JPH02268896A - Method for acclimatizing and incubating microbe for cleaning fish farming water tank such as living sea-fish preserve - Google Patents

Method for acclimatizing and incubating microbe for cleaning fish farming water tank such as living sea-fish preserve

Info

Publication number
JPH02268896A
JPH02268896A JP1089984A JP8998489A JPH02268896A JP H02268896 A JPH02268896 A JP H02268896A JP 1089984 A JP1089984 A JP 1089984A JP 8998489 A JP8998489 A JP 8998489A JP H02268896 A JPH02268896 A JP H02268896A
Authority
JP
Japan
Prior art keywords
seawater
nitrogen compounds
activated sludge
sewage
fish
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
JP1089984A
Other languages
Japanese (ja)
Inventor
Masahiro Fujii
正博 藤井
Osamu Miki
理 三木
Yoshinori Takezaki
義則 竹崎
Yasushi Kamori
裕史 嘉森
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP1089984A priority Critical patent/JPH02268896A/en
Publication of JPH02268896A publication Critical patent/JPH02268896A/en
Pending legal-status Critical Current

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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

  • Farming Of Fish And Shellfish (AREA)
  • Activated Sludge Processes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE:To immediately use a fish farming water tank by charging an activated sludge-mixed liq. and blast-furnace water granulated slag into an aeration tank, supplying artificial sewage while being aerated to oxidize the ammoniacal nitrogen compd. to a nitric nitrogen compd. and successively replacing the sewage by seawater. CONSTITUTION:The liq. mixture of sewage and activated sludge and blast-furnace water granulated slag are charged into an activated sludge aeration tank provided with an oxidation reduction potential controller and a pH controller, and aerated with the oxidation-reduction potential as an index. The artificial sewage of fresh water contg. an ammoniacal compd. and an org. material capable of being decomposed by activated sludge to oxidize the ammoniacal nitrogen compd. to a nitric nitrogen compd. When oxidation proceeds until >=80% complete, the artificial sewage is successively replaced by seawater. When the >=90% of the ammoniacal nitrogen compd. is oxidized to the nitric nitrogen compd. or the water is completely replaced by seawater, the water is used for cleaning a living-fish preserve. Consequently, the module for cleaning the fish farming water tank can be immediately used.

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は、海水活魚用イケス等の蓄養水槽の浄化処理
に適した好気性及び嫌気性微生物の馴養、培養方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for acclimating and cultivating aerobic and anaerobic microorganisms suitable for purifying a culture tank for seawater live fish such as Ikes.

(従来の技術) 近年、食生活の高級化に伴い、鯛、ヒラメ等の高級海水
魚を生きたままトラック、鉄道貨車等により輸送したり
、あるいは、魚市場、魚屋、料理屋等の店頭にイケスを
設置し、これらの海水魚を生きたまま販売したり、或は
、料理することが多くなった。
(Conventional technology) In recent years, as eating habits have become more sophisticated, high-quality saltwater fish such as sea bream and flounder are being transported alive by trucks, railway wagons, etc., or being displayed at fish markets, fish stores, restaurants, etc. These seawater fish are often sold alive or cooked by setting up cages.

海水魚を生きたまま輸送したり、或は、イケス等の蓄養
水槽で飼育する場合、魚の排泄物や投餌の残漬物等の腐
敗により発生するアンモニア性窒素化合物、硫化物、有
機物等の有害物質によって魚が死んだり、弱ったりする
。このため、これらのイケス等の蓄養水槽は、海水の浄
化処理装置の設置が必要である。
When marine fish are transported alive or reared in fish tanks, etc., harmful substances such as ammonia nitrogen compounds, sulfides, and organic substances are generated due to decomposition of fish excrement and leftover bait. The substance kills or weakens the fish. For this reason, it is necessary to install a seawater purification treatment device in the storage tanks for these fish.

従来、海水活魚用イケス等の蓄養水槽の浄化処理は、微
生物の固定化担体として砂、砂利、珊瑚、プラスチック
、セラミックス等を充填した浄化処理装置に活魚を飼育
しているイケス等の蓄養水槽の海水を循環させて、固定
化担体の表面に浄化作用のある微生物を自然に発生させ
て、浄化処理する方法が一般的である。
Conventionally, purification treatment of aquariums such as Ikesu for live seawater fish is carried out in a purification treatment device filled with sand, gravel, coral, plastic, ceramics, etc. as a carrier for immobilizing microorganisms. A common method for purification treatment is to circulate seawater to naturally generate purifying microorganisms on the surface of the immobilized carrier.

例えば、「水処理技術」(VOl、29. NCL9.
1988゜p、29〜34)に記載されている方法は、
淡水魚を飼育している水槽の浄化処理に関するもので、
多孔性セラミックスを粉砕して篩分けし、粒径4〜6腸
のものをイケス等の蓄養水槽の浄化処理用微生物の固定
化担体に用いて、多孔性セラミックスの表面に微生物を
自然発生させて固定化し浄化処い。
For example, "Water Treatment Technology" (VOl, 29. NCL9.
1988, p. 29-34),
This is related to the purification treatment of aquariums in which freshwater fish are kept.
Porous ceramics are crushed and sieved, and those with a particle size of 4 to 6 in size are used as immobilization carriers for microorganisms for purification treatment of storage tanks such as Ikesu, and microorganisms are naturally generated on the surface of the porous ceramics. Fixed and purified.

イケス等の蓄養水槽の海水は、魚の排泄物、投餌の残漬
物から発生するアンモニア性窒素化合物、硫化物、有機
物等による汚染がある。これらの汚濁物の除去は、物理
化学的方法だと添加する酸化剤、凝集剤等の薬品を用い
るので、魚への影響を考えると、薬品を用いない生物化
学的処理の方が適切と思われる。即ち、アンモニア性窒
素化合物は、硝化、脱窒法により、硫化物は硫酸イオン
に酸化するのが、また、有機物は酸化分解して炭酸ガス
と増殖汚泥に変換して、それぞれ除去するのが適切と思
われる。
The seawater in fish breeding tanks is contaminated with ammonia nitrogen compounds, sulfides, organic matter, etc. generated from fish excrement and bait leftovers. To remove these pollutants, physicochemical methods use chemicals such as oxidizing agents and flocculants, so considering the impact on fish, biochemical treatment that does not use chemicals seems more appropriate. It will be done. In other words, it is appropriate to remove ammonia nitrogen compounds by nitrification and denitrification methods, oxidize sulfides to sulfate ions, and remove organic substances by oxidative decomposition and convert them into carbon dioxide and grown sludge. Seem.

アンモニア性窒素化合物の除去に関与する微生物は、亜
硝酸化菌、硝化菌と脱窒菌であり、この内、亜硝酸化菌
を固定化法により馴養、培養する方法が知られている。
Microorganisms involved in the removal of ammonia nitrogen compounds include nitrite-oxidizing bacteria, nitrifying bacteria, and denitrifying bacteria. Among these, a method of acclimatizing and culturing nitrite-oxidizing bacteria by immobilization is known.

例えば、特開昭63−44995号公報においては、亜
硝酸化菌を含む活性汚泥を活性炭と固定酸からなる包括
体固定化担体に固定化して汚水処理を行っている。即ち
、活性炭を固定酸に加えて形成した吸着剤に亜硝酸化菌
を含む活性汚泥を付着させ、次にアルギン酸ナトリュム
、カラギンナン、ポリアクリルアミド等のゲルで包括す
る。そして、この混合物を酸素含有ガスの曝気下で、C
OD成分と接触させて、汚水を効率良く処理する方法で
ある。
For example, in Japanese Patent Application Laid-Open No. 63-44995, sewage treatment is performed by immobilizing activated sludge containing nitrite-oxidizing bacteria on an inclusion immobilization carrier consisting of activated carbon and immobilized acid. That is, activated sludge containing nitrite-oxidizing bacteria is attached to an adsorbent formed by adding activated carbon to a fixed acid, and then encased in a gel of sodium alginate, carrageenan, polyacrylamide, or the like. Then, this mixture was heated under aeration of oxygen-containing gas with C.
This is a method for efficiently treating wastewater by bringing it into contact with OD components.

