JPH0584495A - Device for waste water treatment and cleaning method thereof - Google Patents

Device for waste water treatment and cleaning method thereof

Info

Publication number
JPH0584495A
JPH0584495A JP3247884A JP24788491A JPH0584495A JP H0584495 A JPH0584495 A JP H0584495A JP 3247884 A JP3247884 A JP 3247884A JP 24788491 A JP24788491 A JP 24788491A JP H0584495 A JPH0584495 A JP H0584495A
Authority
JP
Japan
Prior art keywords
valve
air
support member
tank
pipe
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.)
Pending
Application number
JP3247884A
Other languages
Japanese (ja)
Inventor
Kyozo Kawachi
内 恭 三 河
Masahiko Tsutsumi
正 彦 堤
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP3247884A priority Critical patent/JPH0584495A/en
Publication of JPH0584495A publication Critical patent/JPH0584495A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)

Abstract

PURPOSE:To provide a device for waste water treatment possible to effectively and simply execute cleaning work. CONSTITUTION:The treating vessel 10, the upper supporting member 21 and lower supporting member 22 provided in the treating vessel 10 and the filtration medium 23 held between the upper supporting member 21 and the lower supporting member 23 are provided. The air jetting nozzle 40 having the air opening and closing valve 41 is provided downward of the lower supporting member 22. The 1st discharge pipe 31 having the 1st opening and closing valve 31a is connected to right above the upper supporting member 21 and the 2nd discharge pipe 34 having the 2nd opening and closing valve 34a is connected to the bottom of the treating vessel 10.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は生物膜を用いた廃水処理
装置およびその洗浄方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment apparatus using a biofilm and a cleaning method therefor.

【0002】[0002]

【従来の技術】従来の廃水処理装置について、図3によ
り説明する。廃水管1によって処理槽2内に流入する廃
水は、処理槽2内に設けられた瀘材3の表面に形成され
た生物膜によって浄化される。続いて、浄化された処理
水は、貯留槽4内に貯留された後、放流される。
2. Description of the Related Art A conventional wastewater treatment apparatus will be described with reference to FIG. The wastewater flowing into the treatment tank 2 through the wastewater pipe 1 is purified by the biofilm formed on the surface of the filter material 3 provided in the treatment tank 2. Subsequently, the purified treated water is stored in the storage tank 4 and then discharged.

【0003】処理槽2内の処理が所定時間行なわれた場
合、処理槽2内の洗浄を行なう。すなわち、処理槽2と
貯留槽4との間の開閉弁7を閉じ、排水弁6を開とす
る。続いて逆洗ポンプ5を駆動して処理槽2内を逆洗
し、廃水処理で過剰に成長した生物膜を排水弁6から排
水槽8に排出している。
When the processing in the processing tank 2 is performed for a predetermined time, the inside of the processing tank 2 is cleaned. That is, the on-off valve 7 between the processing tank 2 and the storage tank 4 is closed, and the drain valve 6 is opened. Subsequently, the backwash pump 5 is driven to backwash the inside of the treatment tank 2, and the biofilm excessively grown in the wastewater treatment is discharged from the drain valve 6 to the drain tank 8.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、従来の
廃水処理装置においては、洗浄時において処理槽2から
排出される洗浄排水の量が増加するため、大きな排水槽
8を設けなければならないという問題がある。また、洗
浄時に貯留槽4から処理槽2内に送り込む洗浄水量が多
くなるため、逆洗ポンプ5の動力を大きくする必要があ
る。
However, in the conventional wastewater treatment apparatus, since the amount of cleaning wastewater discharged from the processing tank 2 at the time of cleaning increases, there is a problem that a large drain tank 8 must be provided. is there. Further, since the amount of cleaning water sent from the storage tank 4 into the processing tank 2 during cleaning increases, it is necessary to increase the power of the backwash pump 5.

【0005】本発明はこのような点を考慮してなされも
のであり、効率良くかつ簡単に洗浄することができる廃
水処理装置およびその洗浄方法を提供することを目的と
する。
The present invention has been made in view of the above points, and an object of the present invention is to provide a wastewater treatment apparatus and a method for washing the same, which can be washed efficiently and easily.

