[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JPS6377508A - Moving bed type water treating apparatus - Google Patents

Moving bed type water treating apparatus

Info

Publication number
JPS6377508A
JPS6377508A JP61222855A JP22285586A JPS6377508A JP S6377508 A JPS6377508 A JP S6377508A JP 61222855 A JP61222855 A JP 61222855A JP 22285586 A JP22285586 A JP 22285586A JP S6377508 A JPS6377508 A JP S6377508A
Authority
JP
Japan
Prior art keywords
water
washing
sand
granular
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.)
Pending
Application number
JP61222855A
Other languages
Japanese (ja)
Inventor
Masao Fushiki
伏木 将生
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.)
AKASHI JIYOUKA KK
Original Assignee
AKASHI JIYOUKA KK
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 AKASHI JIYOUKA KK filed Critical AKASHI JIYOUKA KK
Priority to JP61222855A priority Critical patent/JPS6377508A/en
Publication of JPS6377508A publication Critical patent/JPS6377508A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D24/00Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/46Regenerating the filtering material in the filter
    • B01D24/4668Regenerating the filtering material in the filter by moving the filtering element
    • B01D24/4689Displacement of the filtering material to a compartment of the filtering device for regeneration

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To continuously obtain clarified water without performing the replacement and regeneration of granular mediums and a backwashing process by separating the fluidized granular mediums from raw water and treated water to perform washing and separation and circulating them and arbitrarily adjusting both the circulated amount of the above-mentioned mediums and the discharged amount of washing water. CONSTITUTION:Granular mediums 10 are passed through holes (a), (b) opened to a control cylinder 6 for the circulated amount thereof and fed to an aeration scrubber 14 and a cylindrical washing chamber 2 and furthermore lifted with a sand lifter 3 while being subjected to secondary sand washing and reached to a solid-liquid separator 15 equipped with a conical type screen cylinder 4 and furthermore subjected to tertiary sand washing with sprayers 5 and uniformly fall on the upper layer part of a granular medium layer, regenerated and circulated. On the other hand, tertiary washing water and sand-lifting water are reached to the lower part of the sand lifter 3 through a washing/pumping return pipe 16 from the solid-liquid separator 15 and one part thereof is again lifted as sand-lifting water and one part is passed through the control holes (a), (b) and treated together with raw water and excess amount of water is discharged as primary washing water through a drainage hole (c) provided on a controller 7 of washing water and drainage.

Description

【発明の詳細な説明】 この発明は、移動床式水処理装置に関するもので、処理
すべき原水を洗浄された粒状媒体層と対向流をなしなが
ら、上向流で連続してろ過及び生物処理して、清澄水を
得るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a moving bed water treatment device, in which raw water to be treated is continuously filtered and biologically treated in an upward flow while forming a counterflow with a washed granular media layer. Then, clear water is obtained.

(1)産業上の利用分野 この発明は、移床する粒状媒体が常に3重に洗浄さ九な
がら循環するため、下水等の3次処理、産業廃水処理、
プール水のろ過等は勿論、工業用水道、上水道のろ過装
置並びに処理装置として幅広い分野で活用できるもので
ある。
(1) Industrial application field This invention is useful for tertiary treatment of sewage, industrial wastewater treatment,
It can be used in a wide range of fields, not only for filtration of pool water, but also as a filtration device and treatment device for industrial water supply and water supply.

(2)従来の技術 これまで一般に1粒状媒体の曝気槽下部での曝気循環に
よる上澄水装置や固定ろ床式ろ過装置及び、活性炭吸着
’3A置等で原水の生物処理又はろ過を行なう場合、大
がかりな粒状媒体循環洗浄装置や逆洗装置及びろ材の取
替え再生等大きな問題があった。
(2) Conventional technology Up until now, biological treatment or filtration of raw water has generally been carried out using a supernatant water system, a fixed filter bed type filtration system, an activated carbon adsorption '3A system, etc. using aeration circulation in the lower part of the aeration tank using a single granular medium. There were major problems such as large-scale granular media circulation cleaning equipment, backwashing equipment, and replacement and regeneration of filter media.