また、特開昭63−36898号公報においては、培養
液中で多孔質担体に亜硝酸化菌を付着生息させて培養液
に栄養物質を補給して培養を続けた固定化細菌と活性汚
泥とをアンモニア性窒素化合物含有汚水に作用させて、
アンモニア性窒素化合物の亜硝酸化を行う方法である。
Furthermore, in JP-A No. 63-36898, nitrite-oxidizing bacteria were allowed to adhere to and live on a porous carrier in a culture solution, and the culture was continued by supplying nutrients to the culture solution. by acting on wastewater containing ammonia nitrogen compounds,
This is a method of oxidizing ammoniacal nitrogen compounds to nitrite.

これらの公知の方法は、アンモニア性窒素化合物を亜硝
酸性窒素化合物に酸化する方法で、魚のイケス等の蓄養
水槽の浄化処理に用いるには、魚に対して神経性前にな
る亜硝酸性窒素化合物を生成するので好ましくない。
These known methods oxidize ammonia nitrogen compounds to nitrite nitrogen compounds, and when used for purification treatment of fish breeding tanks, etc., nitrite nitrogen compounds, which are pre-nervous to fish, are This is not preferable because it generates compounds.

(発明が解決しようとする課題) 従来の活魚用イケス等の蓄養水槽の浄化処理は、次のよ
うな問題点がある。
(Problems to be Solved by the Invention) Conventional purification treatment of culture tanks such as Ikesu for live fish has the following problems.

(1)浄化処理は、浄化処理装置の塔、リアクター等に
微生物の固定化担体として砂、砂利、珊瑚、プラスチッ
ク、セラミックス等を充填し、これに魚を飼育している
イケス等の蓄養水槽の水を循環させて、固定化担体の表
面に自然に発生した微生物を用いて浄化処理を行ってい
る。このため、固定化担体の表面に微生物が発生するま
で、がなりの日数を要し、その間、魚を飼育することが
できず、また、微生物が高密度に増殖しない。
(1) Purification treatment involves filling the tower, reactor, etc. of the purification treatment equipment with sand, gravel, coral, plastic, ceramics, etc. as a carrier for immobilizing microorganisms, and then filling it with sand, gravel, coral, plastic, ceramics, etc. as a carrier for immobilizing microorganisms. Purification treatment is performed by circulating water and using microorganisms that naturally occur on the surface of the immobilization carrier. For this reason, it takes several days for microorganisms to appear on the surface of the immobilization carrier, during which time fish cannot be raised and microorganisms do not grow at a high density.

(2〕  イケス等の蓄養水槽の汚染物質であるアンモ
ニア性窒素化合物を魚に対して有害な亜硝酸性窒素化合
物をほとんど生成せずに魚に対して殆ど毒性が無い硝酸
性窒素化合物に酸化する硝化菌、特に耐海水性硝化菌が
イケス等の蓄養水槽の浄化処理に用いられていない。
(2) Oxidizes ammonia nitrogen compounds, which are contaminants in fish breeding tanks, to nitrate nitrogen compounds, which are almost non-toxic to fish, without producing nitrite nitrogen compounds, which are harmful to fish. Nitrifying bacteria, especially seawater-resistant nitrifying bacteria, are not used for purification of fish storage tanks.

(3)魚の排泄物、投餌の残漬物等の有機物及びこれら
の腐敗によって生成した有機物、硫化物等を酸化、分解
して無毒化する微生物、特に耐海水性微生物が用いられ
ていない。
(3) Microorganisms, especially seawater-resistant microorganisms, that oxidize, decompose, and detoxify organic matter such as fish excrement and bait leftovers, as well as organic matter and sulfides generated by their decay, are not used.

(4)耐海水性硝化菌及び有害な有機物、硫化物等を酸
化、分解して無毒化する耐海水性微生物の馴養、培養方
法が確立されていない。
(4) A method for acclimating and cultivating seawater-resistant nitrifying bacteria and seawater-resistant microorganisms that oxidize and decompose harmful organic matter, sulfides, etc. to render them nontoxic has not been established.

このため、イケス等の蓄養水槽の浄化処理に関与する微
生物は、浄化処理装置に固定化後、馴養を行わずに直ち
に浄化処理を開始し、また、浄化処理装置のコンパクト
化を計るため、効率良く浄化処理が可能な微生物が必要
である。
For this reason, the microorganisms involved in the purification process of the storage aquarium, such as Ikes, start the purification process immediately after being immobilized in the purification treatment equipment without acclimatization, and in order to make the purification treatment equipment more compact, the efficiency Microorganisms that can be well purified are required.

(課題を解決するための手段) 本発明者らは、上記に述べた従来のイケス等の蓄養水槽
の浄化処理の問題点を解決するため蓄養水槽の浄化処理
に適した微生物の馴養、培養方法を確立した。
(Means for Solving the Problems) In order to solve the above-mentioned problems in the conventional purification process for aquariums, etc. established.

本発明は、酸化還元電位(ORP)制御装置とpH制御
装置とを備えた活性汚泥処理の曝気槽に下水≠活性汚泥
の混合液と高炉水砕を入れ、この曝気槽のORPを指標
にして空気を曝気しながら曝気槽にアンモニア性化合物
と活性汚泥によって分解可能な有機物を含む淡水の人工
下水を供給し、アンモニア性窒素化合物の80%以上が
硝酸性窒素化合物に酸化されるようになって、人工廃水
の淡水を海水に逐次置き換え、最終的に海水100%の
人工廃水のアンモニア性窒素化合物が硝酸性窒素化合物
に90%以上酸化されるようになったら海水活魚用イケ
スの浄化処理に用いる事を特徴とする海水活魚用イケス
等の蓄養水槽の浄化処理に適した好気性微生物の馴養、
培養方法、並びに、攪拌機、ORP ffA御装置及び
pHIII御装置を備えた嫌気性リアクターに下水処理
場の活性汚泥混合液と高炉水砕を入れ、リアクター内を
攪拌しながら硝酸性窒素化合物と活性汚泥によって分解
可能な有機物を含む淡水系の人工下水を供給し、硝酸性
窒素化合物の80%以上が還元、除去されるようになっ
たら、人工下水の淡水を海水に逐次置き換え、最終的に
海水100%の人工下水の硝酸性窒素化合物が90%以
上が還元されるようになったら海水活魚用イケス等の蓄
養水槽の浄化処理に用いる事を特徴とする海水活魚用イ
ケスの浄化処理に適した嫌気性微生物の馴養、培養方法
である。
The present invention involves putting sewage≠activated sludge mixture and granulated blast furnace water into an aeration tank for activated sludge treatment equipped with an oxidation-reduction potential (ORP) control device and a pH control device, and using the ORP of this aeration tank as an index. Freshwater artificial sewage containing ammoniacal compounds and organic matter that can be decomposed by activated sludge is supplied to the aeration tank while aerating the air, and more than 80% of the ammoniacal nitrogen compounds are oxidized to nitrate nitrogen compounds. , The freshwater of the artificial wastewater is successively replaced with seawater, and when the ammonia nitrogen compounds in the artificial wastewater, which is 100% seawater, are finally oxidized to nitrate nitrogen compounds by more than 90%, it is used for the purification treatment of Ikesu for seawater live fish. Acclimation of aerobic microorganisms suitable for purification treatment of culture tanks such as Ikesu for seawater live fish, characterized by
Cultivation method: Put activated sludge mixture from a sewage treatment plant and granulated blast furnace water into an anaerobic reactor equipped with a stirrer, an ORP ffA control device, and a pHIII control device, and while stirring the inside of the reactor, nitrate nitrogen compounds and activated sludge are mixed. When 80% or more of the nitrate nitrogen compounds have been reduced and removed, the freshwater in the artificial sewage is gradually replaced with seawater, and finally the seawater is reduced to 100%. When 90% or more of the nitrate nitrogen compounds in artificial sewage have been reduced, it can be used for purification of culture tanks such as Ikes for seawater live fish. This is a method for acclimating and cultivating sexual microorganisms.

(作 用) 本発明者らは、イケス等の蓄養水槽における汚濁物を、
魚の排泄物、投餌の残漬物、これらの腐敗によって生成
した有機物、硫化物、亜硝酸性窒素化合物及びアンモニ
ア性窒素化合物と推定し、悪影響が少ない生物化学的処
理法の方が適していると考えた。
(Function) The present inventors removed contaminants in a breeding tank for fish, etc.
It is estimated that the waste is fish excrement, bait leftovers, organic matter, sulfides, nitrite nitrogen compounds, and ammonia nitrogen compounds produced by their decay, and that biochemical treatment methods with fewer negative effects are more suitable. Thought.