【0006】[0006]

【課題を解決するための手段】本発明は、廃水処理を行
なう処理槽と、この処理槽内に設けられた上部支持材お
よび下部支持材と、これら上部支持材と下部支持材との
間に保持され表面に生物膜が形成された瀘材とを備え、
前記処理槽内の下部支持材下方に空気開閉弁を有する空
気吹出ノズルを設け、前記処理槽の上部支持材直上に第
1開閉弁を有する第1排水管を接続し、前記処理槽の底
部に第2開閉弁を有する第2排水管を接続したことを特
徴とする廃水処理装置および処理槽への廃水の流入を停
止し、空気開閉弁を開として空気吹出ノズルから空気を
供給しながら第1開閉弁を開として瀘材の上方から第1
排水管を介して排水し、続いて空気開閉弁を閉とした
後、第2開閉弁を開として瀘材の下方から第2排水管を
介して排水することを特徴とする請求項1記載の廃水処
理装置の洗浄方法である。
According to the present invention, there is provided a treatment tank for treating wastewater, an upper support member and a lower support member provided in the treatment tank, and a space between the upper support member and the lower support member. With a filter material that is retained and has a biofilm formed on its surface,
An air blowing nozzle having an air opening / closing valve is provided below the lower support member in the treatment tank, a first drain pipe having a first opening / closing valve is connected directly above the upper support material of the treatment tank, and the bottom portion of the treatment tank is connected. A second drain pipe having a second on-off valve is connected to the waste water treatment apparatus and the inflow of waste water to the treatment tank is stopped, and the air on-off valve is opened to supply air from the air blowing nozzle. Open the on-off valve and open from above the filter
The water is drained through a drain pipe, the air on-off valve is subsequently closed, and then the second on-off valve is opened to drain the water from below the filter through the second drain pipe. It is a method of cleaning a wastewater treatment device.

【0007】[0007]

【作用】本実施例によれば、逆洗時空気開閉弁を開と
し、空気吹出ノズルから空気を提供しながら第1開閉弁
を開とすることにより、瀘材の上方から比較的大きな剥
離生物膜を第1排水管から排出し、続いて、空気開閉弁
を閉とした後、第2開閉弁を開とすることにより、瀘材
の下方から微細の剥離生物膜を第2排水管から排出する
ことができる。
According to the present embodiment, the air opening / closing valve is opened during backwashing, and the first opening / closing valve is opened while air is being supplied from the air blowing nozzle. The membrane is discharged from the first drainage pipe, then the air opening / closing valve is closed, and then the second opening / closing valve is opened to discharge the finely separated biofilm from the bottom of the filter material from the second drainage pipe. can do.

【0008】[0008]

【実施例】以下、図面を参照して本発明の実施例につい
て説明する。図1および図2は本発明の実施例を示す図
である。図1において、廃水処理装置は、廃水を処理す
る処理槽10を備え、処理槽10には廃水弁37を有す
る廃水管36が接続されている。また、処理槽10内に
は上方および下方に液絡部12,13を形成する隔壁1
4が配設され、隔壁14の一方側に酸素溶解部15、他
方側に反応部16が形成されている。また酸素溶解部1
5内の隔壁14の下端よりもやや上方に散気管17が配
設され、この散気管17は調整弁18を介して加圧空気
管19に接続されている。
Embodiments of the present invention will be described below with reference to the drawings. 1 and 2 are views showing an embodiment of the present invention. In FIG. 1, the wastewater treatment apparatus includes a treatment tank 10 for treating wastewater, and a wastewater pipe 36 having a wastewater valve 37 is connected to the treatment tank 10. Further, in the processing tank 10, partition walls 1 that form liquid junctions 12 and 13 above and below are formed.
4 are provided, and the oxygen dissolving portion 15 is formed on one side of the partition wall 14, and the reaction portion 16 is formed on the other side. Also, the oxygen dissolution part 1
An air diffuser 17 is arranged slightly above the lower end of the partition wall 14 in the container 5, and the air diffuser 17 is connected to a pressurized air pipe 19 via a regulating valve 18.

