JPH01262909A - Up-flow filter apparatus - Google Patents
Up-flow filter apparatusInfo
- Publication number
- JPH01262909A JPH01262909A JP63091144A JP9114488A JPH01262909A JP H01262909 A JPH01262909 A JP H01262909A JP 63091144 A JP63091144 A JP 63091144A JP 9114488 A JP9114488 A JP 9114488A JP H01262909 A JPH01262909 A JP H01262909A
- Authority
- JP
- Japan
- Prior art keywords
- water
- nozzle
- filtration
- filter medium
- port switching
- 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
Landscapes
- Filtration Of Liquid (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は改良された上向流濾過装置に関するものである
。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to an improved upflow filtration device.
詳しくは、本発明は、水に浮上する炉材を充填した濾過
塔に被処理水を上向流で通水することにより、被処理水
中に懸濁されている濁質を除去する、上向流p過装置に
おいて、通水後の炉材を塔外に設置されたエゼクタ−の
吸入入口から塔底部に循環させることにより炉材に付着
した濁質を炉材から分離させることにより濁質を容易に
除去することができる上向流テ過装置に関する。Specifically, the present invention provides an upward flow system in which suspended solids in the water to be treated are removed by passing the water to be treated in an upward flow through a filtration tower filled with a furnace material that floats on water. In the filtration device, the turbidity adhered to the furnace material is separated from the furnace material by circulating the furnace material after passing water through the suction inlet of the ejector installed outside the tower to the bottom of the tower. The present invention relates to an upflow filter device that can be easily removed.
〈従来の技術〉
近年、冷却塔循環水、水圧試験用水、養魚用水等におけ
る供給水の濁質の除去を目的としたν過装置として、上
向流濾過装置が開発されている。<Prior Art> In recent years, an upflow filtration device has been developed as a ν filtration device for removing turbidity from feed water such as cooling tower circulating water, water pressure testing water, fish farming water, and the like.
この上向流ν過装置は、下向流濾過装置に比べ多量の濁
質を捕捉する能力を有するものである。This upward flow filtration device has the ability to capture a larger amount of suspended solids than the downward flow filtration device.
しかし、上向流濾過装置は、炉材の比重が水よりも高い
ため、被処理水の通水流速を速めたり、あるいは、濾過
層内に濁質が捕捉されていくにつれて濾過層が流動し、
濁質を捕捉できなくなるという問題があった。However, in upflow filtration devices, the specific gravity of the furnace material is higher than that of water, so the flow rate of the water to be treated must be increased, or the filtration layer may flow as turbidity is captured within the filtration layer. ,
There was a problem that suspended solids could not be captured.
そこで、かかる流動化を防止するため、水よりも比重の
小さい炉材を用いて濾過塔内に浮上濾過層を構成させ、
被処理水を上向流で通水して濾過する方法が知られてい
る。Therefore, in order to prevent such fluidization, a floating filtration layer is constructed in the filtration tower using a furnace material with a specific gravity smaller than that of water.
A method is known in which water to be treated is filtered by passing it in an upward flow.
ところが、この浮上する炉材を用いた上向流濾過装置に
おいては、被処理水中の濁質を捕捉して汚染した濾過層
の洗浄にあっては、従来性なわれている濾過層の下部よ
り洗浄水を早い流速で通水して濾過層を流動させ洗浄す
るいわゆる逆洗操作が採用できないため特別の操作が必
要である。However, in an upflow filtration device using this floating furnace material, when cleaning the filtration layer that has been contaminated by trapping suspended matter in the water to be treated, it is difficult to clean the filtration layer from the bottom of the filtration layer, which is the conventional method. A special operation is required because a so-called backwash operation in which washing water is passed through at a high flow rate to fluidize and wash the filtration layer cannot be used.
例えば、濾過塔内に攪拌機を設け、これにより濾過塔の
濾過層を保有水と共に攪拌し、テ過層を流動化させ、濾
過層中の濁質を保有水中に分散し沈降させた後、濁質を
保有水と共に濾過塔外に排出する方法が採用されている
。For example, a stirrer is installed in the filtration tower, which agitates the filtration layer of the filtration tower together with the retained water, fluidizes the filtration layer, disperses the turbidity in the filtration layer into the retained water, causes it to settle, and then A method is adopted in which the waste water is discharged to the outside of the filtration tower along with the retained water.
