JP2000000591A - Method for purifying sewage of sewerage or the like - Google Patents

Method for purifying sewage of sewerage or the like

Info

Publication number
JP2000000591A
JP2000000591A JP10220963A JP22096398A JP2000000591A JP 2000000591 A JP2000000591 A JP 2000000591A JP 10220963 A JP10220963 A JP 10220963A JP 22096398 A JP22096398 A JP 22096398A JP 2000000591 A JP2000000591 A JP 2000000591A
Authority
JP
Japan
Prior art keywords
sewage
microorganisms
sedimentation basin
returned
purifying
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
JP10220963A
Other languages
Japanese (ja)
Inventor
Mitsuhiro Fujiwara
充弘 藤原
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP10220963A priority Critical patent/JP2000000591A/en
Publication of JP2000000591A publication Critical patent/JP2000000591A/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

Abstract

PROBLEM TO BE SOLVED: To provide a method for purifying sewage of sewerage or the like so as to still more effectively achieve sewage purifying effect. SOLUTION: In a method for purifying sewage of sewerage or the like constituted so as to pass microorganisms effective for purifying sewage through a sedimentation basin 15, a part of microorganisms in the sedimentation basin 15 are returned to the stage before an equipment including a sand sedimentation basin 3. Further, oxygen is supplied on the way of the return of effective microorganisms and the effective microorganisms are may be returned through an equipment piping or in the vicinity of the outside thereof.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、例えば、下水処
理設備における最終沈澱池に流入し存続する有効微生物
の一部を同沈澱池より前の段階に返送して投入活用する
ことで汚水の浄化を促進するようにした下水等の汚水浄
化方法に関する。
The present invention relates to the purification of sewage by, for example, returning some of the effective microorganisms that have flowed into a final sedimentation basin in a sewage treatment plant to a stage preceding the sedimentation basin for input and utilization. And a method for purifying sewage such as sewage.

【0002】[0002]

【従来の技術】例えば、下水処理システムには、図6に
示すように、雨水や生活汚水が配管を通じて抽水所(ポ
ンプ場)に流れ込み、同抽水所からの汚水は配管(流入
水路)1から沈砂池3に流れ込み、ここで除塵機5によ
り比較的大きなゴミが除去されるとともに沈砂させるよ
うになっている。沈砂池3からの汚水は、流入水槽7を
経由して次の予備反応タンク(予備曝気槽)9→最初沈
澱池11→反応タンク(曝気槽)13に導かれ、反応タ
ンク13において投入される微生物入り活性汚泥、エア
ーの供給、攪拌作用により浄化処理される。汚水は、そ
の後、最終沈澱池15に送られて反応タンク13から汚
水とともに導かれる微生物により汚水の浄化がなされ
る。こうして浄化に寄与する微生物は有効微生物として
存続するので、その一部を濃縮槽17に導くようにして
いる。それとともに、反応タンク13にも返送して供給
し浄化に寄与するようにしている。曝気槽17以降の処
理システムはここで説明は省略する。
2. Description of the Related Art For example, in a sewage treatment system, as shown in FIG. 6, rainwater or domestic wastewater flows into a water extraction station (pump station) through a pipe, and sewage from the water extraction station flows through a pipe (inflow channel) 1. The dust flows into the sand basin 3, where relatively large dust is removed by the dust remover 5 and the sand is settled. The sewage from the settling basin 3 is guided to the next preliminary reaction tank (preliminary aeration tank) 9 → the first settling basin 11 → the reaction tank (aeration tank) 13 via the inflow water tank 7, and is introduced into the reaction tank 13. Purification treatment is performed by activated sludge containing microorganisms, air supply, and stirring. The sewage is then sent to the final sedimentation basin 15 where purification of the sewage is carried out by microorganisms guided together with the sewage from the reaction tank 13. Since the microorganisms contributing to the purification remain as effective microorganisms, a part of them is led to the concentration tank 17. At the same time, it is returned to the reaction tank 13 and supplied to contribute to purification. The description of the processing system after the aeration tank 17 is omitted here.

