JPH0621525Y2 - Continuous sand filter - Google Patents

Continuous sand filter

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Publication number
JPH0621525Y2
JPH0621525Y2 JP14362688U JP14362688U JPH0621525Y2 JP H0621525 Y2 JPH0621525 Y2 JP H0621525Y2 JP 14362688 U JP14362688 U JP 14362688U JP 14362688 U JP14362688 U JP 14362688U JP H0621525 Y2 JPH0621525 Y2 JP H0621525Y2
Authority
JP
Japan
Prior art keywords
sand
pipe
tank
water
pressure
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
JP14362688U
Other languages
Japanese (ja)
Other versions
JPH0266205U (en
Inventor
康男 小林
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP14362688U priority Critical patent/JPH0621525Y2/en
Publication of JPH0266205U publication Critical patent/JPH0266205U/ja
Application granted granted Critical
Publication of JPH0621525Y2 publication Critical patent/JPH0621525Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【考案の詳細な説明】 (産業上の利用分野) 本考案は連続式の砂ろ過装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to a continuous sand filter.

(従来の技術) 上下水や廃水の処理において用いられている砂ろ過装置
としては、急速ろ過を目的とするものとして、圧力式砂
ろ過装置及び連続式砂ろ過装置がある。圧力式のもの
は、ろ過は良好に行われるが、ろ過と砂の洗浄とを交互
に行うため間欠運転となり、操作が繁雑化し処理能力が
低いという欠点がある。また、連続式のものは、エアリ
フトによってろ過砂を循環させて、ろ過と同時に砂の洗
浄を行う方式のもので、連続したろ過ができるという利
点はあるが、ろ過砂の洗浄、分離に難があり、良好なろ
過ができないという欠点を有している。
(Prior Art) As sand filters used in the treatment of sewage and wastewater, there are pressure sand filters and continuous sand filters for the purpose of rapid filtration. Although the pressure type can satisfactorily perform filtration, it has a drawback that the operation is complicated and the treatment capacity is low because the operation is intermittent because filtration and sand washing are performed alternately. In addition, the continuous type is a system that circulates the filtered sand by an air lift to wash the sand at the same time as the filtration, and has the advantage that continuous filtration is possible, but it is difficult to wash and separate the filtered sand. However, it has a drawback that good filtration cannot be performed.

そこで、本出願人は、エアリフトによってろ過砂を循環
させる連続式砂ろ過装置に関し、実願昭59−6121
1号等により改善を図ってきた。この装置は、ろ過槽の
上部に砂溜を設けて、揚砂管より流出の砂を一時これに
貯溜し、この貯溜された砂を、砂溜の放出開口の開閉に
より間欠的に逆洗しながらろ過層に戻すようにしたもの
である。
Therefore, the applicant of the present invention relates to a continuous sand filter device for circulating filtered sand by an air lift, and discloses an application in Japanese Patent Application No. 59-6121.
We have been trying to improve it with No. 1 etc. This equipment has a sand reservoir on the top of the filtration tank to temporarily store the sand flowing out from the sand raising pipe, and intermittently backwash the stored sand by opening and closing the discharge opening of the sand reservoir. While returning to the filtration layer.

(考案が解決しようとする課題) 上記の改善した装置では、ろ過砂がエアリフトによる揚
砂過程で洗浄が行われると共に、砂溜から落下時にろ過
水で逆洗されるため、ろ過砂の洗浄、分離が良好に行な
われるようになった。
(Problems to be solved by the invention) In the improved device described above, since the filter sand is washed in the sand lifting process by the air lift, and is backwashed with the filter water when the filter sand falls, The separation is now well done.

しかし、前記の改善した装置では、ろ過砂の洗浄をろ過
水によって行なっているため、ろ過水の水質悪化時に
は、エアリフト揚砂量を増加させたとしても、揚砂管内
の混合液はろ過前の原水に近いものであるため、洗浄効
果があがらないばかりでなく、槽内へ落下する洗砂の通
過断面が小さいため、揚砂の大巾な増加はできない等の
問題を有している。
However, in the improved device described above, since the filter sand is washed with the filter water, when the quality of the filter water is deteriorated, the mixed liquid in the filter tube is not filtered even if the air lift sand load is increased. Since it is close to that of raw water, not only the cleaning effect is not improved, but also the cross-section of the washed sand falling into the tank is small, so there is a problem that the amount of lifted sand cannot be greatly increased.

