JP2003245686A - Water treatment apparatus - Google Patents

Water treatment apparatus

Info

Publication number
JP2003245686A
JP2003245686A JP2002047578A JP2002047578A JP2003245686A JP 2003245686 A JP2003245686 A JP 2003245686A JP 2002047578 A JP2002047578 A JP 2002047578A JP 2002047578 A JP2002047578 A JP 2002047578A JP 2003245686 A JP2003245686 A JP 2003245686A
Authority
JP
Japan
Prior art keywords
water
tank
treated
filter medium
aeration
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
JP2002047578A
Other languages
Japanese (ja)
Inventor
Satoru Kobayashi
悟 小林
Yasuyuki Kawamoto
保行 川本
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.)
SAKAMOTO SEKKEI JIMUSHO KK
SANKEN SETSUBI SEKKEI KK
Original Assignee
SAKAMOTO SEKKEI JIMUSHO KK
SANKEN SETSUBI SEKKEI 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 SAKAMOTO SEKKEI JIMUSHO KK, SANKEN SETSUBI SEKKEI KK filed Critical SAKAMOTO SEKKEI JIMUSHO KK
Priority to JP2002047578A priority Critical patent/JP2003245686A/en
Publication of JP2003245686A publication Critical patent/JP2003245686A/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

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Biological Wastes In General (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a water treatment apparatus which is simple in structure, can remove pollutants efficiently from water, and can purify water to be recycled at low costs. <P>SOLUTION: Oxygen is supplied to raw water from a flow rate adjustment tank 10 by aeration in an attached aeration tank 20, the inside of the tank is agitated, the raw water is repeatedly brought into contact with a filter medium 21 to which aerobic microorganisms adhere, and organic pollutants in water are chiefly decomposed/removed. Next, after the pollutants are precipitated in a precipitation tank 30, organic substances in supernatant after being separated are decomposed and gasified in a biological filtration tank 40 by using metabolism action of anaerobic microorganisms, and purified treatment water is obtained finally in a treatment water tank 50. In this way, purification treatment is done surely with the structure simplified, the cost of the entire apparatus can be reduced, reliability is improved, and labor and costs for maintenance can be reduced. <P>COPYRIGHT: (C)2003,JPO

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】本発明は、水を所定状態に調
整処理する水処理装置に関し、特に工場や家庭などから
の廃水を再利用可能な状態に浄化処理する水処理装置に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment device for adjusting and treating water to a predetermined state, and more particularly to a water treatment device for purifying waste water from a factory, a household or the like into a reusable state.

【0002】[0002]

【従来の技術】生活用水使用量は年々増加の傾向を示し
ているが、水資源は限られており、使用後の生活廃水の
再利用が求められている。近年、単独浄化槽及び合併浄
化槽の後に三次処理槽を追加するなどの処置を施した一
連の処理設備により廃水を再利用可能な程度に浄化す
る、いわゆる中水処理装置が提案されている。こうした
中水処理装置で得られた処理水(中水)は主にトイレの
洗浄水及び洗車用水、樹木への灌水などの用途に利用す
ることができ、一人当たりに換算した一日の水使用量の
約1/5〜1/4を処理水の使用に置換え可能である。
2. Description of the Related Art Although the amount of domestic water used has been increasing year by year, water resources are limited, and it is required to reuse domestic waste water after use. In recent years, there has been proposed a so-called intermediate water treatment device that purifies waste water to a reusable degree by a series of treatment facilities that have been treated such as adding a third treatment tank after an individual septic tank and a combined septic tank. The treated water (medium water) obtained by such a medium water treatment device can be mainly used for toilet wash water, car wash water, watering trees, etc. About 1/5 to 1/4 of the amount can be replaced by the use of treated water.

【0003】[0003]

【発明が解決しようとする課題】従来の中水処理装置は
以上のように構成されており、大規模な汚水処理システ
ムと同じ思想の処理機構であったことから、設置コスト
は家庭等で導入されている合併浄化槽の1.3〜1.5
倍になってしまうことに加え、装置が複雑化しているこ
とで保守の負担も増大し、こうしたデメリットが廃水再
利用による環境負荷の軽減、水使用の低コスト化等のメ
リットを打消してしまうという課題を有していた。
Since the conventional gray water treatment device is constructed as described above and has a treatment mechanism of the same idea as a large-scale wastewater treatment system, the installation cost is introduced at home. 1.3-1.5 of the combined septic tank being used
In addition to doubling, the burden of maintenance increases due to the complexity of the device, and such demerits negate the merits of reducing the environmental load by recycling wastewater, lowering the cost of water use, etc. Had a problem.

【0004】本発明は前記課題を解消するためになされ
たもので、簡略な構造で水中から効率良く汚濁物質を除
去でき、低コストに水質を再利用可能な状態まで浄化処
理できる水処理装置を提供することを目的とする。
The present invention has been made to solve the above problems, and provides a water treatment device capable of efficiently removing pollutants from water with a simple structure and purifying the water quality to a reusable state at low cost. The purpose is to provide.

【0005】[0005]

【課題を解決するための手段】本発明に係る水処理装置
は、所定容量の水槽で形成され、所定の廃水を処理対象
水として流入させて一時的に貯留すると共に、前記処理
対象水の送出流量を調整しつつ次工程へ送出す流量調整
槽と、好気性微生物の付着する濾材を充填される水槽で
形成され、前記流量調整槽から処理対象水を供給され、
曝気を行いつつ処理対象水を前記濾材間に通して浄化す
る付着曝気槽と、所定容量の水槽で形成され、前記付着
曝気槽から排出された処理対象水を供給され、当該処理
対象水中の汚濁物質を沈殿させる沈殿槽と、嫌気性微生
物の付着する多孔質の濾材を充填される水槽で形成さ
れ、前記沈殿槽で汚濁物質と分離された上澄み水を供給
され、当該上澄み水を前記濾材間に通して浄化する生物
濾過槽と、当該生物濾過槽から排出された水を殺菌した
上で貯留する処理水槽とを備えるものである。
A water treatment apparatus according to the present invention is formed of a water tank having a predetermined capacity, allows a predetermined wastewater to flow in as treatment target water and temporarily stores the same, and also delivers the treatment target water. A flow rate adjusting tank which sends out to the next step while adjusting the flow rate, and a water tank which is filled with a filter medium to which aerobic microorganisms adhere, and is supplied with water to be treated from the flow rate adjusting tank,
Contamination in the water to be treated, which is formed by an adhering aeration tank that purifies the water to be treated by passing between the filter media while performing aeration, and a water to be treated that is discharged from the adhering aeration tank. A sedimentation tank for precipitating a substance, and a water tank filled with a porous filter medium to which anaerobic microorganisms are attached are supplied with the supernatant water separated from the pollutants in the sedimentation tank, and the supernatant water is passed between the filter media. The biological filtration tank for purifying the biological filtration tank through the above, and the treated water tank for sterilizing the water discharged from the biological filtration tank and storing the sterilized water.