〈発明が解決しようとする課題〉
しかしながら、上記の方法では、浮上濾過層全体を流動
化させる必要があることから、比較的大きな動力容量の
攪拌装置の搭載が必要であるために、濾過塔の構造が複
雑になり、しかも炉材が摩耗し、ひいては設備コストが
嵩むという問題点があった。<Problems to be Solved by the Invention> However, in the above method, since it is necessary to fluidize the entire floating filtration layer, it is necessary to install a stirring device with a relatively large power capacity, which causes problems in the filtration tower. There were problems in that the structure was complicated, the furnace materials wore out, and the equipment cost increased.
本発明は、水に浮上する炉材により濾過層を構成した上
向流濾過装置において、濾過層の洗浄のための攪拌装置
を必要とせず、簡単な配管接続により、炉材を摩耗させ
ることなく濾過層を洗浄できる上向流濾過装置の提供を
目的とする。The present invention is an upflow filtration device in which a filtration layer is formed by a furnace material floating on water, which does not require an agitation device for cleaning the filtration layer and can be easily connected to piping without causing wear on the furnace material. The object of the present invention is to provide an upflow filtration device that can wash a filtration layer.
〈課題を解決するための手段〉
すなわち、本発明は、水に浮上するろ材がろ過層(7)
として充填されているろ過塔(1)、濾過塔の底部には
排水ノズル(4)、排水ノズルの上方に散水ノズル(2
)、そして、散水ノズルの上方にろ材返送ノズル(3)
が設置され、濾過塔の上方部には集水ノズル(5)、そ
して、集水ノズルの上方にろ材抜出ノズル(6)が設置
され、炉材抜出しノズルは塔外のエゼクタ−(9)の吸
入入口に連結され。<Means for Solving the Problems> In other words, the present invention provides a method in which the filter material floating on water is a filter layer (7).
A filtration tower (1) filled with water, a drainage nozzle (4) at the bottom of the filtration tower, and a water spray nozzle (2) above the drainage nozzle.
), and a filter medium return nozzle (3) above the water spray nozzle.
is installed, a water collection nozzle (5) is installed above the filtration tower, a filter material extraction nozzle (6) is installed above the water collection nozzle, and the furnace material extraction nozzle is connected to the ejector (9) outside the tower. connected to the suction inlet of.
エゼクタ−の出口はろ材返送ノズル(3)に連結され、
エゼクタ−の駆動水入口と散水ノズルとが吐出口切替三
方弁(6)の三方に連結され、三方弁の残る一方が循環
ポンプ(8)の出口に連結され、循環ポンプの入口は吸
込口切替三方弁(7)の一方に連結され、吸込口切替三
方弁の一方は被処理水供給管(2)に連結され、吸込口
切替三方弁の残る一方は吐出口切替三方弁の一方を介し
て散水ノズルに連結され、炉材返送lノズルとろ材抜出
しノズルとの空間に適宜量のろ材が充填されていること
を特徴とする上向流濾過装置を要旨とするものである。The outlet of the ejector is connected to the filter medium return nozzle (3),
The driving water inlet of the ejector and the water spray nozzle are connected to three sides of a three-way discharge port switching valve (6), the remaining one of the three-way valves is connected to the outlet of a circulation pump (8), and the inlet of the circulation pump is connected to a suction port switching valve. One of the suction port switching three-way valves is connected to one of the three-way valves (7), one of the suction port switching three-way valves is connected to the treated water supply pipe (2), and the remaining one of the suction port switching three-way valves is connected to one side of the discharge port switching three-way valve. The gist of the present invention is an upflow filtration device which is connected to a water spray nozzle and is characterized in that a space between a furnace material return nozzle and a filter material extraction nozzle is filled with an appropriate amount of filter material.
本発明は、浮上している濾過層を濾過塔頂部よりエゼク
タ−の吸引力を利用して抜き出し、それらをエゼクタ−
の駆動水と共に濾過塔の下部へ返送するように設計(エ
ゼクタ−(9)の出口とろ材返送ノズル(3)との間に
設置)された循環管路に通水することにより、濾過層を
流動化させ、炉材を循環管路において炉材粒子相互ある
いは管路壁に衝突させることにより、濁質を炉材から剥
離し、剥離した濁質とろ材とを濾過塔内において沈降・
浮上分離することにより濾過層の洗浄が行なえるように
したものである。The present invention extracts the floating filtration layer from the top of the filtration tower using the suction force of the ejector.
