JP2961442B2 - Continuous filtration device - Google Patents

Continuous filtration device

Info

Publication number
JP2961442B2
JP2961442B2 JP31618690A JP31618690A JP2961442B2 JP 2961442 B2 JP2961442 B2 JP 2961442B2 JP 31618690 A JP31618690 A JP 31618690A JP 31618690 A JP31618690 A JP 31618690A JP 2961442 B2 JP2961442 B2 JP 2961442B2
Authority
JP
Japan
Prior art keywords
filter
filter bed
backwash
water
tank
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
JP31618690A
Other languages
Japanese (ja)
Other versions
JPH04190806A (en
Inventor
雄一 谷
英司 中丸
徹 葛原
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.)
GOYO KENSETSU KK
Original Assignee
GOYO KENSETSU KK
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 GOYO KENSETSU KK filed Critical GOYO KENSETSU KK
Priority to JP31618690A priority Critical patent/JP2961442B2/en
Publication of JPH04190806A publication Critical patent/JPH04190806A/en
Application granted granted Critical
Publication of JP2961442B2 publication Critical patent/JP2961442B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は連続濾過装置、特に浚渫泥水を濃縮した際に
生ずる泥水を濾過処理するための連続濾過装置に関する
ものである。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous filtration device, and more particularly to a continuous filtration device for filtering muddy water generated when condensing dredged muddy water.

〔従来の技術〕[Conventional technology]

従来、浚渫泥水を濃縮した際に生ずる泥水を濾過処理
するためには種々の濾過装置が用いられている。
Conventionally, various filtration devices have been used for filtering muddy water generated when the dredged muddy water is concentrated.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

本発明の連続濾過装置は筒状の濾過槽本体と、この濾
過槽本体内に互に隣接して配置した固定濾床及び複数の
移動濾床を並設して成る移動濾床ユニットと、この隣接
する移動濾床ユニットの側から処理原水を供給し固定濾
床の側から処理原水を取り出す機構と、逆洗槽と、上記
移動濾床ユニットを構成する一つの移動濾床が上記逆洗
槽内に位置されたとき他の一つの移動濾床が上記固定濾
床に隣接されるように上記移動濾床ユニットを移動せし
める機構とより成ることを特徴とする。
The continuous filtration device of the present invention comprises a cylindrical filter tank body, a mobile filter bed unit having a fixed filter bed and a plurality of mobile filter beds arranged adjacent to each other in the filter tank body, A mechanism for supplying treated raw water from the side of the adjoining moving filter unit and removing treated water from the side of the fixed filter bed, a backwash tank, and one moving filter bed constituting the moving filter unit is the backwash tank And a mechanism for moving said mobile filter unit such that another mobile filter bed is positioned adjacent to said fixed filter bed when positioned therein.

〔作用〕[Action]

本発明の連続濾過装置においては固定濾床に隣接する
移動濾床が目詰まりしたときこの移動濾床が逆洗層内に
移動されて逆洗されると同時にこの移動濾床に並設され
ている目詰まりしていない他の移動濾床が上記固定濾床
に隣接される位置となり、処理原水の処理が続行され
る。
In the continuous filtration device of the present invention, when the mobile filter bed adjacent to the fixed filter bed is clogged, the mobile filter bed is moved into the backwash layer and backwashed, and at the same time, it is juxtaposed with the mobile filter bed. Another unfiltered mobile filter bed is located adjacent to the fixed filter bed, and the treatment of the treated raw water is continued.

〔実 施 例〕〔Example〕

以下図面によって本発明の実施例を説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.

