficult to apply to non-small-scale sewage treatment and the first settling tank of the existing sewage treatment plant cannot be used.
【0005】[0005]
【発明が解決しようとする課題】本発明は上記した従来
の問題点を解消して、下水中のSSを効率よく分離する
ことができ、中、大規模の下水処理に適用でき、しかも
既存の下水処理場の設備を活用できる固液分離装置を提
供するために完成されたものである。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned conventional problems and can efficiently separate SS in sewage, and can be applied to middle and large scale sewage treatment. It was completed to provide a solid-liquid separation device that can utilize the equipment of a sewage treatment plant.
【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
めになされた本発明は、下水が水平方向に流れる横向流
槽の流出側に、仕切壁を隔ててろ材充填槽を設け、その
内部に比重が1以下のろ材を充填するとともに、ろ材充
填部の下部にろ材洗浄用の空気導入管を配置したことを
特徴とするものである。SUMMARY OF THE INVENTION The present invention, which has been made to solve the above problems, provides a filter medium filling tank with a partition wall on the outflow side of a lateral flow tank in which sewage flows horizontally, and the inside thereof. Is filled with a filter medium having a specific gravity of 1 or less, and an air introducing pipe for cleaning the filter medium is arranged below the filter medium filling portion.
【0007】[0007]
【実施例】以下に本発明を図示の実施例によって更に詳
細に説明する。図1及び図2において、1は固液分離装
置の横向流槽であり、その底部には従来と同様のかき寄
せ機2が設置されている。3は横向流槽1への下水の流
入口である。このような横向流槽1の流出側には、仕切
壁4を隔てて複数のろ材充填槽5が設けられている。横
向流槽1の流出側に達した下水は、仕切壁4の上端をオ
ーバーフローまたはトラフれ集水され各ろ材充填槽5へ
流入することとなる。なお、横向流槽1の水面積:ろ材
充填槽5全体の水面積は、4:1〜2:1程度が好まし
い。The present invention will be described in more detail below with reference to the embodiments shown in the drawings. 1 and 2, reference numeral 1 denotes a lateral flow tank of a solid-liquid separation device, and a scraper 2 similar to the conventional one is installed at the bottom of the tank. Reference numeral 3 is an inlet for sewage to the lateral flow tank 1. A plurality of filter medium filling tanks 5 are provided on the outflow side of such a lateral flow tank 1 with a partition wall 4 interposed therebetween. The sewage that has reached the outflow side of the lateral flow tank 1 overflows or troughs the upper end of the partition wall 4 and is collected, and flows into each filter medium filling tank 5. The water area of the lateral flow tank 1 and the water area of the entire filter medium filling tank 5 are preferably about 4: 1 to 2: 1.
【0008】上記のろ材充填槽5には、比重が1以下の
ろ材が充填されている。このようなろ材としては、例え
ばプラスチック製のろ材を使用することができる。その
一例として、例えば直径40mm以下、長さ50mm以下の中空
円筒状のろ材を使用することができる。このような中空
円筒状のろ材は、直径20mm以下、長さ30mm以下とすると
更に好ましい。しかしろ材の形状は特に限定されるもの
ではなく、その間隙を下水が流れるときにSS分が捕捉
できるものであればよい。The filter medium filling tank 5 is filled with a filter medium having a specific gravity of 1 or less. As such a filter medium, for example, a plastic filter medium can be used. For example, a hollow cylindrical filter medium having a diameter of 40 mm or less and a length of 50 mm or less can be used. It is more preferable that such a hollow cylindrical filter medium has a diameter of 20 mm or less and a length of 30 mm or less. However, the shape of the filter medium is not particularly limited as long as the SS component can be captured when the sewage flows through the gap.
【0009】これらのろ材の流出を防止するために、ろ
材充填部5aの上面および下面には網6を設けておくこと
が好ましい。またろ材全体を網で覆うようにしておけ
ば、ろ材の交換等の作業が容易に行えるようになる。In order to prevent these filter media from flowing out, it is preferable to provide a mesh 6 on the upper and lower surfaces of the filter media filling section 5a. Further, if the entire filter medium is covered with a net, the work such as replacement of the filter medium can be easily performed.
