JP2009060872A - Method for treating water for breeding, device for treating water for breeding and system for breeding - Google Patents

Method for treating water for breeding, device for treating water for breeding and system for breeding Download PDF

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JP2009060872A
JP2009060872A JP2007232985A JP2007232985A JP2009060872A JP 2009060872 A JP2009060872 A JP 2009060872A JP 2007232985 A JP2007232985 A JP 2007232985A JP 2007232985 A JP2007232985 A JP 2007232985A JP 2009060872 A JP2009060872 A JP 2009060872A
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water
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breeding water
biological filtration
filtration tank
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JP4960182B2 (en
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Hiroyuki Miyajima
宏行 宮嶋
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TOKYO KYUEI KK
Tokyo Kyuei Co Ltd
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Tokyo Kyuei Co Ltd
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<P>PROBLEM TO BE SOLVED: To provide a method for treating water for breeding, a device for treating the water for breeding and a system for breeding, capable of further small-sizing and simplifying equipment. <P>SOLUTION: This method for treating the water for breeding is for treating water for breeding 1, by removing suspended materials and also nitration-treating the water by aerobic microorganisms and is provided by pulling in the water for rearing 1, made to flow into a biological filtering vessel 2 that houses these microorganisms, into a foam separation device 3 for removing the suspended materials 4 by a foam-separating treatment and for improving the amount of dissolved oxygen, and then returning it to the biological filtering vessel 2 for accelerating the nitrating action by the aerobic microorganisms. Also, the device for treating the water for breeding is provided with the biological filtering vessel 2 for holding the aerobic microorganisms, by a filtering material 6 forming gaps 8 for passing the suspended materials 4 contained in the water for breeding 1 and nitration-treating the flowing-in water for breeding 1 by the microorganisms; and the foam separation device 3 for drawing-in the water for breeding 1 from the biological filtering vessel 2, removing the suspended materials by aeration from an aerator 9, and improving the amount of the dissolved oxygen and returning the water to the biological filtering vessel 2. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は飼育水処理方法、飼育水処理装置、および飼育システムに関するもので、より詳細には、魚や海獣などの飼育に適した飼育水の処理方法および処理装置、並びに魚や海獣などの飼育システムに関するものである。   The present invention relates to a breeding water treatment method, a breeding water treatment apparatus, and a breeding system, and more particularly, to a breeding water treatment method and treatment apparatus suitable for breeding fish and sea animals, and a breeding system such as fish and sea animals. Is.

飼育水を懸濁物除去処理するとともに、好気性の微生物により硝化処理する飼育水処理方法としては、従来、特許文献1に記載のものが知られている。この従来例において、魚介類を飼育する飼育水槽内の水は、飼育水槽から沈殿槽、泡沫分離槽、硝化槽を順次経由して再び飼育水槽に戻る閉鎖的な循環経路を循環して浄化処理される。   As a breeding water treatment method in which breeding water is treated for removing suspended matter and nitrified with aerobic microorganisms, the method described in Patent Document 1 has been known. In this conventional example, the water in the breeding aquarium where the fish and shellfish are bred is clarified by circulating through a closed circulation path that returns from the breeding tank to the breeding tank through the sedimentation tank, foam separation tank, and nitrification tank in order. Is done.

上記沈殿槽は、槽内に一定時間飼育水を滞留させて水中の残餌や糞などを沈殿させ、水から分離する。また、上記泡沫分離槽は、エアレーションすることによって、気泡表面に浮遊物質を付着させたり、泡立てによって溶解性有機物の発泡を促進させて有機物を泡沫として水から分離する。さらに、上記硝化槽は、該硝化槽内に充填してある粒状の濾過材に付着する微生物としての好気性の硝化菌の硝化作用によって、水中のアンモニアを分解する。   In the settling tank, breeding water is retained in the tank for a certain period of time to precipitate residual bait, feces, etc. in the water and separate from the water. In addition, the foam separation tank separates the organic substance from the water as a foam by aeration to attach a floating substance to the bubble surface or promote foaming of the soluble organic substance by foaming. Further, the nitrification tank decomposes ammonia in water by the nitrification action of aerobic nitrifying bacteria as microorganisms attached to the particulate filter medium filled in the nitrification tank.