本発明においては第1図〜第5図に示すように所定高
さの筒状体1内に発泡した樹脂製で比重が水より小さい
粒状濾材を流動可能な密度で充填し、この筒状体1の上
下開口を仕切網2で塞いで固定濾床3を形成し、又これ
より高さの低い同様の移動濾床4を2個横方向に互に連
結して移動濾床ユニット5を形成し、垂立した筒状の濾
過槽本体6内上部に上記固定濾床3を固定し、上記濾過
槽本体6の中間部に上記移動濾床ユニット5を横方向に
移動自在に指示する保持部分7を設け、上記濾過槽本体
6の下部に泥水入口8を形成し、上部に処理水排水口9
を形成すると共に、上記濾過槽本体6の下端部に沈降部
10を設ける。
In the present invention, as shown in FIGS. 1 to 5, a cylindrical filter medium made of foamed resin and having a specific gravity smaller than water is filled into a cylindrical body 1 having a predetermined height at a flowable density. A fixed filter bed 3 is formed by closing the upper and lower openings 1 with a partition net 2, and a mobile filter bed unit 5 is formed by connecting two similar mobile filter beds 4 having a lower height to each other in the horizontal direction. The fixed filter bed 3 is fixed to the upper part of the upright cylindrical filter tank main body 6, and a holding portion for instructing the movable filter bed unit 5 to be movable in the lateral direction at an intermediate portion of the filter tank main body 6. 7, a muddy water inlet 8 is formed at the lower part of the filter tank main body 6, and a treated water drainage port 9 is formed at the upper part.
And a sedimentation section at the lower end of the filtration tank body 6.
10 is provided.

又上記支持部分7の両側には夫々逆洗槽11を設け、こ
の逆洗槽11内には1個の移動濾床4を収納できる室12
と、この室12の下側に設けた孔あきパイプ13を介して空
気を供給する空気パイプ14と、上記孔あきパイプ13の下
部に設けた逆洗水排出口15と、上記室12の上側に設けた
逆洗水ノズル16を介して逆洗水を供給する逆洗水供給パ
イプ17とを設けると共に、上記移動濾床ユニット保持部
分7には上記移動濾床ユニット5の一方の移動濾床4を
上記固定濾床3に隣接する位置としたとき他方の移動濾
床4が逆洗槽11内の室12内に押し出されるようにする押
し出し機構18を設ける。
A backwash tank 11 is provided on both sides of the support portion 7, and a chamber 12 in which one mobile filter bed 4 can be stored is provided in the backwash tank 11.
An air pipe 14 for supplying air through a perforated pipe 13 provided on the lower side of the chamber 12, a backwash water outlet 15 provided on a lower part of the perforated pipe 13, and an upper side of the chamber 12 And a backwash water supply pipe 17 for supplying backwash water via a backwash water nozzle 16 provided in the moving bed unit. An extruding mechanism 18 is provided to allow the other mobile filter bed 4 to be extruded into the chamber 12 in the backwash tank 11 when 4 is positioned adjacent to the fixed filter bed 3.

本発明の連続濾過装置においては処理原水である泥水
は泥水入口8より供給され、沈降可能な物質は濾過槽本
体下部の沈降部10内に沈澱する。沈降しにくい物質は移
動濾床4、固定濾床3の順に上向きに通過し、濾材中に
捕捉される。
In the continuous filtration apparatus of the present invention, the muddy water which is the raw water for treatment is supplied from the muddy water inlet 8, and the sedimentable substance precipitates in the sedimentation section 10 at the lower part of the main body of the filtration tank. The substance that hardly settles passes upward in the order of the moving filter bed 4 and the fixed filter bed 3 and is captured in the filter medium.

濾過処理された処理水は濾過槽本体上部の処理水排出
口9より排出される。
The treated water subjected to the filtration treatment is discharged from the treated water discharge port 9 at the upper part of the main body of the filtration tank.

一定時間通水した後、これによって最も目詰まりが大
きくなる移動濾床ユニット5の一方の移動濾床4を押し
出し機構18によって横にスライドし逆洗槽11の室12内に
移動し、他方の目詰まりしていない移動濾床4を固定濾
床3の下部に移動する。この間通水は停止する事なく、
濾過機能は連続する。
After passing water for a certain period of time, one of the mobile filter beds 4 of the mobile filter unit 5 in which clogging becomes the largest due to this is slid sideways by the pushing mechanism 18 and moved into the chamber 12 of the backwash tank 11, and the other. The moving filter bed 4 that is not clogged is moved to the lower part of the fixed filter bed 3. During this time, the water flow does not stop,
The filtration function is continuous.