【0003】[0003]

【発明が解決しようとする課題】ところで、これまでの
最終沈澱池15での有効微生物は、同沈澱池15の1段
階手前の反応タンク13に返送するに過ぎなかったた
め、汚水の浄化効果が全般的に今一つ有効でなく、その
対策が望まれていた。
The effective microorganisms in the final sedimentation basin 15 are only returned to the reaction tank 13 one stage before the sedimentation basin 15 so far, so that the purification effect of the sewage is generally improved. It was not effective one by one, and the countermeasure was desired.

【0004】この発明は前記課題を解決するためになさ
れたもので、汚水の浄化効果がより一層有効に行われる
ようにした下水等の汚水浄化方法を提供することを目的
としている。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and has as its object to provide a method for purifying sewage and other sewage in which sewage is more effectively purified.

【0005】[0005]

【課題を解決するための手段】前記課題を細決するた
め、請求項1記載の発明は、汚水を浄化処理する有効微
生物が沈澱池を経由するようにした下水等の汚水浄化方
法において、前記沈澱池内の微生物の一部を沈砂池を含
む設備よりも前の段階に返送するように構成されている
ことを特徴とする。
Means for Solving the Problems In order to finely solve the above problems, the invention according to claim 1 is directed to a method for purifying sewage such as sewage in which effective microorganisms for purifying sewage pass through a sedimentation pond. It is characterized in that a part of the microorganisms in the pond is returned to a stage before the equipment including the sand basin.

【0006】請求項2記載の発明は、請求項1におい
て、有効微生物を返送する途中で酸素を補給するように
する。
According to a second aspect of the present invention, in the first aspect, oxygen is supplied while returning the effective microorganisms.

【0007】請求項3記載の発明は、請求項1または2
において、有効微生物を、設備配管の内部あるいは外部
近傍を通して返送するようにする。
[0007] The invention described in claim 3 is claim 1 or 2.
In the above, the effective microorganisms are returned through the inside or outside of the facility piping.

【0008】[0008]

【発明の実施の形態】以下、図示した実施形態を参照し
てこの発明を詳細に説明する。図1は、この発明の好適
な一実施形態を示すもので、図1において、1は流入水
路、3は沈砂池で、同沈砂池3には、ゲート4が昇降調
整自在に設けられている。5は除塵機で、コンベア掻揚
式等のものが設置されている。7は流入水槽で、沈砂池
3からの汚水が流れ込み、同水槽7はゲート8を備え
る。9は予備反応タンク(予備曝気槽)、11は最初沈
澱池、13は反応タンク(曝気槽)をそれぞれ示す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to the illustrated embodiments. FIG. 1 shows a preferred embodiment of the present invention. In FIG. 1, reference numeral 1 denotes an inflow channel, 3 denotes a sand basin, and a gate 4 is provided in the sand basin 3 so as to be able to move up and down. . Reference numeral 5 denotes a dust remover, of which type is a conveyer scooping type or the like. Reference numeral 7 denotes an inflow water tank, into which sewage from the sand basin 3 flows, and the water tank 7 has a gate 8. 9 is a preliminary reaction tank (preliminary aeration tank), 11 is a first settling tank, and 13 is a reaction tank (aeration tank).

【0009】15は最終沈澱池、17は濃縮槽を示す。
最終沈澱池15は、ピット16を備えて矢印Aのように
濃縮槽17に有効微生物の一部を送るようになってい
る。ところで、この実施形態では、同ピット16で存続
する有効微生物を汚泥とともに矢印Bのように流入水路
1の前段階に返送して導入するようにしている。同有効
微生物を活性な状態のまま返送するため、返送路20途
上にエアー(あるいは酸素)供給手段21が設けられて
いる。攪拌手段も同時に構成してもよい。返送用のポン
プは図示省略されている。
Reference numeral 15 denotes a final sedimentation basin, and 17 denotes a concentration tank.
The final sedimentation basin 15 is provided with a pit 16 so as to send a part of the effective microorganisms to a concentration tank 17 as shown by an arrow A. By the way, in this embodiment, the effective microorganisms remaining in the pit 16 are returned to the preceding stage of the inflow channel 1 and introduced together with the sludge as shown by the arrow B. An air (or oxygen) supply means 21 is provided on the return path 20 in order to return the effective microorganisms in an active state. The stirring means may be configured at the same time. The return pump is not shown.