【0006】このように本発明においては、流量調整槽
から送られる処理対象水に対し付着曝気槽内で曝気によ
り酸素を供給するとともに槽内を攪拌して、好気性微生
物の付着する濾材と処理対象水とを繰り返し接触させ、
水中の主として有機性の汚濁物質の分解除去を行い、次
いで沈殿槽で汚濁物質を沈殿させた後、さらに、分離さ
れた後の上澄み水中の有機物を生物濾過槽内で嫌気性微
生物の代謝作用を利用して分解(低分子化)・ガス化
し、最終的に処理水槽内に浄化した処理水を得られるこ
とにより、簡略な構造で確実に浄化処理が行え、装置全
体のコストダウンが図れると共に、信頼性を向上させら
れ、保守の手間及びコストも低減できる。
As described above, according to the present invention, oxygen is supplied by aeration in the adhering aeration tank to the water to be treated sent from the flow rate adjusting tank and the inside of the tank is agitated, and the filter medium to which aerobic microorganisms adhere and the treatment. Repeated contact with the target water,
Decomposes and removes mainly organic pollutants in the water, then precipitates the pollutants in the settling tank, and further separates the organic matter in the supernatant water after separation into the biological filtration tank for the metabolic action of anaerobic microorganisms. By utilizing it to decompose (lower the molecular weight), gasify it, and finally obtain purified water in the treated water tank, it is possible to reliably perform purification treatment with a simple structure and reduce the cost of the entire device, The reliability can be improved, and the labor and cost of maintenance can be reduced.

【0007】また、本発明に係る水処理装置は必要に応
じて、前記流量調整槽が、前記付着曝気槽への送水量を
調整する計量調整部を配設されるものである。このよう
に本発明においては、流量調整槽に送水量調整用の計量
調整部を配設し、次工程以降で浄化処理する処理対象水
量を適宜調整可能とすることにより、処理水使用量に応
じて流量調整槽からの送水量を調整して処理水として必
要な水量のみを浄化処理でき、無駄な処理水の発生を抑
えられる。さらに、装置全体の浄化処理能力に対応させ
て適正量の処理対象水を浄化処理工程へ供給できること
となり、処理対象水に対し効率的に浄化処理を行え、浄
化処理の信頼性を向上させられると共に、濾材の目詰り
も進行しにくく、保守コストを低減できる。
Further, in the water treatment apparatus according to the present invention, the flow rate adjusting tank is provided with a metering adjusting section for adjusting the amount of water supplied to the adhesion aeration tank, if necessary. As described above, according to the present invention, the flow rate adjusting tank is provided with a metering adjusting unit for adjusting the amount of water to be supplied, and the amount of water to be treated to be purified in the subsequent steps can be appropriately adjusted, so that the amount of treated water can be adjusted according to the amount of treated water used. The amount of water sent from the flow rate adjusting tank can be adjusted to purify only the amount of water required as treated water, and wasteful treated water can be suppressed. Further, an appropriate amount of water to be treated can be supplied to the purification treatment step in accordance with the purification treatment capacity of the entire apparatus, so that the treatment water can be efficiently purified and the reliability of the purification treatment can be improved. Also, clogging of the filter medium is less likely to proceed, and maintenance costs can be reduced.

【0008】また、本発明に係る水処理装置は必要に応
じて、前記流量調整槽が、空気の噴出口を設置され、前
記処理対象水中に空気を送込まれるものである。このよ
うに本発明においては、流量調整槽で処理対象水に対し
空気を送込み、処理対象水中に酸素を供給するとともに
槽内を攪拌することにより、貯留した処理対象水の流動
を促すこととなり、処理対象水の腐敗を防止できると共
に、処理対象水の均質化が図れる。
Further, in the water treatment apparatus according to the present invention, the flow rate adjusting tank is provided with an air ejection port, and air is sent into the water to be treated, if necessary. As described above, in the present invention, air is sent to the water to be treated in the flow rate adjusting tank to supply oxygen into the water to be treated and to stir the inside of the tank, thereby promoting the flow of the stored water to be treated. The decomposition of the water to be treated can be prevented and the water to be treated can be homogenized.

【0009】また、本発明に係る水処理装置は必要に応
じて、前記付着曝気槽が、濾材として牡蠣殻を不規則配
置状態で充填されると共に、曝気用空気の噴出口を下部
に設置されるものである。このように本発明において
は、付着曝気槽に充填する濾材を牡蠣殻とし、曝気用空
気の噴出口を付着曝気槽下部に配置して、充填された牡
蠣殻間へ曝気により十分な酸素を送込むことにより、牡
蠣殻表面の好気性微生物と空気とが効率よく接触するこ
ととなり、細菌の有機物分解作用を最大限発揮させら
れ、好気性微生物で処理対象水中の有機性汚濁物質を確
実に分解除去できる。さらに、処理対象水に塩素化合物
が含まれている場合には、牡蠣殻中のCaの溶解で処理
対象水のPH調整が図れ、水のPHを適切な状態として
細菌の活動を最大限に高められ、浄化処理の効率を維持
できる。
Further, in the water treatment apparatus according to the present invention, the attached aeration tank is filled with oyster shells as a filter material in an irregularly arranged state, and a jet of aeration air is installed at a lower portion, if necessary. It is something. As described above, in the present invention, the filter medium to be filled in the adhering aeration tank is oyster shell, and the jet of aeration air is arranged in the lower part of the adhering aeration tank to send sufficient oxygen by aeration between the filled oyster shells. By incorporating the oyster shells, the aerobic microorganisms on the surface of the oyster shells and the air will efficiently come into contact with each other, so that the organic substance decomposing effect of the bacteria can be maximized, and the aerobic microorganisms will surely decompose organic pollutants in the water to be treated. Can be removed. Furthermore, when the water to be treated contains chlorine compounds, the pH of the water to be treated can be adjusted by dissolving Ca in the oyster shell, and the pH of the water can be adjusted to an appropriate state to maximize bacterial activity. Therefore, the efficiency of the purification process can be maintained.