By passing water through a circulation pipe designed to be returned to the lower part of the filtration tower together with the driving water of the filter (installed between the outlet of the ejector (9) and the filter medium return nozzle (3)), By fluidizing the furnace material and causing the furnace material particles to collide with each other or the pipe wall in the circulation pipe, the suspended solids are separated from the furnace material, and the separated suspended solids and the filter medium are allowed to settle and settle in the filter tower.
The filtration layer can be washed by flotation separation.
〈実施例〉 以下1本発明の実施例を図面に基づいて説明する。<Example> An embodiment of the present invention will be described below based on the drawings.
第1図は本発明の上向流濾過装置を示すフローシートで
ある。FIG. 1 is a flow sheet showing the upward flow filtration device of the present invention.
この上向流涙過装置は、濾過塔(1)及びこれに配管接
続された循環ポンプ(8)を主構成要素としている。This upward flow lacrimal filtration device has a filtration tower (1) and a circulation pump (8) connected to the filtration tower (1) as main components.
濾過塔(1)は密閉タンクで下部には底部から排水ノズ
ル(4)、散水ノズル(2)及び炉材返送ノスル(3)
がこの順序で、上部には頂部より炉材抜き出しノズル(
6)及び集水ノズル(5)がこの順序で内設されており
、この内部には水に浮上する炉材が充填され、濾過層(
7)が構成されている。The filtration tower (1) is a closed tank with a drainage nozzle (4), a watering nozzle (2) and a furnace material return nozzle (3) at the bottom.
In this order, the furnace material extraction nozzle (
6) and a water collection nozzle (5) are installed in this order, and the inside is filled with a furnace material that floats on water, and a filtration layer (
7) is configured.
この水に浮上する炉材としては、比重l以下で粒径O0
j〜i、o ttm程度のもの、例えば、発泡スチロー
ル、発泡ホリエチレン、ホリエチレンピーズ等が採用で
きる。The furnace material that floats on this water has a specific gravity of 1 or less and a particle size of O0.
For example, foamed polystyrene, foamed polyethylene, polyethylene peas, etc. can be used.
また炉材の充填量は濾過層(7)の層高が3QO〜i、
ooo、程度になるようにし、被処理水中の濁質の量に
応じて変化させれば良い。In addition, the filling amount of the furnace material is such that the height of the filtration layer (7) is 3QO~i,
ooo, and may be changed according to the amount of suspended solids in the water to be treated.
循環ポンプ(8)には、吸込口側及び吐出口側に各々吸
込口切替三方弁αQ及び吐出口切替三方弁αηが配管接
続されている。そして、前者の一方の接続口には、被処
理水供給管(2)が配管接続され、他方の接続口には、
吐出口切替三方弁の一方を介して散水ノズル(2)が配
管接続されている。A suction port switching three-way valve αQ and a discharge port switching three-way valve αη are connected via piping to the circulation pump (8) on the suction port side and the discharge port side, respectively. A water supply pipe (2) to be treated is connected to one of the former connection ports, and the other connection port is connected to the water supply pipe (2).
A water spray nozzle (2) is connected via piping through one of the three-way discharge port switching valves.
さらに後者の一方の接続口には、エゼクタ−(9)の駆
動水入口が、他方の接続口には散水ノズル(2)が配管
接続されている。又、エゼクタ−(9)の吸入入口はろ
材抜出しノズル(6)に連結され、エゼクタ−(9)の
出口はろ材循環配管α→を経て炉材返送ノズル(3)に
連結されている。Furthermore, a driving water inlet of the ejector (9) is connected to one of the latter connection ports, and a water spray nozzle (2) is connected to the other connection port. Further, the suction inlet of the ejector (9) is connected to the filter material extraction nozzle (6), and the outlet of the ejector (9) is connected to the furnace material return nozzle (3) via the filter material circulation pipe α→.
本発明で採用する循環ポンプ(8)及び各切替三方弁(
至)、αηは特別なものであることはなく、従来の水処
理装置に用いられているものでよい。The circulation pump (8) and each switching three-way valve (
) and αη are not special, and may be those used in conventional water treatment equipment.
またエゼクタ−(9)はろ材がスラリー状態で抜き出す
ことが出来るものであれば良い。Further, the ejector (9) may be of any type as long as it can extract the filter material in a slurry state.
炉材抜出しノズル(6)はろ材を均一に抜き出せるよう
に、放射状枝管構造にしておくとよい。The furnace material extraction nozzle (6) may have a radial branch pipe structure so that the filter material can be extracted uniformly.