更に移動床式ろ過装置においても、粒状媒体の洗浄・分
離が困難で多量の洗浄水を嬰し、処理水中に洗浄水が混
入する問題を避けることができなかった。
Furthermore, even in the moving bed type filtration apparatus, it is difficult to wash and separate the granular media, and a large amount of washing water is generated, making it impossible to avoid the problem of mixing of the washing water into the treated water.

又更に、原水の水成・水質、処理水質及び粒状媒体の性
状によって、粒状媒体の循環量や洗浄水量の調節を行な
うことは困難で、従来の移動床式ろ過装置においても粒
状媒体の循環量は揚砂水量と比例して多くなり1粒状媒
体の循環量を大きくすると原水の処理水への混入や粒状
媒体の流出が生じ。
Furthermore, it is difficult to adjust the circulation amount of granular media and the amount of washing water depending on the composition and quality of raw water, the quality of treated water, and the properties of granular media. increases in proportion to the amount of pumped sand water, and if the circulating amount of granular media is increased, raw water will be mixed into the treated water and granular media will flow out.

揚砂水量を少なくすると洗砂機能が妨げられ、更に粒状
媒体の循環も妨げられて目づまり現象の問題があった。
When the amount of sand pumped water is reduced, the sand washing function is hindered, and the circulation of the granular medium is also hindered, resulting in the problem of clogging.

これら粒状媒体の循環量や洗浄水量の調節を行なうには
、例えば〈特公報 昭57−12434>のように外部
に大がかりな装置を設ける必要があった。
In order to adjust the amount of circulation of these granular media and the amount of washing water, it is necessary to provide a large-scale external device as disclosed in, for example, Japanese Patent Publication No. 57-12434.

(3)発明の解決しようとする問題 そこでこの発明の目的は、流動粒状媒体を原水及び処理
水と隔絶して洗浄・分離を行ない、循環させることによ
って処理水中への原水及び洗浄水の混入を防ぎ、流動粒
状媒体の循環量及び洗浄排水量を任意に調節することに
より原水の水質水量に合わせて所定の処理水質を得られ
るようにして1粒状媒体の入替え・再生や逆洗工程なし
で連続して清澄水を得ようとするものである。
(3) Problems to be Solved by the Invention Therefore, the purpose of the present invention is to isolate the fluidized granular medium from the raw water and treated water, wash and separate it, and circulate it to prevent the contamination of the raw water and the washed water into the treated water. By arbitrarily adjusting the circulation rate of the fluidized granular medium and the amount of washing water discharged, a predetermined treated water quality can be obtained according to the water quality and amount of raw water. The purpose is to obtain clear water using water.

(4)問題を解決する手段 このため本発明は、処理水中への原水及び洗浄水の混入
を防ぐために、流動粒状媒体層の中に隔絶された洗浄室
を設け、且つ固液分離装置を水面上部に設け、更に原水
性状や粒状媒体性状による粒状媒体循環量調節装置及び
洗浄排水量調節装置を設けることによって解決するもの
でその構成は、原水流入部及び原水分配装置を下方に有
し、且つ処理水流出部を上方に有する処理槽体に粒状媒
体を充填配備し、該粒状媒体層中心部に粒状媒体洗浄室
筒を設けてろ過及び処理層を形成し、該洗浄基筒中心部
には洗浄・揚砂水返送管と向応に設けられた揚砂管と、
洗浄水排水量調節管を装備し、下方には内側に粒状媒体
循環量調節筒及びその底部に散気装置を設けて1次洗砂
部を構成すると共に、該洗浄筒上部水面上に円錐状に形
成されたスクリーン筒体及び集水皿からなる固液分離装
置を設け、且つスプレーによる3次洗浄装置を設けたこ
とを特徴とする移動床式水処理装置である。
(4) Means for Solving the Problem Therefore, in order to prevent mixing of raw water and washing water into the treated water, the present invention provides an isolated washing chamber in the fluidized granular medium layer, and also sets the solid-liquid separator at the water surface. This problem can be solved by installing a granular medium circulation rate adjustment device and a cleaning drainage amount adjustment device according to the raw water properties and granular media properties in the upper part. A processing tank body having a water outflow portion above is filled with granular media, a granular media cleaning chamber cylinder is provided in the center of the granular media layer to form a filtration and processing layer, and a filtration and treatment layer is formed in the center of the cleaning base cylinder.・A sand pumping pipe installed in response to the pumping sand water return pipe,
It is equipped with a cleaning water drainage volume adjustment pipe, and a granular medium circulation volume adjustment pipe is provided inside at the bottom and an aeration device is provided at the bottom of the pipe to form the primary sand washing section. This is a moving bed type water treatment equipment characterized by being provided with a solid-liquid separation device consisting of a formed screen cylinder and a water collection dish, and a tertiary cleaning device using spray.

