JP2003326289A - Polluted water treatment apparatus - Google Patents

Polluted water treatment apparatus

Info

Publication number
JP2003326289A
JP2003326289A JP2003104989A JP2003104989A JP2003326289A JP 2003326289 A JP2003326289 A JP 2003326289A JP 2003104989 A JP2003104989 A JP 2003104989A JP 2003104989 A JP2003104989 A JP 2003104989A JP 2003326289 A JP2003326289 A JP 2003326289A
Authority
JP
Japan
Prior art keywords
polluted
raw water
effective microorganisms
purification
polluted water
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
JP2003104989A
Other languages
Japanese (ja)
Inventor
Hideki Morishita
日出旗 森下
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.)
OSAKA SEIBUTSU KANKYO KAGAKU K
OSAKA SEIBUTSU KANKYO KAGAKU KENKYUSHO KK
Original Assignee
OSAKA SEIBUTSU KANKYO KAGAKU K
OSAKA SEIBUTSU KANKYO KAGAKU KENKYUSHO 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 OSAKA SEIBUTSU KANKYO KAGAKU K, OSAKA SEIBUTSU KANKYO KAGAKU KENKYUSHO KK filed Critical OSAKA SEIBUTSU KANKYO KAGAKU K
Priority to JP2003104989A priority Critical patent/JP2003326289A/en
Publication of JP2003326289A publication Critical patent/JP2003326289A/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

<P>PROBLEM TO BE SOLVED: To provide a polluted water treatment apparatus which is high in cleaning efficiency, does not give rise to secondary pollution, does not require an apparatus for a waste treatment, does not require a wide space for installation and is low in cost. <P>SOLUTION: The apparatus is provided with reaction chambers 14 and 15 for adsorbing effective microorganisms on adsorbent materials and holding the same and a spray water jetting device 18 for spraying and jetting the polluted raw water into the reaction chambers 14 and 15 and passing the water to flow therein. The effective microorganisms are formed or retrieved and specified by the adequateness of the decomposition cleaning effect to the previously collected polluted raw water and the apparatus is provided with a culture tank for culturing the effective microorganisms formed or retrieved and specified separately from a polluted water cleaning line. <P>COPYRIGHT: (C)2004,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、汚濁水処理装置に
関する。
TECHNICAL FIELD The present invention relates to a polluted water treatment device.

【0002】[0002]

【従来の技術】従来、汚水の浄化方法は、例えば、調整
槽、曝気槽、沈殿槽等を浄化ラインに設け、調整槽で
は、比較的大きな異物の沈殿と予備的な曝気をおこな
い、曝気槽にて、本格的な曝気をおこなった後、沈殿槽
にて、凝集剤を投入して、浮遊している汚濁物質を凝集
沈殿させた後、放流すると共に、凝集させた余剰汚泥
は、例えば、脱水機等を用いて乾燥処理した後、産業廃
棄物として処理していた。
2. Description of the Related Art Conventionally, a method for purifying sewage has, for example, provided an adjusting tank, an aeration tank, a sedimentation tank, etc. in a purification line. In the adjustment tank, a relatively large amount of foreign matter is precipitated and preliminary aeration is performed. At that time, after performing a full-scale aeration, in the settling tank, a coagulant is added to coagulate and settle the floating pollutants, and the coagulated surplus sludge is discharged, for example, After being dried using a dehydrator or the like, it was treated as industrial waste.

【0003】[0003]

【発明が解決しようとする課題】しかし、上述のような
従来の浄化方法では、浄化率が低い上に、余剰汚泥が多
量に発生し、それを処理するための脱水、乾燥、焼却、
取引等々に要する経費(産廃処理費)が嵩み、コスト高
になるという問題があった。しかも、硫酸アルミニウム
やポリアクリルアミドの様な凝集剤を使用する場合が多
く、運転コストが嵩む上に、二次公害が発生することも
あった。
However, in the conventional purification method as described above, in addition to a low purification rate, a large amount of excess sludge is generated, and dehydration, drying, incineration, and
There has been a problem that the cost required for transactions and the like (industrial waste processing cost) increases and the cost increases. Moreover, a coagulant such as aluminum sulfate or polyacrylamide is often used, which increases operating costs and may cause secondary pollution.