【0010】尚、仮想線矢印Bのように前記ゲート4
の後あるいは前段階に返送するようにしてもよい。ま
た、仮想線矢印Bのように前記沈砂池3から流入水槽
5間の流路にあるゲートの前あるいは後近傍位置に返送
するようにしてもよい。これら矢印B、B、Bの全
てあるいは2つ以上の組み合わせ、または択一的に実施
してもよい。仮想線矢印Cのように、反応タンク13へ
の返送を同時に実施してもよい。この実施形態における
新たな返送の範囲は、図1に矢印Xで示す範囲で、後方
は流入水槽7より前段階で、前方は特定はない。
[0010] Note that the like a virtual line arrow B 1 gate 4
It may be returned after or before. Further, it may be returned from the settling basin 3 as a virtual line arrow B 2 in front or rear position near the gate in the flow path between the inflow water tank 5. All of these arrows B, B 1 , and B 2 , or a combination of two or more of them, or alternatively, may be implemented. The return to the reaction tank 13 may be performed at the same time as indicated by a virtual arrow C. The range of the new return in this embodiment is a range indicated by an arrow X in FIG. 1, the rear is in front of the inflow water tank 7, and the front is not specified.

【0011】尚、23はエアー導入手段で、流入水路1
内にエアーを導入して浄化を促進するためのもので、2
4は新規微生物(種菌)供給手段で、流入水路1内に新
規なび導入する。また、反応タンク13からの有効微生
物を前記のような経路で返送するようにしてもよい。新
規微生物供給手段24は、し尿などに多く生息するパチ
ルス属の微生物を供給可能なものにしてもよい。
Reference numeral 23 denotes an air introduction means, and
To promote air purification by introducing air into the
Reference numeral 4 denotes a new microorganism (seed fungus) supply means, which is newly introduced into the inflow channel 1. Further, the effective microorganisms from the reaction tank 13 may be returned through the above-described route. The novel microorganism supply means 24 may be capable of supplying microorganisms of the genus Paillus which frequently inhabit human waste and the like.

【0012】図2は最終沈澱池15を上からみた様子を
示し、これら複数の沈澱池15…からそれぞれ汚泥抜出
管26を取り出し、これらにそれぞれ切換弁27…を介
して返送管28を接続する一方同弁27を介して濃縮槽
17への汚泥導入管29を接続してある。切換弁27
は、返送管28の方向と汚泥導入管29の方向へ汚泥の
流れを切り換えるためのものである。
FIG. 2 shows the final sedimentation basin 15 viewed from above. Sludge discharge pipes 26 are respectively taken out of the plurality of sedimentation basins 15 and connected to return pipes 28 via switching valves 27. On the other hand, a sludge introduction pipe 29 to the concentration tank 17 is connected via the valve 27. Switching valve 27
Is for switching the sludge flow in the direction of the return pipe 28 and the direction of the sludge introduction pipe 29.

【0013】図3は他の返送方法を示すもので、沈澱池
からの有効微生物混じりの汚泥をマンホール31まで返
送管32を通じて返送するようにしてある。この場合の
返送管32は、図3の実線及び図4の実線で示すよう
に、マンホール31からの配管33内を通じてある。同
返送管2は図4の仮想線のように配管33外部を通じて
もよい。
FIG. 3 shows another return method in which sludge mixed with effective microorganisms from a sedimentation tank is returned to a manhole 31 through a return pipe 32. The return pipe 32 in this case passes through the pipe 33 from the manhole 31, as shown by the solid line in FIG. 3 and the solid line in FIG. The return pipe 2 may pass through the outside of the pipe 33 as shown by a virtual line in FIG.

