JP2820384B2 - Method of cleaning filter media for water treatment / filtration equipment - Google Patents
Method of cleaning filter media for water treatment / filtration equipmentInfo
- Publication number
- JP2820384B2 JP2820384B2 JP7144554A JP14455495A JP2820384B2 JP 2820384 B2 JP2820384 B2 JP 2820384B2 JP 7144554 A JP7144554 A JP 7144554A JP 14455495 A JP14455495 A JP 14455495A JP 2820384 B2 JP2820384 B2 JP 2820384B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- washing
- filter medium
- time
- amount
- 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 - Lifetime
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Filtration Of Liquid (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、圧縮性の浮遊濾材を充
填した水処理・濾過装置の濾材洗浄方法に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for washing a filter medium in a water treatment / filtration apparatus filled with a compressible floating filter medium.
【0002】[0002]
【従来の技術】一般に、水処理装置には、処理槽内に充
填した濾材表面に増殖した微生物によって汚濁物質を除
去する水処理設備と、被処理水中の懸濁物質を濾材を用
いて除去する濾過装置とがある。これら水処理・濾過装
置を長時間使用していると、濾材の間隙に捕捉された懸
濁物質や濾材の表面に増殖した菌体により目詰まりを起
こし、処理効率が低下してくる。従って、濾材の間隙に
捕捉された懸濁物質や増殖した菌体を適切な時間間隔で
洗浄・除去することにより、処理効率を復元させる必要
がある。濾材洗浄の時期は処理水中の懸濁物質が一定濃
度以上に到達した時点もしくは目詰まりにより圧損が所
定以上に到達した時点の何れか早い時期に実施される。
通常、濾材洗浄はこの時点に到達する前に計画的に実施
される。2. Description of the Related Art In general, a water treatment apparatus is provided with a water treatment facility for removing pollutants by microorganisms grown on the surface of a filter medium filled in a treatment tank and a filter medium for removing suspended substances in water to be treated. There is a filtration device. If these water treatment / filtration apparatuses are used for a long time, clogging occurs due to suspended substances trapped in the gaps between the filter media and bacteria growing on the surface of the filter media, and the treatment efficiency is reduced. Therefore, it is necessary to restore the treatment efficiency by washing / removing the suspended substances and the proliferating cells trapped in the gaps between the filter media at appropriate time intervals. The filter medium is washed at the earlier time when the suspended substance in the treated water reaches a certain concentration or more or when the pressure loss reaches a predetermined value or more due to clogging.
Typically, filter media cleaning is performed systematically before reaching this point.
【0003】この水処理・濾過装置における濾材の洗浄
は、濾材層に下部より洗浄用空気を吹き込み濾材を攪拌
し、捕捉された懸濁物質や菌体を分離し、洗浄用水を通
常の被処理水の流れと同じ方向や逆方向に流して分離さ
れた懸濁物質や菌体を処理槽外に流出させることにより
行っている。この洗浄操作から水処理・濾過装置の通常
の処理操作、すなわち、運転処理操作に移行する前の処
理槽内に水を供給する操作により濾材の最終的な洗浄を
行う。この時、濾材洗浄方法は図1の工程(8)の給水
操作において、従来処理槽内へ運転処理操作時の水量よ
りも多量の水を供給し、満水後もそのまま供給を続け、
処理槽の給水と濾材層の洗浄を短時間で完了させる方法
が採用されている。この洗浄が終了した後、運転処理操
作に移行している。[0003] The washing of the filter medium in this water treatment / filtration apparatus is performed by blowing washing air from below into the filter medium layer to stir the filter medium, to separate trapped suspended substances and cells, and to wash the washing water in a normal manner. It is performed by flowing suspended substances and cells separated in the same or opposite direction to the flow of water to the outside of the treatment tank. From this washing operation, the water treatment and filtration equipment
, That is, the operation of supplying water into the processing tank before shifting to the operation processing operation, thereby performing the final washing of the filter medium. At this time, in the filter medium washing method, in the water supply operation of step (8) in FIG. 1, a larger amount of water is supplied into the conventional treatment tank than the amount of water during the operation treatment operation , and the supply is continued even after the water is full.