【0004】また、脱水、乾燥、焼却等をおこなうため
の各種(産廃処理)装置類を必要として、設備全体が、
大掛かりで高価なものとなり、かつ、設置のために広い
スペース(敷地面積)を必要とするという問題もあっ
た。
Further, various equipments (industrial waste treatment) for performing dehydration, drying, incineration, etc. are required, and the entire equipment is
There is also a problem that it is large-scale and expensive and requires a large space (site area) for installation.

【0005】そこで、本発明は、浄化率が高く、二次公
害が発生せず、産廃処理のための装置が不要で、設置の
ために広いスペースを必要とせず、コスト安な、汚濁水
処理装置を提供することを目的としている。
Therefore, the present invention has a high purification rate, does not cause secondary pollution, does not require a device for industrial waste treatment, does not require a large space for installation, and is low in cost and treats polluted water. The purpose is to provide a device.

【0006】[0006]

【課題を解決するための手段】本発明の汚濁水処理装置
は、汚濁水浄化ラインに、有効微生物を吸着物質に吸着
させて保持する反応槽と、汚濁原水を該反応槽中に散水
噴射して流過させるための散水噴射装置と、を設け、上
記有効微生物は予め採取された上記汚濁原水に対する分
解浄化作用の好適性により作成又は検索して特定され、
作成又は検索して特定された該有効微生物を培養する培
養槽を、上記汚濁水浄化ラインとは別に設けたものであ
る。また、上記吸着物質が、石英粗面岩,活性炭,木
炭,カキ殻,サンゴ砂,セラミックス,ナイロン綱,黒
雲母流紋岩,黒雲母花崗岩,流紋岩,花崗岩の内の一種
又は二種以上の組合せであるのも好ましい。さらに、上
記有効微生物が、シュードモナス,プロテアバクテリ
ア,フラボバクテリア,コリネバクテリア,アクチノバ
クテリア,サイトファーガ,ノカルデイア,アルカリジ
ェネス,クロモバクテリア,ニトロソモナス,ニトロバ
クター,ゾーグレア,バシルス,アシネトバクターの内
の一種又は二種以上の組合せであるも好ましい。
The polluted water treatment apparatus of the present invention comprises a reaction tank for adsorbing and retaining active microorganisms in a polluted water purification line, and spraying of polluted raw water into the reaction tank. And a sprinkler injection device for flowing through, and the effective microorganisms are created or searched by the suitability of decomposition and purification action on the polluted raw water previously collected, and are specified by
A culture tank for culturing the effective microorganism that has been created or searched and specified is provided separately from the polluted water purification line. Further, the adsorbed material is one or more of quartz trachyte, activated carbon, charcoal, oyster shell, coral sand, ceramics, nylon rope, biotite rhyolite, biotite granite, rhyolite, and granite. It is also preferable that the combination of Further, the above-mentioned effective microorganism is one or two of Pseudomonas, Proteabacteria, Flavobacteria, Corynebacteria, Actinobacteria, Cytoferga, Nocardia, Alkaline Genes, Chromobacteria, Nitrosomonas, Nitrobacter, Zogrea, Bacillus, Acinetobacter. A combination of two or more species is also preferable.

【0007】[0007]

【発明の実施の形態】以下、本発明の実施の形態を示す
図面に基づき、本発明を詳説する。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described below in detail with reference to the drawings showing an embodiment of the present invention.