(5)作用 そこで本発明は、原水流入部を下方に有し且つ処理水流
出部を上方に有すると共に、流動する粒状媒体が充填配
備された処理槽と、該槽中心部に原水及び処理水と隔絶
された洗浄室を設け、該洗浄室内に粒状媒体循環量調節
装置を有し且つ曝気洗浄による1次洗砂装置・揚砂装置
・揚砂洗浄水返送装置及び洗浄水排水量調節装置を設け
て、その上部水面上に固液分離装置及び3次洗砂装置を
設けているため粒状媒体の洗浄及び揚砂循環は原水・処
理水と完全に隔絶され、曝気洗浄による1次洗砂、揚砂
管による2次洗砂、皿にスプレー水による3次洗砂の工
程を経るため粒状媒体は十分洗砂され再生循環される。
(5) Effect Therefore, the present invention provides a treatment tank which has a raw water inlet at the bottom and a treated water outlet at the top, and is filled with a flowing granular medium, and the center of the tank has the raw water and the treated water. A washing room is provided which is isolated from the washing room, and the washing room is equipped with a granular medium circulation rate adjusting device, and is also equipped with a primary sand washing device for aeration cleaning, a sand pumping device, a pumped sand washing water return device, and a washing water drainage amount adjusting device. Since a solid-liquid separation device and a tertiary sand washing device are installed above the upper water surface, the washing of granular media and the sand pumping circulation are completely isolated from the raw water and treated water, and the primary sand washing and sand pumping by aeration washing are completely isolated from the raw water and treated water. The granular media undergoes a second sand washing process using a sand pipe and a tertiary sand washing process using water sprayed onto a plate, so that the granular media is thoroughly washed and recycled.

一方揚砂水及び3次洗浄水は返送管を通って再び揚砂水
として、一部は1次洗浄水として装置外に排出され、一
部は原水と共に効果的に処理されるので、処理水中への
洗浄水の混入を防ぎながら流動粒状媒体を連続再生させ
て清澄水を得ることができる水処理装置である。
On the other hand, the sand pumping water and the tertiary washing water pass through the return pipe and become sand pumping water again, some of it is discharged outside the equipment as the primary washing water, and some of it is effectively treated together with the raw water, so that This is a water treatment device that can obtain clear water by continuously regenerating fluidized granular media while preventing washing water from entering the water.