即ち、これらの汚濁物を生物化学的方法により除去する
場合、有機物、硫化物、亜硝酸性窒素化合物及びアンモ
ニア性窒素化合物は、好気性微生物により、即ち、有機
物は酸化分解により炭酸ガスと菌体に、硫化物は酸化し
て硫酸イオンに、亜硝酸性窒素化合物とアンモニア性窒
素化合物は酸化して硝酸性窒素化合物に、それぞれ変換
し、ま脱窒菌によって窒素ガスに還元して除去するのが
適切である。
That is, when these pollutants are removed by biochemical methods, organic substances, sulfides, nitrite nitrogen compounds, and ammonia nitrogen compounds are removed by aerobic microorganisms, that is, organic substances are oxidized and decomposed into carbon dioxide and bacterial cells. First, sulfide is oxidized to sulfate ions, and nitrite nitrogen compounds and ammonia nitrogen compounds are oxidized to nitrate nitrogen compounds, which are then reduced to nitrogen gas by denitrification bacteria and removed. Appropriate.

また、これらの汚濁物を除去する微生物を馴養、培養す
る場合、個々の汚濁物を分解、又は、酸化する微生物を
個別に培養、増殖するのは大変手間が掛かるので、いわ
ゆる好気性微生物と嫌気性微生物とを分けて馴養、培養
した方が有利である。
In addition, when cultivating and culturing microorganisms that remove these pollutants, it is very time-consuming to cultivate and grow microorganisms that decompose or oxidize individual pollutants individually, so we have to distinguish between so-called aerobic microorganisms and anaerobic microorganisms. It is more advantageous to acclimatize and culture the microorganisms separately from the sexually active microorganisms.

本発明者らは、このような観点からイケス等の蓄養水槽
の浄化処理に適した微生物の馴養、培養方法について研
究開発を行った結果、これらの条件を満足する微生物の
馴養、培養方法を発明したので、その内容について説明
する。
From this perspective, the present inventors conducted research and development on a method for acclimating and cultivating microorganisms suitable for purification of aquariums, etc. Therefore, I will explain its contents.

下水の活性汚−泥は、有機物を分解する微生物、アンモ
ニア性窒素化合物、亜硝酸性窒素化合物を酸化して硝酸
性窒素化合物にする微生物(硝化菌)硫化物を酸化して
硫酸化合物にする微生物(硫黄酸化菌)及び硝酸性窒素
化合物を窒素ガスに還元する微生物(脱窒菌)などが棲
息している事が明らかになっている。
Activated sludge from sewage consists of microorganisms that decompose organic matter, microorganisms (nitrifying bacteria) that oxidize ammonia nitrogen compounds and nitrite nitrogen compounds, and microorganisms that oxidize sulfides to sulfate compounds. It has been revealed that microorganisms that reduce nitrate nitrogen compounds to nitrogen gas (denitrifying bacteria) live there.

そこで、本発明者らは、下水の活性汚泥を用いて、イケ
ス等の蓄養水槽の浄化処理に適用できる耐海水性の好気
性微生物及び嫌気性微生物の馴養、について説明する。
Therefore, the present inventors will explain the acclimatization of seawater-resistant aerobic microorganisms and anaerobic microorganisms that can be applied to the purification treatment of a storage tank for fish, etc., using activated sludge from sewage.

下水の活性汚泥をイケス等の蓄養水槽の浄化処理に通用
できる微生物の集合体に馴養するには、まず、曝気槽に
p)I!IJ御装置及びORP制御装置をセットした活
性汚泥処理装置に、下水処理場の活性汚泥処理設備の曝
気槽より採取した活性汚泥混合液を入れ、これに高炉水
砕の微粉(20〜200μm)を曝気槽容量に対して1
〜10重量%添加し、これに肉エキス、ペプトン、酵母
エキス、デキストリンなどの有機物(BODとして約1
0〜50■/りと硫酸アンモン(アンモニア窒素として
約50■/I2)よりなる人工下水を供給して処理を行
う。この時、曝気量は、曝気槽のORPが+100〜+
200 mV (Ag  AgC1電極基準)になるよ
うに管理、制御し、また、曝気槽のpHは、海水の混合
比率が約50%以下の場合は、7.0〜7.5に、また
、海水の混合比率が約50%以上の場合は、7.5〜8
.0になるように5%硫酸、または、5%苛性ソーダ水
溶液で制御する。
In order to acclimatize activated sludge from sewage to a collection of microorganisms that can be used for purification treatment in a storage tank such as Ikesu, first add p) I! to the aeration tank. The activated sludge mixture collected from the aeration tank of the activated sludge treatment equipment in the sewage treatment plant is put into an activated sludge treatment equipment equipped with an IJ control device and an ORP control device, and fine powder (20 to 200 μm) of granulated blast furnace water is added to this. 1 per aeration tank capacity
~10% by weight is added, and organic substances such as meat extract, peptone, yeast extract, and dextrin (approximately 1% as BOD) are added to this.
Treatment is carried out by supplying artificial sewage consisting of 0 to 50 μ/l and ammonium sulfate (approximately 50 μ/I as ammonia nitrogen). At this time, the amount of aeration is determined by the ORP of the aeration tank being +100 to +
It is managed and controlled to be 200 mV (Ag AgC1 electrode standard), and the pH of the aeration tank is 7.0 to 7.5 when the seawater mixing ratio is about 50% or less. If the mixing ratio is about 50% or more, 7.5 to 8
.. 0 using 5% sulfuric acid or 5% caustic soda aqueous solution.

下水の活性汚泥から海水魚用のイケス等の蓄養水槽の浄
化処理に適用できる好気性の耐海水性微生物の馴養、培
養するのに、ORP制御装置及びpH制御装置をセット
した活性汚泥処理装置及び人工廃水を用いたのは、次の
理由による。
An activated sludge treatment device equipped with an ORP control device and a pH control device for acclimating and culturing aerobic seawater-resistant microorganisms that can be applied to the purification treatment of culture tanks for saltwater fish, etc. from activated sludge of sewage, and The reason why artificial wastewater was used is as follows.

ORP制御装置は、発明者の一人が曝気槽のQRPと硝
化反応、有機物の分解性との間に密接な関係があること
を見い出しており、本発明においても硝化反応及び有機
物の分解を効率良く行うために好気性微生物を馴養、培
養する曝気槽のORPを指標にして曝気量を管理・制御
を行うのでORPを制御するのに用いた。
One of the inventors of the ORP control device discovered that there is a close relationship between the QRP of the aeration tank, the nitrification reaction, and the decomposition of organic matter, and the present invention also efficiently controls the nitrification reaction and decomposition of organic matter. In order to do this, the amount of aeration is managed and controlled using the ORP of the aeration tank in which aerobic microorganisms are acclimatized and cultured as an index, so it was used to control the ORP.

本発明に於ける曝気槽の0RPIIJ御は、+100〜
250m V (A g−AgCI電極基準)の範囲が
最適であり、+100mV以下では硝化反応が十分に起
こらないため硝化菌の馴養、培養が、また、ORPが+
250mV以上だと硝化菌及び有機物を分解する微生物
の自己消化が起こり、これらの微生物の馴性窒素化合物
が硝酸性窒素化合物に酸化されると、曝気槽のpHが低
下して、活性汚泥(微生物の集合体)の機能を阻害する
ため、曝気槽のpHを適正値に、即ち、海水の混合比率
が約50%以下の場合は、7.0〜7.5に、また、海
水の混合比率が約50%以上の場合は、7.5〜8.0
になるように5%硫酸、または、5%苛性ソーダ水溶液
で制御するのに用いる。
The 0RPIIJ control of the aeration tank in the present invention is +100~
The range of 250mV (Ag-AgCI electrode standard) is optimal, and below +100mV the nitrification reaction does not occur sufficiently, making it difficult for the nitrifying bacteria to acclimate and culture, and for ORP to be +
At 250 mV or higher, self-digestion of nitrifying bacteria and microorganisms that decompose organic matter occurs, and when the adapted nitrogen compounds of these microorganisms are oxidized to nitrate nitrogen compounds, the pH of the aeration tank decreases and activated sludge (microorganisms) In order to inhibit the function of aggregates of is about 50% or more, 7.5 to 8.0
It is used to control with 5% sulfuric acid or 5% caustic soda aqueous solution.