【0010】また、本発明に係る水処理装置は必要に応
じて、前記生物濾過槽が、濾材の一部として大きさが5
〜15mm程度となる粒状の多孔質材を充填されるもの
である。このように本発明においては、生物濾過槽に充
填する濾材の一部を粒状の多孔質材とし、濾材の表面積
を十分確保して濾材表面の嫌気性微生物を汚濁物質の含
まれた水と効率よく接触させられることにより、細菌の
有機物分解作用を最大限発揮させられ、嫌気性微生物で
水中の有機性汚濁物質を確実に分解除去できる。
Also, in the water treatment apparatus according to the present invention, the biological filtration tank may have a size of 5 as a part of the filter medium, if necessary.
It is filled with a granular porous material having a size of about 15 mm. As described above, in the present invention, a part of the filter medium to be filled in the biological filter tank is a granular porous material, and the surface area of the filter medium is sufficiently ensured so that the anaerobic microorganisms on the surface of the filter medium are efficiently treated with water containing pollutants. By bringing them into close contact with each other, the organic substance decomposing action of the bacteria can be maximized, and the organic pollutants in the water can be surely decomposed and removed by the anaerobic microorganisms.

【0011】また、本発明に係る水処理装置は必要に応
じて、前記生物濾過槽が、濾材に酸生成菌に属する通性
嫌気性微生物群及び絶対嫌気性のメタン生成菌を付着さ
れてなるものである。このように本発明においては、生
物濾過槽における濾材に付着する嫌気性微生物を酸生成
菌とメタン生成菌とし、水中に含まれる汚濁物質である
高分子有機物を酸生成菌で酢酸、プロピオン酸、酪酸等
の揮発性有機酸と低級アルコール類に分解した後、生じ
た前記有機酸をメタン生成菌でメタン、二酸化炭素、又
はアンモニア等に分解することにより、水中の有機性汚
濁物質を効率よく短時間で分解除去でき、処理対象水の
浄化処理能力のより一層の向上が図れる。
Further, in the water treatment apparatus according to the present invention, the biological filtration tank has, if necessary, a facultative anaerobic microbial group belonging to an acid-producing bacterium and an absolutely anaerobic methanogenic bacterium attached to a filter medium. It is a thing. As described above, in the present invention, the anaerobic microorganisms attached to the filter medium in the biological filtration tank are acid-producing bacteria and methanogenic bacteria, and the high-molecular organic matter that is a pollutant contained in water is acetic acid-producing bacteria, propionic acid, After decomposing into volatile organic acids such as butyric acid and lower alcohols, and then decomposing the resulting organic acids into methane, carbon dioxide, ammonia, etc. with a methanogenic bacterium, organic pollutants in water can be efficiently reduced. It can be decomposed and removed in time, and the purification capacity of the water to be treated can be further improved.

【0012】[0012]

【発明の実施の形態】以下、本発明の一実施の形態に係
る水処理装置を図1に基づいて説明する。本実施の形態
に係る水処理装置は、生活廃水を処理対象水とし、浄化
処理により再利用可能な処理水を得るものである。図1
は本実施の形態に係る水処理装置の概略構成説明図であ
る。
BEST MODE FOR CARRYING OUT THE INVENTION A water treatment apparatus according to an embodiment of the present invention will be described below with reference to FIG. The water treatment device according to the present embodiment uses domestic wastewater as treatment target water to obtain reusable treated water by purification treatment. Figure 1
FIG. 2 is a schematic configuration explanatory diagram of a water treatment device according to the present embodiment.

【0013】前記各図に示すように、本実施の形態に係
る水処理装置1は、一般家庭などからの生活廃水を処理
対象水として流入させて一時的に貯留する流量調整槽1
0と、この流量調整槽10から供給される処理対象水中
の汚濁物質を濾過し且つ好気性微生物により分解する付
着曝気槽20と、この付着曝気槽20からの排水を流入
させて汚濁物質を沈降分離させる沈殿槽30と、この沈
殿槽30で汚濁物質と分離された後の上澄み水を供給さ
れ、上澄み水中の有機物を濾過すると共に嫌気性微生物
の代謝作用で分解する生物濾過槽40と、この生物濾過
槽40から排出された処理水を殺菌処理して貯留する処
理水槽50とを備える構成である。
As shown in each of the above figures, the water treatment apparatus 1 according to the present embodiment is a flow rate adjusting tank 1 in which domestic wastewater from a general household or the like is introduced as water to be treated and temporarily stored.
0, an aeration tank 20 for filtering pollutants in the water to be treated supplied from the flow rate adjusting tank 10 and decomposing them by aerobic microorganisms, and a waste water from the aeration tank 20 for inflow to flow in to settle the pollutants. A settling tank 30 to be separated, and a biological filter tank 40 which is supplied with supernatant water after being separated from pollutants in the settling tank 30 and which filters organic matters in the supernatant water and decomposes by the metabolic action of anaerobic microorganisms. A treated water tank 50 for sterilizing and storing the treated water discharged from the biological filtration tank 40.

【0014】前記流量調整槽10は、処理対象水を集め
て一時貯留し、処理水量の調整を行いつつ次工程に供給
する水槽であり、その有効容量は一日当りの処理水量の
2/3以上とされる構成である。この流量調整槽10に
は、微小気泡を噴出させて処理対象水中に酸素を溶解さ
せると共に、噴出力により処理対象水を攪拌し均質化を
図る散気装置11、処理対象水を次工程側へ移送させる
ためのポンプ12、ポンプ12により揚水された処理対
象水を計量して送水量を調整する計量調整部13、及
び、処理能力以上の排水が流入した時に水を外部へ逃が
すオーバ-ブロー管(図示を省略)等の付属装置が配設
される。
The flow rate adjusting tank 10 is a water tank that collects and temporarily stores the water to be treated and supplies it to the next step while adjusting the amount of treated water, and its effective capacity is 2/3 or more of the amount of treated water per day. It is a configuration that is said to be. In the flow rate adjusting tank 10, air bubbles are jetted to dissolve oxygen in the water to be treated, and the air jetting device 11 that agitates the water to be treated to homogenize the water to be treated, and the water to be treated to the next process side. A pump 12 for transferring, a measurement adjusting unit 13 for measuring the water to be treated pumped up by the pump 12 to adjust the amount of water to be sent, and an over-blow pipe for letting the water out when a wastewater having a treatment capacity or more flows in. Attached devices such as (not shown) are provided.

