JPH04349995A - Water treatment - Google Patents

Water treatment

Info

Publication number
JPH04349995A
JPH04349995A JP3149290A JP14929091A JPH04349995A JP H04349995 A JPH04349995 A JP H04349995A JP 3149290 A JP3149290 A JP 3149290A JP 14929091 A JP14929091 A JP 14929091A JP H04349995 A JPH04349995 A JP H04349995A
Authority
JP
Japan
Prior art keywords
bacteria
wastewater
waste water
magnetotaxis
magnetotactic bacteria
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
JP3149290A
Other languages
Japanese (ja)
Inventor
Toshihito Kondo
敏仁 近藤
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.)
Fujita Corp
Original Assignee
Fujita Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fujita Corp filed Critical Fujita Corp
Priority to JP3149290A priority Critical patent/JPH04349995A/en
Publication of JPH04349995A publication Critical patent/JPH04349995A/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

  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Activated Sludge Processes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PURPOSE:To separate bacteria efficiently using a simple device without any chemical by using magnetotaxis bacteria as microbes and separating waste water treated by the active bacteria from spent water treated by the action of a line of magnetic force, when organic waste water is purified by proliferating microbes in an organic spent water. CONSTITUTION:A magnetotaxis microbe (for example, Aguaspir; llummagnetotoacticum ATCC 31632) is used as a microbe when an organic waste water is purified by proliferating the microbe in the organic waste water. The waste water treated which contains the proliferating magnetotaxis bacteria is supplied to a magnetic field on which a magnet 9 acts in a bacterium separation device 7 and the magnetotaxis bacteria is gathered in a place in the waste water by the action of the line of magnetic force. In addition, the part, of the waste water, where the magnetotaxis bacteria is collected is extracted from a bottom flow path 11. Consequently, the bacteria can be separated efficiently using a simple device without the use of chemicals.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、微生物を利用して有機
性排水を浄化処理する方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying organic wastewater using microorganisms.

【0002】0002

【従来の技術】都市下水、工場排水等の各種排水中で微
生物を増殖させ、排水中に含まれる有機物および無機塩
類を微生物に摂取させることにより排水を浄化する生物
学的水処理方法においては、担体に固定した微生物を利
用する場合以外は、増殖した微生物菌体を処理後の水か
ら分離する必要がある。菌体分離は、従来、重力沈降法
、膜分離法、凝集沈殿法などの方法により行われている
が、重力沈降法は沈降性の高いフロックを形成する微生
物群の場合に限って実施可能であり、膜分離法は装置コ
ストおよび操業コストが高いという難点があり、さらに
凝集沈殿法は、凝集剤を添加する必要があるためその費
用がかさむことと分離された菌体が水処理に再使用でき
ないものになるため種汚泥の継続的投入が必要であると
いう問題点がある。微生物を担体に固定して行う水処理
においては上述のような菌体分離の問題は生じないが、
被処理水に対する菌体量をあまり多くすることができな
いため、浄化能率が悪い。
[Prior Art] In biological water treatment methods, microorganisms are grown in various types of wastewater such as urban sewage and industrial wastewater, and the wastewater is purified by allowing the microorganisms to ingest organic matter and inorganic salts contained in the wastewater. Unless microorganisms immobilized on a carrier are used, it is necessary to separate the grown microbial cells from the treated water. Conventionally, bacterial cell isolation has been carried out using methods such as gravity sedimentation, membrane separation, and coagulation sedimentation, but gravity sedimentation is only possible for microorganisms that form highly sedimentable flocs. However, the membrane separation method has the disadvantage of high equipment and operating costs, and the coagulation-sedimentation method requires the addition of a flocculant, which increases the cost, and the separated bacterial cells cannot be reused for water treatment. There is a problem in that it is necessary to continuously input seed sludge. In water treatment where microorganisms are immobilized on carriers, the above-mentioned problem of bacterial cell separation does not occur;
Since the amount of bacteria in the water to be treated cannot be increased too much, the purification efficiency is poor.

【0003】0003

【発明が解決しようとする課題】本発明の目的は、従来
の生物学的水処理方法が上述の理由により処理水からの
菌体分離に多くの費用を要していたことに鑑み、より簡
単で低コストの菌体分離が可能な生物学的水処理方法を
提供することにある。
[Problems to be Solved by the Invention] In view of the fact that conventional biological water treatment methods require a lot of expense for separating bacterial cells from treated water due to the above-mentioned reasons, it is an object of the present invention to The object of the present invention is to provide a biological water treatment method that enables low-cost bacterial cell separation.