(6)実施例 以下本発明の実施例につき図面を参照して説明すると、
第1図において流動粒状媒体10が充填配備された処理
槽1の下方に原水流入管11を有し、且つ処理水流出管
12を上方に有する処理槽体において、該槽中心部に洗
浄室筒2を設けて流動粒状媒体層を形成し1粒状媒体1
0は原水分配装置13の下方の槽円錐状底部と洗浄室筒
2によって形成される流動粒状媒体層最下部に第3図に
示すように洗浄室筒2下方周囲部に粒状媒体循環孔aを
設け、内側に粒状媒体循環量調節筒6を設けて、該調節
筒に開口された孔すとを通って洗浄室筒2の底部に設け
られた曝気洗砂装置14を経て洗浄室筒2内に更に、洗
浄・揚水返送管16と向応に設けられた揚砂装置3によ
り2次洗砂されながら揚砂され、処理水水面上の洗浄室
筒2上部に設けられた円錐型スクリーン筒体4を装備し
た固液分離装置15に達し、更にスプレー装置5 によ
る3次洗砂を経て固液分離装置15全周にわたって均等
に粒状媒体層の上層部に落下し、再生・循環させるもの
である。
(6) Examples Hereinafter, examples of the present invention will be explained with reference to the drawings.
In FIG. 1, in a processing tank body that has a raw water inflow pipe 11 below a processing tank 1 filled with a fluidized granular medium 10 and a treated water outflow pipe 12 above, a cleaning chamber cylinder is provided at the center of the tank. 2 to form a fluidized granular media layer, 1 granular media 1
As shown in FIG. A granular medium circulation amount adjusting tube 6 is provided inside the cleaning chamber tube 2, and the inside of the cleaning chamber tube 2 passes through a hole opened in the adjusting tube and passes through an aeration sand washing device 14 provided at the bottom of the cleaning chamber tube 2. Furthermore, sand is lifted while being subjected to secondary washing by the sand pumping device 3 provided in correspondence with the washing/pumping water return pipe 16, and the conical screen cylinder is provided at the top of the washing chamber cylinder 2 above the treated water surface. The sand reaches the solid-liquid separator 15 equipped with the solid-liquid separator 15, which is equipped with the solid-liquid separator 15, and is then subjected to tertiary sand washing by the spray device 5, and then falls evenly over the entire circumference of the solid-liquid separator 15 onto the upper layer of the granular media layer, where it is regenerated and circulated. .

他方3次洗浄水及び揚砂水は、固液分離装置15から返
送管16を通って揚砂装置3の下部に達し、一部は揚砂
水 として再び揚水され、一部は粒状媒体循環量調節孔
a、bを通って原水と共に効率的に処理され、余分の水
量は一次洗浄水となって洗浄室筒2上部に設けられた洗
浄水排水調節装!i!7に設けられた排水孔Cを通って
装置外に排出される。
On the other hand, the tertiary washing water and pumped sand water pass from the solid-liquid separator 15 through the return pipe 16 and reach the lower part of the sand pumping device 3, and some of them are pumped up again as pumped sand water, and some of them are used as part of the granular medium circulation amount. It passes through the adjustment holes a and b and is efficiently treated together with the raw water, and the excess water becomes primary cleaning water, which is then sent to the cleaning water drainage adjustment device installed at the top of the cleaning chamber cylinder 2! i! It is discharged to the outside of the device through a drainage hole C provided at 7.

従って揚砂装置3の空気供給装置と向応に設けられた回
転継手装置i!17により粒状媒体循環量、1glff
1Ill筒6をレバー6〃により回転して粒状媒体循環
量の調節を行ない、下部−次洗浄空気調節弁9及び揚砂
水空気調節弁8を調節することにより粒状媒体の洗砂度
を調節する。
Therefore, the rotary joint device i! is provided in correspondence with the air supply device of the sand lifting device 3! 17, the granular media circulation amount is 1glff
The granular medium circulation amount is adjusted by rotating the 1Ill cylinder 6 with the lever 6, and the degree of sand washing of the granular medium is adjusted by adjusting the lower-second cleaning air control valve 9 and the sand pumping water air control valve 8. .

(7)発明の効果 従って本発明は、流動粒状媒体の洗浄・分離・循環を原
水及び処理水と隔絶して行ない、洗浄工程を3回経てい
るため清浄な処理水が得られるため上水用としても使用
することができる。
(7) Effects of the Invention Accordingly, the present invention performs cleaning, separation, and circulation of fluidized granular media separately from raw water and treated water, and because the cleaning process is performed three times, clean treated water can be obtained, which can be used for drinking water. It can also be used as