【0015】前記付着曝気槽20は、前記流量調整槽1
0の3/5以上の有効容量を有する水槽であり、内部へ
の濾材21の充填で濾床を形成され、流量調整槽10を
出た処理対象水を上部から流下させて濾材21間に通
し、処理対象水中の汚濁成分を物理的に濾過すると共
に、濾材21に付着した好気性微生物に汚濁成分の分解
を行わせる構成である。
The adhesion aeration tank 20 is the flow rate adjusting tank 1
It is a water tank having an effective capacity of 3/5 or more of 0, a filter bed is formed by filling the inside of the filter medium 21, and the water to be treated which has flowed out of the flow rate adjusting tank 10 is made to flow down from the upper part and passed between the filter medium 21. The configuration is such that the pollutant component in the water to be treated is physically filtered and the aerobic microorganisms attached to the filter material 21 decompose the pollutant component.

【0016】この付着曝気槽20は、処理対象水に対し
微小気泡を噴出させて空気中の酸素を溶解させる散気装
置22を配設されてなり、槽内下部からの曝気で濾材2
1間に十分な酸素を供給し、濾材21に付着した好気性
微生物を繁殖・活動させ、この好気性微生物による有機
物分解を促す仕組みである。濾材21としては牡蠣殻を
使用しており、粒状不定形の牡蠣殻を樹脂製の網袋に入
れたものの上側に、牡蠣殻をやや小さめの20〜50m
m程度の大きさに砕いたものを入れた樹脂製の網袋を1
0〜15cmの厚さとなるように積層し、濾床を形成し
ている。なお、濾材21は20〜25cm積層するごと
にプラスチックル−バ−23を配置して空気泡の平坦化
を図っている。濾材21である牡蠣殻は空気との接触を
有効に行わせるために不規則な形状並びに袋内配置状態
とされ、付着曝気槽20の有効容量の55%〜60%ま
で充填される。
The adhering aeration tank 20 is provided with an air diffuser 22 for ejecting fine bubbles to the water to be treated to dissolve oxygen in the air, and the filter medium 2 is aerated from the lower part of the tank.
This is a mechanism in which sufficient oxygen is supplied during the period 1, the aerobic microorganisms attached to the filter medium 21 are propagated and activated, and the decomposition of organic substances by the aerobic microorganisms is promoted. Oyster husks are used as the filter material 21, and the oyster husks in the shape of granular oysters are placed in a resin net bag, and the oyster husks are slightly smaller than 20 to 50 m.
1 plastic mesh bag containing crushed pieces of about m
The filter bed is formed by stacking layers to have a thickness of 0 to 15 cm. The filter medium 21 is provided with a plastic louver 23 for every 20 to 25 cm of stacking to flatten air bubbles. The oyster shell that is the filter material 21 has an irregular shape and a state of being arranged in a bag in order to effectively make contact with air, and is filled up to 55% to 60% of the effective capacity of the adhesion aeration tank 20.

【0017】また、この付着曝気槽20と組合わせて、
水を逆流させて肥厚した生物膜を濾材21から剥離させ
る逆洗装置(図示を省略)、槽内に沈殿した汚泥を汲み
上げるエアーリフトポンプ(図示を省略)、汲み上げが
困難な汚泥を吸引除去するための清掃口(図示を省
略)、濾材21逆洗時に水面上に発生したスカムを移送
するスカムスキ−マ(図示を省略)などが配設される。
Also, in combination with this adhesion aeration tank 20,
A backwashing device (not shown) that causes water to flow backward to separate the thickened biofilm from the filter medium 21, an air lift pump (not shown) that pumps up sludge that has settled in the tank, and suction removal of sludge that is difficult to pump up A cleaning port (not shown) for this purpose, a scum skimmer (not shown) for transferring scum generated on the water surface at the time of backwashing the filter medium 21, and the like are provided.

【0018】前記沈殿槽30は、有効容量を前記付着曝
気槽20の1/2以上とされる水槽であり、付着曝気槽
20から流入して下部から上部へ向う処理対象水中の汚
濁物質を沈降させて分離すると共に、水中内の浮遊空気
を分離するものである。汚濁物質を分離された上澄み水
は沈殿槽30から次工程の生物濾過槽40へ向け排出さ
れる。
The settling tank 30 is a water tank having an effective capacity of 1/2 or more of that of the adhesion aeration tank 20, and settles contaminants in the water to be treated flowing from the adhesion aeration tank 20 to the upper part. In addition to the separation, the floating air in the water is separated. The supernatant water from which the contaminants have been separated is discharged from the settling tank 30 to the biological filtration tank 40 in the next step.

【0019】前記生物濾過槽40は、前記付着曝気槽2
0の1/2以上の有効容量を有する水槽であり、内側に
は所定の濾材41、42を容量の50%以上を占める状
態として収容してなり、沈殿槽30から処理対象水を一
旦槽内下部に流入させ、下部より上昇させて濾材41、
42間に通し、処理対象水中の汚濁成分を物理的に濾過
すると共に、濾材41、42表面に生息する嫌気性微生
物の代謝作用を利用して水浄化を図るものである。濾材
41としては、粒状不定形の牡蠣殻を20〜50mm程
度の大きさに砕き、樹脂製の網袋に入れたものを15〜
20cm厚として使用する。一方、濾材41上側には、
濾材42として5〜15mm程度の大きさとなる粒状の
多孔性廃材、例えば火力発電所での燃焼に使用した石炭
の燃え殻(コークス)などを所定厚さ分積層している。
The biological filtration tank 40 is the adhesion aeration tank 2
It is a water tank having an effective capacity of ½ or more of 0, and contains predetermined filter media 41 and 42 in a state of occupying 50% or more of the capacity inside, and the water to be treated is temporarily stored in the tank from the settling tank 30. It is made to flow into the lower part and raised from the lower part,
It is intended to physically filter the polluted components in the water to be treated through the space 42, and to purify the water by utilizing the metabolic action of the anaerobic microorganisms living on the surfaces of the filter media 41, 42. As the filter medium 41, granular oyster shells crushed to a size of about 20 to 50 mm and put in a resin net bag are used for 15 to
Used as 20 cm thick. On the other hand, above the filter medium 41,
As the filter material 42, granular porous waste material having a size of about 5 to 15 mm, for example, a cinder of coal used for combustion in a thermal power plant is laminated by a predetermined thickness.