【0008】図1は本発明の汚濁水処理方法を実施する
ための装置の基本的な構成の好ましい一例を示し、1
は、汚濁原水を取り込み、砂等の比較的大きな異物を沈
殿させるための沈砂槽で、内部に仕切板や堰等を設けて
いる。2は、沈砂槽1から導入した汚濁原水を一時貯留
するための原水槽である。なお、5は、汚濁原水を濾過
するためのフィルターを内蔵した細目スクリーンであ
る。3は、原水槽2から導入した汚濁原水のpHや温度
等を調整するための調整槽であり、4は、pHや温度等
の調整をおこなうための測定器、6は、曝気をおこなう
ためのエアパイプで、ブロア7と接続されている。
FIG. 1 shows a preferred example of the basic construction of an apparatus for carrying out the polluted water treatment method of the present invention.
Is a sand settling tank for taking in polluted raw water and precipitating relatively large foreign matter such as sand, and has a partition plate and a weir inside. Reference numeral 2 is a raw water tank for temporarily storing the polluted raw water introduced from the sand settling tank 1. In addition, 5 is a fine screen incorporating a filter for filtering the contaminated raw water. 3 is an adjusting tank for adjusting pH, temperature, etc. of the contaminated raw water introduced from the raw water tank 2, 4 is a measuring instrument for adjusting pH, temperature, etc., 6 is an aerator. It is connected to the blower 7 with an air pipe.

【0009】8,9は調整された原水を浄化のために曝
気させる曝気槽、10,11は、曝気槽8,9の底部に配設
されたポンプ、12,13は、曝気をおこなうためのエアパ
イプである。14,15は、曝気槽8,9の直上位置に配設
された散水噴射濾床式バイオリアクターと称される反応
槽(散水噴射反応槽)で、その内部には、吸着物質担体
として、例えば、多孔質の黒雲母流紋岩16…が投入・堆
積されており、その底部には、多数の細孔を有する濾床
17が敷設されている。一方、曝気槽8,9の上部には、
ポンプ10,11に接続された散水用ノズル(散水装置)18
…が多く配設されている。なお、吸着物質としては、上
記黒雲母流紋岩16の他に、石英粗面岩,活性炭,木炭,
カキ殻,サンゴ砂,セラミックス,ナイロン綱,黒雲母
花崗岩,流紋岩,花崗岩を用いても良い。このとき、二
種以上を適宜組合せても良い。
Reference numerals 8 and 9 are aeration tanks for aerating the adjusted raw water for purification, 10, 11 are pumps arranged at the bottom of the aeration tanks 8 and 12, and 13 are aeration tanks for performing aeration. It is an air pipe. Reference numerals 14 and 15 denote reaction tanks (sprinkling injection reaction tanks) called sprinkling injection filter bed bioreactors arranged directly above the aeration tanks 8 and 9. , Porous biotite rhyolite 16 ... has been deposited and deposited, and a filter bed with many pores at the bottom
17 are laid. On the other hand, above the aeration tanks 8 and 9,
Sprinkler nozzle (sprinkler) 18 connected to pumps 10 and 11
Many are arranged. In addition to the above biotite rhyolite 16, quartz trachyte, activated carbon, charcoal,
Oyster shell, coral sand, ceramics, nylon rope, biotite granite, rhyolite, granite may be used. At this time, two or more kinds may be appropriately combined.

【0010】上述の黒雲母流紋岩16…には、浄化の対象
となる汚濁原水に対して、好適な浄化作用を有する有効
微生物(分解有効菌)が吸着・保持されている。その有
効微生物は、予め、浄化の対象となる汚濁原水を採取し
て、その汚濁原水に対して好適な浄化作用を有するもの
が作成又は検索され、好気的、嫌気的等をも勘案して、
別途、培養槽等で効率よく培養・育生されたものであ
り、例えば、シュードモナス、バシルス、アシネトバク
ター,プロテアバクテリア,フラボバクテリア,コリネ
バクテリア,アクチノバクテリア,サイトファーガ,ノ
カルデイア,アルカリジェネス,クロモバクテリア,ニ
トロソモナス,ニトロバクター,ゾーグレア等がある。
なお、これらを二種以上を適宜組合せても良い。
The biotite rhyolite 16 ... Adsorbs and retains effective microorganisms (decomposition effective bacteria) having a suitable purification action on the contaminated raw water to be purified. The effective microorganisms are collected in advance from the polluted raw water to be purified, and those having a suitable purifying action for the polluted raw water are created or searched for, taking into consideration aerobic, anaerobic, etc. ,
Separately, it has been efficiently cultivated and raised in a culture tank or the like, and examples thereof include Pseudomonas, Bacillus, Acinetobacter, Proteabacterium, Flavobacterium, Corynebacterium, Actinobacteria, Cytophaga, Nocardia, Alcaligenes, Chromobacteria, Nitroso. Monas, Nitrobacter, Zogrea, etc.
It should be noted that two or more of these may be appropriately combined.