本考案は、上記のような問題を解決するためになされた
もので、揚砂管より流出のろ過砂の逆洗効果良好、ろ過
性能を一段と向上できると共に、逆洗効果をあげるため
の空気量を増加しても、逆洗の水量ひいては排出ろ過水
量を一定に保つことができ、水質の大巾な変動に対応で
き、ろ過性能を一段と向上できる連続式の砂ろ過装置を
提供しようとするものである。
The present invention has been made to solve the above problems, and has a good backwashing effect on the filtered sand flowing out from the sand lifting pipe, which can further improve the filtering performance and the amount of air for increasing the backwashing effect. Even if the amount of water is increased, the amount of backwash water and hence the amount of discharged filtered water can be kept constant, it is possible to cope with wide fluctuations in water quality, and it is intended to provide a continuous sand filtration device that can further improve filtration performance. Is.

(課題を解決するための手段) 上記の目的を達成するための本考案の構成について、実
施例に対応する図面を参照して説明すると、本考案は、
エアリフトによる揚砂管5を中心部に立設したろ過槽1
の上部に、前記揚砂管5の上部を突入させた、ろ過砂と
排水との分離室4を設けると共に、分離室4の底部に接
続して、揚砂管5を囲み下部に送気管12を接続した上
下に長い洗砂落下管8を設け、前記分離室4内には、揚
砂管5の上端部を囲んで下端を開放した圧力槽13を昇
降調節自在に設けると共に、ろ過槽1上部に設けた排出
管15と前記圧力槽13との間に、堰板16を設け、こ
の堰板16をまたいで、下端を開放した圧力室18を形
成し、この圧力室18と前記圧力槽13との各上部間を
連通19したことを特徴とするものである。
(Means for Solving the Problems) The structure of the present invention for achieving the above object will be described with reference to the drawings corresponding to the embodiments.
Filtration tank 1 with sand lifting pipe 5 by air lift standing in the center
In the upper part of the above, provided is a separation chamber 4 for filtering sand and drainage, in which the upper part of the sand lifting pipe 5 is projected, and it is connected to the bottom of the separation chamber 4 to enclose the sand lifting pipe 5 and to send an air pipe 12 to the lower part. A long sand washing drop pipe 8 connected to the above is provided, and a pressure tank 13 which surrounds the upper end of the sand lifting pipe 5 and whose lower end is opened is provided in the separation chamber 4 so as to be adjustable up and down, and the filtration tank 1 A weir plate 16 is provided between the discharge pipe 15 provided at the upper part and the pressure tank 13, and a pressure chamber 18 having an open lower end is formed across the weir plate 16 to form the pressure chamber 18 and the pressure tank. It is characterized in that the upper part of each of the parts 13 and 13 communicates with each other.

(作用) 上記のように構成されたろ過装置では、原水は流入管7
から入りろ過層aを通って清澄なろ過水となり、流出管
15より槽1外に取出される。ろ過層の砂は揚砂管5の
下端からエアリフト作用で管中を上昇し、その間空気と
水の流動で洗砂される。揚砂管5の上端より出たろ過砂
は、洗砂落下管8中を落下し、その下端より出てろ過層
に戻ることになる。その際、ろ過砂は洗砂落下管8の下
部に吹込まれた空気の気泡の上昇で気固衝突による洗砂
と付着汚濁物の除去、分離作用を受けて浄化される。
(Operation) In the filtering device configured as described above, the raw water is supplied to the inflow pipe 7
Then, it passes through the filtration layer a to become clear filtered water, which is taken out of the tank 1 through the outflow pipe 15. The sand in the filtration layer rises in the pipe from the lower end of the sand raising pipe 5 by the air lift action, and is washed by the flow of air and water during that time. The filtered sand that has come out from the upper end of the sand lifting pipe 5 falls through the washed sand drop pipe 8 and comes out from the lower end thereof and returns to the filtration layer. At that time, the filtered sand is purified by the action of removing and separating the washed sand and the adhered contaminants due to the gas-solid collision due to the rise of the air bubbles blown into the lower portion of the washed sand drop tube 8.