【0014】尚、水処理設備35への流入配管36は、
直線状のものの他、図5にその平面図を示すように、迂
回状になったものもあり、この場合、迂回することから
返送管37は比較的近い距離を介して接続することがで
きる。
The inflow pipe 36 to the water treatment facility 35 is
In addition to the straight one, as shown in the plan view of FIG. 5, there is a detoured one. In this case, the return pipe 37 can be connected through a relatively short distance due to the detour.

【0015】尚、前記水処理設備あるいはその前段階の
配管内に流れる汚水の汚泥に対しては+あるいは−イオ
ンに帯電して、これが沈澱池などに流入した際にマグネ
ットで吸着して即時沈降を促進するようにしてもよい。
この場合、マグネットによる電磁吸着力を作用させる以
外に超音波振動を作用させるようにしてもよい。この超
音波振動は、マグネットによる作用の後あるいは前の段
階で、または、マグネットによる作用と同時に行う。
The sludge flowing into the water treatment facility or the pipe at the preceding stage is charged with + or-ions, and when the sludge flows into a sedimentation basin or the like, it is adsorbed by a magnet and immediately settles. May be promoted.
In this case, an ultrasonic vibration may be applied in addition to the electromagnetic attraction by the magnet. This ultrasonic vibration is performed after or before the action by the magnet or simultaneously with the action by the magnet.

【0016】尚、前記実施形態のような水処理設備内・
外その他一般生活用等の焼成炭の生産方法を付加的な例
をとしてここで説明する。すなわち、原材料として用い
るものは、雑草等の草、ひまわりやれんげ、檜やケナフ
等の幹、茎、葉、磁性を帯びるヨモギの葉や茎であり、
これらを所望に選択して、微細チップ状にし、泥(汚泥
でもよい)や砂等と混ぜて(オガ屑を同時に混合するこ
ともある)適度の粘性を帯びるようにし、これを成形機
に通す。
In the water treatment equipment as in the above embodiment,
The method of producing calcined charcoal for general use and other purposes will be described here as an additional example. That is, the materials used as raw materials are grasses such as weeds, sunflowers and lotus roots, stems such as hinoki and kenaf, stems, leaves, leaves and stems of magnetic mugwort,
These are selected as desired, formed into fine chips, mixed with mud (sludge may be used) or sand, etc. (sometimes sawdust is mixed at the same time) so as to have an appropriate viscosity, and then passed through a molding machine. .

【0017】成形機は、ボディに多数の平行な絞り孔を
備えたもので、孔後方から押し出し手段を挿入して線香
状のようにして孔前方に順次粘性剤を押し出すようにす
る。これにより得られた成形品を寸切りして(寸切りし
なくともよい)のら蒸し焼き(燻製)にする。こうして
蒸し焼きにすることで効果的に超微細孔を無数に有する
活性炭が出来上がる。これらの製品を水や空気の清浄化
のために利用する。尚、麦飯石等の石材を途中で混合し
てもよい。
The molding machine is provided with a number of parallel throttle holes in the body, and inserts a pushing means from the rear of the hole to sequentially extrude the viscous agent to the front of the hole like an incense stick. The molded article thus obtained is cut into pieces (there is no need to cut the pieces) and then steamed (smoked). Activated carbon having an innumerable number of ultrafine pores can be effectively produced by steaming. These products are used for water and air purification. Incidentally, stone materials such as barley stone may be mixed in the middle.