次に、馴養、培養に用いた人工下水の成分について説明
する。
Next, the components of the artificial sewage used for acclimatization and culture will be explained.

まず、人工下水にアンモニア性窒素化合物を添加したが
、これは硝化菌がアンモニア性窒素化合物を酸化して、
硝酸性窒素化合物を生成して、増殖するために用いた。
First, ammoniacal nitrogen compounds were added to artificial sewage, but this caused nitrifying bacteria to oxidize the ammoniacal nitrogen compounds.
Nitrate nitrogen compounds were produced and used for growth.

アンモニア性窒素化合物の人工廃水への添加量は、海水
魚を飼育しているイケス等の蓄養水槽におけるアンモニ
ア性窒素化合物の生成量が、海水魚を2〜10重量%(
イケス等の蓄養水槽の容量に対して)飼育した場合、2
〜30■/1 (アンモニア性窒素として)なので、ア
ンモニア性窒素化合物を約50mg/β(アンモニア窒
素として〕添加した。
The amount of ammoniacal nitrogen compounds added to artificial wastewater is such that the amount of ammoniacal nitrogen compounds produced in a culture tank such as Ikesu where saltwater fish are kept is 2 to 10% by weight (
When rearing (relative to the capacity of the storage tank for Ikes, etc.), 2
~30 μ/1 (as ammonia nitrogen), so about 50 mg/β (as ammonia nitrogen) of the ammonia nitrogen compound was added.

また、微生物の馴養、培養用の人工下水に添加する有機
物は肉エキス、ペプトン、酵母エキス、デキストリン等
を用いたのは、これらの有機物が各種の微生物の培養、
馴養に最適なためである。
In addition, we used meat extract, peptone, yeast extract, dextrin, etc. as organic substances added to artificial sewage water for the cultivation and cultivation of microorganisms.
This is because it is perfect for acclimatization.

また、他の理由として肉エキスは、還元性の硫黄化合物
を含有しており、これが硫黄化合物を酸化する微生物を
馴養、培養するのに適している。
Another reason is that meat extracts contain reducing sulfur compounds, which are suitable for acclimating and cultivating microorganisms that oxidize sulfur compounds.

これらの有機物の濃度は、BODによって表示される有
機物が約10〜50■/2の範囲が適正である。これは
、硝化反応がBODによって表示される有機物の分解が
完了した後に起こることが知られており、硝化反応が起
こり、硝化菌及び有機物を分解する微生物の馴養、培養
が順調に起こるためには、このBOD範囲が適切である
。即ち、BODが10mg/f以下では、有機物を分解
する微生物の馴養、培養が順調に行われず、また、BO
Dが50■/!以上では、BODが若干残ると硝化菌の
馴養、培養が順調に行われない。
The appropriate concentration of these organic substances is within the range of approximately 10 to 50 .mu./2 as expressed by BOD. It is known that the nitrification reaction occurs after the decomposition of organic matter indicated by BOD is completed, and in order for the nitrification reaction to occur and the acclimatization and cultivation of nitrifying bacteria and microorganisms that decompose organic matter to occur smoothly. , this BOD range is appropriate. That is, if the BOD is less than 10 mg/f, the acclimatization and cultivation of microorganisms that decompose organic matter will not proceed smoothly, and the BO
D is 50■/! In the above case, if some BOD remains, the nitrifying bacteria will not acclimatize and culture smoothly.

このように下水の活性汚泥を馴養しても、供給する人工
下水が総て海水でないと、この活性汚泥は、海水魚用イ
ケス等の蓄養水槽の浄化処理に使う事ができない。この
ため、この活性汚泥に耐海水性を付与させる必要がある
Even if activated sludge from sewage is acclimatized in this way, unless all of the artificial sewage to be supplied is seawater, this activated sludge cannot be used for purification treatment of aquariums for breeding saltwater fish, etc. Therefore, it is necessary to impart seawater resistance to this activated sludge.

活性汚泥に耐海水性を付与する方法として、活性汚泥に
与える下水を徐々に海水に置き換えて、活性汚泥を海水
に馴養すれば良いが、耐海水性が付与されたかの可否を
判定する適切な方法が知られていない。
A method of imparting seawater resistance to activated sludge is to gradually replace the sewage fed to the activated sludge with seawater to acclimate the activated sludge to seawater, but there is an appropriate method to determine whether or not seawater resistance has been imparted. is not known.

そこで、本発明者らは、耐海水性が付与されたか可否を
判定する方法としてアンモニア性窒素化合物を亜硝酸性
窒素化合物、硝酸性窒素化合物に酸化する硝化菌の機能
に着目した。即ち、硝化菌は、増殖速度が遅く、また、
各種の要因によって機能が容易に阻害され、更に、沈降
性が悪いため活性汚泥処理装置の系外に流出し易い性状
を有しており、このため硝化菌の馴養、培養が非常に大
変である。
Therefore, the present inventors focused on the function of nitrifying bacteria that oxidizes ammonia nitrogen compounds to nitrite nitrogen compounds and nitrate nitrogen compounds as a method for determining whether seawater resistance has been imparted. That is, nitrifying bacteria have a slow growth rate, and
Its function is easily inhibited by various factors, and furthermore, because of its poor settling properties, it tends to flow out of the activated sludge treatment equipment, making it extremely difficult for nitrifying bacteria to acclimatize and culture it. .

従って、馴養、培養中に供給している原水(本発明の場
合は、人工下水を用いた。)の海水の4力ψ 度半適切でなかったら、硝化菌の機能が阻害されて、ア
ンモニア性窒素化合物の酸化率が低下することが考えら
れるので、活性汚泥の海水への馴養の度合いは、アンモ
ニア性窒素化合物が酸化されて硝酸性窒素化合物に変換
する割合、即ち、アンモニア性窒素化合物の酸化率から
推定し、海水の混合比率を変えた。
Therefore, if the raw water (in the case of the present invention, artificial sewage was used) supplied during acclimatization and culture is not suitable for the four forces of seawater, the function of nitrifying bacteria will be inhibited and the ammonia Since the oxidation rate of nitrogen compounds is thought to decrease, the degree of acclimatization of activated sludge to seawater is determined by the rate at which ammoniacal nitrogen compounds are oxidized and converted into nitrate nitrogen compounds, that is, the oxidation rate of ammoniacal nitrogen compounds. The mixing ratio of seawater was estimated from the ratio and the seawater mixing ratio was changed.

このような考えに基づいて、活性汚泥処理に供給する人
工下水の海水の混合割合について検討した結果、アンモ
ニア性窒素化合物の硝酸性窒素化合物への転換率(酸化
率)が80%以上であれば、人工下水の海水の混合率を
高めても良いことが明らかになった。具体的には、人工
下水の海水の混合比率は、約5〜10日間で海水を約l
O%ずつ高めて良く、従って、人工下水の全量が海水に
置換できて、海水魚用イケス等の蓄養水槽の浄化処理に
使用出来るのは約5〜10日間要する。
Based on this idea, we investigated the mixing ratio of seawater in artificial sewage to be supplied to activated sludge treatment, and found that if the conversion rate (oxidation rate) of ammonia nitrogen compounds to nitrate nitrogen compounds is 80% or more, It has become clear that it is possible to increase the mixing ratio of seawater in artificial sewage. Specifically, the mixing ratio of seawater in artificial sewage is approximately 1 liter of seawater in approximately 5 to 10 days.
Therefore, it takes about 5 to 10 days for the entire amount of artificial sewage to be replaced with seawater and used for the purification treatment of a breeding tank for saltwater fish such as Ikes.

なお、アンモニア性窒素化合物の酸化率が低い時、例え
ば、80%以下で人工下水の海水の混合比率を高めると
、硝化菌の機能が阻害され正常な状態に回復するのに長
期間を要する。
Note that when the oxidation rate of ammonia nitrogen compounds is low, for example, 80% or less, if the mixing ratio of seawater in artificial sewage is increased, the function of nitrifying bacteria will be inhibited and it will take a long time to recover to a normal state.

次に、本発明における活性汚泥の高濃度化について説明
する。
Next, increasing the concentration of activated sludge in the present invention will be explained.