A method has been adopted in which the water supply to the treatment tank and the washing of the filter medium layer are completed in a short time. After the cleaning is finished, the operation processing Misao
It is shifting to work .
【0004】[0004]
【発明が解決しようとする課題】本発明は、処理槽内に
濾材を充填した水処理・濾過装置において、濾材の洗浄
操作から通常の処理操作に移行する前の処理槽内に水を
供給する改善された方法を提供するものである。SUMMARY OF THE INVENTION According to the present invention, in a water treatment / filtration device in which a filter medium is filled in a treatment tank, water is supplied into the treatment tank before the filter medium is shifted from a washing operation to a normal treatment operation. It provides an improved method.
【0005】[0005]
【課題を解決するための手段】上記課題を解決する本発
明は、圧縮性の浮遊濾材を充填し、該濾材の上部への流
出防止のための上部流出防止手段を有し、運転停止後、
濾材の洗浄に当たり、一部排水・空気洗浄・排水・給水
・空気洗浄からなる濾材の洗浄操作を一回以上実施し、
通水洗浄し、運転処理操作に移る水処理・濾過装置の濾
材洗浄方法において、前記通水洗浄時、(1)運転処理
操作時の処理水量より多量の洗浄用水を供給し、その供
給を浮上する濾材層の上部が上部流出防止手段に到達す
る直前又は直後に停止し、その後運転処理操作時の処理
水量で通水洗浄を継続する、(2)運転処理操作時と同
じ処理水量で供給する際に、濾材層の下部から空気を一
定時間供給して濾材を攪拌する、あるいは(3)前記通
水洗浄時の多量の洗浄用水の供給を停止した後、運転処
理操作時と同じ処理水量で供給する前に濾材層の下部か
ら空気を一定時間供給して濾材を攪拌することを特徴と
する濾材洗浄方法を包含するものである。尚、以下の説
明において、「通常」としているものは「運転処理操
作」のことである。 The present invention for solving the above problems SUMMARY OF THE INVENTION fills the floating filter media compressibility, have a top outflow preventing section for outflow prevention to the top of filtrate material, after stopping the operation,
Partial drainage / air cleaning / drainage / water supply when cleaning filter media
・ Perform washing operation of the filter media consisting of air washing at least once,
Water treatment and filtration of water treatment / filtration equipment for washing and passing to operation processing
In the material washing method , (1) operation processing
Supply a larger amount of cleaning water than the amount of water treated during operation, and
The upper part of the filter medium layer that floats the feed reaches the upper outflow prevention means.
Stop immediately before or immediately after,
Continue flushing with water flow. (2) Same as during operation
When supplying the same amount of treated water, remove air from the bottom of the filter media layer.
Stir the filter media by supplying it for a fixed time, or (3)
After stopping the supply of a large amount of cleaning water during water cleaning,
Before supplying with the same amount of treated water as during the
The air is supplied for a certain period of time to stir the filter media.
The method includes a method of washing a filter medium. The following theory
In the following, what is referred to as "normal"
Work ".
【0006】以下、本発明を詳細に説明する。Hereinafter, the present invention will be described in detail.
【0007】本発明においては、濾材層の圧損により圧
縮される浮遊濾材を使用する水処理・濾過装置に効果的
に使用される浮遊濾材の洗浄方法を提供する。ここで使
用される浮遊濾材としては、エチレン、プロピレンなど
に他の単量体を共重合させた非結晶性の樹脂、或いはポ
リエチレン、ポリプロピレンを混合させた樹脂などを発
泡させて得られた浮遊濾材が挙げられる。The present invention provides a method for cleaning a floating filter medium which is effectively used in a water treatment / filtration apparatus using a floating filter medium compressed by pressure loss of a filter medium layer. The floating filter medium used here is a non-crystalline resin obtained by copolymerizing ethylene, propylene or the like with another monomer, or a resin obtained by foaming a resin obtained by mixing polyethylene or polypropylene. Is mentioned.
【0008】次に本発明の洗浄方法について図面を参照
して説明する。Next, the cleaning method of the present invention will be described with reference to the drawings.