【0011】従って、散水噴射用ノズル18…から散水噴
射された原水は、バイオリアクターとしての多孔質の流
紋岩16…を流過する際に、その中に含まれている汚濁物
質が有効微生物によって効率よく分解・浄化された後、
濾床17を経て、直下に配置されている曝気槽8,9に落
下する。この曝気槽8,9では、常時、エアパイプ12,
13によって曝気がおこなわれており、汚濁物質が分解さ
れやすい状態とされ、ポンプ10,11で吸い上げられて、
散水噴射・濾過の循環が繰り返しおこなわれて浄化が重
ねられ、所定の浄化率に達した後に、その原水は、下流
側に配設されている循環槽19に流下し、さらに沈降槽20
にて異物を沈降させた後に、放流される。なお、図1
中、24は曝気のオン・オフを操作するための開閉弁であ
る。
Therefore, when the raw water sprayed from the spray nozzles 18 ... Flows through the porous rhyolite 16 ... As a bioreactor, the pollutants contained therein are effective microorganisms. After being efficiently decomposed and purified by
It passes through the filter bed 17 and falls into the aeration tanks 8 and 9 arranged immediately below. In the aeration tanks 8 and 9, the air pipe 12,
Aeration is performed by 13 and pollutants are easily decomposed, and pumped up by pumps 10 and 11,
After repeating the spraying and filtration cycles to carry out purification to reach a predetermined purification rate, the raw water flows down to the circulation tank 19 disposed on the downstream side, and further to the sedimentation tank 20.
After the foreign matter is settled at, it is discharged. Note that FIG.
24 is an on-off valve for operating on / off of aeration.

【0012】そして、最終段の沈降槽20の底部には、還
流用のポンプ21が設けられており、一点鎖線で示す還流
ライン25によって、原水槽2及び調整槽3又は曝気槽
8,9に還流させることにより、その還流水中に含まれ
ている有効微生物を再度の浄化のために使用し、無駄な
流失を防ぐことができる。このような還流操作によっ
て、分解効率を、常時、安定に保持することができ、浄
化率を顕著に向上させることができる。また、三方切換
弁27を操作することによって、一点鎖線で示す還流ライ
ン25を二点鎖線で示す還流ライン26と接続し、最終段の
沈降槽20の未分解物及び分解菌を原水槽2又は調整槽
3,曝気槽8に還流させることにより、より一層の浄化
を図ることもできる。
A reflux pump 21 is provided at the bottom of the final settling tank 20, and the raw water tank 2 and the adjusting tank 3 or the aeration tanks 8 and 9 are connected by a reflux line 25 indicated by a chain line. By refluxing, the effective microorganisms contained in the refluxed water can be used again for purification, and wasteful flushing can be prevented. By such a reflux operation, the decomposition efficiency can be constantly kept stable, and the purification rate can be remarkably improved. Further, by operating the three-way switching valve 27, the reflux line 25 shown by the one-dot chain line is connected to the reflux line 26 shown by the two-dot chain line, and undegraded substances and degrading bacteria in the final settling tank 20 are fed to the raw water tank 2 or Further purification can be achieved by refluxing to the adjusting tank 3 and the aeration tank 8.