また、上記沈殿槽等のそれぞれの槽からは、上述した循環経路に加えてそれぞれの槽での浄化処理に伴って発生する汚泥を水とともに固液分離手段に取り出すための取り出し経路が設けられ、この固液分離手段で汚泥と分離された水は戻し経路によって沈殿槽に返送されて浄化処理に伴う水の減少が防止される。循環経路に流れる水量の例えば1/2から1/10までの程度の水量が固液分離手段に取り出される。
特開2002-223667号公報
Moreover, from each tank such as the settling tank, in addition to the above-described circulation path, a take-out path for taking out sludge generated along with the purification treatment in each tank together with water to the solid-liquid separation means is provided, The water separated from the sludge by this solid-liquid separation means is returned to the sedimentation tank by the return path, and the reduction of the water accompanying the purification treatment is prevented. For example, a water amount of about 1/2 to 1/10 of the amount of water flowing through the circulation path is taken out by the solid-liquid separation means.
JP 2002-223667 A

しかしながら、上記従来例は、飼育水の処理のための設備が大型化、あるいは複雑化してしまうという欠点がある。   However, the above conventional example has a drawback that the equipment for the treatment of breeding water becomes larger or complicated.

すなわち、上記従来例における硝化槽のような好気性の微生物による硝化処理は、一般に、処理効率があまり良好ではないために設備、すなわち硝化槽が大型化してしまうという問題がある。このような低い処理効率は酸素供給量不足による微生物の非活性化が大きな原因とされており、このために例えば従来においては、攪拌装置等を槽内に別途設置し、濾材表面を流れる飼育水の流速を速めて微生物への酸素の供給を良好にするなどの対応が取られる場合があるが、この場合には攪拌装置の設置により設備がより複雑化してしまうという新たな問題が生じてしまう。   In other words, the nitrification treatment using an aerobic microorganism such as the nitrification tank in the above conventional example generally has a problem that the equipment, that is, the nitrification tank is enlarged because the treatment efficiency is not so good. Such low treatment efficiency is largely caused by inactivation of microorganisms due to insufficient oxygen supply. For this reason, conventionally, for example, a stirrer or the like is separately installed in the tank, and the breeding water flowing on the surface of the filter medium is used. Although measures such as increasing the flow rate of oxygen to improve the supply of oxygen to microorganisms may be taken, in this case, a new problem arises that the installation of the stirring device makes the facility more complicated .

本発明は以上の欠点を解消すべくなされたものであって、設備をより小型化、単純化することができる飼育水処理方法、飼育水処理装置、および飼育システムの提供を目的とする。   The present invention has been made to solve the above drawbacks, and an object of the present invention is to provide a breeding water treatment method, a breeding water treatment apparatus, and a breeding system capable of further downsizing and simplifying equipment.

本発明によれば上記目的は、
飼育水1を懸濁物除去処理するとともに、好気性の微生物により硝化処理する飼育水処理方法であって、
前記微生物を収容する生物濾過槽2に流入された飼育水1を泡沫分離装置3に引き込み、泡沫分離処理により懸濁物4を除去するとともに溶存酸素量を高めた後、前記生物濾過槽2に戻して好気性の微生物の硝化作用を促進させる飼育水処理方法を提供することにより達成される。
According to the present invention, the object is
A breeding water treatment method in which the breeding water 1 is subjected to a suspension removal treatment and nitrified with an aerobic microorganism,
The breeding water 1 that has flowed into the biological filtration tank 2 containing the microorganisms is drawn into the foam separation device 3, and the suspension 4 is removed by foam separation treatment and the amount of dissolved oxygen is increased. This is achieved by providing a breeding water treatment method that promotes the nitrification action of aerobic microorganisms.

本発明によれば、生物濾過槽2に流入された飼育水1は泡沫分離装置3に引き込まれて泡沫分離処理された後、再度生物濾過槽2に戻される。泡沫分離処理における泡沫の発生、すなわち飼育水1中への空気の供給は、懸濁物4の除去と同時に溶存酸素量を増大させ、泡沫分離処理を経由した飼育水1が生物濾過槽2に帰還されることにより、生物濾過槽2内の飼育水1の溶存酸素量を増大させることができ、好気性の微生物の処理効率を向上させることができる。   According to the present invention, the breeding water 1 that has flowed into the biological filtration tank 2 is drawn into the foam separation device 3 and subjected to foam separation, and then returned to the biological filtration tank 2 again. The generation of foam in the foam separation process, that is, the supply of air into the breeding water 1 increases the amount of dissolved oxygen simultaneously with the removal of the suspension 4, and the breeding water 1 via the foam separation process enters the biological filtration tank 2. By returning, the amount of dissolved oxygen in the breeding water 1 in the biological filtration tank 2 can be increased, and the treatment efficiency of aerobic microorganisms can be improved.