【0009】他方、反応部16内には多数の開口部21
aを有する上部支持材21と、多数の開口22aを有す
る下部支持材22とが配設され、これら上部支持材21
と下部支持材22との間に瀘材23が充填されている。
瀘材23としては、比重が1よりも大きいプラスチック
の成形材が用いられ、瀘材23の充填体積は上部支持材
21と下部支持材22の間の空間容積の50〜80%と
なっている。
On the other hand, a large number of openings 21 are formed in the reaction section 16.
The upper support member 21 having a and the lower support member 22 having a large number of openings 22a are arranged.
A filter material 23 is filled between the lower support member 22 and the lower support member 22.
A plastic molding material having a specific gravity of more than 1 is used as the filter 23, and the filling volume of the filter 23 is 50 to 80% of the space volume between the upper support 21 and the lower support 22. ..

【0010】また上部支持材21の直上の処理槽10槽
壁には第1排水口30が設けられ、この第1排水口30
には第1開閉弁31aを有する第1排水管31が接続さ
れ、第1排水管31は排水管32に接続されている。ま
た処理槽10の底部には第2排水口33が設けられ、こ
の第2排水口33には第2開閉弁34aを有する第2排
水管34が接続され、第2排水管34は排水管32に接
続されている。
A first drainage port 30 is provided on the wall of the treatment bath 10 directly above the upper supporting member 21, and the first drainage port 30 is provided.
Is connected to a first drain pipe 31 having a first opening / closing valve 31 a, and the first drain pipe 31 is connected to a drain pipe 32. A second drainage port 33 is provided at the bottom of the processing tank 10, and a second drainage pipe 34 having a second opening / closing valve 34a is connected to the second drainage port 33, and the second drainage pipe 34 is the drainage pipe 32. It is connected to the.

【0011】処理槽10内であって下部支持材22の下
方には、空気吹出ノズル40が設けられ、この空気吹出
ノズル40は空気開閉弁41および調整弁42を介して
加圧空気管19に接続されている。また下部支持材22
と空気吹出ノズル40との間には、処理水管43の一端
44が開口し、処理水管43の他端は液位調整管46を
介して放流管47に接続されている。
An air blowing nozzle 40 is provided in the processing tank 10 and below the lower support member 22, and the air blowing nozzle 40 is connected to the pressurized air pipe 19 via an air opening / closing valve 41 and a regulating valve 42. Has been done. Also, the lower support member 22
The one end 44 of the treated water pipe 43 is opened between the and the air blowing nozzle 40, and the other end of the treated water pipe 43 is connected to a discharge pipe 47 via a liquid level adjusting pipe 46.

【0012】本実施例において、廃水管38から処理槽
10へ流入する廃水の流入量をQL (m3 /h)、散気
管17の通気量をQG1(N−m3 /h)、空気吹出ノズ
ル40の通気量をQG2(N−m3 /h)、処理槽10の
有効容積をV(m3/h)とした場合、V/QL すなわ
ち処理槽10における廃水の水理学的滞留時間HRTは
0.5〜10(h)、QG1の容積倍率すなわちQG1/V
は0.01〜1(h-1)、QG2の容積倍率すなわちQG2
/Vは0.1〜10(h-1)程度に設定されている。
[0012] In this example, the inflow of waste water flowing from the waste water pipe 38 to the treatment tank 10 Q L (m 3 / h ), the ventilation amount of diffusion pipe 17 Q G1 (N-m 3 / h), If the aeration amount of air discharge nozzles 40 Q G2 (N-m 3 / h), the effective volume of the processing tank 10 was set to V (m 3 / h), V / Q L i.e. hydraulics wastewater in the treatment tank 10 retention time HRT is 0.5 to 10 (h), the volume ratio of Q G1 i.e. Q G1 / V
The 0.01~1 (h -1), Q volume ratio i.e. Q of G2 G2
/ V is set to about 0.1 to 10 (h -1 ).