【0009】図1は、一連の濾材洗浄操作の工程を示
す。上向流濾過装置に、圧縮性の浮遊濾材を1m充填
し、一定時間濾過操作を行った。その後図1に示す工程
(1)〜(7)の一連の濾材洗浄操作を行い、工程
(8)で給水を洗浄用水ポンプより通常の通水速度の3
倍の量で開始した。浮遊濾材層の上部が上部流出防止手
段の位置に達した時点で給水を停止して、通常の水量で
被処理水を流す。この出口の処理水は再び被処理水の受
け槽に戻される。この操作を処理水の水質の回復の状況
を観察しながら継続し、その後処理水を通常の送水に切
り替える。また、同じく濾材層の上部が上部流出防止手
段に到達する直前または直後に、水の供給を継続しなが
ら、または停止した状態で、濾材層の下部より空気を一
定時間供給して濾材層を攪拌し、その後再度水を供給し
出口の処理水を被処理水の受け槽に戻す。この操作を処
理水の水質の回復の状況を観察しながら継続し、その後
処理水を通常の送水に切り替える。FIG. 1 shows the steps of a series of filter medium washing operations. The upward-flow filtration device was filled with 1 m of a compressible floating filter medium, and a filtration operation was performed for a certain period of time. Thereafter, a series of filter medium washing operations in steps (1) to (7) shown in FIG. 1 are performed, and in step (8), water is supplied from the washing water pump at a normal flow rate of 3 times.
Started with double volume. When the upper part of the floating filter medium layer reaches the position of the upper outflow prevention means, the supply of water is stopped, and the water to be treated flows with a normal amount of water. The treated water at this outlet is returned to the receiving tank for treated water again. This operation is continued while observing the state of recovery of the quality of the treated water, and then the treated water is switched to normal water supply. Also, immediately before or immediately after the upper part of the filter medium layer reaches the upper outflow prevention means, while supplying water or while stopping, air is supplied from the lower part of the filter medium layer for a certain time to stir the filter medium layer. Then, water is supplied again, and the treated water at the outlet is returned to the receiving water receiving tank. This operation is continued while observing the state of recovery of the quality of the treated water, and then the treated water is switched to normal water supply.
【0010】本発明において、処理槽内の濾材の上部流
出防止手段としては、材質を問わず強度を有する網、バ
ースクリーンまたは孔開き板等、濾材を槽内にとどめる
と共に被処理水および処理水等を支障なく通過させる構
造を有するものであればよい。またこれらの網、バース
クリーンまたは孔開き板等を組み合わせて使用すること
もできる。In the present invention, means for preventing the filter medium from flowing out of the treatment tank from the upper part include a net, a bar screen or a perforated plate having a high strength irrespective of the material. Any structure may be used as long as it has a structure that allows the passage of the same without any trouble. Further, these nets, bar screens, perforated plates, and the like can be used in combination.
【0011】本発明において、生物学的処理装置で、排
水中に曝気用空気を送風する好気性生物膜処理の方法に
対して用いることができる。また空気を吹き込まずに嫌
気性生物膜処理の方法に対しても用いることができる。
更に微細な懸濁物質を除去する濾過装置に対しても用い
ることができる。In the present invention, the present invention can be used in a biological treatment apparatus for an aerobic biofilm treatment method in which aeration air is blown into wastewater. It can also be used for anaerobic biofilm treatment without blowing air.
It can also be used for a filtration device for removing fine suspended substances.
【0012】本発明において、洗浄操作から通常の処理
操作に移行する前に処理槽内に供給される水および洗浄
用水は処理水または被処理水を用いることができる。In the present invention, treated water or water to be treated can be used as the water and cleaning water supplied to the treatment tank before shifting from the washing operation to the ordinary treatment operation.
【0013】本発明において、通常の水量より多量に供
給される洗浄用水は、通常の通水速度の1.5〜20
倍、好ましくは2〜10倍の量で供給される。また洗浄
用水は通常の被処理水の流れと同じ方向あるいは逆方向
に供給される。[0013] In the present invention, the washing water supplied in a larger amount than the usual amount of water is 1.5 to 20 times the normal flow rate.
It is supplied in an amount of 2 times, preferably 2 to 10 times. The cleaning water is supplied in the same direction as the flow of the normal water to be treated or in the opposite direction.