【0013】このような循環を伴う散水反応槽14,15を
用いた汚濁水処理方法では、その汚濁原水に対して好適
な浄化作用を有する有効微生物(分解有効菌)を、予
め、検索(特定)又は作成して浄化処理をおこなうの
で、無駄がなく、効率の高い浄化をおこなうことがで
き、従来よりも、はるかに高い浄化率を確保することが
できる。
In the polluted water treatment method using the sprinkling reaction tanks 14 and 15 with such circulation, effective microorganisms (decomposition effective bacteria) having a suitable purifying action for the contaminated raw water are searched (specified) in advance. ) Or producing and performing purification treatment, it is possible to perform purification with high efficiency without waste and to secure a much higher purification rate than in the past.

【0014】その浄化率の向上により、従来は(浄化率
が低いために)大量に発生していた余剰汚泥が著しく減
少し、産業廃処理のための装置が不要となる。また、余
剰汚泥を処理する場合(脱水、乾燥、焼却、取引等)に
おいては、大幅な経費節減となる。しかも、薬液を使用
しないので、二次公害がないことも大きな利点である。
なお、導入した有効微生物は、浄化後は、自己分解して
自然消滅し、公害は一切ない。
With the improvement of the purification rate, a large amount of excess sludge that has been generated in the past (due to the low purification rate) is significantly reduced, and an apparatus for industrial waste treatment is not required. Also, when treating excess sludge (dehydration, drying, incineration, trading, etc.), significant cost savings can be achieved. Moreover, since no chemicals are used, there is no secondary pollution, which is a great advantage.
After purification, the introduced effective microorganisms self-decompose and disappear spontaneously without any pollution.

【0015】また、装置の構成が簡素であるため、安
価、小規模で、設置のために広いスペースを要さないの
で、従来の装置に比べて、大幅なコストの削減が可能と
なる。しかも、容易に、既設装置の浄化能力を向上させ
ることができる。そのためには、例えば、予め、検索し
て、特定の培養した有効微生物を、適当な担体(多孔質
吸着物質等)に担持させて、既設装置の曝気槽(反応
槽)内に投入すればよく、設備を増加することなく、浄
化能力をコスト安に強化(実質的な増設)することがで
きる。
Further, since the structure of the device is simple, it is inexpensive, small-scale, and does not require a large space for installation, so that the cost can be greatly reduced as compared with the conventional device. Moreover, the purification capacity of the existing device can be easily improved. For that purpose, for example, it is sufficient to carry out a search in advance and carry a specific cultured effective microorganism on an appropriate carrier (porous adsorbing substance etc.) and put it in the aeration tank (reaction tank) of the existing device. The purification capacity can be strengthened at a low cost (substantially increased) without increasing the equipment.

【0016】一方、比較的規模の大きな浄化プラントに
本発明の方法を適用する場合には、有効微生物に活発な
分解作用をおこなわせるための反応槽として、例えば、
散水噴射型の水槽を用い、その水槽中で、担体(多孔質
吸着物質等)に有効微生物を担持させ、分解処理をおこ
なわせるようにすれば、有効微生物の分解活性をダイナ
ミックに増大させることができ、高い浄化能力を確保で
きる。
On the other hand, when the method of the present invention is applied to a relatively large-scale purification plant, as a reaction tank for causing active microorganisms to actively decompose, for example,
If a sprinkling jet type water tank is used and the carrier (porous adsorbing substance, etc.) is loaded with the effective microorganisms in the water tank so that the decomposition treatment is carried out, the decomposition activity of the effective microorganisms can be dynamically increased. It is possible to secure high purification ability.