【0013】次にこのような構成からなる本実施例の作
用について説明する。
Next, the operation of this embodiment having such a configuration will be described.

【0014】まず、通常運転時、廃水弁37を開とし、
廃水管36から処理槽10内に廃水が流入する。同時に
調整弁18を開として散気管17から空気を供給する。
この場合、散気管17からの空気により生じた気泡のエ
アリフトによって廃水が循環し、廃水は瀘材23内を降
下する。瀘材23の表面には、生物膜が形成されてお
り、廃水はこの生物膜により浄化され、処理水となって
処理水管43から放流管47を経て外方へ放流される。
First, during normal operation, the waste water valve 37 is opened,
Waste water flows into the treatment tank 10 from the waste water pipe 36. At the same time, the adjusting valve 18 is opened to supply air from the air diffuser 17.
In this case, the wastewater is circulated by the air lift of bubbles generated by the air from the air diffuser 17, and the wastewater descends in the filter 23. A biofilm is formed on the surface of the filter material 23, and the wastewater is purified by this biofilm and becomes treated water, which is discharged from the treated water pipe 43 to the outside through the discharge pipe 47.

【0015】次に、処理槽10における廃水処理が進行
すると、処理槽10内の洗浄を次のように行なう(図2
参照)。まず廃水弁37を閉じ、処理槽10内への廃水
の流入を停止する。続いて、空気弁41を開として空気
吹出ノズル40から気泡を噴出する。この場合、処理槽
10内の瀘材23は、その占有体積が増加する。そして
瀘材23は上部支持材21まで達し、気泡によるせん断
作用を受ける。このような気泡のせん断作用によって、
瀘材23の表面に付着した過剰の生物膜が剥離し、比較
的大きな剥離生物膜は液面35近傍に集まる。他方、微
細化した剥離生物膜は処理槽10内を均一に流動する。
Next, when the wastewater treatment in the treatment tank 10 progresses, the inside of the treatment tank 10 is cleaned as follows (FIG. 2).
reference). First, the waste water valve 37 is closed to stop the inflow of waste water into the processing tank 10. Then, the air valve 41 is opened to eject the bubbles from the air ejection nozzle 40. In this case, the volume of the filter 23 in the processing tank 10 increases. Then, the filter material 23 reaches the upper support material 21 and is subjected to the shearing action of the bubbles. By the shearing action of such bubbles,
Excessive biofilm attached to the surface of the filter material 23 is peeled off, and a relatively large peeled biofilm gathers near the liquid surface 35. On the other hand, the micronized separated biofilm uniformly flows in the processing tank 10.

【0016】時間t1 (5〜10分程度)経過後に、時
間t2 (5〜10分程度)の間、第1開閉弁31aを開
とする。そして、上部支持材21の上方に存在する比較
的大きな剥離生物膜を、第1排水管31および排水管3
2を介して外方へ排出する。ここまでの洗浄作業を第1
の工程と呼ぶ。
After the time t 1 (about 5 to 10 minutes) has elapsed, the first on-off valve 31a is opened for the time t 2 (about 5 to 10 minutes). Then, the relatively large detached biofilm existing above the upper support member 21 is replaced with the first drain pipe 31 and the drain pipe 3.
Discharge to the outside via 2. The cleaning work up to here is the first
Called the process of.

【0017】次に洗浄作業の第2の工程を行なう。すな
わち、第1開閉弁31aを閉とし、同時に空気開閉弁4
1を閉として空気吹出ノズル40からの気泡の噴出を停
止し、微細化した剥離生物膜を沈降させる。時間t
3 (10〜30分程度)経過の後に、第2開閉弁34a
を時間t4 (1〜10分程度)だけ開として、処理槽1
0の底部近傍に体積した微細の剥離生物膜を第2排水管
34および排水管32を介して外方へ排出する。このよ
うにして、洗浄の第2の工程が終了する。
Next, the second step of the cleaning work is performed. That is, the first opening / closing valve 31a is closed, and at the same time, the air opening / closing valve 4a is closed.
1 is closed to stop the ejection of bubbles from the air blowing nozzle 40, and the finely separated biofilm is settled. Time t
After 3 (about 10 to 30 minutes), the second on-off valve 34a
Is opened for a time t 4 (about 1 to 10 minutes), and the treatment tank 1
The finely separated biofilm deposited in the vicinity of the bottom of 0 is discharged to the outside through the second drain pipe 34 and the drain pipe 32. In this way, the second step of cleaning is completed.