また、揚砂管5の上端より流出した洗浄水や汚濁物(汚
水)は、分離室から堰板を越えて排出管15より槽外に
排出される。そして、揚砂管5の上端より出た空気によ
り、圧力槽13及び圧力室18中は共に与圧され、それ
によって圧力槽13及び圧室18内は、揚砂管5からの
流出空気量に関係なくほぼ一定の同水位に保たれること
になる。そのため、揚砂量を増大するために揚砂管への
送気量を多くしても、排水はほぼ一定に維持されること
になり、洗砂効果を変えて水質の変動に対応することが
できる。また、圧力槽13の位置を上下に調節してやれ
ばその水位cと共に圧力室3の水位dが変化し、堰板1
6の越流量即ち排水の量も調節することができる。
Further, the wash water and contaminants (dirt water) flowing out from the upper end of the sand lifting pipe 5 are discharged from the separation chamber to the outside of the tank through the discharge pipe 15 over the barrier plate. Then, the air discharged from the upper end of the sand lifting pipe 5 pressurizes both the pressure tank 13 and the pressure chamber 18, so that the pressure tank 13 and the pressure chamber 18 have the same amount of outflow air from the sand lifting pipe 5. Regardless of the water level, the water level will be kept almost constant. Therefore, even if the amount of air sent to the lifting sand pipe is increased to increase the amount of lifted sand, the drainage will be kept almost constant, and it is possible to change the sand washing effect and respond to fluctuations in water quality. it can. If the position of the pressure tank 13 is adjusted up and down, the water level c and the water level d of the pressure chamber 3 change, and the dam plate 1
The overflow of 6 or the amount of drainage can also be adjusted.

(実施例) 以下、本考案装置の実施例について図面を参照して説明
する。
Embodiment An embodiment of the device of the present invention will be described below with reference to the drawings.

図において1は上下に長く形成したろ過槽で、その上部
には越流溝2を介してろ過水流出管3が設けられてい
る。また、ろ過槽1の上部には、上端をろ過水の流出水
位aより高く形成した、ろ過砂と洗浄水との分離室4が
上部を開放して設けられている。5はろ過槽1の中心部
に立設された揚砂管で、その下端は槽底との間に所要の
間隔を有しており、上端は分離室4の上部に開口され、
揚砂管5の下部には槽1外の図示を略した送気源に連通
した送気管6が接続されている。そして、ろ過槽1の下
部には原水流管7,7が突入されている。
In the figure, reference numeral 1 is a vertically long filtration tank, and a filtered water outflow pipe 3 is provided in an upper portion thereof through an overflow groove 2. Further, in the upper part of the filtration tank 1, a separation chamber 4 for filtering sand and washing water, the upper end of which is formed higher than the outflow water level a of the filtered water, is provided with the upper part open. 5 is a sand lifting pipe that is erected in the center of the filtration tank 1, its lower end has a required distance from the tank bottom, and its upper end is opened at the upper part of the separation chamber 4,
An air supply pipe 6 communicating with an air supply source (not shown) outside the tank 1 is connected to a lower portion of the sand lifting pipe 5. The raw water flow pipes 7, 7 are inserted into the lower portion of the filtration tank 1.

分離室4の底部には、揚砂管5を囲んで配置した上下に
長い洗砂落下管8の上端が接続され、洗砂落下管8の上
端が接続され、洗浄砂落下管8の上端は、揚砂管5の中
間部に設けた傘状の散開板9の上方に開口されている。
また、洗砂落下管8の下部には、管周に沿って多数の噴
気口10,10が隔設され、それら噴気孔10,10は
送気管12に接続された配気管11に連通されている。
At the bottom of the separation chamber 4, the upper end of the vertically long sand washing drop pipe 8 arranged surrounding the sand lifting pipe 5 is connected, the upper end of the sand washing drop pipe 8 is connected, and the upper end of the washing sand drop pipe 8 is An opening is provided above an umbrella-shaped spreading plate 9 provided in the middle part of the sand lifting pipe 5.
In addition, a large number of fumaroles 10 and 10 are provided in the lower part of the sand washing drop pipe 8 along the circumference of the pipe, and these fumaroles 10 and 10 are connected to an air distribution pipe 11 connected to an air feeding pipe 12. There is.