【0018】図7は付加的な提案例を示すもので、同例
は、マンホール50…間を継ぐ配管51がガス等により
損傷を受けることがあることに鑑み、該ガス類を吸・排
システムにより強制的に排除してやることにより、配管
類の保護を図るようにしたものである。即ち、Cは新気
送り込み側、Dは内ガス導出側である。新気送り込み側
Cにおいては、マンホール50上に第1ハウス52を立
設し、その内部に吸気自在な構造としてある。第1ハウ
ス52内には、外部のガスを中和して通す手段53と、
同中和分を吸い込み排出する第1ファン54が内装され
ている。第1ファン54の排出側には、第1担体55が
セットされ、その中にカビ取りバイオ等が内填されてい
る。これらによると、第1ファン54の駆動により外気
が中和・カビ取りされながら吸引・排出され、マンホー
ル50から配管51内に導かれる。
FIG. 7 shows an example of an additional proposal. In this example, in consideration of the fact that the pipe 51 connecting between the manholes 50... The pipes are forcibly removed for protection of piping. That is, C is a fresh air feeding side, and D is an internal gas outlet side. On the fresh air feeding side C, a first house 52 is erected on the manhole 50 and has a structure in which air can be freely taken. Means 53 for neutralizing and passing an external gas in the first house 52;
A first fan 54 for sucking and discharging the neutralized component is provided. On the discharge side of the first fan 54, a first carrier 55 is set, in which a mold removing biomaterial or the like is loaded. According to these, the outside air is sucked and discharged while being neutralized and mold-removed by driving the first fan 54, and is guided from the manhole 50 into the pipe 51.

【0019】一方、内ガス導出側Dにも同様の第2ハウ
ス60が立設され、前記により送入された空気を内ガス
を伴なって吸引・除去する構成になっている。即ち、6
1は第2担体で活性炭を含浸させてあり、又、62は排
気ファンを示す。
On the other hand, a similar second house 60 is also provided upright on the internal gas outlet side D to suck and remove the air fed in with the internal gas. That is, 6
Reference numeral 1 denotes a second carrier impregnated with activated carbon, and 62 denotes an exhaust fan.

【0020】尚、第1ファン54等の吸入・排気システ
ムは、仮想線で示す第2ファン56等に代えて構成して
もよい。このことは内ガス導出側Dについても同様であ
る。又、マンホール50,50間が可成り離間している
場合、仮想線のように仮埋設ホール63を設けてここで
排気すべく対応してもよい。更に、マンホール50,5
0以外のマンホールについては、出方向に一方的に絞る
弁機構(装置)をセットして対応することがある。
The suction / exhaust system of the first fan 54 and the like may be configured in place of the second fan 56 and the like shown by phantom lines. The same applies to the internal gas outlet side D. Further, when the manholes 50 and 50 are considerably apart from each other, a provisionally buried hole 63 may be provided as shown by a virtual line to cope with exhaust. Furthermore, manholes 50 and 5
For manholes other than 0, a valve mechanism (apparatus) that unilaterally restricts in the exit direction may be set.

【0021】[0021]

【発明の効果】この発明は以上のように汚水を浄化処理
する有効微生物が沈澱池を経由するようにした下水等の
汚水浄化方法において、前記沈澱池内の微生物の一部を
沈砂池を含む設備よりも前の段階に返送するように構成
されていることを特徴とするので、汚水の浄化効果がよ
り一層有効に行われるようにした下水等の汚水浄化方法
を提供することができる。
According to the present invention, there is provided a method for purifying sewage or the like in which effective microorganisms for purifying sewage are passed through a sedimentation basin as described above, wherein a part of the microorganisms in the sedimentation basin includes a sand basin. Since it is configured to return to an earlier stage, it is possible to provide a method of purifying sewage such as sewage, in which the effect of purifying sewage is more effectively performed.

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

【図1】この発明の一実施形態を水処理設備の模式図。FIG. 1 is a schematic view of a water treatment facility according to an embodiment of the present invention.

【図2】複数の沈澱池からの返送と曝気槽への汚泥導入
方法を示す平面説明図。
FIG. 2 is an explanatory plan view showing a method of returning sludge from a plurality of sedimentation basins and introducing sludge into an aeration tank.

【図3】返送汚泥をマンホールに持ち込む方法を示す縦
断面模式図。
FIG. 3 is a schematic vertical sectional view showing a method of bringing returned sludge into a manhole.

【図4】図3の断面模式図。FIG. 4 is a schematic sectional view of FIG. 3;

【図5】迂回配管による汚水導入経路に汚泥を返送する
例を示す平面図。
FIG. 5 is a plan view showing an example of returning sludge to a sewage introduction path by a bypass pipe.