生物濾過槽2と泡沫分離装置3との間での飼育水1の循環は、生物濾過槽2内の飼育水1の全量をそのまま泡沫分離装置3に導入し、泡沫分離処理後の飼育水1の全量をそのまま生物濾過槽2に戻して行う、すなわち生物濾過槽2、泡沫分離装置3にそれぞれ飼育水1を一度ずつのみ通すなどして処理させることも可能であるが、生物濾過処理と泡沫分離処理のそれぞれに必要な処理時間の違いを利用すれば、生物濾過槽2内の飼育水1の全量のうちの一部の適量を泡沫分離装置3に順次引き込み、生物濾過処理に比して泡沫分離処理の処理回数を増やして実質的に全量に対して泡沫分離処理をさせることも可能で、この場合には、泡沫分離装置3をより小型化することができる上に、泡沫分離処理の繰り返しによって溶存酸素量をより増大させることができる。上記処理回数は、浄化すべき水質を考慮して適宜実験により決定することができる。   Circulation of the breeding water 1 between the biological filtration tank 2 and the foam separation apparatus 3 introduces the whole amount of the breeding water 1 in the biological filtration tank 2 into the foam separation apparatus 3 as it is, and the breeding water 1 after the foam separation process It is possible to return the whole amount to the biological filtration tank 2 as it is, that is, the biological filtration tank 2 and the foam separation device 3 can be treated by passing the breeding water 1 only once. If the difference in processing time required for each separation process is used, an appropriate amount of a part of the total amount of the breeding water 1 in the biological filtration tank 2 is sequentially drawn into the foam separation device 3, and compared with the biological filtration process. It is also possible to increase the number of times of the foam separation process and cause the foam separation process to be performed on substantially the entire amount. In this case, the foam separation device 3 can be further downsized, and the foam separation process Repeatedly increase the amount of dissolved oxygen It can be. The number of treatments can be appropriately determined by experiment in consideration of the water quality to be purified.

また、上述した従来例のように飼育水1を生物濾過槽2を介して循環させたときには、泡沫分離装置3から帰還する水量により生物濾過槽2の導入水量が増えることによって、生物濾過槽2内の流速を速めて微生物への酸素供給の機会を増大させることができる。   In addition, when the breeding water 1 is circulated through the biological filtration tank 2 as in the above-described conventional example, the amount of water introduced into the biological filtration tank 2 is increased by the amount of water returned from the foam separation device 3, thereby the biological filtration tank 2. The flow rate inside can be increased to increase the chance of oxygen supply to the microorganism.

したがって本発明によれば、酸素供給量の増大により、生物濾過処理時における好気性の微生物による硝化処理効率を向上させることができ、水質浄化性能を維持して、生物濾過槽2をより小型化、単純化することができる。また、上述したように飼育水1を循環処理する場合において、処理水量の増大を生物濾過処理に限れば、泡沫分離処理のためなどの他の設備について大型化を招くことはない。   Therefore, according to the present invention, by increasing the oxygen supply amount, it is possible to improve the nitrification efficiency by aerobic microorganisms during the biological filtration process, maintain the water purification performance, and further reduce the size of the biological filtration tank 2. Can be simplified. Moreover, in the case where the breeding water 1 is circulated as described above, if the increase in the amount of treated water is limited to the biological filtration process, the size of other equipment such as for the foam separation process is not increased.