【0020】この生物濾過槽40では、濾材41、42
表面の嫌気性微生物の代謝作用を利用して有機物の低分
子化を図り、最終的にはガス化させる。すなわち、酸生
成菌に属する通性嫌気性微生物群により、水中の高分子
の有機物が酢酸、プロピオン酸、酪酸等の揮発性有機酸
と低級アルコール類とに分解され、さらに、前記有機酸
は絶対嫌気性のメタン生成菌によって、メタン、二酸化
炭素、アンモニア等に分解される仕組みである。
In this biological filtration tank 40, filter media 41, 42
By utilizing the metabolic action of the anaerobic microorganisms on the surface, the molecular weight of organic substances is reduced and finally gasified. That is, by facultative anaerobic microorganisms belonging to the acid-producing bacterium, high molecular organic matter in water is decomposed into volatile organic acids such as acetic acid, propionic acid, butyric acid and lower alcohols, and further, the organic acid is absolutely It is a mechanism that is decomposed into methane, carbon dioxide, ammonia, etc. by anaerobic methanogens.

【0021】前記処理水槽50は、生物濾過槽40を通
過して排出された処理水を殺菌・消毒後、貯留する水槽
であり、その有効容量を中水としての一日当りの使用水
量の約2/3とされる構成である。処理水槽50入口に
は、処理対象水に塩素系の殺菌剤を混入させて処理対象
水内の大腸菌等の病原菌を殺菌・消毒する消毒器51が
配設される。また、処理水槽50には処理水の取水部5
2も配設され、ここで取水された処理水が使用に供され
る。
The treated water tank 50 is a tank for storing treated water discharged through the biological filtration tank 40 after sterilizing and disinfecting it, and its effective capacity is about 2 times the amount of water used as medium water per day. The configuration is / 3. At the inlet of the treated water tank 50, a disinfecting device 51 for sterilizing and disinfecting pathogenic bacteria such as Escherichia coli in the water to be treated by mixing a chlorine-based germicide into the water to be treated is disposed. In addition, the treated water tank 50 has a treated water intake portion 5
2 is also provided, and the treated water taken here is provided for use.

【0022】次に、本実施形態に係る水処理装置におけ
る浄化処理について説明する。処理対象水は流量調整槽
10に流入して一時貯留された後、計量調整部13で送
水量を調整されつつ次工程の付着曝気槽20へ送水され
る。流量調整槽10で処理対象水に対し空気を送り込ん
でいることにより、槽内で処理対象水の流動が促され、
水の腐敗を防止できると共に、攪拌効果による処理対象
水の均質化も図れる。
Next, the purification process in the water treatment device according to this embodiment will be described. The water to be treated flows into the flow rate adjusting tank 10 and is temporarily stored therein, and then is sent to the adhering aeration tank 20 in the next step while the amount of water to be sent is adjusted by the measurement adjusting unit 13. By sending air to the water to be treated in the flow rate adjusting tank 10, the flow of the water to be treated is promoted in the tank,
Water spoilage can be prevented, and the water to be treated can be homogenized by the stirring effect.

【0023】付着曝気槽20では、流量調整槽10から
供給された処理対象水に対し、濾材21による物理的な
濾過で比較的大きな汚濁物質を取除く。また、散気装置
22からの空気注入、すなわち曝気により、充填された
濾材21としての牡蠣殻間へ十分な酸素を供給すると共
に槽内を攪拌して、処理対象水と濾材21に付着した好
気性微生物の生物膜とを繰り返し接触させる。これによ
り、細菌の有機物分解作用を最大限発揮させ、処理対象
水中の有機性汚濁物質を分解除去する。この処理対象水
に塩素化合物が含まれている場合でも、牡蠣殻中のCa
の溶解で処理対象水のPHが適切な状態に保たれ、微生
物の活動を抑制することもなく、浄化処理の効率を維持
できる。
In the adhering aeration tank 20, relatively large contaminants are removed from the water to be treated supplied from the flow rate adjusting tank 10 by physical filtration with the filter medium 21. Further, by injecting air from the air diffuser 22, that is, aeration, sufficient oxygen is supplied between the oyster shells as the filled filter medium 21 and the inside of the tank is agitated so that the water to be treated and the filter medium 21 are adhered to each other. Repeated contact with the biofilm of aerial microorganisms. As a result, the organic substance decomposing action of bacteria is maximized, and the organic pollutants in the water to be treated are decomposed and removed. Even if the water to be treated contains chlorine compounds, Ca in the oyster shells
The pH of the water to be treated can be maintained in an appropriate state by the dissolution of, and the efficiency of the purification treatment can be maintained without suppressing the activity of microorganisms.

【0024】浄化処理の継続により、生物膜が必要以上
に肥厚して濾材21間の間隙を小さくし、処理対象水の
流動性を損う場合には、逆洗装置(図示を省略)を作動
させて水を逆流させ、生物膜を濾材21から剥離させ、
適切な濾材21間の間隙が維持されるようにする。付着
曝気槽20を通過した水は沈殿槽30に達し、汚濁物質
を含む水が沈澱槽30内をゆっくり流れる間に汚濁物質
は沈降し、底部に沈殿して堆積する。汚濁物質を分離さ
れた上澄み水は沈殿槽30から次工程の生物濾過槽40
に流入する。
If the biofilm is thickened more than necessary due to the continuation of the purification treatment to reduce the gap between the filter media 21 and impair the fluidity of the water to be treated, a backwashing device (not shown) is activated. Water to flow back to separate the biofilm from the filter medium 21,
Ensure that a suitable gap between the filter media 21 is maintained. The water that has passed through the adhesion aeration tank 20 reaches the settling tank 30, and while the water containing the pollutant slowly flows in the settling tank 30, the pollutant is settled and settles and accumulates at the bottom. The supernatant water from which contaminants have been separated is transferred from the sedimentation tank 30 to the biological filtration tank 40 in the next step.
Flow into.

【0025】生物濾過槽40では、沈殿槽30から流入
した水の中に残る汚濁成分に対し、まず、濾材41、4
2表面の嫌気性微生物のうち、酸生成菌に属する通性嫌
気性微生物群の代謝作用によって、水中の高分子の有機
物が低分子化、すなわち、酢酸、プロピオン酸、酪酸等
の揮発性有機酸と低級アルコール類とに分解される。そ
して、前記有機酸は絶対嫌気性のメタン生成菌の代謝作
用によって、メタン、二酸化炭素、アンモニア等に分解
され、水中から除去される。この他、比較的大きな汚濁
物質は濾材41、42による物理的な濾過で取除かれ
る。
In the biological filtration tank 40, first, for the pollutant components remaining in the water flowing from the settling tank 30, first, the filter media 41, 4
2 Among the anaerobic microorganisms on the surface, the metabolic action of a facultative anaerobic microorganism group belonging to an acid-producing bacterium lowers the molecular weight of high-molecular organic substances, that is, volatile organic acids such as acetic acid, propionic acid, and butyric acid. And lower alcohols. Then, the organic acid is decomposed into methane, carbon dioxide, ammonia and the like by the metabolic action of the absolutely anaerobic methanogen, and is removed from water. In addition to this, relatively large contaminants are removed by physical filtration with the filter media 41, 42.