既に、下水の活性汚泥処理に於いて7、活性汚泥処理設
備の曝気槽に高炉水砕を添加すると、活性汚泥が高炉水
砕に付着して、曝気槽の活性汚泥を高濃度に維持でき、
その結果、高効率処理が可能になることが、例えば、特
開昭63−42796号公報で明らかにされている。
Already in the activated sludge treatment of sewage7, when granulated blast furnace water is added to the aeration tank of activated sludge treatment equipment, the activated sludge adheres to the granulated blast furnace water and the activated sludge in the aeration tank can be maintained at a high concentration.
As a result, it has been disclosed in, for example, Japanese Patent Laid-Open No. 63-42796 that highly efficient processing becomes possible.

そこで、本発明に於いても、イケス等の蓄養水槽の浄化
処理に関与する微生物の高濃度化に高炉水砕を馴養の段
階から用いた。即ち、先に述べた下水処理場の活性汚泥
の混合液を曝気槽に入れると共に高炉水砕を曝気槽の容
量に対して1日に約1重量%の割合で、所定量添加する
。例えば、高炉水砕を5重量%添加する場合、高炉水砕
を5日間にわたって添加する。この時、人工下水は、処
理時間が6〜8時間になるように曝気槽に供給する。な
お、汚泥返送率は、20〜30%とし、余剰汚泥の抜き
取りは、海水への馴養期間中は行わない。
Therefore, in the present invention, blast furnace granulation was used from the acclimatization stage to increase the concentration of microorganisms involved in the purification treatment of a storage tank for Ikesu and the like. That is, the above-mentioned mixed solution of activated sludge from the sewage treatment plant is put into an aeration tank, and a predetermined amount of granulated blast furnace granules is added at a rate of about 1% by weight per day to the capacity of the aeration tank. For example, when adding 5% by weight of blast furnace granules, the blast furnace granules are added over 5 days. At this time, artificial sewage is supplied to the aeration tank so that the treatment time is 6 to 8 hours. Note that the sludge return rate is 20 to 30%, and excess sludge is not removed during the acclimatization period to seawater.

このような方法で、イケス等の蓄養水槽の浄化処理に適
用できる好気性微生物の馴養、培養を行うと、有機性汚
泥の指標であるMLVSS(Mixed l1quor
 volatile 5uspended 5olid
s)は、実験開始時の約1500〜2000■/!が海
水への馴養終了時には約5000〜7500■/lに増
加した。このように、高炉水砕の添加は、有機性汚泥の
増殖に著しく効果があることが明らかになった。
By acclimating and culturing aerobic microorganisms that can be applied to the purification treatment of Ikesu culture tanks, etc. using this method, MLVSS (Mixed l1quar), which is an indicator of organic sludge,
volatile 5uspended 5olid
s) is approximately 1500 to 2000 ■/! at the beginning of the experiment. increased to approximately 5,000 to 7,500 μ/l at the end of acclimatization to seawater. In this way, it has been revealed that the addition of blast furnace granulation has a significant effect on the growth of organic sludge.

また、高炉水砕の別の効果として、高炉水砕をイケス等
の蓄養水槽の浄化処理に適用できる好気性微生物の馴養
、培養に用いると、有機性汚泥の高濃度化の他に、アン
モニア性窒素化合物を酸化する硝化菌の機能に著しく影
響する。
Another effect of blast furnace granulation is that when blast furnace granulation is used for acclimation and cultivation of aerobic microorganisms that can be applied to the purification treatment of storage tanks such as Ikesu, in addition to increasing the concentration of organic sludge, it also produces ammonia Significantly affects the ability of nitrifying bacteria to oxidize nitrogen compounds.

硝化菌をする場合、高炉水砕を用いないとアンモニア性
窒素化合物を硝酸性窒素化合物に酸化する硝化菌の他に
亜硝酸性窒素化合物に酸化する亜硝酸菌も一緒に培養、
増殖する。このため、これらの混合菌をイケス等の蓄養
水槽の浄化処理に用いるとアンモニア性窒素化合物は、
硝酸性窒素化合物の他に魚に対して神経毒である亜硝酸
性窒素化合物も生成するので好ましくない。
When culturing nitrifying bacteria, if blast furnace granulation is not used, in addition to nitrifying bacteria that oxidize ammonia nitrogen compounds to nitrate nitrogen compounds, nitrite bacteria that oxidize nitrite nitrogen compounds will also be cultured.
Multiply. Therefore, when these mixed bacteria are used to purify a storage tank such as Ikesu, ammonia nitrogen compounds are removed.
In addition to nitrate nitrogen compounds, nitrite nitrogen compounds, which are neurotoxic to fish, are also produced, which is undesirable.

しかし、高炉水砕を微生物の固定化担体に用いて先に述
べた方法により好気性の微生物の馴養、培養を行い、得
られた微生物でイケス等の蓄養水槽の浄化処理を行うと
、魚に対して有害な亜硝酸性窒素化合物の生成は、0.
5■/2以下で、また、残存しているアンモニア性窒素
化合物も0.5■/f以下であり、飼育している魚に対
しては何ら悪影響しない。
However, if aerobic microorganisms are acclimatized and cultured using the above-mentioned method using granulated blast furnace water as a carrier for immobilizing microorganisms, and the obtained microorganisms are used to purify a storage tank for fish, fish, etc. On the other hand, the production of harmful nitrite nitrogen compounds is 0.
The amount of the remaining ammonia nitrogen compound is also less than 0.5 μ/f, and has no adverse effect on the fish being raised.

これらの結果から、高炉水砕をイケス等の蓄養水槽の浄
化処理に用いる微生物の馴養、培養に於ける固定化担体
に用いると微生物の高濃度化、有害な亜硝酸性窒素化合
物を生成する微生物の馴養、培養が殆ど無く、イケス等
の蓄養水槽の浄化処理に適した好気性微生物が得られる
事が明らかになった。
From these results, we found that when blast furnace granulation is used for the acclimation of microorganisms used in the purification treatment of storage tanks such as Ikesu, and when used as an immobilization carrier in culture, the microorganisms become highly concentrated, and the microorganisms that produce harmful nitrite-nitrogen compounds. It has become clear that an aerobic microorganism suitable for the purification treatment of aquariums for breeding fish, etc., can be obtained with almost no acclimatization or cultivation.

次に嫌気性微生物、即ち、好気性微生物によって生成し
た硝酸性窒素化合物を窒素ガスに還元する脱窒菌の馴養
、培養方法について説明する。
Next, a method for acclimating and cultivating denitrifying bacteria that reduces nitrate nitrogen compounds produced by anaerobic microorganisms, ie, aerobic microorganisms, to nitrogen gas will be explained.

嫌気性条件において脱窒菌を馴養、培養する場合、脱窒
菌の他に嫌気性の微生物、例えば、硫黄還元菌等が同時
に馴養、培養されると好ましくない。即ち、硫黄還元菌
が存在すると好気性微生物が魚の排泄物、投餌の残渣物
等に含まれている硫化物を酸化して生成した硫酸イオン
を還元して魚の呼吸前である硫化物を再び生成する。こ
のため、脱窒菌の他に硫黄還元菌等の嫌気性微生物が馴
養、培養するのを極力抑制する必要がある。
When acclimating and culturing denitrifying bacteria under anaerobic conditions, it is not preferable if anaerobic microorganisms, such as sulfur-reducing bacteria, are acclimated and cultured at the same time in addition to the denitrifying bacteria. In other words, when sulfur-reducing bacteria are present, aerobic microorganisms oxidize sulfide contained in fish excrement, bait residue, etc., reducing the sulfate ions produced and regenerating sulfide before fish respiration. generate. Therefore, it is necessary to suppress as much as possible the acclimatization and cultivation of anaerobic microorganisms such as sulfur-reducing bacteria in addition to denitrifying bacteria.

発明者等は、鋭意研究した結果、リアクターのORPを
管理、制御すると硫黄還元菌等の嫌気性微生物の馴養、
培養を抑制して脱窒菌をかなり優先的に馴養、培養する
ことができる方法を確立した。
As a result of intensive research, the inventors have found that managing and controlling the ORP of the reactor will improve the habituation of anaerobic microorganisms such as sulfur-reducing bacteria.
We have established a method that allows denitrifying bacteria to be habituated and cultured in a fairly preferential manner by suppressing culture.