このような飼育水処理方法を用いた閉鎖循環式の飼育水処理によって高効率な飼育水1の浄化を行えば、水族館における海獣等の飼育のほか、早期に大きく育てるために多量に餌を与えることによる残餌や、このような餌の大量摂取に伴って多量に排泄される糞や尿が発生するような養殖魚等の飼育であってもより簡易に、かつ良好に飼育水1の水質を維持することができる。また、水質の良好な維持により、新しい水の補充による病原菌の混入のおそれを低減させて安定して良好に飼育、養殖を行うことができる。さらに、養殖の休閑期などの場合には、飼育水1を生物濾過処理と泡沫分離処理との間でのみ循環させれば、良好に経費を節減しつつ微生物を維持させることができる。さらに、万一疾病が発生したときには、泡沫分離処理設備を利用して空気の代わりにオゾンを飼育水1に供給し、殺菌処理することも可能である。   If highly efficient breeding water 1 is purified by such a closed-circulation breeding water treatment using the breeding water treatment method, a large amount of food is given for breeding sea animals in an aquarium, as well as for early growth. The quality of the breeding water 1 is simpler and better even if it is reared by cultured fish such as residual food due to the occurrence of such a thing, or feces and urine excreted in large quantities due to such large intake of food. Can be maintained. In addition, by maintaining good water quality, the possibility of contamination by pathogenic bacteria due to replenishment of new water can be reduced and stable breeding and aquaculture can be performed. Furthermore, in the fallow season of aquaculture, if the breeding water 1 is circulated only between the biofiltration process and the foam separation process, the microorganisms can be maintained with good cost savings. Furthermore, in the unlikely event that a disease occurs, ozone can be supplied to the breeding water 1 in place of air using a foam separation treatment facility and sterilized.

また、以上の飼育水処理は、
飼育水1に含まれた懸濁物4を通過させる間隙8を形成する濾材6によって好気性の微生物を保持し、流入された飼育水1を微生物により硝化処理する生物濾過槽2と、
該生物濾過槽2から飼育水1を引き込み、エアレータ9からのエアレーションにより懸濁物除去処理するとともに溶存酸素量を高めて前記生物濾過槽2に帰還させる泡沫分離装置3とを有する飼育水処理装置を用いて行うことができる。
In addition, the above breeding water treatment
A biological filtration tank 2 for holding aerobic microorganisms by a filter medium 6 that forms a gap 8 through which a suspension 4 contained in the breeding water 1 passes, and nitrifying the fed breeding water 1 with microorganisms;
A breeding water treatment apparatus having a foam separation device 3 that draws the breeding water 1 from the biological filtration tank 2 and removes suspended matter by aeration from an aerator 9 and returns the amount of dissolved oxygen to the biological filtration tank 2. Can be used.

生物濾過槽2は、懸濁物4が除去される前の飼育水1の流入によって懸濁物4が蓄積されてしまうことを防ぐことができるように、懸濁物4を通過させる間隙8を形成する濾材6によって硝化作用のある微生物を保持する。懸濁物4を通過させる間隙8を形成するには、例えば、濾材6を多数の粒状体で構成する場合には、粒状体の粒径や形状などを調節すれば足り、この粒径等については、飼育水1に含まれる懸濁物4のサイズ、すなわち飼育する水棲生物の糞の大きさなどを考慮して適宜実験により決定することが可能である。   The biological filtration tank 2 has a gap 8 through which the suspension 4 passes so as to prevent the suspension 4 from accumulating due to the inflow of the breeding water 1 before the suspension 4 is removed. The filter medium 6 to be formed holds microorganisms having a nitrifying action. In order to form the gap 8 through which the suspension 4 passes, for example, when the filter medium 6 is composed of a large number of granular materials, it is sufficient to adjust the particle size and shape of the granular materials. Can be appropriately determined by experiment in consideration of the size of the suspension 4 contained in the breeding water 1, that is, the size of feces of aquatic organisms to be reared.

また、生物濾過槽2から泡沫分離装置3への飼育水1の導入には、泡沫分離装置3のエアレータ9によって生じる泡沫7の浮上による水流を利用することも可能である。このようにエアレータ9を泡沫7の発生のみならず水流を起こすためのポンプのように機能させる、いわゆるエアリフト方式を採用すれば、泡沫分離装置3に飼育水1を導入するための独立の動力を必要としないことから、より設備を簡略化することができる。   In addition, for introducing the breeding water 1 from the biological filtration tank 2 to the foam separation device 3, it is possible to use a water flow caused by the rising of the foam 7 generated by the aerator 9 of the foam separation device 3. In this way, if the so-called air lift system is used in which the aerator 9 functions not only as the generation of the foam 7 but also as a pump for generating a water flow, independent power for introducing the breeding water 1 into the foam separation device 3 is obtained. Since it is not necessary, the equipment can be further simplified.