【0026】生物濾過槽40から排出された処理水は処
理水槽50に入り、塩素系の殺菌剤による大腸菌などの
殺菌・消毒後、この処理水槽50内に所定期間貯留され
る。この貯留された処理水は、取水部52を通じてトイ
レの洗浄水、樹木への潅水など必要とされる箇所へ送水
され、使用に供されることとなる。
The treated water discharged from the biological filtration tank 40 enters the treated water tank 50, is sterilized and disinfected with E. coli and the like by a chlorine-based bactericide, and is then stored in the treated water tank 50 for a predetermined period. The stored treated water is sent to the required places such as toilet flushing water and irrigation of trees through the water intake unit 52 for use.

【0027】このように、本実施の形態に係る水処理装
置においては、流量調整槽10からの処理対象水に対し
付着曝気槽20内で曝気により酸素を供給すると共に槽
内を攪拌して、好気性微生物の付着する濾材21と処理
対象水とを繰り返し接触させ、水中の主として有機性の
汚濁物質の分解除去を行い、次いで沈殿槽30で汚濁物
質を沈殿させた後、さらに、分離された後の上澄み水中
の有機物を生物濾過槽40内で嫌気性微生物の代謝作用
を利用して分解・ガス化し、最終的に処理水槽50内に
浄化した処理水を得られることから、簡略な構造で確実
に浄化処理が行え、装置全体のコストダウンが図れると
共に、信頼性を向上させられ、保守の手間及びコストも
低減できる。加えて、流量調整槽10の計量調整部13
で次工程以降への送水量を適宜調整可能とすることか
ら、処理水使用量に応じて流量調整槽10からの送水量
を調整して処理水として必要な水量のみを浄化処理で
き、無駄な処理水の発生を抑えられる。なお、前記実施
の形態に係る水処理装置においては、付着曝気槽20で
は、濾材21として牡蠣殻を使用する構成としている
が、これに限らず、有機物の分解除去の目的では他の多
孔性の濾材を用いる構成とすることもできる。
As described above, in the water treatment apparatus according to the present embodiment, oxygen is supplied by aeration in the adhering aeration tank 20 to the water to be treated from the flow rate adjusting tank 10 and the inside of the tank is agitated. The filter medium 21 to which aerobic microorganisms adhere is repeatedly brought into contact with the water to be treated to decompose and remove mainly organic pollutants in the water, and then the pollutants are precipitated in the settling tank 30 and then separated. Since the organic matter in the subsequent supernatant water is decomposed and gasified in the biological filtration tank 40 by utilizing the metabolic action of anaerobic microorganisms, and finally the purified water can be obtained in the treated water tank 50, the structure is simple. The purification process can be performed reliably, the cost of the entire apparatus can be reduced, the reliability can be improved, and the labor and cost of maintenance can be reduced. In addition, the measurement adjustment unit 13 of the flow rate adjustment tank 10
Since it is possible to appropriately adjust the amount of water to be sent to the next process and thereafter, the amount of water to be sent from the flow rate adjusting tank 10 can be adjusted according to the amount of treated water used, so that only the amount of water required as treated water can be purified, which is wasteful. Generation of treated water can be suppressed. In addition, in the water treatment apparatus which concerns on the said embodiment, although it is set as the structure which uses the oyster shell as the filter medium 21 in the adhesion aeration tank 20, it is not restricted to this but other porous materials are used for the purpose of decomposing and removing an organic substance. It is also possible to adopt a configuration using a filter medium.

【0028】[0028]

【発明の効果】以上のように本発明によれば、流量調整
槽からの処理対象水に対し付着曝気槽内で曝気により酸
素を供給するとともに槽内を攪拌して、好気性微生物の
付着する濾材と処理対象水とを繰り返し接触させ、水中
の主として有機性の汚濁物質の分解除去を行い、次いで
沈殿槽で汚濁物質を沈殿させた後、さらに、分離された
後の上澄み水中の有機物を生物濾過槽内で嫌気性微生物
の代謝作用を利用して分解・ガス化し、最終的に処理水
槽内に浄化した処理水を得られることにより、簡略な構
造で確実に浄化処理が行え、装置全体のコストダウンが
図れると共に、信頼性を向上させられ、保守の手間及び
コストも低減できるという効果を奏する。
As described above, according to the present invention, oxygen is supplied by aeration in the adhering aeration tank to the water to be treated from the flow rate adjusting tank and the inside of the tank is agitated to attach aerobic microorganisms. The filter medium and the water to be treated are repeatedly contacted to decompose and remove mainly organic pollutants in the water, and then the pollutants are allowed to settle in the settling tank. By decomposing and gasifying by utilizing the metabolic action of anaerobic microorganisms in the filtration tank, and finally obtaining purified water in the treated water tank, purification treatment can be performed reliably with a simple structure, The cost can be reduced, the reliability can be improved, and the labor and cost for maintenance can be reduced.

【0029】また、本発明によれば、流量調整槽に送水
量調整用の計量調整部を配設し、次工程以降で浄化処理
する処理対象水量を適宜調整可能とすることにより、処
理水使用量に応じて流量調整槽からの送水量を調整して
処理水として必要な水量のみを浄化処理でき、無駄な処
理水の発生を抑えられるという効果を有する。さらに、
装置全体の浄化処理能力に対応させて適正量の処理対象
水を浄化処理工程へ供給できることとなり、処理対象水
に対し効率的に浄化処理を行え、浄化処理の信頼性を向
上させられると共に、濾材の目詰りも進行しにくく、保
守コストを低減できるという効果を有する。
Further, according to the present invention, the treated water is used by arranging a metering adjustment unit for adjusting the amount of water supply in the flow rate adjusting tank and appropriately adjusting the amount of water to be treated for purification treatment in the subsequent steps. The amount of water sent from the flow rate adjusting tank can be adjusted according to the amount, and only the amount of water required as treated water can be purified, and the effect that wasteful treated water is suppressed can be suppressed. further,
An appropriate amount of water to be treated can be supplied to the purification treatment process in accordance with the purification capacity of the entire device, and the water to be treated can be efficiently purified, the reliability of the purification treatment can be improved, and the filter media can be improved. It is also difficult to proceed with the clogging, and the maintenance cost can be reduced.

