JPH022408Y2 - - Google Patents

Info

Publication number
JPH022408Y2
JPH022408Y2 JP11659485U JP11659485U JPH022408Y2 JP H022408 Y2 JPH022408 Y2 JP H022408Y2 JP 11659485 U JP11659485 U JP 11659485U JP 11659485 U JP11659485 U JP 11659485U JP H022408 Y2 JPH022408 Y2 JP H022408Y2
Authority
JP
Japan
Prior art keywords
liquid
discharge port
flow
air lift
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
Application number
JP11659485U
Other languages
Japanese (ja)
Other versions
JPS6227705U (en
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 filed Critical
Priority to JP11659485U priority Critical patent/JPH022408Y2/ja
Publication of JPS6227705U publication Critical patent/JPS6227705U/ja
Application granted granted Critical
Publication of JPH022408Y2 publication Critical patent/JPH022408Y2/ja
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、槽内の床下部の材をエアリフト
管によつて上昇させて洗浄し、洗浄済の材を再
び床上部に還流させるようにした上向流式連続
過装置において、特に材の洗浄及び洗浄排水
の分離排出を効果的たらしめた装置に関するもの
である。
[Detailed description of the invention] [Industrial application field] The present invention is designed to raise the material at the bottom of the floor in the tank using an air lift pipe to clean it, and to return the cleaned material to the upper part of the floor. The present invention relates to an upflow type continuous filtration device which is particularly effective in cleaning materials and separating and discharging cleaning wastewater.

〔従来の技術〕[Conventional technology]

槽内の床下部の材をエアリフト管によつて
上昇させて洗浄し、洗浄済の材を再び床上部
に還流させるようにした上向流式連続過装置で
は、材の洗浄効率が装置の機能を左右するもの
で、材洗浄のための簡単かつ効率のよい構造の
ものが要求されている。このような要求にもとづ
き、材と洗浄液との間の向流による洗浄の利益
を利用し、比較的簡単な構造をもつものとして、
特公昭56−51808号公報に示されるものが考案さ
れるに至つている。
In an upward flow continuous filtration system, the material at the bottom of the floor of the tank is lifted up by an air lift pipe to be cleaned, and the cleaned material is returned to the top of the floor.The cleaning efficiency of the material is a function of the equipment. There is a need for a simple and efficient structure for cleaning materials. Based on these requirements, we have created a system with a relatively simple structure that utilizes the benefits of cleaning through countercurrent flow between the material and the cleaning fluid.
The method shown in Japanese Patent Publication No. 56-51808 has been devised.

〔考案が解決しようとする問題点〕[Problem that the invention attempts to solve]

前記特公昭56−51808号の装置は、エアリフト
管上端から吐出された汚れた材が、洗浄路を下
降して還流される間に、洗浄路内を上向流にて流
れる液と向流洗浄させられるものであるが、洗
浄によつて材から剥離された汚染物をも上昇さ
せるために、大量の洗浄用液を必要とし、また
洗浄路内が閉塞する恐れも多かつた。
The device disclosed in Japanese Patent Publication No. 56-51808 is designed to perform countercurrent cleaning with the liquid flowing upward in the cleaning path while the dirty material discharged from the upper end of the air lift tube descends through the cleaning path and is refluxed. However, in order to lift up the contaminants peeled off from the material during cleaning, a large amount of cleaning liquid is required, and there is also a risk that the inside of the cleaning channel will become clogged.

本考案は、このような従来の問題点を解消し、
より少ない水量で材の洗浄を効率よく行い、流
路閉塞の恐れも全くない簡単な構造をもつた上向
流式連続過装置を提供しようとするものであ
る。
This invention solves these conventional problems and
It is an object of the present invention to provide an upward flow type continuous filtration device that can efficiently wash materials with a smaller amount of water and has a simple structure with no fear of flow path blockage.