この場合において、上述した閉鎖循環式の水処理として構成し、エアレータ9によって生じる水流を生物濾過槽2の排出口5から排出される、すなわち飼育水槽14に繋がる循環水路13に流れ出る水流よりも強く設定し、泡沫分離装置3への導入水量を排出口5からの排出水量よりも大きくすれば、飼育水1から懸濁物4を良好に除去して閉鎖循環させることができる。   In this case, the water flow generated by the aerator 9 is configured as the above-described closed-circulation type water treatment and is discharged from the discharge port 5 of the biological filtration tank 2, that is, stronger than the water flow flowing out to the circulation water channel 13 connected to the breeding water tank 14. If set and the amount of water introduced into the foam separator 3 is made larger than the amount of water discharged from the outlet 5, the suspension 4 can be well removed from the breeding water 1 and closed and circulated.

以上の説明から明らかなように、本発明によれば、飼育水の処理に要する設備をより小型化、単純化することができ、コストを抑えて飼育水の水質を良好に維持することができる。また、水質の良好な維持によって閉鎖循環式で処理される飼育水の補充による病原菌の混入のおそれを低減させて良好に飼育を行うことができる。   As is clear from the above description, according to the present invention, the equipment required for the treatment of breeding water can be further reduced in size and simplified, and the quality of the breeding water can be maintained well at a reduced cost. . Moreover, by maintaining good water quality, it is possible to reduce the risk of contamination with pathogenic bacteria due to supplementation of breeding water that is treated in a closed circulation manner, and breed well.

図1および図2に本発明の実施の形態を示す。この実施の形態はタイやヒラメ、フグといった魚の養殖を目的とする飼育システムを構築したもので、魚を飼育する飼育水槽14内の飼育水1を浄化処理するために、飼育水槽14には循環水路13を用いた水処理装置、すなわち閉鎖循環式の飼育水1の処理装置が接続される。   1 and 2 show an embodiment of the present invention. In this embodiment, a breeding system is constructed for the purpose of cultivating fish such as Thailand, flounder, and puffer fish. In order to purify the breeding water 1 in the breeding tank 14 for breeding fish, the breeding tank 14 is circulated. A water treatment device using the water channel 13, that is, a treatment device for the closed circulation breeding water 1 is connected.

飼育水1の処理装置は、生物濾過槽2と、懸濁物除去装置(泡沫分離装置3)と、温度調節装置20と、殺菌装置21とを有し、飼育水槽14内の飼育水1の適量を循環水路13を介してこれらを経由して処理された浄化処理水と常時入れ替えることにより、飼育水槽14内の飼育水1を清浄化した状態に維持する。   The treatment device for the breeding water 1 includes a biological filtration tank 2, a suspension removing device (foam separation device 3), a temperature control device 20, and a sterilization device 21, and the breeding water 1 in the breeding water tank 14. The breeding water 1 in the breeding aquarium 14 is maintained in a purified state by constantly replacing an appropriate amount with the purified treated water that has been treated via these through the circulation water channel 13.

上記生物濾過槽2は硝化処理、すなわち、主に魚が飼育水1中に排泄する毒性の強いアンモニアを微生物(硝化微生物)によって酸化させて亜硝酸、硝酸へと変える処理をするためのもので、硝化作用を有する好気性の微生物が付着する多数の粒状体からなる濾材6を槽2内部に収容する。図2に示すように、この濾材6は適宜メッシュサイズの網22に保持あるいは規制されて生物濾過槽2からの流出を防止され、飼育水1の通過により、飼育水1に溶存する酸素の供給を受けた微生物によって硝化処理を施す。   The biological filtration tank 2 is used for nitrification treatment, that is, a treatment that mainly oxidizes highly toxic ammonia excreted in the breeding water 1 by a microorganism (nitrification microorganism) into nitrous acid and nitric acid. The filter medium 6 composed of a large number of granular materials to which aerobic microorganisms having a nitrifying action adhere is accommodated in the tank 2. As shown in FIG. 2, the filter medium 6 is appropriately held or regulated by a mesh-sized net 22 to prevent outflow from the biological filtration tank 2, and supply of oxygen dissolved in the breeding water 1 by passing the breeding water 1 Nitrification is performed by the microorganisms that have undergone the treatment.