さらに、分離室4内には、揚砂管5の上部を囲んで、下
端を開放した圧力槽13がその下端を揚砂管5の上端よ
り相当低い位置にして、昇降機構14により昇降調節自
在に設けられている。また、前記越流溝2に対向する槽
1の上部の、越流溝2より相当の低位置に設けられた洗
浄水の排出管15と圧力槽との中間部には、上端を排出
管15とほぼ同高位置とした堰板16が設けられ、それ
によって、排出管15と堰板16との間に越流室17が
形成されている。そして、堰板16の上部をまたいで、
下端が開放された堰圧力室18が設けられ、圧力槽13
及び堰圧力室13,18の上部間は通気管19により互
に連通されている。
Further, in the separation chamber 4, the pressure tank 13 which surrounds the upper part of the sand lifting pipe 5 and whose lower end is opened has its lower end positioned considerably lower than the upper end of the sand lifting pipe 5 and can be lifted and lowered by the lifting mechanism 14. It is provided in. In addition, an upper end of the drain pipe 15 is provided at an intermediate portion between the pressure tank and the drain pipe 15 of the wash water, which is provided at a position considerably lower than the overflow groove 2 on the upper part of the bath 1 facing the overflow groove 2. A weir plate 16 is provided at substantially the same height as the above, and thereby an overflow chamber 17 is formed between the discharge pipe 15 and the weir plate 16. And, straddling the upper part of the barrier plate 16,
A weir pressure chamber 18 having an open lower end is provided, and the pressure tank 13
The upper portions of the weir pressure chambers 13 and 18 are connected to each other by a ventilation pipe 19.

上記の装置において、槽1内には散開板9の下方の位置
までの高さにろ過砂が収容されてろ過層が形成される。
そして、原水は流入管7,7より槽1の下部に流入さ
れ、ろ過層中を上昇し、汚濁物が取除かれて清澄なろ過
水となり、上部の越流溝2にオーバーフローして流出管
3より槽外に取出される。汚濁物を捕捉したろ過層のろ
過砂は、送気管6より揚砂管5に吹込まれた空気による
エアリフト作用で、揚砂管5の下端より導入され同管5
中を上方に移送され、同管5の上端から分離室4内に流
入する。その際、揚砂管5内においては、砂と水と空気
とがそれぞれ異った速度で上昇するため、砂に付着され
ている汚濁物の分離、洗浄作用が行なわれることにな
る。
In the above apparatus, the filtration sand is formed in the tank 1 at a height up to the position below the spreading plate 9 to form a filtration layer.
Then, the raw water flows into the lower part of the tank 1 through the inflow pipes 7 and 7, rises in the filtration layer, removes contaminants and becomes clear filtered water, overflows into the overflow groove 2 in the upper part, and the outflow pipe. It is taken out of the tank from 3. The filtered sand in the filtration layer that has captured the contaminants is introduced from the lower end of the sand lifting pipe 5 by the air lift action of the air blown into the sand lifting pipe 5 from the air supply pipe 6
The liquid is transferred upward and flows into the separation chamber 4 from the upper end of the pipe 5. At this time, since sand, water, and air rise at different speeds in the sand lifting pipe 5, the contaminants adhering to the sand are separated and washed.

分離室4に流入した砂は、自重により分離室4の底部か
ら洗砂落下管8に入って落下し、その下端から出て散開
板12の作用でろ過層の上部に分散して戻されることに
なる。揚砂管5より出た汚水(水及び汚濁物)は、分離
室4の堰板16を越えて越流室17に入り、排出管15
より槽外に排出されることになる。この排出管15は、
ろ過水の水位aより相当低く設定されているため、分離
室4の水位bはろ過水の水位aより低く維持されること
になる。この水位差により、槽1中のろ過水は洗砂落下
管8の下端から流出して、ろ過砂の落下とは反対に上向
きに流れて分離室4に流入することになり、そこでろ過
砂への逆洗が行なわれることになる。また、洗砂落下管
8中へは、その下部の噴気孔10,10から空気が吹込
まれ、その気泡が管8中を上昇することになる。それに
よって気固衝突による洗浄作用が発揮されることにな
り、上記の逆洗作用と併せてろ過砂の洗浄効果が著しく
向上することになる。
The sand that has flowed into the separation chamber 4 should enter the sand washing drop pipe 8 from the bottom of the separation chamber 4 due to its own weight and drop, and then be discharged from the lower end thereof and dispersed back to the upper part of the filtration layer by the action of the spreading plate 12. become. Sewage (water and contaminants) discharged from the sand lifting pipe 5 crosses the weir plate 16 of the separation chamber 4 and enters the overflow chamber 17, and the discharge pipe 15
Will be discharged outside the tank. This discharge pipe 15
Since the water level a of the filtered water is set considerably lower than the water level a, the water level b of the separation chamber 4 is kept lower than the water level a of the filtered water. Due to this difference in water level, the filtered water in the tank 1 flows out from the lower end of the wash sand drop pipe 8, flows upward in the opposite direction of the fall of the filtered sand, and flows into the separation chamber 4, where it flows into the filtered sand. Will be backwashed. In addition, air is blown into the sand washing drop pipe 8 through the fumaroles 10 and 10 in the lower part thereof, and the bubbles rise in the pipe 8. As a result, the washing action due to gas-solid collision is exerted, and the washing effect of the filter sand is remarkably improved together with the above-mentioned backwashing action.