【0014】本発明において、濾材層下部より空気を一
定時間供給して濾材層の攪拌を行うが、その時間は、特
に制限はなく、濾材層の洗浄及び濾過層の均一化に効果
が十分あらわれるように適宜決定すれば良い。通常は、
0.5〜5分程度で十分である。In the present invention, the filter medium layer is stirred by supplying air from the lower part of the filter medium layer for a certain period of time, but the time is not particularly limited, and the effect of sufficiently washing the filter medium layer and making the filter layer uniform can be sufficiently obtained. May be appropriately determined as described above. Normally,
About 0.5 to 5 minutes is sufficient.
【0015】本発明において、処理槽内への給水の開始
・停止、流量の変更、空気攪拌の開始、攪拌継続時間な
どは処理槽内の水面位置を測定器によって検出しあるい
は時間設定装置により自動的に行うことができる。本発
明において処理槽出口の最初の処理水は再び被処理水の
受け槽に戻され、その後通常の送水に切り替えられる
が、この操作は処理水の水質状況を測定し、自動的にま
たは時間設定によって自動弁を作動させることにより行
うことができる。In the present invention, the start / stop of water supply to the processing tank, the change of flow rate, the start of air agitation, the duration of agitation, etc. are detected by measuring the water surface position in the processing tank by a measuring instrument or automatically by a time setting device. Can be done In the present invention, the first treated water at the outlet of the treated tank is returned to the receiving tank for treated water again, and then switched to normal water supply.This operation measures the quality of the treated water and automatically or automatically sets the time. This can be done by operating an automatic valve.
【0016】[0016]
【作用】本発明の濾材洗浄方法は、図1の工程(8)の
給水操作において、従来は処理槽内へ通常の水量より多
量の水を供給し、満水後もそのまま供給を続け、処理槽
への給水と濾材層の洗浄を短時間で完了させる方法が行
われており、従来方法では濾材として弾力性のあるもの
を使用すると濾材が上部流出防止手段に押さえつけられ
て圧縮し、圧損の急激な上昇を招き、その後の処理操作
に支障をきたすことがあるが、濾材が上部流出防止手段
に押さえつけられる前に多量の水による給水を中止する
ことによって濾材の圧縮を防ぐことができ、ひいては圧
損の急激な上昇を防止することができ、また、この時点
で濾材層下部より空気を供給し濾材層を攪拌し、層の厚
さを均一にすることによって部分的な処理効率の低下を
防ぐことができる。According to the filter medium washing method of the present invention, in the water supply operation of the step (8) in FIG. 1, conventionally, a larger amount of water is supplied into the treatment tank than the usual amount of water, and the supply is continued as it is after the water is full. In the conventional method, water is supplied to the filter and the washing of the filter medium layer is completed in a short time.In the conventional method, when an elastic filter medium is used, the filter medium is pressed against the upper outflow prevention means and compressed, causing a rapid drop in pressure loss. May cause troubles in the subsequent treatment operation.However, by stopping water supply with a large amount of water before the filter medium is pressed down by the upper outflow prevention means, compression of the filter medium can be prevented, and consequently pressure loss At this time, air is supplied from the lower part of the filter medium layer to agitate the filter medium layer to make the thickness of the layer uniform, thereby preventing a partial decrease in treatment efficiency. Can
【0017】[0017]
【実施例】以下、実施例により本発明を具体的に説明す
る。The present invention will be described below in detail with reference to examples.
【0018】実施例1 上向流濾過装置に、圧縮性の浮遊濾材を1m充填し、ア
オコなどの懸濁物質を20mg/l含む池水に凝集剤と
して硫酸バンド(Al2O3換算)を4mg/l添加して
一定時間濾過操作を行った。その後、図1に示す工程
(1)〜(7)の一連の濾材洗浄操作を行い、工程
(8)で給水を洗浄用水ポンプより通常の通水速度の3
倍の量で開始した。浮遊濾材層の上部が上部流出防止手
段の位置に達した時点で給水を停止し、通常の水量で被
処理水を流し、この出口の処理水は再び被処理水の受け
槽に戻した。この操作を10分間継続し、その後処理水
を通常の送水に切り替えた。この時の運転状況を表1に
示す。Example 1 An upflow filter was filled with 1 m of a compressible floating filter medium, and 4 mg of a sulfuric acid band (in terms of Al 2 O 3 ) was used as a flocculant in pond water containing 20 mg / l of a suspended substance such as algae. / L was added and a filtration operation was performed for a certain period of time. Thereafter, a series of filter medium washing operations in steps (1) to (7) shown in FIG. 1 are performed, and in step (8), water is supplied from the washing water pump at a normal flow rate of 3 times.