更に粒状媒体の循環量を任意に調節できるため一循環量
を多くして急速ろ過装置としても使用でき、又循環量を
少なくして粒状媒体に生物膜を生成させて生物処理も行
なわせることができるもので、原水の水量・水質・処理
水の水質に合わせて揚砂空気量の調節及び循環量調節孔
の開度調節により簡単に粒状媒体量の循環量を調節でき
、又1次洗浄空気量及び揚砂空気量、更にスプレー水の
設定により1粒状媒体の洗浄度を任意に調節することが
できる。
Furthermore, since the circulation rate of the granular media can be adjusted arbitrarily, it can be used as a rapid filtration device by increasing the circulation rate, or it can be used as a rapid filtration device by decreasing the circulation rate to generate biofilm on the granular media and perform biological treatment. The amount of circulating granular media can be easily adjusted by adjusting the amount of sand pumping air and adjusting the opening of the circulation amount adjustment hole according to the amount and quality of raw water and the quality of treated water. The degree of cleaning of one granular medium can be arbitrarily adjusted by setting the amount of air, the amount of sand pumping air, and the spray water.

更に又、洗浄水水位調節装置により、原水の性状・水量
、粒状媒体の性状の特性に合わせて洗浄排水量の調節が
でき。
Furthermore, the washing water level adjustment device allows the amount of washing water to be adjusted according to the characteristics of the raw water, the amount of water, and the properties of the granular media.

幅広い所定の水質の処理水を得ることができる。Treated water with a wide range of predetermined water qualities can be obtained.

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

第1図は、本発明の実施例を示す縦断側面図、第2図は
、洗浄室筒下部縦断側面詳細図、第3図は循環i調節袋
rflvi断面図を示す。 図中1は処理槽、2は洗浄室筒、3は揚砂装置、4は円
錐状スクリーン、5はスプレー装置、6は粒状媒体循環
址調節装置、7は洗浄排水水位調節装置、8は揚砂空気
調節弁、9は一次洗浄空気調節弁、10は粒状媒体を示
す、11は流入管、12は流出管、13は原水分配装置
、14は曝気洗砂装置、15は固液分離装置、16は3
次洗浄水・揚砂水返送管、17は回転継手、 r特許出願人」 株式会社 明石浄化 代表者 松村達
部手続補正書(方式)
FIG. 1 is a longitudinal side view showing an embodiment of the present invention, FIG. 2 is a detailed longitudinal side view of the lower part of the cleaning chamber cylinder, and FIG. 3 is a cross-sectional view of the circulation i adjustment bag rflvi. In the figure, 1 is a treatment tank, 2 is a cleaning chamber cylinder, 3 is a sand pumping device, 4 is a conical screen, 5 is a spray device, 6 is a granular medium circulation site adjustment device, 7 is a cleaning drainage water level adjustment device, and 8 is a pumping device. Sand air control valve, 9 is a primary cleaning air control valve, 10 is a granular medium, 11 is an inflow pipe, 12 is an outflow pipe, 13 is a raw water distribution device, 14 is an aeration washing sand device, 15 is a solid-liquid separation device, 16 is 3
Next wash water/pumped sand water return pipe, 17 is a rotary joint, r Patent Applicant” Akashi Purification Co., Ltd. Representative Tatsubu Matsumura Procedural Amendment (Method)

Claims (1)

【特許請求の範囲】[Claims] 移床する粒状媒体が充填配備されている処理槽と、該槽
中心部に原水及び処理水と隔絶した洗浄室を設け、粒状
媒体層下方から上向流で通水する手段と、水面上部に設
けた円錐状スクリーンから洗浄供給され、下向きに流動
して処理水と対向流をなして移動床式水処理装置を構成
すると共に、洗浄室筒内側下方に粒状媒体の循環量を調
整する調節筒を設け、該洗浄室筒上方に洗浄水排水量調
節装置を設け、更に3次洗浄水及び揚砂水を返送管によ
り揚砂装置部に戻したことを特徴とする移動床式水処理
装置。
A treatment tank filled with the granular media to be transferred, a washing chamber isolated from the raw water and treated water in the center of the tank, a means for passing water in an upward flow from below the granular media layer, and a means for passing water above the water surface. The water is supplied for cleaning through a conical screen, flows downward and forms a counterflow with the treated water, forming a moving bed type water treatment device, as well as an adjustment tube that adjusts the circulation rate of the granular media at the lower inside of the cleaning chamber cylinder. A moving bed type water treatment device characterized in that a washing water drainage amount adjusting device is provided above the washing chamber cylinder, and further, the tertiary washing water and sand pumping water are returned to the sand pumping device section through a return pipe.
JP61222855A 1986-09-20 1986-09-20 Moving bed type water treating apparatus Pending JPS6377508A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61222855A JPS6377508A (en) 1986-09-20 1986-09-20 Moving bed type water treating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61222855A JPS6377508A (en) 1986-09-20 1986-09-20 Moving bed type water treating apparatus