さて、濁質を含んだ被処理水を濾過する通水工程は以下
のように行なわれる。Now, the water passing step for filtering the water to be treated containing suspended solids is carried out as follows.
被処理水供給管(2)により導入される被処理水は、吸
込口切替三方弁αQ、循環ポンプ(8)及び吐出口切替
三方弁αυを経て、濾過塔(1)の底部にある散水ノズ
ル(2)よシシ過塔(1)に供給される。The treated water introduced through the treated water supply pipe (2) passes through the suction port switching three-way valve αQ, the circulation pump (8) and the discharge port switching three-way valve αυ, and is then delivered to the water spray nozzle at the bottom of the filtration tower (1). (2) It is fed to the sifting tower (1).
濾過塔(1)に供給された被処理水は濾過層(7)を上
向流で通過し濾過された後、集水ノズル(5)を経て処
理水流出配管(至)より処理水として弁(ト)を通り流
出する。濾過塔(1)への通水流速は30〜40m/H
を目安に行う。The water to be treated that is supplied to the filtration tower (1) passes through the filtration layer (7) in an upward flow and is filtered, then passes through the water collection nozzle (5) and is discharged as treated water from the treated water outflow pipe (to) the valve. It flows out through (g). The flow rate of water to the filtration tower (1) is 30 to 40 m/h
Use this as a guideline.
通水工程を所定時間行なったら、あるいは、捕捉された
濁質により濾過層(7)が汚染され、−定の圧力損失に
なったら通水工程を停止する。When the water passage process has been carried out for a predetermined period of time, or when the filtration layer (7) is contaminated by the trapped turbidity and a certain pressure loss is reached, the water passage process is stopped.
次に、濾過層(7)を洗浄する洗浄工程を行い通水工程
で濾過層(7)に捕捉され蓄積した濁質を濾過塔(1)
外へ排出する。Next, a washing process is performed to wash the filtration layer (7), and the suspended solids captured and accumulated in the filtration layer (7) during the water flow process are transferred to the filtration tower (1).
Discharge outside.
すなわち、循環ポンプ(8)に配管接続された吸込口切
替三方弁00および吐出口切替三方弁(ロ)の流路を洗
浄工程を行う所定の流路に切替えると、濾過塔(1)の
下部に残留する保有水は散水ノズル(2)、吸込口切替
三方弁a4を経て循環ポンプ(8)により吸引され、吐
出口切替三方弁αηを経てエゼクタ−(9)の駆動水と
して使用される。That is, when the flow paths of the suction port switching three-way valve 00 and the discharge port switching three-way valve (b) connected via piping to the circulation pump (8) are switched to a predetermined flow path for performing the cleaning process, the lower part of the filtration tower (1) The remaining water is sucked by the circulation pump (8) through the water spray nozzle (2) and the suction port switching three-way valve a4, and is used as driving water for the ejector (9) via the discharge port switching three-way valve αη.
エゼクタ−(9)の駆動により濾過塔(1)内の濾過層
(7)は、蓄積した濁質と共に濾過塔(1)の頂部の炉
材抜き出しノズル(6)より徐々e二抜き出され、駆動
水と共にスラリー状態になってF材循環配管α→を通過
し濾過塔下部の炉材返送ノズル(3)より再び濾過塔(
1)に戻される。By driving the ejector (9), the filtration layer (7) in the filtration tower (1) is gradually extracted from the furnace material extraction nozzle (6) at the top of the filtration tower (1) together with the accumulated turbidity. Together with the driving water, it becomes a slurry, passes through the F material circulation pipe α→, and is returned to the filtration tower (
1).
濾過塔(1)に返送された炉材は浮力により上昇し、再
びこの糸路を循環し、この間に、炉材はろ材粒子相互あ
るいは配管壁に衝突して、濁質が剥離され炉材は洗浄さ
れる。The furnace material returned to the filtration tower (1) rises due to buoyancy and circulates through this thread path again. During this time, the filter material particles collide with each other or the piping wall, and the suspended solids are separated and the furnace material is Washed.
炉材の循環時間はろ材の汚染の程度によるが、通常10
〜30分間を目安にすれば良い。The circulation time of the furnace material depends on the degree of contamination of the filter material, but is usually 10
Aim for ~30 minutes.