【図6】従来の水処理システムを示す模式図。FIG. 6 is a schematic diagram showing a conventional water treatment system.

【図7】マンホール間の配管内ガスを抜く案を示す模式
図.
FIG. 7 is a schematic view showing a plan for extracting gas in a pipe between manholes.

【符号の説明】[Explanation of symbols]

1…配管(流入水路) 3…沈砂池 5…除塵機 7…
流入水路 9…予備反応タンク(予備曝気槽) 11…
最初沈澱池 13…反応タンク(曝気槽) 15…最初
沈澱池 17…濃縮槽
1 ... piping (inflow water channel) 3 ... sand basin 5 ... dust remover 7 ...
Inflow channel 9… Preliminary reaction tank (preliminary aeration tank) 11…
First settling basin 13 ... Reaction tank (aeration tank) 15 ... First settling basin 17 ... Concentration tank

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 汚水を浄化処理する有効微生物が沈澱池
を経由するようにした下水等の汚水浄化方法において、
前記沈澱池内の微生物の一部を沈砂池を含む設備よりも
前の段階に返送するように構成されていることを特徴と
する下水等の汚水浄化方法。
1. A method for purifying sewage or other sewage in which effective microorganisms for purifying sewage are passed through a sedimentation basin.
A method for purifying sewage or other sewage, characterized in that a part of the microorganisms in the sedimentation basin is returned to a stage before the equipment including the sand basin.
【請求項2】 請求項1において、有効微生物を返送す
る途中で酸素を補給するようにした下水等の汚水浄化方
法。
2. The method for purifying sewage such as sewage according to claim 1, wherein oxygen is supplied during the return of the effective microorganisms.
【請求項3】 請求項1または2において、有効微生物
を、設備配管の内部あるいは外部近傍を通して返送する
下水等の汚水浄化方法。
3. The method for purifying sewage such as sewage according to claim 1, wherein the effective microorganisms are returned through the inside or outside of the facility piping.
JP10220963A 1998-06-17 1998-06-17 Method for purifying sewage of sewerage or the like Pending JP2000000591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10220963A JP2000000591A (en) 1998-06-17 1998-06-17 Method for purifying sewage of sewerage or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10220963A JP2000000591A (en) 1998-06-17 1998-06-17 Method for purifying sewage of sewerage or the like

Publications (1)

Publication Number Publication Date
JP2000000591A true JP2000000591A (en) 2000-01-07

Family

ID=16759308

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10220963A Pending JP2000000591A (en) 1998-06-17 1998-06-17 Method for purifying sewage of sewerage or the like

Country Status (1)

Country Link
JP (1) JP2000000591A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007222749A (en) * 2006-02-22 2007-09-06 Sumiju Kankyo Engineering Kk Waste water treatment apparatus and method
JP2008126169A (en) * 2006-11-22 2008-06-05 Asahi Kasei Clean Chemical Co Ltd Sewage treatment method
JP2020075234A (en) * 2018-11-07 2020-05-21 株式会社京玉エンジニアリング Sewage treatment system
JP2020097024A (en) * 2018-12-17 2020-06-25 株式会社京玉エンジニアリング Sewage treatment system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007222749A (en) * 2006-02-22 2007-09-06 Sumiju Kankyo Engineering Kk Waste water treatment apparatus and method
JP2008126169A (en) * 2006-11-22 2008-06-05 Asahi Kasei Clean Chemical Co Ltd Sewage treatment method
JP2020075234A (en) * 2018-11-07 2020-05-21 株式会社京玉エンジニアリング Sewage treatment system
JP2020104114A (en) * 2018-11-07 2020-07-09 株式会社京玉エンジニアリング Sewage treatment system
JP2020104113A (en) * 2018-11-07 2020-07-09 株式会社京玉エンジニアリング Sewage treatment system
JP2020097024A (en) * 2018-12-17 2020-06-25 株式会社京玉エンジニアリング Sewage treatment system

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