【0030】また、本発明によれば、流量調整槽で処理
対象水に対し酸素を送込み、処理対象水中に酸素を供給
するとともに槽内を攪拌することにより、貯留した処理
対象水の流動を促すこととなり、処理対象水の腐敗を防
止できるという効果を有する。
Further, according to the present invention, oxygen is sent to the water to be treated in the flow rate adjusting tank, oxygen is supplied into the water to be treated, and the inside of the tank is agitated so that the flow of the stored water to be treated is changed. As a result, the water to be treated can be prevented from spoiling.

【0031】また、本発明によれば、付着曝気槽に充填
する濾材を牡蠣殻とし、曝気用空気の噴出口を付着曝気
槽下部に配置して、充填された牡蠣殻間へ曝気により十
分な酸素を送込むことにより、牡蠣殻表面の好気性微生
物と空気とが効率よく接触することとなり、細菌の有機
物分解作用を最大限発揮させられ、好気性微生物で処理
対象水中の有機性汚濁物質を確実に分解除去できる。さ
らに、処理対象水に塩素化合物が含まれている場合に
は、牡蠣殻中のCaの溶解で処理対象水のPH調整が図
れ、水のPHを適切な状態として細菌の活動を最大限に
高められ、浄化処理の効率を維持できるという効果を有
する。
Further, according to the present invention, the filter medium to be filled in the adhering aeration tank is made of oyster shells, and the jet of air for aeration is arranged at the lower part of the adhering aeration tank so that the space between the filled oyster shells is sufficiently aerated. By sending oxygen, the aerobic microorganisms on the surface of the oyster shell and the air are efficiently contacted, and the organic substance decomposing effect of the bacteria can be maximized, and the aerobic microorganisms remove organic pollutants in the water to be treated. Can be reliably decomposed and removed. Furthermore, when the water to be treated contains chlorine compounds, the pH of the water to be treated can be adjusted by dissolving Ca in the oyster shell, and the pH of the water can be adjusted to an appropriate state to maximize bacterial activity. Therefore, it is possible to maintain the efficiency of the purification treatment.

【0032】また、本発明によれば、生物濾過槽に充填
する濾材を粒状の多孔質材とし、濾材の表面積を十分確
保して濾材表面の嫌気性微生物を汚濁物質の含まれた水
と効率よく接触させられることにより、細菌の有機物分
解作用を最大限発揮させられ、嫌気性微生物で水中の有
機性汚濁物質を確実に分解除去できるという効果を有す
る。
Further, according to the present invention, the filter medium to be filled in the biological filtration tank is made of a granular porous material, and the surface area of the filter medium is sufficiently secured so that anaerobic microorganisms on the surface of the filter medium are efficiently treated with water containing pollutants. By bringing them into close contact with each other, the effect of decomposing the organic matter of bacteria can be exerted to the maximum, and the anaerobic microorganisms can surely decompose and remove the organic pollutants in the water.

【0033】また、本発明によれば、生物濾過槽におけ
る濾材に付着する嫌気性微生物を酸生成菌とメタン生成
菌とし、水中に含まれる汚濁物質である高分子有機物を
酸生成菌で酢酸、プロピオン酸、酪酸等の揮発性有機酸
と低級アルコール類に分解した後、生じた前記有機酸を
メタン生成菌でメタン、二酸化炭素、又はアンモニア等
に分解することにより、水中の有機性汚濁物質を効率よ
く短時間で分解除去でき、処理対象水の浄化処理能力の
より一層の向上が図れるという効果を有する。
Further, according to the present invention, the anaerobic microorganisms adhering to the filter material in the biological filtration tank are acid-producing bacteria and methanogenic bacteria, and the high-molecular organic matter which is a pollutant contained in water is acetic acid-producing bacteria. After decomposing into volatile organic acids such as propionic acid and butyric acid, and lower alcohols, the resulting organic acids are decomposed into methane, carbon dioxide, or ammonia by methanogens to remove organic pollutants in water. This has the effect that it can be efficiently decomposed and removed in a short time, and the purification treatment capacity of the water to be treated can be further improved.

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

【図1】本発明の一実施の形態に係る水処理装置の概略
構成説明図である。
FIG. 1 is a schematic configuration explanatory diagram of a water treatment device according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 水処理装置 10 流量調整槽 11 散気装置 12 ポンプ 13 計量調整部 20 付着曝気槽 21 濾材 22 散気装置 23 プラスチックルーバー 30 沈殿槽 40 生物濾過槽 41、42 濾材 50 処理水槽 51 消毒器 52 取水部 1 Water treatment device 10 Flow rate adjustment tank 11 Air diffuser 12 pumps 13 Weighing adjustment section 20 Adhesive aeration tank 21 Filter media 22 Air diffuser 23 plastic louvers 30 settling tank 40 biological filtration tank 41, 42 filter media 50 treated water tank 51 disinfectant 52 Water intake

───────────────────────────────────────────────────── フロントページの続き (72)発明者 川本 保行 福岡県小郡市大保1627−14 Fターム(参考) 4D003 AA01 AB02 BA01 BA02 BA04 CA02 CA05 CA07 CA08 DA02 DA18 DA19 DA22 EA01 EA22 EA23 EA31 FA10 4D027 AA01 AA14 AA20 AB07 AB14 4D040 BB51 BB91    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Yasuyuki Kawamoto             1627-14 Oho, Ogori-shi, Fukuoka F-term (reference) 4D003 AA01 AB02 BA01 BA02 BA04                       CA02 CA05 CA07 CA08 DA02                       DA18 DA19 DA22 EA01 EA22                       EA23 EA31 FA10                 4D027 AA01 AA14 AA20 AB07 AB14                 4D040 BB51 BB91