目詰まりを起こし逆洗槽11の室12内に移動された移動
濾床4には逆洗水供給パイプ17から逆洗水ノズル16を介
して逆洗水を供給し、空気パイプ14から孔あきパイプ13
を介して空気を供給することによって移動濾床4内の粒
状濾材を流動化させ、濾材中に捕捉された物質を剥離・
洗浄したうえで、次の濾床切り替えに備える。洗浄に使
用された水は逆洗槽下部の逆洗水排出口15より引き抜
く。
Backwash water is supplied from the backwash water supply pipe 17 through the backwash water nozzle 16 to the mobile filter bed 4 moved into the chamber 12 of the backwash tank 11 due to clogging, and a hole is formed from the air pipe 14. Pipe 13
By supplying air through the filter, the granular filter medium in the moving filter bed 4 is fluidized, and the substance trapped in the filter medium is peeled off.
After washing, prepare for the next filter bed change. The water used for washing is withdrawn from the backwash water outlet 15 at the bottom of the backwash tank.

また濾過槽本体下部の沈降部10内に沈澱した物質は適
宜沈澱排出口19より引き抜くようにする。
The substance precipitated in the sedimentation section 10 at the lower part of the filter tank body is appropriately pulled out from the sedimentation discharge port 19.

尚上記固定濾床3も長時間の使用により目詰まりする
ものであるから上記濾過槽本体6の下部及び上端には夫
々逆洗槽11におけると同様の孔あきパイプ13及び逆洗水
ノズル16を設けてこの濾過槽本体6内に位置する固定濾
床3及び移動濾床4をその位置で逆洗できるようにする
のが好ましい。
Since the fixed filter bed 3 is also clogged with use for a long time, a perforated pipe 13 and a backwash water nozzle 16 similar to those in the backwash tank 11 are provided at the lower and upper ends of the filter tank body 6, respectively. It is preferable that the fixed filter bed 3 and the movable filter bed 4 located in the filter tank main body 6 are provided so that the backwash can be performed at the positions.

〔発明の効果〕〔The invention's effect〕

本発明の連続濾過装置は上記のような構成であるから
下記のような効果を有する。
Since the continuous filtration device of the present invention has the above configuration, it has the following effects.

目詰まりを起こした移動濾床を通水中に濾過槽本体よ
り抜き出し、代わりに洗浄済の移動濾床を供給すること
で、連続して濾過を行う事が出来る。
By continuously removing the clogged mobile filter bed from the main body of the filtration tank through the water and supplying a washed mobile filter bed instead, continuous filtration can be performed.

逆洗の為の予備の濾過槽が不要であるということか
ら、処理設備をコンパクト化できる。
Since no extra filtration tank is required for backwashing, the processing equipment can be made compact.

濾過装置により高濃度の排水を処理する場合、目詰ま
りを起こすまでの時間が短く、逆洗をひんぱんに行わな
ければならなかったが、本発明の連続濾過装置では通水
と逆洗を平行して行う為、時間的なロスがなく、高濃度
な排水処理にも対応可能となる。
When treating high-concentration wastewater with a filtration device, the time until clogging is short, and backwashing has to be performed frequently, but in the continuous filtration device of the present invention, water flow and backwashing are performed in parallel. Therefore, it is possible to cope with high-concentration wastewater treatment without time loss.

濾材洗浄を専用の逆洗槽で行うため、洗浄の効率が良
く、洗浄に必要な水量も少なくて済む。
Since the filter medium is washed in a dedicated backwash tank, the washing efficiency is high and the amount of water required for washing is small.

尚従来の沈降濃縮槽を用いて清澄な余水を得ようとし
た場合、通常水面積1m2当たり2〜5m3/hの処理能力であ
るに対し、上記実施例のように粒状濾材を使用した上向
流濾過装置では同じく10〜20m3/hの処理能力をもってい
る。
In addition, when it is intended to obtain clear residual water using a conventional sedimentation and concentration tank, the processing capacity is usually 2 to 5 m 3 / h per 1 m 2 of water area, but a granular filter medium is used as in the above example. The upflow filtration device has a processing capacity of 10 to 20 m 3 / h.

然しながら通常の濾材を用いても良いことは勿論であ
る。
However, it is a matter of course that ordinary filter media may be used.

又濾過槽本体6を垂立する代わりに横向きとすること
もできる。
Also, the filtration tank body 6 can be set to be horizontal instead of standing upright.