Started with double volume. When the upper part of the floating filter medium layer reached the position of the upper outflow prevention means, the water supply was stopped, the water to be treated was flowed with a normal amount of water, and the treated water at the outlet was returned to the receiving tank of the treated water again. This operation was continued for 10 minutes, after which the treated water was switched to normal water supply. Table 1 shows the operating conditions at this time.
【0019】実施例2 実施例1と同じ装置で、図1に示す工程(1)〜(7)
の一連の濾材洗浄操作を行い、工程(8)で給水を洗浄
用水ポンプより通常の通水速度の3倍の量で開始した。
浮遊濾材層の上部が上部流出防止手段の位置に達した時
点で給水を停止し、下部より空気を供給し濾材層を攪拌
して層の厚さを均一にした。その後、通常の水量で被処
理水を流し、この出口の処理水は再び被処理水の受け槽
に戻した。この操作を10分間継続し、その後処理水を
通常の送水に切り替えた。この時の運転状況を表1に示
す。Example 2 The same apparatus as in Example 1 was used, and the steps (1) to (7) shown in FIG.
Was performed, and in step (8), water supply was started from the washing water pump at an amount three times the normal flow rate.
Water supply was stopped when the upper part of the floating filter medium layer reached the position of the upper outflow prevention means, air was supplied from the lower part, and the filter medium layer was stirred to make the thickness of the layer uniform. Thereafter, the water to be treated was flowed with a normal amount of water, and the treated water at the outlet was returned to the receiving tank for the treated water again. This operation was continued for 10 minutes, after which the treated water was switched to normal water supply. Table 1 shows the operating conditions at this time.
【0020】比較例 実施例1と同じ装置で、図1に示す工程(1)〜(7)
の一連の濾材洗浄操作を行い、工程(8)で給水を洗浄
用水ポンプより通常の通水速度の3倍の量で開始した。
浮遊濾材層の上部が上部流出防止手段の位置に達した後
も給水を継続した。この時の出口の処理水は再び被処理
水の受け槽に戻した。この操作を3分間継続し、その後
処理水を通常の送水に切り替えた。この時の運転状況を
表1に示す。Comparative Example Using the same apparatus as in Example 1, steps (1) to (7) shown in FIG.
Was performed, and in step (8), water supply was started from the washing water pump at an amount three times the normal flow rate.
Water supply was continued even after the upper part of the floating filter medium layer reached the position of the upper outflow prevention means. The treated water at the outlet at this time was returned to the receiving tank of the treated water again. This operation was continued for 3 minutes, after which the treated water was switched to normal water supply. Table 1 shows the operating conditions at this time.
【0021】[0021]
【表1】 除去率継続期間:処理水中のSS濃度(懸濁濃度)がゼ
ロから1mg/lに達するまでの時間。 所定圧損到達時間:濾材層の圧損が5m水柱に達する時
間。[Table 1] Removal rate duration: Time required for the SS concentration (suspension concentration) in treated water to reach zero to 1 mg / l. Predetermined pressure drop reaching time: Time when the pressure drop of the filter medium layer reaches 5 m water column.
【0022】懸濁物質の除去率が1mg/lに到達した
時点もしくは圧損が5m水柱に到達した時点の何れか早
く到達した時点で濾材の洗浄を実施する。The filter medium is washed when the removal rate of the suspended substances reaches 1 mg / l or when the pressure loss reaches 5 m water column, whichever comes earlier.