即ち、本発明者らは、リアクターに於ける脱窒反応が0
RP(1〜−150m V (A g −AgC1電極
基準)の範囲で起こり、リアクターの硝酸性窒素化合物
が窒素ガスに還元されて硝酸イオンが殆ど無くなるとO
RPが急激に低下して著しく嫌気性になることを見いだ
した。
That is, the present inventors found that the denitrification reaction in the reactor was 0.
RP (occurs in the range of 1 to -150 mV (Ag-AgC1 electrode reference), and when the nitrate nitrogen compound in the reactor is reduced to nitrogen gas and almost all nitrate ions disappear, O
We found that RP decreased rapidly and became significantly anaerobic.

このことから、リアクターのORPをO〜−150mV
 (A g−AgC1電極基準)の範囲に管理、制御す
れば脱窒菌が優先的に増殖して、他の硫黄還元菌等の嫌
気性微生物の馴養が抑制できると考え、脱窒菌を優先的
に馴養、培養を行ったので、その方法について説明する
From this, we can set the ORP of the reactor to 0~-150mV.
(Ag-AgC1 electrode standard) If managed and controlled within the range of Since we have carried out acclimatization and culture, we will explain the method.

まず、ORP制御装置、pH制御装置及び攪拌機をセッ
トしたりアクタ−と汚泥沈降槽からなる嫌気性の生物化
学的処理装置に都市下水処理場の活性汚泥処理装置の曝
気槽より採取した活性汚泥混合液を入れ、これに高炉水
砕の微粉(20〜200μm)をリアクターの容量に対
して1〜10重量%添加し、活性汚泥及び高炉水砕が沈
降しない程度に攪拌を行う。このリアクターに先に説明
した人工下水のアンモニア性窒素化合物の代わりに硝酸
性窒素化合物を50■/β(硝酸性窒素として)添加し
た人工下水を、処理時間が6〜8時間になるように供給
する。なお、汚泥沈降槽からりアクタへの汚泥返送率は
約25%とした。
First, the activated sludge collected from the aeration tank of the activated sludge treatment equipment at a municipal sewage treatment plant is mixed into an anaerobic biochemical treatment equipment consisting of an ORP control device, a pH control device, and an agitator, and an actor and a sludge settling tank. 1 to 10% by weight of granulated blast furnace powder (20 to 200 μm) based on the capacity of the reactor is added, and the mixture is stirred to an extent that activated sludge and blast furnace granulated water do not settle. To this reactor, artificial sewage with 50 μ/β (as nitrate nitrogen) added of nitrate nitrogen compounds instead of the ammonia nitrogen compounds in the artificial sewage described above is supplied so that the treatment time is 6 to 8 hours. do. Note that the sludge return rate from the sludge settling tank to the Riactor was approximately 25%.

この時、リアクターのORPは、O〜−150mV(A
 g−AgC1電極基準)に管理、制御し、ORPが1
50mV以下になると曝気し、−150mVに回復する
と曝気が停止するオン−オフ自動制御を行った。また、
はとんど曝気を行わないためリアクターにおいて汚泥及
び高炉水砕が沈降するので、これを防止するためリアク
ター内を機械的に攪拌しながら硝酸性窒素化合物を含有
した人工下水の処理を行う。なお、リアクターのpHは
、耐海水性脱窒菌が馴養、培養につれて上昇する傾向が
あるので、人工下水の海水の比率が約50%以下の場合
は、8.0〜8.5程度に、海水の比率が約50%以上
になったら海水のpH,即ち、7.6〜8.0程度に管
理、制御する。このような方法で処理を行うと処理水の
硝酸イオン濃度が1mg/42以下になり、硝酸性窒素
化合物が効率良く還元除去されることが明らかになった
At this time, the ORP of the reactor is O~-150mV (A
g-AgC1 electrode standard) and ORP is 1.
Automatic on-off control was performed in which aeration was started when the voltage was below 50 mV, and aeration was stopped when the voltage returned to -150 mV. Also,
Since sludge and blast furnace granules settle in the reactor because aeration is rarely performed, in order to prevent this, the artificial sewage containing nitrate nitrogen compounds is treated while stirring the reactor mechanically. Note that the pH of the reactor tends to increase as seawater-resistant denitrifying bacteria become acclimated and cultured, so if the proportion of seawater in artificial sewage is about 50% or less, the pH of the reactor should be around 8.0 to 8.5. When the ratio becomes about 50% or more, the pH of seawater is managed and controlled to be about 7.6 to 8.0. It has been revealed that when the treatment is carried out in this manner, the nitrate ion concentration of the treated water becomes 1 mg/42 or less, and nitrate nitrogen compounds are efficiently reduced and removed.

なお、脱窒菌は、先に説明した硝化菌と同様に増殖速度
が遅く、また、沈降性が悪いため処理水に容易に流出す
るので、リアクターの脱窒菌を高濃度に維持するのが困
難である。このため、リアクターに高炉水砕を添加し、
高炉水砕に脱窒菌を固定化して汚泥沈降槽における沈降
性を良くし、脱窒菌の処理水への流出を抑制し、リアク
ターの脱窒菌の高濃度化を計った。
It should be noted that denitrifying bacteria, like the nitrifying bacteria described above, have a slow growth rate and have poor sedimentation properties, so they easily leak into the treated water, making it difficult to maintain a high concentration of denitrifying bacteria in the reactor. be. For this reason, blast furnace granulation is added to the reactor,
We immobilized denitrifying bacteria in the blast furnace granules to improve sedimentation in the sludge settling tank, suppress the flow of denitrifying bacteria into the treated water, and increase the concentration of denitrifying bacteria in the reactor.

また、肉エキス、ペプトン、酵母エキス、デキストリン
等の有機物(BODとして約10〜50■/l)を含む
人工下水を用いたのは、硝酸性窒素化合物を窒素ガスに
還元する時に水素供与体として有機物が必要であり、ま
た、これらの有機物が各種の微生物の培養、増殖に適し
ている。
In addition, artificial sewage containing organic substances such as meat extract, peptone, yeast extract, and dextrin (approximately 10 to 50 μ/L as BOD) was used as a hydrogen donor when reducing nitrate nitrogen compounds to nitrogen gas. Organic substances are required, and these organic substances are suitable for culturing and propagating various microorganisms.

次に、脱窒菌の海水への馴養について説明する。Next, the acclimatization of denitrifying bacteria to seawater will be explained.

脱窒菌に耐海水性を付与する方法は、先に説明した耐海
水性硝化菌の馴養の場合と同様に人工下水の海水の混合
比率を徐々に増加すれば良い。具体的には、硝酸性窒素
化合物(硝酸性窒素として約50■/l)を含む人工下
水の処理を行い、処理水の硝酸性窒素化合物が、硝酸性
窒素として10■/!以下になったら海水の混合比率を
約10%づつアップし、最終的には海水100%で硝酸
性窒素化合物をほぼ100%還元することができる耐海
水性脱窒菌が得られる。
A method for imparting seawater resistance to denitrifying bacteria is to gradually increase the mixing ratio of seawater in artificial sewage, as in the case of acclimatization of seawater-resistant nitrifying bacteria described above. Specifically, artificial sewage containing nitrate nitrogen compounds (approximately 50 μ/l as nitrate nitrogen) is treated, and the nitrate nitrogen compounds in the treated water are 10 μ/l as nitrate nitrogen. When the ratio is below, the mixing ratio of seawater is increased by about 10%, and finally seawater-resistant denitrifying bacteria that can reduce almost 100% of nitrate nitrogen compounds with 100% seawater can be obtained.

このようにして得られた脱窒菌は、イケス等の蓄養水槽
の浄化処理に用いる場合、まずイケス等の蓄養水槽の海
水を、先に培養、増殖方法を説明した耐海水性硝化菌を
固定化したモジュールに通水し、次に、この海水を耐海
水性脱窒菌を固定化したモジュールに通水する。この時
、イケス等の蓄養水槽の海水の1部を耐海水性脱窒菌を
固定化したモジュールに通水する。これは、耐海水性脱
窒菌が硝酸性窒素化合物を還元する時に水素供与体とし
て有機物を必要とするためイケス等の蓄養水槽の海水に
含まれている投餌の残漬物、魚の排泄物等の有機物を水
素供与体として用いるためである。
When the denitrifying bacteria obtained in this way is used for the purification treatment of a culture tank such as Ikesu, the seawater of the culture tank such as Ikesu is first cultured and the seawater-resistant nitrifying bacteria whose growth method was explained above are immobilized. This seawater is then passed through a module in which seawater-resistant denitrifying bacteria have been immobilized. At this time, a part of the seawater in the Ikesu culture tank is passed through a module in which seawater-resistant denitrifying bacteria are immobilized. This is because seawater-resistant denitrifying bacteria require organic matter as a hydrogen donor when reducing nitrate nitrogen compounds, so this is due to the fact that the leftovers from feeding, fish excrement, etc. contained in the seawater of the Ikesu culture tank, etc. This is because organic matter is used as a hydrogen donor.