【0004】0004

【課題を解決するための手段】本発明が提供することに
成功した新規な生物学的水処理方法は、微生物として走
磁性細菌を利用し、増殖した走磁性細菌を含有する処理
済み排水を磁場に供給して走磁性細菌を磁力線の作用に
より排水中で偏在させ、偏在する走磁性細菌が含まれる
部分の排水を分取することにより処理済み排水から走磁
性細菌を分離することを特徴とするものである。
[Means for Solving the Problems] A novel biological water treatment method successfully provided by the present invention utilizes magnetotactic bacteria as microorganisms, and the treated wastewater containing the grown magnetotactic bacteria is subjected to a magnetic field. The method is characterized by separating magnetotactic bacteria from treated wastewater by feeding magnetotactic bacteria into the wastewater to cause magnetotactic bacteria to be unevenly distributed in the wastewater by the action of magnetic lines of force, and separating the wastewater in a portion containing the unevenly distributed magnetotactic bacteria. It is something.

【0005】[0005]

【作用】走磁性細菌(Magnetotactic b
acteria)と呼ばれる一群の細菌は、量的には少
ないが通常の活性汚泥中にも存在し、単独でも有機性排
水の浄化に利用可能な菌学的性質特性を備えているが、
それだけでなく、鉄イオンを菌体内に取り込み、磁性体
である四三酸化鉄(Fe3O4)に変換して細胞内に蓄
える性質がある。したがって、磁場に置かれると、菌体
内の酸化鉄が磁力線に感応することにより菌体は特定の
磁極の方向に移動する(N極に向かうかS極に向かうか
は地球上の位置によって異なり、北半球ではN極に向か
うが南半球ではS極に向かう。)。本発明の水処理方法
は、走磁性細菌のこの性質を利用して処理水からの菌体
濃縮と分離を行うものである。
[Action] Magnetotactic b
A group of bacteria called ``acteria'' exist in ordinary activated sludge, although in small quantities, and have mycological properties that can be used alone to purify organic wastewater.
In addition, it has the property of taking iron ions into the bacterial cells, converting them into triferric tetroxide (Fe3O4), which is a magnetic substance, and storing it within the cells. Therefore, when placed in a magnetic field, the iron oxide within the bacteria body responds to the magnetic field lines, causing the bacteria to move in the direction of a specific magnetic pole (whether toward the north or south pole depends on the location on the earth, In the Northern Hemisphere, it goes towards the North Pole, but in the Southern Hemisphere, it goes towards the South Pole.) The water treatment method of the present invention utilizes this property of magnetotactic bacteria to concentrate and separate bacterial cells from treated water.

【0006】本発明の水処理法に使用可能な走磁性細菌
の具体例としては、Aquaspirillummag
netotacticum ATCC31632 があ
る。利用する走磁性細菌はまた、一般的な活性汚泥法に
よる活性汚泥含有処理水を磁場に置いてその中の走磁性
細菌を濃縮し、それを排水処理に使用して再び磁場によ
る濃縮処理に付する操作を反復することにより、活性汚
泥から分離したものであってもよい。微生物として走磁
性細菌を利用することを除けば、本発明による水処理方
法における微生物処理工程は従来の好気的微生物処理と
同様にして行うことができる。ただし、走磁性細菌は微
好気条件を好むので、従来の一般的な活性汚泥法に比べ
ると曝気量はかなり少なくてよい。
Specific examples of magnetotactic bacteria that can be used in the water treatment method of the present invention include Aquaspirillum mag.
netotacticum ATCC31632. The magnetotactic bacteria used can also be obtained by placing activated sludge-containing treated water in a magnetic field in a general activated sludge method to concentrate the magnetotactic bacteria in it, and then using it for wastewater treatment and subjecting it to concentration treatment using a magnetic field again. It may be separated from the activated sludge by repeating this operation. Except for the use of magnetotactic bacteria as microorganisms, the microbial treatment step in the water treatment method according to the present invention can be carried out in the same manner as conventional aerobic microbial treatment. However, since magnetotactic bacteria prefer microaerophilic conditions, the amount of aeration may be much smaller than in conventional activated sludge methods.

【0007】走磁性細菌の増殖に伴う浄化処理を受けた
排水は、磁場に送って菌体分離を行う。地磁気よりも強
い磁束密度の磁場に置かれると、走磁性細菌の菌体は特
定磁極方向に移動し、その磁極側の装置器壁付近に凝集
するように集まるから、これを最小限度の水と共に任意
の手段で分取する。菌体を除いた後の水は、そのまま放
流するか、さらに高度の浄化処理に付する。分取した汚
泥状の走磁性細菌菌体は処理槽に返送し、排水処理に再
利用する。この菌体分離操作は、浄化に使用する走磁性
細菌のスクリーニングにもなるので、被処理排水と共に
雑菌が処理槽に入り込んで来てもその量は一定の水準を
超えることはない。菌体分離装置で分離された菌体のう
ち過剰のものは、マグネタイト原料として利用すること
もできる。
[0007] Wastewater that has been purified due to the growth of magnetotactic bacteria is sent to a magnetic field to separate the bacteria. When placed in a magnetic field with a magnetic flux density stronger than the earth's magnetic field, magnetotactic bacterial cells move in the direction of a specific magnetic pole and aggregate near the wall of the device on the magnetic pole side. Separate by any method. After the bacterial cells have been removed, the water is either discharged as is or undergoes a more advanced purification process. The collected sludge-like magnetotactic bacterial cells are returned to the treatment tank and reused for wastewater treatment. This bacterial cell separation operation also serves as a screening for magnetotactic bacteria to be used for purification, so even if miscellaneous bacteria enter the treatment tank along with the wastewater to be treated, the amount will not exceed a certain level. Excess of the bacterial cells separated by the bacterial cell separation device can also be used as a raw material for magnetite.