【0018】この間、調整弁18を開としておいてもよ
い。調整弁18を開とした場合、液面35が隔壁14の
上端よりも低下するので、処理槽10内に循環流が生じ
ることはない。このため、微細化した生物膜の沈降を阻
害することはない。
During this time, the adjusting valve 18 may be left open. When the adjustment valve 18 is opened, the liquid surface 35 is lower than the upper end of the partition wall 14, so that no circulating flow occurs in the processing tank 10. Therefore, it does not hinder the sedimentation of the finely divided biofilm.

【0019】このような洗浄作業が終了した後、第1開
閉弁31a、第2開閉弁34aおよび空気開閉弁41を
閉とし、廃水弁37を開として通常運転を再開する。
After such cleaning work is completed, the first opening / closing valve 31a, the second opening / closing valve 34a and the air opening / closing valve 41 are closed, and the waste water valve 37 is opened to resume the normal operation.

【0020】以上説明したように、本実施例によれば、
上下に液絡部12,13を形成する隔壁14によって処
理槽10を仕切り、酸素溶解部15と反応部16を設け
たので、処理槽10内に適度の循環流を発生させ撹拌を
行なうことができる。このため瀘材23に付着した生物
膜を均一化し廃水の処理効率を高めることができる。ま
た、瀘材23の充填量を上部および下部支持材21およ
び22の間の空間容積の50〜80%としたので、洗浄
時において瀘材23の占有体積を増加させ均一な洗浄作
業を行なうことができる。さらに、散気管17から常時
通気することによって、洗浄時においても適度の溶存酸
素の供給を行なうことができる。
As described above, according to this embodiment,
Since the processing tank 10 is partitioned by the partition wall 14 which forms the liquid junctions 12 and 13 on the upper and lower sides and the oxygen dissolving section 15 and the reaction section 16 are provided, it is possible to generate an appropriate circulating flow in the processing tank 10 to perform stirring. it can. Therefore, the biological film attached to the filter material 23 can be made uniform and the treatment efficiency of wastewater can be improved. Moreover, since the filling amount of the filter material 23 is set to 50 to 80% of the space volume between the upper and lower support members 21 and 22, it is possible to increase the occupied volume of the filter material 23 at the time of cleaning and perform uniform cleaning work. You can Further, by constantly ventilating from the air diffuser 17, it is possible to appropriately supply dissolved oxygen even during cleaning.

【0021】なお、上記実施例において瀘材23として
比重が1よりも大きなプラスチックを用いた例を示した
が、これに限らず比重が1よりも小さいプラスチックや
内部に独立気泡を持つ焼成物などの浮上性の材料を使用
することも可能である。この際に比重もしくはかさ比重
を例えば0.95〜0.99にすることにより洗浄時に
瀘材23の占有体積を容易に増加させ、瀘材23の流動
性を高めることができる。
In the above embodiment, an example in which a plastic having a specific gravity of more than 1 is used as the filter material 23 is not limited to this, but a plastic having a specific gravity of less than 1 or a fired product having closed cells inside, etc. It is also possible to use a floatable material. At this time, by setting the specific gravity or bulk specific gravity to, for example, 0.95 to 0.99, the volume occupied by the filter material 23 can be easily increased during cleaning, and the fluidity of the filter material 23 can be enhanced.