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

第1図は本発明連続濾過装置の縦断正面図、第2図はそ
のA−A線面図、第3図はB−B線面図、第4図は移動
濾床ユニットの縦断正面図、第5図はその平面図であ
る。 1……筒状体、2……仕切網、3……固定濾床、4……
移動濾床、5……移動濾床ユニット、6……濾過槽本
体、7……保持部分、8……泥水入口、9……処理水排
水口、10……沈降部、11……逆洗槽、12……室、13……
孔あきパイプ、14……空気パイプ、15……逆洗水排出
口、16……逆洗水ノズル、17……逆洗水供給パイプ、18
……押し出し機構。
FIG. 1 is a longitudinal sectional front view of the continuous filtration device of the present invention, FIG. 2 is a sectional view taken along line AA, FIG. 3 is a sectional view taken along line BB, FIG. FIG. 5 is a plan view thereof. 1 ... tubular body, 2 ... partition net, 3 ... fixed filter bed, 4 ...
Mobile filter bed, 5: Mobile filter bed unit, 6: Filter tank body, 7: Holding part, 8: Muddy water inlet, 9: Treated water drainage port, 10: Sedimentation part, 11: Backwash Vessel, 12 …… Room, 13 ……
Perforated pipe, 14… Air pipe, 15… Backwash water outlet, 16… Backwash water nozzle, 17… Backwash water supply pipe, 18
…… Extrusion mechanism.

フロントページの続き (56)参考文献 実開 昭50−115275(JP,U) 特許2761805(JP,B2) 特公 昭53−26861(JP,B2) (58)調査した分野(Int.Cl.6,DB名) B01D 24/00 - 24/48 B01D 41/02 Continuation of the front page (56) References Japanese Utility Model 50-115275 (JP, U) Patent 2761805 (JP, B2) Japanese Patent Publication No. 53-26861 (JP, B2) (58) Fields investigated (Int. Cl. 6) B01D 24/00-24/48 B01D 41/02

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】筒状の濾過槽本体と、この濾過槽本体内に
互に隣接して配置した固定濾床及び複数の移動濾床を並
設して成る移動濾床ユニットと、この隣接する移動濾床
ユニットの側から処理原水を供給し固定濾床の側から処
理原水を取り出す機構と、逆洗槽と、上記移動濾床ユニ
ットを構成する一つの移動濾床が上記逆洗槽内に位置さ
れたとき他の一つの移動濾床が上記固定濾床に隣接され
るよう上記移動濾床ユニットを移動せしめる機構とより
成ることを特徴とする連続濾過装置。
1. A mobile filter unit comprising a cylindrical filter tank main body, a fixed filter bed and a plurality of mobile filter beds arranged adjacent to each other in the filter tank main body, and adjacent thereto. A mechanism for supplying treated raw water from the side of the moving filter bed unit and removing treated water from the side of the fixed filter bed, a backwash tank, and one moving filter bed constituting the moving filter unit are provided in the backwash tank. A mechanism for moving said mobile filter unit so that another mobile filter bed, when positioned, is adjacent to said fixed filter bed.
【請求項2】少なくとも上記移動濾床が発泡した樹脂製
で比重が水より小さい粒状濾材を有し、上記濾過槽本体
が垂立しており、上記逆洗槽が下方より空気を供給する
機構と、上方より逆洗水を供給する機構とを有する請求
項1記載の連続濾過装置。
2. A mechanism wherein at least the moving filter bed is made of foamed resin and has a granular filter medium having a specific gravity smaller than water, the filter tank main body is upright, and the backwash tank supplies air from below. The continuous filtration device according to claim 1, further comprising a mechanism for supplying backwash water from above.
JP31618690A 1990-11-22 1990-11-22 Continuous filtration device Expired - Fee Related JP2961442B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31618690A JP2961442B2 (en) 1990-11-22 1990-11-22 Continuous filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31618690A JP2961442B2 (en) 1990-11-22 1990-11-22 Continuous filtration device

Publications (2)

Publication Number Publication Date
JPH04190806A JPH04190806A (en) 1992-07-09
JP2961442B2 true JP2961442B2 (en) 1999-10-12

Family

ID=18074257

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31618690A Expired - Fee Related JP2961442B2 (en) 1990-11-22 1990-11-22 Continuous filtration device

Country Status (1)

Country Link
JP (1) JP2961442B2 (en)

Also Published As

Publication number Publication date
JPH04190806A (en) 1992-07-09

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