【0008】[0008]

【実施例】本発明実施のための装置構成の概要を図1に
示す。処理槽1はパイプ2により原水貯槽3と結ばれて
おり、ここから被処理排水の供給を受ける。処理槽1に
は撹拌装置4および通気装置5が付属している。処理槽
1中の菌体含有排水はパイプ6により菌体分離装置7に
移送されるようになっている。菌体分離装置7は、図2
に拡大して示したように、末端で上下2本に分かれる管
状の排水流路8および該排水流路8を挟むようにN極と
S極とが前者を下側にして配置された電磁石9からなる
。末端で分岐した排水流路8の上側流路10は放流水出
口に通じ、下側流路11は菌体返送管12により処理槽
1に通じている。
Embodiment FIG. 1 shows an outline of the apparatus configuration for carrying out the present invention. The treatment tank 1 is connected to a raw water storage tank 3 through a pipe 2, from which it is supplied with wastewater to be treated. A stirring device 4 and an aeration device 5 are attached to the processing tank 1. The bacterial cell-containing wastewater in the treatment tank 1 is transferred to a bacterial cell separation device 7 through a pipe 6. The bacterial cell isolation device 7 is shown in FIG.
As shown in the enlarged view, there is a tubular drainage channel 8 that is divided into two upper and lower sections at the end, and an electromagnet 9 in which an N pole and a S pole are arranged with the former facing downward so as to sandwich the drainage channel 8. Consisting of An upper flow path 10 of the drainage flow path 8 branched at the end communicates with the discharge water outlet, and a lower flow path 11 communicates with the treatment tank 1 through a bacterial return pipe 12.

【0009】処理する排水は、原水貯槽3においてpH
、BOD等を調整した後、パイプ2経由で処理槽1に送
り、あらかじめ投入して置いた走磁性細菌の種汚泥と混
合し、撹拌装置4による撹拌および通気装置5による曝
気を行なって微好気条件を維持しながら走磁性細菌によ
る浄化処理を進める。その後、処理済みの排水を走磁性
細菌と共にパイプ6経由で菌体分離装置7に送る。電磁
石9の磁束密度を地磁気のそれよりも十分強くしておく
と、排水中の走磁性細菌菌体は排水流路8を流れる間に
N極側に吸引され、排水流路8のN極側管壁に沿って流
れるようになる。そして末端で下側流路11に流入し、
菌体返送管12を通って処理槽1に返送され、再び浄化
処理に関与する。菌体が分離された処理水は上側流路1
0を通って放流水出口に向かう。
[0009] The wastewater to be treated has a pH of
, BOD, etc., are sent to the treatment tank 1 via the pipe 2, mixed with the seed sludge of magnetotactic bacteria that has been placed in advance, and stirred by the stirring device 4 and aerated by the aeration device 5 to make the microorganisms fine. Proceed with the purification process using magnetotactic bacteria while maintaining atmospheric conditions. Thereafter, the treated wastewater is sent to a bacterial cell separation device 7 via a pipe 6 along with magnetotactic bacteria. If the magnetic flux density of the electromagnet 9 is made sufficiently stronger than that of the earth's magnetism, the magnetotactic bacterial cells in the wastewater will be attracted to the north pole side while flowing through the wastewater flow path 8, and will be attracted to the north pole side of the wastewater flow path 8. It begins to flow along the tube wall. Then, it flows into the lower flow path 11 at the end,
The microbial cells are returned to the treatment tank 1 through the cell return pipe 12 and participate in the purification process again. The treated water from which the bacterial cells have been separated is passed through the upper flow path 1.
0 and head towards the discharge water outlet.