炉材を充分に循環し、炉材の洗浄が終ったら、循環を停
止し、浮上濾過層(7)の構成と、剥離した濁質を濾過
塔(1)の下部に沈降させるため炉材を静置する。この
静置時間は7〜j分間程度で良い。After the furnace material has been sufficiently circulated and the furnace material has been cleaned, the circulation is stopped and the furnace material is removed to form the floating filtration layer (7) and to settle the separated suspended solids at the bottom of the filtration tower (1). Leave it still. This standing time may be about 7 to j minutes.
静置後、濾過塔排水弁αηを開き、排水ノズル(4)、
排出配管αQより、沈降した濁質を保有水と共に排出す
ることにより濾過層(7)の洗浄工程を終了する。After standing still, open the filter tower drain valve αη and drain the drain nozzle (4),
The cleaning step of the filter layer (7) is completed by discharging the settled suspended solids together with the retained water through the discharge pipe αQ.
沈降した濁質はできるだけ広範囲に排出されるように排
水ノズル(4)には数本の枝管を付設し、また炉材の濾
過塔外への流出を防止するため、排出配管(ト)は散水
ノズル(2)の取付位置の高さまで立ち上がらせておく
と良い。Several branch pipes are attached to the drainage nozzle (4) so that the settled turbidity can be discharged as widely as possible, and the discharge pipe (T) is installed to prevent the furnace material from flowing out of the filtration tower. It is best to raise it to the height of the installation position of the water spray nozzle (2).
次に、吸込口切替三方弁αQ及び吐出口切替三方弁(ロ
)を通水工程と同じ流路に切替えた後、必要に応じて被
処理水によりテ過層(7)に残留する濁質を水洗し、そ
の洗浄排水は処理水流出配管a3より分岐した弁(至)
を経て排水配管αυより排出した後、再び通水工程を行
う。Next, after switching the suction port switching three-way valve αQ and the discharge port switching three-way valve (b) to the same flow path as the water passage process, if necessary, the suspended matter remaining in the filter layer (7) with the water to be treated is is washed with water, and the washing wastewater is sent to a valve branched from the treated water outflow pipe a3 (to).
After the water is discharged from the drainage pipe αυ, the water flow process is performed again.
本発明では、循環ポンプ(8)の運転、停止、切替三方
弁αQ、αυや弁(ト)、αη、(ト)の開閉、切替は
人手で行なってもよいが、タイマーやコンピューターな
どを用い、一定のプログラムにより自動的に行なうこと
もできる。In the present invention, the operation, stopping, and switching of the three-way valves αQ, αυ, valves (G), αη, and (G) of the circulation pump (8) may be performed manually, but a timer, computer, etc. may be used. This can also be done automatically using a certain program.
〈発明の効果〉
本発明の上向流濾過装置によれば炉材が水に浮上する特
性をたくみに利用して、炉材を配管路内を流動循環させ
ることにより、テ過層に蓄積あるいはろ材の表面に付着
した濁質を極めて少量の水で剥離洗浄することができる
。また、濾過層洗浄のための動力源として、被処理水供
給のための循環ポンプが利用でき、攪拌装置あるいは特
別の機器を必要としないため、設備費の低減化はもちろ
ん、装置設置スペースが少なくて済み、又、炉材の摩耗
も避けられるという特徴を有している。<Effects of the Invention> According to the upward flow filtration device of the present invention, the property of the furnace material to float on water is skillfully utilized to fluidize and circulate the furnace material within the piping path, thereby preventing accumulation or accumulation in the filter layer. Suspended matter adhering to the surface of the filter medium can be removed and washed with a very small amount of water. In addition, a circulation pump for supplying water to be treated can be used as a power source for filter layer cleaning, and there is no need for an agitation device or special equipment, which not only reduces equipment costs but also takes up less equipment installation space. It also has the advantage of avoiding wear of the furnace material.
第1図は本発明の実施例の上向流濾過装置を示すフロー
シートを示す図である。
l・・・濾過塔 2・・・散水ノズル3−・・
ν材返送ノズル ≠・・・排水ノズルj・・・集水ノ
ズル 6・・・炉材抜出ノズル7・・・濾過層
r・・・循環ポンブタ・・・エゼクタ−10・・
・吸込ロ切替三方弁//00.吐出ロ切替三方弁 12
・・・被処理水供給配管/3・・・処理水流出配管 /
4t・・・炉材循環配管/j・・・排水配管 lt
・・・弁/7・・・濾過塔排水弁 ir・・・非出 願
人 日本錬水株式会社
代 理 人 弁理士 長谷用 −ほか1名FIG. 1 is a diagram showing a flow sheet showing an upward flow filtration device according to an embodiment of the present invention. l...filtration tower 2...water nozzle 3-...