【0017】要するに、本発明の汚濁水処理方法は、例
えば、図2のフローチャートに示すように、予め汚濁原
水を採取し(S1)、その汚濁原水に対して好適な浄化
作用を有する有効微生物を検索(特定)又は作成し(S
2)、その有効微生物を(好気的、嫌気的に)培養・育
生して(S3)、バイオリアクターとして反応槽内に投
入し(S4)、これを適当な担体に吸着・保持させ(S
5)、その反応槽内で、汚濁原水を浄化処理する(S
6)ものであり、その装置の構成の詳細の如何を問わな
い。
In short, the method for treating polluted water according to the present invention, for example, as shown in the flow chart of FIG. 2, collects polluted raw water in advance (S1), and selects effective microorganisms having a suitable purification action for the polluted raw water. Search (specific) or create (S
2) Cultivate and grow the effective microorganisms (aerobically and anaerobically) (S3), put them into a reaction tank as a bioreactor (S4), and adsorb and retain them on an appropriate carrier (S3).
5), the polluted raw water is purified in the reaction tank (S
6), regardless of the details of the configuration of the device.

【0018】その装置については、例えば、反応槽は循
環を伴うものが好ましいが、循環を伴わないものであっ
てもよく、また、多段に積み重ねてもよく、多数個を平
面に接続展開してもよく、あるいは、これらを適宜に組
み合わせてもよく、その構成は、使用条件や周囲条件等
に応じて、適宜、必要に応じて改良されてよい。
With respect to the apparatus, for example, it is preferable that the reaction tank is accompanied by circulation, but it may be one not accompanied by circulation, or may be stacked in multiple stages, and a large number of them are connected and developed in a plane. Or, these may be appropriately combined, and the configuration thereof may be appropriately improved according to the use conditions, the ambient conditions, and the like.

【0019】次いで、本発明の実施例につき説明する。 (実施例1)有効微生物としてシュードモナスを用いた
汚濁水処理装置により、食品工場から排出される排水
(原水)を浄化した場合、表1に示すような結果(浄化
実績データ)を得られた。
Next, examples of the present invention will be described. (Example 1) When wastewater (raw water) discharged from a food factory was purified by a polluted water treatment device using Pseudomonas as an effective microorganism, the results (purification record data) shown in Table 1 were obtained.

【0020】[0020]

【表1】 [Table 1]

【0021】表1から、特に、原水中に多量に含まれて
いたSS(浮遊物質)が激減し、その浄化率は、99.8%
であった。なお、表1にて、BODは生物化学的酸素要
求量、CODは化学的酸素要求量、n−Hexはノルマ
ル・ヘキサンを示す。
From Table 1, in particular, a large amount of SS (suspended matter) contained in the raw water was drastically reduced, and the purification rate was 99.8%.
Met. In Table 1, BOD is biochemical oxygen demand, COD is chemical oxygen demand, and n-Hex is normal hexane.

【0022】(実施例2)有効微生物としてバシルスを
用いた汚濁水処理装置により、食品(かまぼこ)工場か
ら排出される排水(原水)を浄化した場合、表2に示す
ような結果を得られた。
(Example 2) When wastewater (raw water) discharged from a food (kamaboko) factory was purified by a polluted water treatment device using Bacillus as an effective microorganism, the results shown in Table 2 were obtained. .

【0023】[0023]

【表2】 [Table 2]

【0024】表2から、原水中に多量に含まれていたB
ODは、そのほとんどが浄化され、その浄化率は、99.9
%であった。
From Table 2, B contained in a large amount in raw water
Most of the OD is purified, and the purification rate is 99.9.
%Met.

【0025】(実施例3)有効微生物としてアシネトバ
クターを用いた汚濁水処理装置により、製油工場から排
出される排水(原水)を浄化した場合、表3に示すよう
な結果を得られた。
(Example 3) When wastewater (raw water) discharged from an oil refinery was purified by a polluted water treatment device using Acinetobacter as an effective microorganism, the results shown in Table 3 were obtained.

【0026】[0026]

【表3】 [Table 3]

【0027】表3から、原水中に多量に含まれていたn
−Hexは、そのほとんどが浄化され、その浄化率は、
99.9%であった。
From Table 3, n contained in a large amount in raw water
Most of Hex is purified, and its purification rate is
It was 99.9%.