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 所定容量の水槽で形成され、所定の廃水
を処理対象水として流入させて一時的に貯留すると共
に、前記処理対象水の送出流量を調整しつつ次工程へ送
出す流量調整槽と、 好気性微生物の付着する濾材を充填される水槽で形成さ
れ、前記流量調整槽から処理対象水を供給され、曝気を
行いつつ処理対象水を前記濾材間に通して浄化する付着
曝気槽と、 所定容量の水槽で形成され、前記付着曝気槽から排出さ
れた処理対象水を供給され、当該処理対象水中の汚濁物
質を沈殿させる沈殿槽と、 嫌気性微生物の付着する多孔質の濾材を充填される水槽
で形成され、前記沈殿槽で汚濁物質と分離された上澄み
水を供給され、当該上澄み水を前記濾材間に通して浄化
する生物濾過槽と、 当該生物濾過槽から排出された水を殺菌した上で貯留す
る処理水槽とを備えることを特徴とする水処理装置。
1. A flow rate adjusting tank which is formed of a water tank having a predetermined capacity, in which a predetermined waste water is made to flow in as treatment target water to be temporarily stored, and at the same time the delivery flow rate of the treatment target water is regulated to be transmitted to the next step. And an adhering aeration tank that is formed of a water tank filled with a filter medium to which aerobic microorganisms adhere, is supplied with water to be treated from the flow rate adjusting tank, and purifies the water to be treated by passing it through the filter medium while performing aeration. , A settling tank that is formed of a water tank of a specified capacity, is supplied with the water to be treated discharged from the aeration tank for adhering, and precipitates contaminants in the water to be treated, and a porous filter medium to which anaerobic microorganisms adhere A biological filtration tank that is formed by a water tank that is supplied with the supernatant water that has been separated from the pollutants in the precipitation tank and that purifies the supernatant water by passing it through the filter media, and the water discharged from the biological filtration tank. Save after sterilizing Water treatment device, characterized in that it comprises a treating tank for.
【請求項2】 前記請求項1に記載の水処理装置におい
て、 前記流量調整槽が、前記付着曝気槽への送水量を調整す
る計量調整部を配設されることを特徴とする水処理装
置。
2. The water treatment apparatus according to claim 1, wherein the flow rate adjustment tank is provided with a metering adjustment unit that adjusts a water supply amount to the adhesion aeration tank. .
【請求項3】 前記請求項1又は2に記載の水処理装置
において、 前記流量調整槽が、空気の噴出口を設置され、前記処理
対象水中に空気を送込まれることを特徴とする水処理装
置。
3. The water treatment apparatus according to claim 1 or 2, wherein the flow rate adjusting tank is provided with an air ejection port, and air is sent into the water to be treated. apparatus.
【請求項4】 前記請求項1ないし3のいずれかに記載
の水処理装置において、 前記付着曝気槽が、濾材として牡蠣殻を不規則配置状態
で充填されると共に、曝気用空気の噴出口を下部に設置
されることを特徴とする水処理装置。
4. The water treatment apparatus according to claim 1, wherein the adhering aeration tank is filled with oyster shells as a filter medium in an irregularly arranged state, and the aeration air outlet is provided. A water treatment device that is installed at the bottom.
【請求項5】 前記請求項1ないし4のいずれかに記載
の水処理装置において、 前記生物濾過槽が、濾材の一部として大きさが5〜15
mm程度となる粒状の多孔質材を充填されることを特徴
とする水処理装置。
5. The water treatment apparatus according to any one of claims 1 to 4, wherein the biological filtration tank has a size of 5 to 15 as a part of a filter medium.
A water treatment device characterized by being filled with a granular porous material having a size of about mm.
【請求項6】 前記請求項1ないし5のいずれかに記載
の水処理装置において、 前記生物濾過槽が、濾材に酸生成菌に属する通性嫌気性
微生物群及び絶対嫌気性のメタン生成菌を付着されてな
ることを特徴とする水処理装置。
6. The water treatment apparatus according to claim 1, wherein the biological filtration tank contains a facultative anaerobic microorganism group belonging to an acid-producing bacterium and an absolutely anaerobic methanogenic bacterium in a filter medium. A water treatment device characterized by being attached.
JP2002047578A 2002-02-25 2002-02-25 Water treatment apparatus Pending JP2003245686A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002047578A JP2003245686A (en) 2002-02-25 2002-02-25 Water treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002047578A JP2003245686A (en) 2002-02-25 2002-02-25 Water treatment apparatus

Publications (1)

Publication Number Publication Date
JP2003245686A true JP2003245686A (en) 2003-09-02

Family

ID=28660598

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002047578A Pending JP2003245686A (en) 2002-02-25 2002-02-25 Water treatment apparatus

Country Status (1)

Country Link
JP (1) JP2003245686A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018030098A (en) * 2016-08-24 2018-03-01 新明和工業株式会社 Wastewater treatment apparatus
CN114436397A (en) * 2022-01-14 2022-05-06 南京大学 A processing apparatus for high concentration organic, difficult biochemical waste water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018030098A (en) * 2016-08-24 2018-03-01 新明和工業株式会社 Wastewater treatment apparatus
CN114436397A (en) * 2022-01-14 2022-05-06 南京大学 A processing apparatus for high concentration organic, difficult biochemical waste water

Similar Documents

Publication Publication Date Title
CN101891336B (en) System and method for leachate treatment in sanitary landfill
CN101148302A (en) Method for treating waste water of livestock and fowl cultivation
CN101318758A (en) Air-float and bio-filter combined water treatment process
CN101538100A (en) Method for treating dyeing wastewater and dedicated device
JP5544512B2 (en) Circulation culture apparatus and method for seafood
CN101468859A (en) Advanced purification treatment system for high concentrated organic wastewater
JP2000312542A (en) Circulatory filtration apparatus for culturing fishes and shellfishes
KR100921194B1 (en) Sewage and wastewater treatment plant
JP5351270B2 (en) Equipment, toilet, livestock shed and method for treatment of urea-containing water
CN1994936A (en) Method for processing and resuing carbinol waste water for circulated cooling water
CN104829050B (en) Full automatic control Hospital Sewage Treatment method and apparatus
CN214060278U (en) Mariculture tail water discharging device
CN1208262C (en) High concentration oxganic effluent treatment composite process and its equipment
CN108408900A (en) Composite reaction device for wastewater treatment
CN2825629Y (en) Bio-wall sewage treatment device
CN210150897U (en) Reclaimed water recycling device
CN102372395A (en) Device for processing papermaking wastewater
JP2003245686A (en) Water treatment apparatus
CN206188598U (en) Waste water treatment equipment that raises pigs intensifies
CN115572017A (en) Internal circulation method and system for aquaculture tail water
KR20030097075A (en) Hybrid Submerged Plate Type Membrane Bioreactor Using microfilter Combined With Biofilm-Activated Carbon for Advanced Treatment of Sewage and Wastewater
JP2002113484A (en) Water cleaning treatment method and apparatus therefor
CN111925070A (en) Domestic sewage treatment process method
CN217077131U (en) Slaughter wastewater treatment system
CN216550036U (en) Microbial purification sewage treatment pond