〔問題点を解決するための手段〕[Means for solving problems]

本考案は、槽内の床下部の材をエアリフト
管によつて上昇させて洗浄し、洗浄済の材を再
び床上部に還流させるようにした上向流式連続
過装置において、前記エアリフト管の吐出口を
槽内上部に形成させた分離室内に連通させて設
け、さらに該分離室に分離液排出口と該分離液排
出口にほぼ横流にて液を導く液導入口を設け
ると共に、前記液の横流部の下部に前記エアリ
フト管の吐出口から吐出された材を導くように
材排出部を開口配備したことを特徴とする上向
流式連続過装置である。
The present invention provides an upward flow type continuous filtration device in which the material at the bottom of the floor of the tank is lifted up by an air lift pipe to be cleaned, and the washed material is returned to the upper part of the floor. A discharge port is provided in communication with a separation chamber formed at the upper part of the tank, and the separation chamber is further provided with a separated liquid outlet and a liquid inlet for introducing the liquid into the separated liquid outlet in a substantially cross-flow manner. This is an upward flow type continuous filtration device characterized in that a material discharge section is opened and arranged at the lower part of the cross flow section to guide the material discharged from the discharge port of the air lift pipe.

〔実施例〕〔Example〕

本考案の一実施例を図面を参照しながら説明す
れば、1はエアリフト管であつて、その下部に送
給される空気の上昇力によつて、槽2内の下方に
形成されている床(図示せず)の下部の材を
上昇させるもので、エアリフト管1内の上方部に
は液流を攪乱させるためのスタテイツクミキサ3
を配備するとよく、エアリフト管1内を上昇する
流れは上部の吐出口4から吐出されるようになつ
ている。
One embodiment of the present invention will be described with reference to the drawings. Reference numeral 1 denotes an air lift pipe, and a floor is formed in the lower part of the tank 2 by the upward force of the air fed to the lower part of the pipe. A static mixer 3 is installed in the upper part of the air lift tube 1 to disturb the liquid flow.
It is preferable to provide the air lift tube 1 so that the flow rising inside the air lift tube 1 is discharged from the upper discharge port 4.

また、吐出口4を包囲して分離室5が槽2内上
部に区画形成されるが、分離室5内の吐出口4付
近には吐出される流れと衝突するバツフル板6を
付設するとよく、バツフル板6の下端は分離室5
の下方の傾斜壁7と離隔させておく。
Further, a separation chamber 5 is formed in the upper part of the tank 2 to surround the discharge port 4, but it is preferable to attach a baffle plate 6 near the discharge port 4 in the separation chamber 5 to collide with the discharged flow. The lower end of the full plate 6 is the separation chamber 5
It is separated from the inclined wall 7 below.

さらに分離室5の底部には、分離液排出口8を
設けて排水管9を接続して槽外に導くが、この分
離液排出口8を分離室5の底部に近接した側壁に
開口させることもできる。さらにまた、分離室5
に液導入口10を設けるが、その位置を液が
ほぼ横流となつて分離液排出口8に導かれるよう
な位置とし、また、前記液の横流部に吐出口4
から吐出された材を導くように、分離液排出口
8と液導入口10間にこれらより低く材排出
部11が開口配備され、材排出部11の下端を
横方向に開口させて槽2内と連通し、この開口部
に自重で閉じ材の堆積圧力によつて開放する
か、或いは適当な開閉手段と連結された開閉扉1
2を設ける。
Further, a separated liquid outlet 8 is provided at the bottom of the separation chamber 5, and a drain pipe 9 is connected to the separated liquid outlet 8 to guide the liquid out of the tank. You can also do it. Furthermore, the separation chamber 5
A liquid inlet 10 is provided at the position where the liquid is guided to the separated liquid discharge port 8 in a substantially horizontal flow, and a discharge port 4 is provided in the horizontal flow portion of the liquid.
A material discharge part 11 is opened lower than these between the separated liquid discharge port 8 and the liquid introduction port 10 so as to guide the material discharged from the tank 2. An opening/closing door 1 that communicates with the opening and opens the opening by the pressure of the closing material deposited under its own weight, or is connected to an appropriate opening/closing means.
2 will be provided.