【0028】[0028]

【発明の効果】請求項1乃至3記載の発明によれば、浄
化の対象となる汚濁原水に対して好適な浄化作用を有す
る有効微生物を予め検索(特定)又は作成して、その有
効微生物を培養して使用するので、無駄がなく、従来よ
りも、はるかに効率の高い浄化をおこなうことができ、
高い浄化率を確保することができる。
According to the inventions of claims 1 to 3, effective microorganisms having a suitable purifying action on the contaminated raw water to be purified are searched (specified) or prepared in advance, and the effective microorganisms are identified. Since it is used after culturing, it is possible to carry out purification without waste and with much higher efficiency than before.
A high purification rate can be secured.

【0029】その浄化率の向上により、従来は(浄化率
が低いために)大量に発生していた余剰汚泥が著しく減
少する。従って、産業廃処理のための装置が不要とな
る。また、余剰汚泥を処理する場合(脱水、乾燥、焼
却、取引等)においては、大幅な経費節減となる。
Due to the improvement of the purification rate, a large amount of excess sludge that has been conventionally generated (due to the low purification rate) is significantly reduced. Therefore, a device for industrial waste treatment becomes unnecessary. Also, when treating excess sludge (dehydration, drying, incineration, trading, etc.), significant cost savings can be achieved.

【0030】また、薬液を使用しないので、二次公害が
ないことも大きな利点である。なお、導入した有効微生
物は、浄化後は、自己分解して自然消滅し、公害は一切
ない。
Since no chemicals are used, there is no secondary pollution, which is a great advantage. After purification, the introduced effective microorganisms self-decompose and disappear spontaneously without any pollution.

【0031】そして、装置の構成が簡素化されているた
め、安価、小規模で、設置のために広いスペースを要さ
ないため、従来の装置に比べて、大幅なコストの削減が
可能となる。
Since the structure of the device is simplified, the device is inexpensive and small in size, and does not require a large space for installation. Therefore, it is possible to significantly reduce the cost as compared with the conventional device. .

【0032】しかも、既設装置の浄化能力を向上するた
めには、例えば、予め、検索して、培養した特定の有効
微生物を、適当な吸着物質に担持させて、既設装置の曝
気槽(反応槽)等内に投入すればよく、設備を増加する
ことなく、浄化能力を容易に強化(実質的な増設)する
ことができる。
In addition, in order to improve the purification capacity of the existing equipment, for example, a specific effective microorganism that has been previously searched and cultivated is supported on an appropriate adsorbent, and the aeration tank (reaction tank) of the existing equipment is supported. ), Etc., the purification capacity can be easily enhanced (substantially increased) without increasing the equipment.

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

【図1】本発明の汚濁水処理装置の実施の一形態を示す
構成図である。
FIG. 1 is a configuration diagram showing an embodiment of a polluted water treatment device of the present invention.

【図2】本発明の汚濁水処理方法の実施の一形態を示す
フローチャートである。
FIG. 2 is a flowchart showing an embodiment of the polluted water treatment method of the present invention.

【符号の説明】[Explanation of symbols]

14 反応槽 15 反応槽 16 吸着物質 18 散水装置(散水用ノズル) 14 Reaction tank 15 reaction tank 16 Adsorbed substance 18 Sprinkler (sprinkling nozzle)

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4B065 AA01X AA04X AA12X AA15X AA24X AA41X BD22 BD23 CA54 4D003 AA01 AB12 DA03 DA15 DA30 EA01 EA14 EA17 EA23 EA24 EA25 EA30 4D040 DD03 DD24    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4B065 AA01X AA04X AA12X AA15X                       AA24X AA41X BD22 BD23                       CA54                 4D003 AA01 AB12 DA03 DA15 DA30                       EA01 EA14 EA17 EA23 EA24                       EA25 EA30                 4D040 DD03 DD24