【0010】このろ材充填部5aの下部には、ろ材洗浄用
の空気導入管7が設置されている。ろ材洗浄は洗浄対象
となるろ材充填槽5への下水の流入を停止した状態で、
空気導入管7から空気を噴出する方法で行われる。これ
によりろ材に付着したSSが水中に分離されるので、下
部より排水すればよい。なお洗浄中のろ材充填槽5は使
用できないため、実施例のように複数のろ材充填槽5を
設けておき、1槽ずつ順次洗浄するようにすれば、全体
の運転を停止する必要がない。An air introducing pipe 7 for cleaning the filter medium is installed below the filter medium filling section 5a. The filter medium cleaning is performed while stopping the inflow of sewage into the filter medium filling tank 5 to be cleaned,
It is performed by a method of ejecting air from the air introduction pipe 7. As a result, the SS adhering to the filter medium is separated into water, so it is sufficient to drain it from the lower part. Since the filter medium filling tank 5 cannot be used during cleaning, it is not necessary to stop the whole operation by providing a plurality of filter medium filling tanks 5 and sequentially cleaning one tank at a time as in the embodiment.
【0011】以上に説明した第1の実施例では、ろ材充
填槽5は下向流ろ過槽とされていたが、図3に示す第2
の実施例ではろ材充填槽5は上向流ろ過槽とされてい
る。この場合には、横向流槽1の流出側の仕切壁4を越
えた下水は集水渠4aに集水されてろ材充填槽5に下面か
ら供給されることとなる。その他の構成は第1の実施例
と同様であるので、説明を省略する。In the first embodiment described above, the filter medium filling tank 5 is a downward flow filtration tank, but the second embodiment shown in FIG.
In this embodiment, the filter medium filling tank 5 is an upflow filtration tank. In this case, the sewage that has crossed the partition wall 4 on the outflow side of the lateral flow tank 1 is collected in the water collection conduit 4a and supplied to the filter medium filling tank 5 from the lower surface. The other structure is similar to that of the first embodiment, and the description thereof is omitted.
【0012】[0012]
【作用】次に本発明の固液分離装置の作動を説明する。
まず下水を流入口3から固液分離装置の横向流槽1に流
入させ、横向流槽1を低速で水平方向に流れる間にSS
分を自然沈降させる。そして沈降したSS分は従来と同
様にかき寄せ機2により取り出される。Next, the operation of the solid-liquid separation device of the present invention will be described.
First, sewage is made to flow into the lateral flow tank 1 of the solid-liquid separation device from the inflow port 3, and SS is fed while flowing horizontally in the lateral flow tank 1 at a low speed.
Allow the minutes to settle. Then, the settled SS component is taken out by the scraper 2 as in the conventional case.
【0013】このようにして自然沈降により粒径が比較
的大きいSS分が除去された下水は、次に仕切壁4の上
端をオーバーフローし、またはトラフや集水渠4aに集め
られて各ろ材充填槽5へ流入する。前述したように、各
ろ材充填槽5には比重が1以下のろ材が充填されている
ので、下水は浮遊しているこれらのろ材の間隙を下向流
または上向流として流れ、その間に横向流槽1では沈降
しなかった粒径が細かいSS分がろ材に捕捉される。こ
のようにろ材充填槽5のろ材により細かいSS分を捕捉
された下水は流出口8から一次処理水として排出され、
次工程へ送られる。The sewage from which SS having a relatively large particle size has been removed by natural sedimentation then overflows at the upper end of the partition wall 4 or is collected in the trough or the water collection conduit 4a to be filled in each filter medium filling tank. Inflow to 5. As described above, since each filter medium filling tank 5 is filled with the filter medium having a specific gravity of 1 or less, the sewage flows as a downward flow or an upward flow through the floating gaps of these filter media, and in the lateral direction between them. In the flow tank 1, SS components having a small particle size that did not settle are captured by the filter medium. Thus, the sewage in which the fine SS component is captured by the filter medium in the filter medium filling tank 5 is discharged from the outlet 8 as the primary treated water,
It is sent to the next process.
【0014】このようにして下水の一次処理を継続し、
ろ材充填槽5のろ材に付着したSS分の量が増加してき
たとき、ろ材充填槽5への下水の流入を1槽ずつ止め、
空気導入管7から空気を噴出してろ材の洗浄を行う。噴
出された空気は気泡となって浮遊しているろ材の間を通
過するが、ろ材は比重が1以下であるために容易に流動
して、その表面に付着しているSS分が除去される。な
お通常の運転時においては、下水中のSS分のうちの沈
降し易い部分は横向流槽1で既に除かれているので、ろ
材充填槽5のろ材に捕捉されるSS分は処理水量に比較
してわずかである。このためにろ材充填槽5のろ材の洗
浄インターバルは十分に長く取ることができ、頻繁に洗
浄を行う必要はない。In this way, the primary treatment of sewage is continued,
When the amount of SS adhering to the filter medium in the filter medium filling tank 5 increases, stop the inflow of sewage into the filter medium filling tank 5 one by one,
Air is ejected from the air introduction pipe 7 to wash the filter medium. The jetted air passes between the floating filter media in the form of bubbles, but the filter media has a specific gravity of 1 or less, so it easily flows and the SS component adhering to the surface is removed. .. During normal operation, the part of SS in sewage that tends to settle has already been removed in the lateral flow tank 1, so the amount of SS captured by the filter material in the filter material filling tank 5 is compared to the amount of treated water. And then there are few. For this reason, the cleaning interval of the filter medium in the filter medium filling tank 5 can be made sufficiently long, and it is not necessary to perform frequent cleaning.