【0023】[0023]
【発明の効果】本発明の濾材洗浄方法に依れば、濾材層
が上部流出防止手段に必要以上に押しつけられることが
防止できるので、濾材による圧損の過度の上昇が防止で
き、処理運転時間をのばすことができる。また、濾材層
の均一化によって部分的効率の低下を防ぐことができ
る。従って、濾材の洗浄の頻度を小さくでき、さらに洗
浄排水の量も減少できるという効果が得られる。According to the filter medium washing method of the present invention, it is possible to prevent the filter medium layer from being pressed more than necessary to the upper outflow prevention means, so that an excessive increase in pressure loss due to the filter medium can be prevented, and the processing operation time can be reduced. Can be extended. In addition, the uniformity of the filter medium layer can prevent a partial decrease in efficiency. Therefore, the effect of reducing the frequency of washing the filter medium and reducing the amount of washing wastewater can be obtained.
【図面の簡単な説明】[Brief description of the drawings]
【図1】本発明の濾材洗浄の工程を示す図である。FIG. 1 is a view showing a filter material washing step of the present invention.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平8−57210(JP,A) 特開 平8−10523(JP,A) (58)調査した分野(Int.Cl.6,DB名) B01D 24/00 - 24/48 B01D 29/00 - 29/96────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-8-57210 (JP, A) JP-A-8-10523 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) B01D 24/00-24/48 B01D 29/00-29/96
Claims (3)
部への流出防止のための上部流出防止手段を有し、運転
停止後、濾材の洗浄に当たり、一部排水・空気洗浄・排
水・給水・空気洗浄からなる濾材の洗浄操作を一回以上
実施し、通水洗浄し、運転処理操作に移る水処理・濾過
装置の濾材洗浄方法において、 前記通水洗浄時、運転処理操作時の処理水量より多量の
洗浄用水を供給し、 その供給を浮上する濾材層の上部が
上部流出防止手段に到達する直前又は直後に停止し、そ
の後運転処理操作時の水量で通水洗浄を継続する濾材洗
浄方法。1. A filled floating filter media compressibility, have a top outflow preventing section for outflow prevention to the top of filtrate material, operating
After the stop, when cleaning the filter media, partially drainage, air cleaning, drainage
Washing operation of filter media consisting of water, water supply and air washing at least once
Water treatment / filtration to be carried out, washing with water, and moving to operation treatment operation
In the filter medium washing method of the apparatus, in the above-mentioned water passing washing, a larger amount of water than the amount of water treated during the operation treatment operation.
A filter medium washing method in which washing water is supplied, and immediately before or immediately after the upper portion of the filter medium layer that floats the supply reaches the upper outflow prevention means, and then the water washing is continued with the amount of water at the time of the operation processing operation .
時と同じ水量で供給する際に、濾材層の下部から空気を
一定時間供給して濾材を攪拌することを特徴とする請求
項1記載の濾材洗浄方法。2. An operation processing operation at the time of said water washing.
When supplying with the same amount of water as at the time, air is
Claiming that the filter medium is stirred for a certain period of time.
Item 4. The method for cleaning a filter medium according to Item 1 .
を停止した後、運転処理操作時と同じ水量で供給する前
に濾材層の下部から空気を一定時間供給して濾材を攪拌
することを特徴とする請求項1記載の濾材洗浄方法。3. A supply of a large amount of washing water at the time of said water washing.
Before stopping and supplying the same amount of water as during the operation processing operation
Air is supplied from the bottom of the filter medium layer for a certain time to stir the filter medium
2. The method for cleaning a filter medium according to claim 1, wherein
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7144554A JP2820384B2 (en) | 1995-06-12 | 1995-06-12 | Method of cleaning filter media for water treatment / filtration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7144554A JP2820384B2 (en) | 1995-06-12 | 1995-06-12 | Method of cleaning filter media for water treatment / filtration equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09822A JPH09822A (en) | 1997-01-07 |
| JP2820384B2 true JP2820384B2 (en) | 1998-11-05 |
Family
ID=15364984
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7144554A Expired - Lifetime JP2820384B2 (en) | 1995-06-12 | 1995-06-12 | Method of cleaning filter media for water treatment / filtration equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2820384B2 (en) |
-
1995
- 1995-06-12 JP JP7144554A patent/JP2820384B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09822A (en) | 1997-01-07 |
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