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 汚濁水浄化ラインに、有効微生物を吸着
物質に吸着させて保持する反応槽と、汚濁原水を該反応
槽中に散水噴射して流過させるための散水噴射装置と、
を設け、上記有効微生物は予め採取された上記汚濁原水
に対する分解浄化作用の好適性により作成又は検索して
特定され、作成又は検索して特定された該有効微生物を
培養する培養槽を、上記汚濁水浄化ラインとは別に設け
たことを特徴とする汚濁水処理装置。
1. A polluted water purification line, a reaction tank for adsorbing and retaining effective microorganisms on an adsorbent, and a spraying device for spraying and flowing contaminated raw water into the reaction tank.
The effective microorganisms are created or searched by the suitability of decomposition and purification action for the polluted raw water previously collected, and the culture tank for culturing the effective microorganisms created or searched is used for the contamination. A polluted water treatment device, which is provided separately from the water purification line.
【請求項2】 上記吸着物質が、石英粗面岩,活性炭,
木炭,カキ殻,サンゴ砂,セラミックス,ナイロン綱,
黒雲母流紋岩,黒雲母花崗岩,流紋岩,花崗岩の内の一
種又は二種以上の組合せである請求項1記載の汚濁水処
理装置。
2. The adsorbent material is quartz trachyte, activated carbon,
Charcoal, oyster shell, coral sand, ceramics, nylon rope,
The polluted water treatment device according to claim 1, which is one or a combination of two or more of biotite rhyolite, biotite granite, rhyolite, and granite.
【請求項3】 上記有効微生物が、シュードモナス,プ
ロテアバクテリア,フラボバクテリア,コリネバクテリ
ア,アクチノバクテリア,サイトファーガ,ノカルデイ
ア,アルカリジェネス,クロモバクテリア,ニトロソモ
ナス,ニトロバクター,ゾーグレア,バシルス,アシネ
トバクターの内の一種又は二種以上の組合せである請求
項1又は2記載の汚濁水処理装置。
3. The effective microorganism is selected from Pseudomonas, Proteabacterium, Flavobacterium, Corynebacterium, Actinobacteria, Cytoferga, Nocardia, Alcaligenes, Chromobacteria, Nitrosomonas, Nitrobacter, Zogrea, Bacillus, Acinetobacter. The polluted water treatment device according to claim 1 or 2, which is one kind or a combination of two or more kinds.
JP2003104989A 2003-04-09 2003-04-09 Polluted water treatment apparatus Pending JP2003326289A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003104989A JP2003326289A (en) 2003-04-09 2003-04-09 Polluted water treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003104989A JP2003326289A (en) 2003-04-09 2003-04-09 Polluted water treatment apparatus

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP11206099A Division JP2001029992A (en) 1999-07-21 1999-07-21 Method and apparatus for treating polluted water

Publications (1)

Publication Number Publication Date
JP2003326289A true JP2003326289A (en) 2003-11-18

Family

ID=29707387

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003104989A Pending JP2003326289A (en) 2003-04-09 2003-04-09 Polluted water treatment apparatus

Country Status (1)

Country Link
JP (1) JP2003326289A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006043575A (en) * 2004-08-04 2006-02-16 Actac Kk Waste liquid treatment device with oil and fat decomposition process
WO2006057287A1 (en) * 2004-11-25 2006-06-01 Toshiaki Kusu Inhibitor for active sludge formation
JP2015092831A (en) * 2013-11-08 2015-05-18 株式会社大阪生物環境科学研究所 Polluted water treatment method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006043575A (en) * 2004-08-04 2006-02-16 Actac Kk Waste liquid treatment device with oil and fat decomposition process
WO2006057287A1 (en) * 2004-11-25 2006-06-01 Toshiaki Kusu Inhibitor for active sludge formation
JPWO2006057287A1 (en) * 2004-11-25 2008-06-05 楠 敏明 Activated sludge production inhibitor
JP2015092831A (en) * 2013-11-08 2015-05-18 株式会社大阪生物環境科学研究所 Polluted water treatment method

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