それで、揚砂管5の上端より出た空気は、圧力槽13に
入るが、圧力槽13の下部は水中に没しているので、槽
内の圧力Pは高くなり槽内の水位cを槽13の下端まで
押し下げ、分離室4内の水位bと水位差Hが生じること
になる。この場合、圧力槽13と堰圧力室18とは通気
管19により連通されていると共に、堰圧力室18の下
部も水中に没しているので、堰圧力室18内の圧力も圧
力槽13内の圧力Pと同圧力となる。それによって、堰
板16の分離室側の水位dは圧力槽13内の水位cと同
水位となり、堰板16の越流室側は排出管15に連通し
ているため、その水位eは前記の水位dより水位差Hだ
け低い水位fとなる。したがって、分離室4に流入した
汚水は堰圧力室18の一方の下端から室内に入って堰板
16を越して越流室17に入り、排出管15より槽外に
取出されることになる。そして、揚砂管5よりの空気量
が増加したときは、その増加した空気は圧力槽13の下
端より逃れることになるため、圧力槽13内の水位c
は、揚砂管5より出る空気量には関係なく常に一定に維
持されることになる。そのため、堰板16を越流する堰
圧力室内の水位dは常に一定に維持され、堰板16の越
流水量即ち排出管15よりの排出水量は揚砂管5より出
る空気量に関係なくほぼ一定量を保ことができるのであ
る。
Therefore, the air coming out from the upper end of the sand raising pipe 5 enters the pressure tank 13, but the lower portion of the pressure tank 13 is submerged in water, so the pressure P in the tank becomes high and the water level c in the tank rises. By pushing down to the lower end of 13, a water level b and a water level difference H in the separation chamber 4 will occur. In this case, since the pressure tank 13 and the weir pressure chamber 18 are communicated with each other by the ventilation pipe 19 and the lower portion of the weir pressure chamber 18 is also submerged in water, the pressure inside the weir pressure chamber 18 is also within the pressure tank 13. It becomes the same pressure as the pressure P. As a result, the water level d of the weir plate 16 on the separation chamber side becomes the same as the water level c of the pressure tank 13, and the overflow chamber side of the weir plate 16 communicates with the discharge pipe 15, so that the water level e is The water level f is lower than the water level d by a water level difference H. Therefore, the sewage that has flowed into the separation chamber 4 enters the chamber from one lower end of the weir pressure chamber 18, passes over the weir plate 16, enters the overflow chamber 17, and is taken out of the tank through the discharge pipe 15. Then, when the amount of air from the sand lifting pipe 5 increases, the increased air escapes from the lower end of the pressure tank 13, so that the water level c in the pressure tank 13 increases.
Is always maintained constant regardless of the amount of air discharged from the sand lifting pipe 5. Therefore, the water level d in the weir pressure chamber that overflows the weir plate 16 is always maintained constant, and the amount of overflow water of the weir plate 16, that is, the amount of water discharged from the discharge pipe 15 is almost independent of the amount of air discharged from the sand lifting pipe 5. A certain amount can be maintained.

また、圧力槽13を昇降機構14により上下に移動させ
れば、それにしたがって水位cが上下に変動することに
なり、それにつれて堰圧力室18内の水位dが変動する
結果、堰板16の越流水量即ち排出管15よりの排出水
量を変えることができることになる。
Further, if the pressure tank 13 is moved up and down by the elevating mechanism 14, the water level c will fluctuate up and down accordingly, and the water level d in the weir pressure chamber 18 will fluctuate accordingly. The amount of flowing water, that is, the amount of water discharged from the discharge pipe 15 can be changed.

上述のことから、ろ過水の水質悪化時には、揚砂管への
空気吹込量を増大させて揚砂量を増加し、砂の洗浄効果
を変えることができることになるのである。
From the above, when the quality of the filtered water deteriorates, it is possible to increase the amount of air blown into the lifting sand pipe to increase the amount of lifted sand and change the sand cleaning effect.