【0015】[0015]
【発明の効果】以上に説明した本発明の固液分離装置
は、下記の通りの優れた効果を有するものである。 下水中のSS分を効率良く除去することができ、従
来の最初沈澱池が単位面積当りの処理水量35m3/m2/day
程度でSS分除去率が40%程度であったのに対して、本
発明の装置では同等の処理水量で90%のSS分除去率を
達成することができる。 大規模な下水処理にも適用することができる。 ろ材充填槽を付加することにより、既設の最初沈澱
池に容易に組み込むことができる。 沈降し易いSSは横向流槽で除かれ、沈降しにくい
SSのみがろ材充填槽で捕捉されるので、ろ材の洗浄を
頻繁に行う必要がなく、洗浄のための動力が少なくて済
み、また洗浄のための運転休止時間を最小限とすること
ができる。The solid-liquid separation device of the present invention described above has the following excellent effects. The SS component in the sewage can be removed efficiently, and the conventional first settling tank has a treated water volume of 35 m 3 / m 2 / day per unit area.
While the SS content removal rate was about 40%, the apparatus of the present invention can achieve an SS content removal rate of 90% with the same amount of treated water. It can also be applied to large-scale sewage treatment. By adding a filter medium filling tank, it can be easily incorporated into an existing first settling tank. SS that easily settle is removed in the lateral flow tank, and only SS that does not easily settle is captured in the filter medium filling tank, so there is no need to frequently wash the filter medium, less power is required for washing, and washing is also possible. Downtime can be minimized.
【図1】本発明の第1の実施例を説明する断面図であ
る。FIG. 1 is a cross-sectional view illustrating a first embodiment of the present invention.
【図2】本発明の実施例を説明する平面図である。FIG. 2 is a plan view illustrating an embodiment of the present invention.
【図3】本発明の第2の実施例を説明する断面図であ
る。FIG. 3 is a cross-sectional view illustrating a second embodiment of the present invention.
1 横向流槽 4 仕切壁 5 ろ材充填槽 7 空気導入管 1 Lateral flow tank 4 Partition wall 5 Filter medium filling tank 7 Air introduction pipe
Claims (1)
側に、仕切壁を隔ててろ材充填槽を設け、その内部に比
重が1以下のろ材を充填するとともに、ろ材充填部の下
部にろ材洗浄用の空気導入管を配置したことを特徴とす
る固液分離装置。1. A filter medium filling tank is provided on the outflow side of a lateral flow tank in which sewage flows horizontally, with a partition wall separating the medium, and a filter medium having a specific gravity of 1 or less is filled in the inside of the tank, and a filter medium filling section is provided below A solid-liquid separator characterized in that an air introduction pipe for cleaning the filter medium is arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4006992A JPH0817899B2 (en) | 1992-01-18 | 1992-01-18 | Solid-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4006992A JPH0817899B2 (en) | 1992-01-18 | 1992-01-18 | Solid-liquid separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05192519A true JPH05192519A (en) | 1993-08-03 |
| JPH0817899B2 JPH0817899B2 (en) | 1996-02-28 |
Family
ID=11653636
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4006992A Expired - Fee Related JPH0817899B2 (en) | 1992-01-18 | 1992-01-18 | Solid-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0817899B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001300592A (en) * | 2000-04-26 | 2001-10-30 | Chisso Corp | Night soil treatment system |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02164096A (en) * | 1988-12-19 | 1990-06-25 | Matsushita Electric Ind Co Ltd | Multilayer electronic circuit board and its manufacture |
| JPH0444296A (en) * | 1990-06-07 | 1992-02-14 | Matsushita Electric Ind Co Ltd | Multi-layer substrate incorporating semiconductor chips |
-
1992
- 1992-01-18 JP JP4006992A patent/JPH0817899B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02164096A (en) * | 1988-12-19 | 1990-06-25 | Matsushita Electric Ind Co Ltd | Multilayer electronic circuit board and its manufacture |
| JPH0444296A (en) * | 1990-06-07 | 1992-02-14 | Matsushita Electric Ind Co Ltd | Multi-layer substrate incorporating semiconductor chips |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001300592A (en) * | 2000-04-26 | 2001-10-30 | Chisso Corp | Night soil treatment system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0817899B2 (en) | 1996-02-28 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19960809 |
|
| LAPS | Cancellation because of no payment of annual fees |