このモジュールの機能は、まず耐海水性硝化菌を固定化
したモジュールで魚の排泄物、投餌の残漬物等の有機物
が酸化分解され、また、アンモニア性窒素化合物が硝酸
性窒素化合物に酸化される。
The function of this module is to first oxidize and decompose organic matter such as fish excrement and bait leftovers in a module immobilized with seawater-resistant nitrifying bacteria, and also to oxidize ammonia nitrogen compounds to nitrate nitrogen compounds. .

次に、耐海水性脱窒菌を固定化したモジュールで、耐海
水性脱窒菌がイケス等の蓄養水槽の海水に含まれている
有機物を水素供与体として利用して、硝酸性窒素化合物
を窒素ガスに還元して除去する。
Next, in a module in which seawater-resistant denitrifying bacteria are immobilized, the seawater-resistant denitrifying bacteria use organic matter contained in the seawater in a storage tank such as Ikesu as a hydrogen donor, converting nitrate nitrogen compounds into nitrogen gas. Reduce and remove.

イケス等の蓄養水槽の海水をこのように処理する事によ
り、海水は、常に清浄化状態を保つことができ、長期間
海水を交換しないでも海水魚を飼育することができる。
By treating the seawater in the aquarium for breeding fish, etc., in this way, the seawater can always be maintained in a clean state, and saltwater fish can be raised without replacing the seawater for a long period of time.

(実施例) 実施例−1 海水魚用イケス等の蓄養水槽の浄化処理に適した好気性
微生物の馴養、培養方法の実施例について説明する。
(Example) Example 1 An example of a method for acclimatizing and cultivating aerobic microorganisms suitable for purifying a culture tank for saltwater fish, etc., will be described.

酸化還元電位制御装置とpH制御装置とを偵えた活性汚
泥処理実験装置の曝気槽(約502)に下水処理場の活
性汚泥処理装置の曝気槽より採取した活性汚泥の混合液
(濃度;1500〜2000■/2)を入れ、これに有
機物成分として肉エキス5■/ρ、ペプトン5 mg/
 e、酵母エキス6■/I!、、デキストリン2.4 
mg/Eと硫酸アンモンを50■/乏(アンモニア性窒
素として)を淡水に溶解した人工下水を曝気槽に通水し
た。また、この曝気槽に活性汚泥の固定化担体として高
炉水砕の微粉(粒度20〜200μm)を1高気槽容量
に対して1重量%づつ、5日間添加した。
A mixed solution of activated sludge (concentration: 1500 ~ 2000■/2), and as organic components, meat extract 5■/ρ and peptone 5mg/
e, yeast extract 6■/I! ,,dextrin 2.4
Artificial sewage in which mg/E and ammonium sulfate (50 μl/poor (as ammonia nitrogen)) were dissolved in fresh water was passed through the aeration tank. In addition, 1% by weight of granulated blast furnace powder (particle size: 20 to 200 μm) was added to the aeration tank as an immobilized carrier for activated sludge for 5 days.

この時の活性汚泥処理条件は、次の通りである。The activated sludge treatment conditions at this time are as follows.

○曝気槽のpH;海水の混合比によって変えた海水混合
比0〜50%;7.0〜7゜5に制御海水混合比50〜
100%;7.5〜8.0に制御O曝気槽のORP H
200〜250m V制御(Ag−AgCI電掻基準) O汚泥返送率;約25% ○処理時間;約6〜8時間 ○曝気量;曝気槽のORPを指標にして行ったこのよう
な活性汚泥処理を行うと、高炉水砕添加完了後5日間で
処理水のアンモニア性窒素の濃度が0.01■/1以下
に、また、硝酸性窒素が約50u/1になった。そこで
、上述の人工下水の淡水の10%を海水に置き換え同じ
処理を行うと、翌日には処理水のアンモニア性窒素が0
.01■/!以下に、また、硝酸性窒素が約50■/l
になった。
○ pH of the aeration tank; seawater mixing ratio changed by seawater mixing ratio 0-50%; control seawater mixing ratio 50-50% at 7.0-7°5
100%; ORP H of control O aeration tank to 7.5-8.0
200 to 250 m V control (Ag-AgCI electric scraping standard) O sludge return rate: Approximately 25% ○ Processing time: Approximately 6 to 8 hours ○ Aeration amount: Such activated sludge treatment performed using the ORP of the aeration tank as an index When this was carried out, the concentration of ammonia nitrogen in the treated water decreased to less than 0.01 μ/1 and the concentration of nitrate nitrogen decreased to approximately 50 u/1 within 5 days after the addition of granulated blast furnace water was completed. Therefore, if 10% of the fresh water in the artificial sewage mentioned above is replaced with seawater and the same treatment is carried out, the ammonia nitrogen in the treated water will be 0 by the next day.
.. 01■/! Below, nitrate nitrogen is also about 50■/l
Became.

更に、この好気性微生物に海水への馴養性を高めるため
にアンモニア性窒素が充分に酸化されても同じ海水濃度
で、約7〜10日間継続して処理を行った。
Furthermore, in order to enhance the adaptability of this aerobic microorganism to seawater, the treatment was continued for about 7 to 10 days at the same seawater concentration even after the ammonia nitrogen was sufficiently oxidized.

その後、人工下水の淡水を海水により約lO%づつ置き
換える度にこのような操作を繰り返して海水濃度を高め
、好気性微生物の海水に対する馴養性を徐々に高め、最
終的に人工下水の淡水を全量海水に置き換えた。この段
階における活性汚泥(7) MLVSS濃度は、約50
00〜7500mg/ 1になり、イケス等の蓄養水槽
の浄化処理に用いることができる。
After that, each time the freshwater in the artificial sewage is replaced with seawater by approximately 10%, this operation is repeated to increase the seawater concentration, gradually increasing the adaptability of aerobic microorganisms to seawater, and finally replacing the entire amount of freshwater in the artificial sewage. Replaced with seawater. The activated sludge (7) MLVSS concentration at this stage is approximately 50
00 to 7,500 mg/1, and can be used for purifying aquariums for breeding fish, etc.

実施例−2 海水魚用イケス等の蓄養水槽の浄化処理に適した好気性
微生物の馴養、培養方法の実施例について説明する。
Example 2 An example of a method for acclimating and cultivating aerobic microorganisms suitable for purifying a culture tank for seawater fish such as Ikes will be described.

攪拌機、ORP制御装置及びpH制御装置を備えた嫌気
性リアクター(リアクター容量的502)に、実施例−
1と同じ方法で下水処理場の活性汚泥処理装置の曝気槽
より採取した活性汚泥の混合液を入れ、リアクター内を
攪拌しながらこれに有機物成分として肉エキス5■/2
、ペプトン5■/れ酵母エキス6■/l、デキストリン
2.4■/I!、と硝酸ナトリウムを50mg/EC硝
酸性窒素として)を淡水に溶解した人工下水をリアクタ
ーに通水した。また、このリアクターに活性汚泥の固定
化担体として高炉水砕の微粉(粒度20〜200μm)
を1日にリアクター容量に対して1重量%づつ、5日間
添加した。
In an anaerobic reactor (reactor volume 502) equipped with a stirrer, an ORP controller and a pH controller, Example-
Using the same method as in step 1, add a mixed solution of activated sludge collected from the aeration tank of the activated sludge treatment equipment at a sewage treatment plant, and add 5/2 of meat extract as an organic component while stirring the inside of the reactor.
, peptone 5■/yeast extract 6■/l, dextrin 2.4■/I! , and sodium nitrate (50 mg/EC as nitrate nitrogen) were dissolved in fresh water and artificial sewage was passed through the reactor. In addition, granulated blast furnace powder (particle size 20 to 200 μm) was added to this reactor as an immobilization carrier for activated sludge.
was added at a rate of 1% by weight based on the reactor capacity per day for 5 days.

この時の嫌気性処理の条件は、次の通りである。The conditions for the anaerobic treatment at this time are as follows.