(考案の効果) 本考案の砂ろ過装置は、上述のような構成のものである
から、揚砂管を出てろ過層に戻るろ過砂は、洗砂落下管
中において、ろ過水による逆洗作用と併せて送気の気泡
による気固衝突作用で、洗浄及び付着汚濁物の除去が十
分に行なえることになり、洗浄効果が大巾に向上され
る。また、本考案装置は、圧力槽と堰板を囲む圧力室と
それらの連通とによって、揚砂管よりの空気量に関係な
く排水量がほぼ一定に保たれるので、ろ過水の水質悪化
時には、それに対応して揚砂量を増大させ、所要の洗浄
効果を得ることができる。さらに、圧力槽の上下位置を
調節することにより、排水量の調節も可能であり、負荷
変動に強く、洗浄効果の優れた装置を提供することがで
きるものである。
(Effect of the device) Since the sand filter device of the present invention has the above-mentioned configuration, the filter sand returning from the lifted sand pipe to the filter layer is backwashed with filtered water in the wash sand drop pipe. In addition to the action, the gas-solid collision action by the bubbles of the air supply enables the washing and the removal of adhered contaminants sufficiently, and the washing effect is greatly improved. Further, in the device of the present invention, the discharge amount is kept substantially constant by the pressure chamber surrounding the pressure tank and the weir plate and their communication, regardless of the amount of air from the sand lifting pipe. Correspondingly, the amount of lifted sand can be increased and the required cleaning effect can be obtained. Further, by adjusting the vertical position of the pressure tank, it is possible to adjust the drainage amount, and it is possible to provide a device that is resistant to load fluctuations and has an excellent cleaning effect.

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

図面は本考案装置の一実施例を示した縦断面図である。 1…ろ過槽、4…分離室、5…揚砂管 6…送気管、8…洗砂落下管 10…噴気孔、12…送気管 13…圧力槽、14…昇降機構 15…排出管、16…堰板 17…越流室、18…圧力室 19…通気管 The drawing is a longitudinal sectional view showing an embodiment of the device of the present invention. DESCRIPTION OF SYMBOLS 1 ... Filtration tank, 4 ... Separation chamber, 5 ... Sand-lifting pipe 6 ... Air supply pipe, 8 ... Sand washing falling pipe 10 ... Fume hole, 12 ... Air supply pipe 13 ... Pressure tank, 14 ... Elevating mechanism 15 ... Exhaust pipe, 16 … Weir plate 17… Overflow chamber, 18… Pressure chamber 19… Ventilation pipe

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B01D 29/62 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI technical display location B01D 29/62

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】エアリフトによる揚砂管を中心部に立設し
たろ過槽の上部に、前記揚砂管の上部を突入させた、ろ
過砂と排水との分離室を設けると共に、分離室の底部に
接続して、揚砂管を囲み下部に送気管を接続した上下に
長い洗砂落下管を設け、前記分離室内には、揚砂管の上
端部を囲んで下端を開放した圧力槽を昇降調節自在に設
けると共に、ろ過槽上部に設けた排出管と前記圧力槽と
の間に、堰板を設け、この堰板をまたいで、下端を開放
した圧力室を形成し、この圧力室と前記圧力槽との各上
部間を連通したことを特徴とする、連続式砂ろ過装置。
1. A separation chamber for filtering sand and drainage, in which the upper part of the sand lifting pipe is projected, is provided in the upper part of a filtration tank in which the sand lifting pipe by an air lift is erected in the center, and the bottom part of the separation chamber is provided. , A long sand wash drop pipe with a blasting pipe connected to the lower part and an air feeding pipe connected to the lower part is installed, and a pressure tank with the lower end surrounded by the upper end of the sand raising pipe is opened and lowered in the separation chamber. A weir plate is provided between the pressure tank and the discharge pipe provided on the upper portion of the filtration tank while being adjustable, and a pressure chamber having an open lower end is formed across the weir plate. A continuous sand filter, characterized in that the upper part of the pressure tank communicates with the upper part.
JP14362688U 1988-11-02 1988-11-02 Continuous sand filter Expired - Fee Related JPH0621525Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14362688U JPH0621525Y2 (en) 1988-11-02 1988-11-02 Continuous sand filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14362688U JPH0621525Y2 (en) 1988-11-02 1988-11-02 Continuous sand filter

Publications (2)

Publication Number Publication Date
JPH0266205U JPH0266205U (en) 1990-05-18
JPH0621525Y2 true JPH0621525Y2 (en) 1994-06-08

Family

ID=31410616

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14362688U Expired - Fee Related JPH0621525Y2 (en) 1988-11-02 1988-11-02 Continuous sand filter

Country Status (1)

Country Link
JP (1) JPH0621525Y2 (en)

Also Published As

Publication number Publication date
JPH0266205U (en) 1990-05-18

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