ν Material return nozzle ≠...Drainage nozzle j...Water collection nozzle 6...Furnace material extraction nozzle 7...Filtration layer
r...Circulation pump...Ejector-10...
・Suction switching three-way valve //00. Discharge flow switching three-way valve 12
...Treated water supply piping/3...Treated water outflow piping/
4t...Furnace material circulation piping/j...Drainage piping lt
...Valve/7...Filtering tower drain valve IR...Non-applicant Nippon Rensui Co., Ltd. Representative Patent attorney Hase - 1 other person
Claims (1)
ているろ過塔(1)、ろ過塔の底部には排水ノズル(4
)、排水ノズルの上方に散水ノズル(2)、そして、散
水ノズルの上方にろ材返送ノズル(3)が設置され、ろ
過塔の上方部には集水ノズル(5)、そして、集水ノズ
ルの上方にろ材抜出ノズル(6)が設置され、ろ材抜出
しノズルは塔外のエゼクター(9)の吸入入口に連結さ
れ、エゼクターの出口はろ材返送ノズル(3)に連結さ
れ、エゼクターの駆動水入口と散水ノズルとが吐出口切
替三方弁(11)の二方に連結され、三方弁の残る一方
が循環ポンプ(8)の出口に連結され、循環ポンプの入
口は吸込口切替三方弁(10)の一方に連結され、吸込
口切替三方弁の一方は被処理水供給管(12)に連結さ
れ、吸込口切替三方弁の残る一方は吐出口切替三方弁の
一方を介して散水ノズルに連結され、ろ材返送ノズルと
ろ材抜出しノズルとの空間に適宜 量のろ材が充填されていることを特徴とする上向流ろ過
装置。(1) A filtration tower (1) filled with filter media that floats on water as a filtration layer (7), and a drainage nozzle (4) at the bottom of the filtration tower.
), a water spray nozzle (2) is installed above the drainage nozzle, a filter medium return nozzle (3) is installed above the water spray nozzle, and a water collection nozzle (5) is installed above the filtration tower; A filter medium extraction nozzle (6) is installed above, the filter medium extraction nozzle is connected to the suction inlet of the ejector (9) outside the column, the outlet of the ejector is connected to the filter medium return nozzle (3), and the drive water inlet of the ejector and a water spray nozzle are connected to two sides of a three-way discharge port switching valve (11), the remaining three-way valve is connected to the outlet of a circulation pump (8), and the inlet of the circulation pump is connected to a three-way suction port switching valve (10). One of the suction port switching three-way valves is connected to the treated water supply pipe (12), and the remaining one of the suction port switching three-way valves is connected to the water sprinkling nozzle via one of the discharge port switching three-way valves. , an upflow filtration device characterized in that a space between a filter medium return nozzle and a filter medium extraction nozzle is filled with an appropriate amount of filter medium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63091144A JPH01262909A (en) | 1988-04-13 | 1988-04-13 | Up-flow filter apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63091144A JPH01262909A (en) | 1988-04-13 | 1988-04-13 | Up-flow filter apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01262909A true JPH01262909A (en) | 1989-10-19 |
| JPH0453562B2 JPH0453562B2 (en) | 1992-08-27 |
Family
ID=14018329
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63091144A Granted JPH01262909A (en) | 1988-04-13 | 1988-04-13 | Up-flow filter apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01262909A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0533808U (en) * | 1991-10-03 | 1993-05-07 | 石垣機工株式会社 | Sewage treatment equipment using floating media |
| CN107260112A (en) * | 2012-12-26 | 2017-10-20 | 奥林巴斯株式会社 | Cleaning and sterilizing device for endoscope, method of rinsing endoscopes |
-
1988
- 1988-04-13 JP JP63091144A patent/JPH01262909A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0533808U (en) * | 1991-10-03 | 1993-05-07 | 石垣機工株式会社 | Sewage treatment equipment using floating media |
| CN107260112A (en) * | 2012-12-26 | 2017-10-20 | 奥林巴斯株式会社 | Cleaning and sterilizing device for endoscope, method of rinsing endoscopes |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0453562B2 (en) | 1992-08-27 |
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