【0010】0010

【発明の効果】上述のように、本発明は微生物として走
磁性細菌を利用し、増殖した走磁性細菌を磁力線の作用
により処理済み排水から分離するものであるから、重力
沈降法よりも速やかに、また膜分離法よりも簡単な装置
で且つ低い操業コストで、さらに凝集沈殿法のように薬
剤の添加を要することなしに、簡単に菌体分離を行うこ
とができる。また、走磁性細菌が微好気条件を好むため
、一般的な従来の活性汚泥法に比べると曝気量を著しく
少なくすることができるから、エネルギー消費も少なく
てすむ。以上により、本発明によれば全体として極めて
低いコストで排水浄化を行うことが可能になる。
[Effects of the Invention] As mentioned above, the present invention uses magnetotactic bacteria as microorganisms and separates the grown magnetotactic bacteria from treated wastewater by the action of magnetic lines of force, so it is more rapid than the gravity sedimentation method. Furthermore, bacterial cells can be easily separated using a simpler device and at a lower operating cost than the membrane separation method, and without requiring the addition of chemicals as in the coagulation-sedimentation method. Furthermore, since magnetotactic bacteria prefer microaerobic conditions, the amount of aeration can be significantly reduced compared to the conventional activated sludge method, resulting in less energy consumption. As described above, according to the present invention, it becomes possible to purify wastewater at an extremely low cost overall.

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

【図1】  本発明実施のための装置構成を示す略図。FIG. 1 is a schematic diagram showing the configuration of an apparatus for implementing the present invention.

【図2】  図1における菌体分離装置の略断面図。FIG. 2 is a schematic cross-sectional view of the bacterial cell separation device in FIG. 1.

【符号の説明】[Explanation of symbols]

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  有機性排水中で微生物を増殖させるこ
とにより該有機性排水を浄化するに当たり、微生物とし
て走磁性細菌を利用し、増殖した走磁性細菌を含有する
処理済み排水を磁場に供給して走磁性細菌を磁力線の作
用により排水中で偏在させ、偏在する走磁性細菌が含ま
れる部分の排水を分取することにより処理済み排水から
走磁性細菌を分離することを特徴とする水処理方法。
Claim 1: In purifying organic wastewater by growing microorganisms in the organic wastewater, magnetotactic bacteria are used as the microorganisms, and the treated wastewater containing the multiplied magnetotactic bacteria is supplied to a magnetic field. A water treatment method characterized by separating magnetotactic bacteria from treated wastewater by making magnetotactic bacteria unevenly distributed in wastewater by the action of magnetic lines of force, and separating the wastewater in a portion containing the unevenly distributed magnetotactic bacteria. .
JP3149290A 1991-05-27 1991-05-27 Water treatment Pending JPH04349995A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3149290A JPH04349995A (en) 1991-05-27 1991-05-27 Water treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3149290A JPH04349995A (en) 1991-05-27 1991-05-27 Water treatment

Publications (1)

Publication Number Publication Date
JPH04349995A true JPH04349995A (en) 1992-12-04

Family

ID=15471952

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3149290A Pending JPH04349995A (en) 1991-05-27 1991-05-27 Water treatment

Country Status (1)

Country Link
JP (1) JPH04349995A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100398455B1 (en) * 1998-12-29 2003-12-24 주식회사 포스코 Method for Cleaning Electrolyte Aqueous Solution
WO2010071059A1 (en) * 2008-12-17 2010-06-24 栗田工業株式会社 Microbial electricity-generating method and microbial electric generator
CN104986870A (en) * 2015-07-10 2015-10-21 浙江大学 Rice planting water heavy-metal pollution recycling treatment apparatus and control method
JP2016153508A (en) * 2016-04-21 2016-08-25 創研株式会社 Cleaner containing microbe and washing method using microbe

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5458951A (en) * 1977-10-19 1979-05-12 Asahi Carbon Co Ltd Method of disposing starch and*or saccharoid containing waste water
JPS6181778A (en) * 1984-09-28 1986-04-25 Hitachi Ltd Separation and recover of aquatic microorganism
JPS6240299A (en) * 1985-08-14 1987-02-21 Hitachi Ltd Separation of aquatic bacteria

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5458951A (en) * 1977-10-19 1979-05-12 Asahi Carbon Co Ltd Method of disposing starch and*or saccharoid containing waste water
JPS6181778A (en) * 1984-09-28 1986-04-25 Hitachi Ltd Separation and recover of aquatic microorganism
JPS6240299A (en) * 1985-08-14 1987-02-21 Hitachi Ltd Separation of aquatic bacteria

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100398455B1 (en) * 1998-12-29 2003-12-24 주식회사 포스코 Method for Cleaning Electrolyte Aqueous Solution
WO2010071059A1 (en) * 2008-12-17 2010-06-24 栗田工業株式会社 Microbial electricity-generating method and microbial electric generator
CN104986870A (en) * 2015-07-10 2015-10-21 浙江大学 Rice planting water heavy-metal pollution recycling treatment apparatus and control method
JP2016153508A (en) * 2016-04-21 2016-08-25 創研株式会社 Cleaner containing microbe and washing method using microbe

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