○曝気槽のpH;海水の混合比によって変えた海水混合
比O〜50%;8.0〜8.5に制御海水混合比50〜
100%;7.6〜8.0に制御○曝気槽のORP H
−150m V制御(Ag−AgC1電極基準) なお、リアクターのORPは、 150mV以下になっ
たら曝気を行い、−150mVに回復したら曝気が停止
する0N−OFF方式で制御を行った。
○ pH of aeration tank; seawater mixing ratio changed by seawater mixing ratio O ~ 50%; control seawater mixing ratio 50 ~ 8.0 ~ 8.5
100%; Controlled to 7.6-8.0 ○ ORP H of aeration tank
-150 mV control (Ag-AgC1 electrode standard) The ORP of the reactor was controlled using an ON-OFF method in which aeration was performed when the voltage was below 150 mV, and aeration was stopped when the voltage was restored to -150 mV.

O汚泥返送率;約25% ○処理時間;約6〜8時間 このような方法で、嫌気性活性汚泥処理を行うと、高炉
水砕添加完了後約5日間で処理水の硝酸そこで、上述の
人工下水の淡水の10%を海水窒素が約0.05■/!
になった。更に、この嫌気性微生物に海水への馴養性を
高めるために硝酸性窒素が充分に還元されても同じ海水
濃度で、約7〜10日間継続して処理を行った。
O sludge return rate: Approximately 25% ○ Processing time: Approximately 6 to 8 hours When anaerobic activated sludge treatment is carried out in this manner, nitric acid in the treated water is removed within approximately 5 days after the addition of granulated blast furnace water is completed. Seawater nitrogen makes up 10% of the fresh water in artificial sewage at approximately 0.05■/!
Became. Further, in order to enhance the adaptability of the anaerobic microorganisms to seawater, the treatment was continued for about 7 to 10 days at the same seawater concentration even after nitrate nitrogen had been sufficiently reduced.

その後、人工下水の淡水を海水により約10%づつ置き
換える度にこのような操作を繰り返して海水濃度を高め
、嫌気性微生物の海水に対する馴養性を徐々に高め、最
終的に人工下水の淡水が全量海水に置き換わった段階で
イケス等の蓄養水槽の浄化処理に用いた。
After that, this operation is repeated every time approximately 10% of the freshwater in the artificial sewage is replaced with seawater to increase the concentration of seawater, gradually increasing the adaptability of anaerobic microorganisms to seawater, and finally the entire amount of freshwater in the artificial sewage is replaced. Once it had been replaced with seawater, it was used to purify fish tanks and other fish tanks.

(発明の効果) 以上説明したように本発明の方法に基づいて馴等の蓄養
水槽の汚濁物を酸化分解、或は硝酸性窒素化合物を窒素
ガスに還元する作用がある。また、これらの微生物を用
いた海水魚用イケス等の蓄養水槽の浄化処理用のモジュ
ールは、従来の浄化処理方法に比べて直ちに使用するこ
とができ、更に、汚濁物の除去性が優れているので、浄
化処理用のモジュールをコンパクトにできる。
(Effects of the Invention) As explained above, the method of the present invention has the effect of oxidatively decomposing pollutants in a culture tank such as fish, or reducing nitrate nitrogen compounds to nitrogen gas. In addition, the module for purifying aquariums such as Ikesu for saltwater fish using these microorganisms can be used immediately compared to conventional purification methods, and is also superior in removing pollutants. Therefore, the purification module can be made compact.

代理人 弁理士  秋 沢 政 光 他1名 自発手続補正書 1.事件の表示 特願平1−89984号 処理に適した微生物の!!71111、培養方法 3、補正をする者 事件との関係  出 願 人 住    所 東京都千代田区大手町2丁目6番3号名
    称 (665)新日本製鐵株式会社東京都中央
区日本橋兜町12番1号 \。
Agent Patent attorney Masamitsu Akizawa and one other person voluntary procedure amendment 1. Case display patent application No. 1-89984 Microorganisms suitable for treatment! ! 71111, Cultivation Method 3, Relationship with the amended person case Application Address 2-6-3 Otemachi, Chiyoda-ku, Tokyo Name (665) Nippon Steel Corporation 12 Nihonbashi Kabutocho, Chuo-ku, Tokyo Number 1\.

Claims (2)

【特許請求の範囲】[Claims] (1)酸化還元電位(ORP)制御装置とpH制御装置
とを備えた活性汚泥処理の曝気槽に下水の活性汚泥の混
合液と高炉水砕を入れ、この曝気槽のORPを指標にし
て空気を曝気しながら曝気槽にアンモニア性化合物と活
性汚泥によって分解可能な有機物を含む淡水の人工下水
を供給し、アンモニア性窒素化合物の80%以上が硝酸
性窒素化合物に酸化されるようになったら、人工廃水の
淡水を海水に逐次置き換え、最終的に海水100%の人
工廃水のアンモニア性窒素化合物が硝酸性窒素化合物に
90%以上酸化されるようになったら海水活魚用イケス
の浄化処理に用いる事を特徴とする海水活魚用イケス等
の蓄養水槽の浄化処理に適した好気性微生物の馴養、培
養方法。
(1) Put the sewage activated sludge mixture and granulated blast furnace water into an aeration tank for activated sludge treatment equipped with an oxidation-reduction potential (ORP) control device and a pH control device, and use the ORP of the aeration tank as an index to air the While aerating, freshwater artificial sewage containing ammoniacal compounds and organic matter that can be decomposed by activated sludge is supplied to the aeration tank, and when more than 80% of the ammoniacal nitrogen compounds have been oxidized to nitrate nitrogen compounds, The freshwater of the artificial wastewater is successively replaced with seawater, and when finally 90% or more of the ammonia nitrogen compounds in the 100% seawater artificial wastewater are oxidized to nitrate nitrogen compounds, it can be used for the purification of seawater live fish. A method for acclimating and cultivating aerobic microorganisms suitable for purifying a culture tank for seawater live fish such as Ikesu, which is characterized by:
(2)攪拌機、ORP制御装置及びpH制御装置を備え
た嫌気性リアクターに下水処理場の活性汚泥混合液と高
炉水砕を入れ、リアクター内を攪拌しながら硝酸性窒素
化合物と活性汚泥によって分解可能な有機物を含む淡水
系の人工下水を供給し、硝酸性窒素化合物の80%以上
が還元、除去されるようになったら、人工下水の淡水を
海水に逐次置き換え、最終的に海水100%の人工下水
の硝酸性窒素化合物が90%以上が還元されるようにな
ったら海水活魚用イケス等の蓄養水槽の浄化処理に用い
る事を特徴とする海水活魚用イケス等の蓄養水槽の浄化
処理に適した嫌気性微生物の馴養、培養方法。
(2) Put the activated sludge mixture from the sewage treatment plant and the granulated blast furnace water into an anaerobic reactor equipped with an agitator, an ORP control device, and a pH control device, and decompose it with nitrate nitrogen compounds and activated sludge while stirring the inside of the reactor. Once more than 80% of the nitrate nitrogen compounds have been reduced and removed, the freshwater in the artificial sewage is gradually replaced with seawater, and finally the artificial sewage is made up of 100% seawater. When 90% or more of nitrate nitrogen compounds in sewage have been reduced, it can be used for purification treatment of culture tanks such as Ikesu for seawater live fish.Suitable for purification treatment of culture tanks such as Ikesu for seawater live fish. Acclimatization and culture methods for anaerobic microorganisms.
JP1089984A 1989-04-10 1989-04-10 Method for acclimatizing and incubating microbe for cleaning fish farming water tank such as living sea-fish preserve Pending JPH02268896A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1089984A JPH02268896A (en) 1989-04-10 1989-04-10 Method for acclimatizing and incubating microbe for cleaning fish farming water tank such as living sea-fish preserve

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JPH02268896A true JPH02268896A (en) 1990-11-02

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05269487A (en) * 1992-03-24 1993-10-19 Nippon Steel Corp Method for acclimatization and growth of sulfur-oxidizing bacteria and method for biological treatment of wastewater containing reducing sulfur compounds
JP2008307459A (en) * 2007-06-13 2008-12-25 Shibaura Institute Of Technology Purification method of contaminated seawater by seawater-derived microorganisms
JP2010201423A (en) * 1999-06-10 2010-09-16 Bicom:Kk High-concentration culture method of denitrifying bacterium contained in activated sludge

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4920955A (en) * 1972-06-17 1974-02-23
JPS5096459A (en) * 1973-12-28 1975-07-31
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