このようにして、分離室5内で槽2内上方部の
液が液導入口10より流入し、材排出部1
1へ沈降してゆく材と横流にて接触したのちに
分離液排出口8へ流れるが、材が液の横流に
伴われて分離液排出口8へ流れることのないよう
にする必要があり、例えば図示例のように、分離
液排出口8に昇降可能な流量調節板13などの流
量調節機構を付設し、槽2外の操作部14により
操作して分離液排出口8からの排水量を調節する
のが好ましい。
In this way, the liquid in the upper part of the tank 2 flows into the separation chamber 5 through the liquid inlet 10, and the material discharge part 1
After coming into contact with the material that is settling to 1 in a lateral flow, it flows to the separated liquid outlet 8, but it is necessary to prevent the material from flowing to the separated liquid outlet 8 due to the lateral flow of the liquid. For example, as shown in the illustrated example, a flow rate adjustment mechanism such as a flow rate adjustment plate 13 that can be raised and lowered is attached to the separated liquid outlet 8, and the amount of water discharged from the separated liquid outlet 8 is adjusted by operating it with an operating section 14 outside the tank 2. It is preferable to do so.

しかして、上向流過によつて汚れた床下部
の材を、エアリフト管1によつて槽内液と共に
上昇させると、その流れは撹乱されながらスタテ
イツクミキサ3の部分においてさらに激しく撹乱
され、材に付着している汚染物が剥離されて効
果的な材の洗浄が行われる。
When the material at the bottom of the floor contaminated by the upward flow is raised together with the liquid in the tank through the air lift pipe 1, the flow is disturbed and is even more violently disturbed at the static mixer 3. Contaminants adhering to the material are removed and the material is effectively cleaned.

次いで、洗浄された材及び剥離された汚染物
を含む液は、吐出口4から分離室5内に吐出され
てバツフル板6に衝突し、材や汚染物は沈降し
つつ傾斜壁7に沿つて移動し材排出部11に至
るが、その途中において液導入口10から導入
された液の横流によつて、材から剥離された
汚染物は分離液排出口8から排水管を経て槽外に
排出される一方、材排出部11に至つた洗浄済
の材は開閉扉12の開放によつて槽2内の床
上部に還流される。このときの分離液排出口8か
らの排水量は、流量調節板13などによつて調節
し、材と汚染物との分離を的確に行わせ、また
砕かれて小さくなつた材を汚染物と共に排出さ
せ、常に均一の粒径の洗浄済材を床上部に還
流させることができる。
Next, the liquid containing the cleaned materials and the peeled contaminants is discharged from the discharge port 4 into the separation chamber 5 and collides with the baffle plate 6, and the materials and contaminants settle along the inclined wall 7. The material moves and reaches the material discharge section 11, but on the way, due to the horizontal flow of the liquid introduced from the liquid introduction port 10, the contaminants separated from the material are discharged from the separated liquid discharge port 8 to the outside of the tank via the drain pipe. Meanwhile, the washed material that has reached the material discharge section 11 is returned to the upper part of the floor in the tank 2 by opening the opening/closing door 12. At this time, the amount of water discharged from the separated liquid discharge port 8 is adjusted by the flow rate adjustment plate 13, etc., to ensure accurate separation of the wood and contaminants, and to discharge the crushed and reduced wood together with the contaminants. This allows washed material with uniform particle size to be constantly refluxed to the upper part of the bed.

〔考案の効果〕[Effect of idea]

以上述べたように本考案によれば、エアリフト
管内を上昇する汚れた材は、エアリフト管内で
撹乱されながら材と汚染物の剥離、洗浄を効果
的に行うことができ、洗浄済の材と剥離された
汚染物との分離を液の横流によつて行うため、
その洗浄用の水量も従来の向流方式より大幅に減
少させることができ、さらに洗浄部などの閉塞の
恐れは皆無であり、さらに砕かれて小さくなつた
材をも汚染物と共に排出することができ、常に
均一粒径の材を還流することができるなどの有
益なる効果を有するものである。
As described above, according to the present invention, the dirty material rising inside the air lift pipe can be effectively separated from the contaminated material and cleaned while being disturbed within the air lift pipe, and the material can be separated from the cleaned material. Because the separation from the contaminated contaminants is carried out by horizontal flow of liquid,
The amount of water used for cleaning can be significantly reduced compared to the conventional countercurrent method, and there is no risk of clogging the cleaning section, and even crushed and small pieces of wood can be discharged together with contaminants. This has beneficial effects such as being able to constantly reflux material with a uniform particle size.