Publications (1)

Publication Number Publication Date
JPS6377508A true JPS6377508A (en) 1988-04-07

Family

ID=16788953

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61222855A Pending JPS6377508A (en) 1986-09-20 1986-09-20 Moving bed type water treating apparatus

Country Status (1)

Country Link
JP (1) JPS6377508A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002533218A (en) * 1998-12-29 2002-10-08 パクエス バイオ システムズ ベスローテン フェンノートシャップ Method of treating wastewater containing heavy metals
JP2013516316A (en) * 2010-01-08 2013-05-13 パークソン コーポレーション Apparatus for treating liquids containing impurities
EP3849683A4 (en) * 2018-09-14 2022-04-20 N P Innovation AB Bio-filter unit for a fish farming system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002533218A (en) * 1998-12-29 2002-10-08 パクエス バイオ システムズ ベスローテン フェンノートシャップ Method of treating wastewater containing heavy metals
JP2013516316A (en) * 2010-01-08 2013-05-13 パークソン コーポレーション Apparatus for treating liquids containing impurities
EP3849683A4 (en) * 2018-09-14 2022-04-20 N P Innovation AB Bio-filter unit for a fish farming system
US11560325B2 (en) 2018-09-14 2023-01-24 N P Innovation Ab Bio-filter unit for a fish farming system

Similar Documents

Publication Publication Date Title
US6426005B1 (en) Sequential descending bed filters with reject/washwater containing impurities being fed to a separate unit for elimination of impurities
US4793934A (en) Method for enhancing the separation capacity of a multi-bed filtration system
US5080808A (en) Method of washing an upflow filter and filter bed employed in said filter
JPH089037B2 (en) Biological contactor for water purification and its control method for drinking water production
US3587861A (en) Apparatus and method of filtering solids from a liquid effluent
US3459302A (en) Apparatus and method of filtering solids from a liquid effluent
US7381336B2 (en) Automated water treatment system and method of use
US5198124A (en) Upflow filter and method of washing same
US5167840A (en) Systems and methods for clarifying liquids
US4659462A (en) Apparatus for pretreatment of water using a bed of granular activated carbon
US8323514B2 (en) Method and system for cleaning filter media support structures
US5314630A (en) Systems and methods for clarifying liquids
USRE28458E (en) Apparatus and method of filtering solids from a liquid effluent
JPS6377508A (en) Moving bed type water treating apparatus
CA1306421C (en) Method and apparatus for pretreatment of water using a bed of granular activated carbon
JP4299396B2 (en) Air-water distribution device and water treatment device using the air-water distribution device
JPH0523664A (en) Method for automatically controlling backwashing of biological activated-carbon treating tower
KR200159128Y1 (en) Counterflow type water filter system
US2233980A (en) Method of and apparatus for filtration
JP2882045B2 (en) Backwash control method for downflow type biological activated carbon treatment tower
JP3377894B2 (en) Water treatment method and apparatus
CA2330528C (en) Operation of an upflow filter and non-buoyant filter bed in serles with a downflow filter and filter bed
JPH055922Y2 (en)
CA2514677C (en) Operation of an upflow filter and non-buoyant filter bed in series with a downflow filter and filter bed
JPH0910786A (en) Sewage treatment apparatus