【0022】[0022]

【発明の効果】以上説明したように、本発明によれば、
洗浄時、瀘材の上方から比較的大きな剥離生物膜を第1
排水管から排出し、瀘材の下方から微細の剥離生物膜を
第2排水管から排出することにより、瀘材に付着した生
物膜を効果的に除去排出することができる。また従来の
ように多量の洗浄水量を使用しないので、大きな排水槽
を設けたり、大きな逆洗ポンプを設ける必要がなくな
る。このため簡単かつ低コストで洗浄作業を行なうこと
ができる。
As described above, according to the present invention,
When cleaning, first remove a relatively large biofilm from above the filter material.
By discharging from the drainage pipe and discharging the finely separated biofilm from below the filter material from the second drainage pipe, the biofilm attached to the filter material can be effectively removed and discharged. Moreover, since a large amount of washing water is not used unlike the conventional case, it is not necessary to provide a large drain tank or a large backwash pump. Therefore, the cleaning operation can be performed easily and at low cost.

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

【図1】本発明による廃水処理装置の一実施例を示す概
略系統図
FIG. 1 is a schematic system diagram showing an embodiment of a wastewater treatment apparatus according to the present invention.

【図2】廃水処理装置の洗浄作用を示す図FIG. 2 is a diagram showing a cleaning action of a wastewater treatment device.

【図3】従来の廃水処理装置を示す概略系統図FIG. 3 is a schematic system diagram showing a conventional wastewater treatment device.

【符号の説明】[Explanation of symbols]

10 処理水槽 21 上部支持材 22 下部支持材 23 瀘材 31 第1排水管 31a 第1開閉弁 34 第2排水管 34a 第2開閉弁 40 空気吹出ノズル 41 空気開閉弁 10 Treated Water Tank 21 Upper Support Material 22 Lower Support Material 23 Filter Material 31 First Drain Pipe 31a First Open / Close Valve 34 Second Drain Pipe 34a Second Open / Close Valve 40 Air Blowing Nozzle 41 Air Open / Close Valve

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】廃水処理を行なう処理槽と、この処理槽内
に設けられた上部支持材および下部支持材と、これら上
部支持材と下部支持材との間に保持され表面に生物膜が
形成された瀘材とを備え、前記処理槽内の下部支持材下
方に空気開閉弁を有する空気吹出ノズルを設け、前記処
理槽の上部支持材直上に第1開閉弁を有する第1排水管
を接続し、前記処理槽の底部に第2開閉弁を有する第2
排水管を接続したことを特徴とする廃水処理措置。
1. A treatment tank for treating wastewater, an upper support member and a lower support member provided in the treatment tank, and a biofilm formed on the surface of the upper support member and the lower support member which are held between the upper support member and the lower support member. And a first drain pipe having a first on-off valve directly above the upper support member of the processing tank is connected to the upper support member of the processing tank. And a second opening / closing valve at the bottom of the processing tank
A wastewater treatment measure characterized by connecting a drainage pipe.
【請求項2】処理槽への廃水の流入を停止し、空気開閉
弁を開として空気吹出ノズルから空気を供給しながら第
1開閉弁を開として瀘材の上方から第1排水管を介して
排水し、続いて空気開閉弁を閉とした後、第2開閉弁を
開として瀘材の下方から第2排水管を介して排水するこ
とを特徴とする請求項1記載の廃水処理装置の洗浄方
法。
2. The inflow of waste water to the treatment tank is stopped, the air on-off valve is opened and air is supplied from an air-blowing nozzle while the first on-off valve is opened to open the filter from above the filter through the first drain pipe. 2. The cleaning of a wastewater treatment device according to claim 1, wherein the wastewater treatment device is drained, and subsequently the air on-off valve is closed, and then the second on-off valve is opened to drain the water from below the filter through the second drainage pipe. Method.
JP3247884A 1991-09-26 1991-09-26 Device for waste water treatment and cleaning method thereof Pending JPH0584495A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3247884A JPH0584495A (en) 1991-09-26 1991-09-26 Device for waste water treatment and cleaning method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3247884A JPH0584495A (en) 1991-09-26 1991-09-26 Device for waste water treatment and cleaning method thereof

Publications (1)

Publication Number Publication Date
JPH0584495A true JPH0584495A (en) 1993-04-06

Family

ID=17170033

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3247884A Pending JPH0584495A (en) 1991-09-26 1991-09-26 Device for waste water treatment and cleaning method thereof

Country Status (1)

Country Link
JP (1) JPH0584495A (en)

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