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

図面は本考案の一実施例を示す要部の切断面図
である。 1……エアリフト管、2……槽、3……スタテ
イツクミキサ、4……吐出口、5……分離室、6
……バツフル板、7……傾斜壁、8……分離液排
出口、9……排水管、10……液導入口、11
……材排出部、12……開閉扉、13……流量
調節板、14……操作部。
The drawing is a cross-sectional view of essential parts showing an embodiment of the present invention. 1... Air lift pipe, 2... Tank, 3... Static mixer, 4... Discharge port, 5... Separation chamber, 6
... Bumpy plate, 7 ... Inclined wall, 8 ... Separated liquid discharge port, 9 ... Drain pipe, 10 ... Liquid inlet, 11
... Material discharge section, 12 ... Opening/closing door, 13 ... Flow rate adjustment plate, 14 ... Operation section.

Claims (1)

【実用新案登録請求の範囲】 (1) 槽内の床下部の材をエアリフト管によつ
て上昇させて洗浄し、洗浄済の材を再び床
上部に還流させるようにした上向流式連続過
装置において、前記エアリフト管の吐出口を槽
内上部に形成させた分離室内に連通させて設
け、さらに該分離室に分離液排出口と該分離液
排出口にほぼ横流にて液を導く液導入口を
設けると共に、前記液の横流部の下部に前記
エアリフト管の吐出口から吐出された材を導
くように材排出部を開口配備したことを特徴
とする上向流式連続過装置。 (2) 前記分離液排出口が流量調節機構を備えたも
のである実用新案登録請求の範囲第1項記載の
上向流式連続過装置。
[Scope of Claim for Utility Model Registration] (1) An upward flow continuous filtration system in which the material at the bottom of the floor in the tank is lifted up by an air lift pipe to be cleaned, and the cleaned material is returned to the top of the floor. In the apparatus, the discharge port of the air lift pipe is provided in communication with a separation chamber formed in the upper part of the tank, and a liquid is introduced into the separation chamber by introducing a liquid into the separation chamber in a substantially horizontal flow to a separated liquid discharge port and the separated liquid discharge port. An upward flow type continuous filtration device, characterized in that an opening is provided and a material discharge section is opened at a lower part of the liquid lateral flow section so as to guide the material discharged from the discharge port of the air lift tube. (2) The upward flow continuous filtration device according to claim 1, wherein the separated liquid outlet is equipped with a flow rate adjustment mechanism.
JP11659485U 1985-07-31 1985-07-31 Expired JPH022408Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11659485U JPH022408Y2 (en) 1985-07-31 1985-07-31

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11659485U JPH022408Y2 (en) 1985-07-31 1985-07-31

Publications (2)

Publication Number Publication Date
JPS6227705U JPS6227705U (en) 1987-02-19
JPH022408Y2 true JPH022408Y2 (en) 1990-01-22

Family

ID=31001335

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11659485U Expired JPH022408Y2 (en) 1985-07-31 1985-07-31

Country Status (1)

Country Link
JP (1) JPH022408Y2 (en)

Also Published As

Publication number Publication date
JPS6227705U (en) 1987-02-19

Similar Documents

Publication Publication Date Title
JPH022408Y2 (en)
JPH03275103A (en) Method and device for discharging settled sand
CN215480166U (en) Sewage treatment device
JPH022409Y2 (en)
JP4198299B2 (en) Sewage treatment equipment
CN2506332Y (en) Continuous inner circulation sand filter
US6077426A (en) Filter filled with loose bulk material
CN207024734U (en) Sewage treatment and recovery pond
JP3842032B2 (en) Moving bed type upward flow filtration device
US4342649A (en) Upflow reactor filter assembly
JPH0262283B2 (en)
JP2007090291A (en) Water filtration apparatus
JPH0317925Y2 (en)
CN218636738U (en) Organic waste water non-maintaining colating device
CN204403613U (en) A kind of novel inside and outside Combined corrugated pipe
CN210825739U (en) Integrated sewage treatment device
CN219290856U (en) Solid-liquid separation device
CN107185301A (en) Circulate filter
HU194065B (en) Filtering device for separating solid matters from fluids
US6149827A (en) Device for separating particles from a particle containing liquid and a method for cleaning such a device
CN207024832U (en) Circulate filter
CN107224762A (en) Sewage treatment and recovery pond
JPH0143128Y2 (en)
JPH0227848Y2 (en)
JPS6337086Y2 (en)