また、上記懸濁物除去装置3は、エアレータ9によって飼育水1中に微細な泡沫7を生じさせる空気を供給し、浮上する泡沫7に飼育水1中を浮遊する懸濁物4を付着させて水面に浮上した泡沫7とともに懸濁物4をスカムとして飼育水1から分離、回収する泡沫分離装置3であり、この実施の形態においては、エアレータ9によるエアレーションによって生じる水流により装置3内部の中空部23に処理対象水となる飼育水1を導入し、また該中空部23から処理済水としての飼育水1を排出させる、すなわちエアレーションによって循環水流を生じさせるいわゆるエアリフト方式の泡沫分離装置3が使用される。図2に示すように、エアリフトで循環させるために、上記中空部23の底部にはエアレータ9の散気部8aに隣接して飼育水1を導入する取水部12が、装置3上部には飼育水1を排出する排水部11が設けられ、装置3天井部には、飼育水1中の懸濁物4を付着した泡沫7が溢れ出やすいように漏斗状にすぼめられた開口部3aが設けられる。懸濁物4を付着させて開口部3aから溢れ出た泡7は、廃棄槽24に蓄積され、この後、適宜固液分離などして処分される。   In addition, the suspension removing device 3 supplies air that generates fine foam 7 in the breeding water 1 by the aerator 9, and attaches the suspension 4 floating in the breeding water 1 to the rising foam 7. The foam separation device 3 separates and collects the suspension 4 from the breeding water 1 as a scum together with the foam 7 floating on the water surface. In this embodiment, the hollow inside the device 3 is generated by the water flow generated by aeration by the aerator 9. A so-called air lift type foam separation device 3 that introduces breeding water 1 to be treated water into the section 23 and discharges the breeding water 1 as treated water from the hollow section 23, that is, generates a circulating water flow by aeration. used. As shown in FIG. 2, in order to circulate by an air lift, a water intake section 12 for introducing the breeding water 1 is introduced at the bottom of the hollow section 23 adjacent to the air diffuser section 8 a of the aerator 9, and the apparatus 3 is raised at the top. A drainage unit 11 for discharging the water 1 is provided, and an opening 3a that is constricted in a funnel shape is provided in the ceiling of the device 3 so that the foam 7 attached with the suspension 4 in the breeding water 1 is likely to overflow. It is done. The bubbles 7 overflowing from the opening 3a due to the suspension 4 are accumulated in the disposal tank 24, and then disposed of by appropriate solid-liquid separation.

上記温度調節装置20は、飼育水槽14内の飼育水1を温度管理するもので、図示しない制御機構に従ってボイラーや冷凍機により加熱、冷却したチューブ内に飼育水1を通し、飼育水槽14内の飼育水1を飼育対象の魚に適した水温に制御する。また、上記殺菌装置21は、導入された飼育水1に紫外線を照射し、ウィルスや大腸菌などの殺菌処理を施す。   The temperature control device 20 controls the temperature of the breeding water 1 in the breeding aquarium 14. The breeding water 1 is passed through a tube heated and cooled by a boiler or a freezer according to a control mechanism (not shown), The breeding water 1 is controlled to a water temperature suitable for the fish to be reared. In addition, the sterilizer 21 irradiates the introduced breeding water 1 with ultraviolet rays and sterilizes viruses, E. coli, and the like.

以上の飼育水処理装置の循環水路13は、図1に示すように、飼育水槽14から生物濾過槽2、温度調節装置20、殺菌装置21を順番に経由して飼育水槽14に戻る循環経路を形成する。循環経路上には、生物濾過槽2から循環水路13へと流れる流速、流量を調整しやすいように、送水用のポンプ25が生物濾過槽2と温度調節装置20とを接続する循環水路13上に設けられ、これにより飼育水1が循環経路内をほぼ一定の流速で流される。飼育水槽14からの飼育水1の引き出しは、沈殿する糞等を取り込みやすいように、例えば、飼育水槽14の底部から行われる。   As shown in FIG. 1, the circulation water channel 13 of the breeding water treatment apparatus described above has a circulation path from the breeding water tank 14 to the breeding water tank 14 through the biological filtration tank 2, the temperature control device 20, and the sterilization device 21 in order. Form. On the circulation path, on the circulation water path 13 where the water supply pump 25 connects the biological filtration tank 2 and the temperature control device 20 so that the flow velocity and flow rate flowing from the biological filtration tank 2 to the circulation water path 13 can be easily adjusted. Thus, the breeding water 1 is caused to flow through the circulation path at a substantially constant flow rate. The withdrawal of the breeding water 1 from the breeding aquarium 14 is performed, for example, from the bottom of the breeding aquarium 14 so that sedimented feces and the like can be easily taken in.

また、上述した循環水路13が直接接続されない泡沫分離装置3は、生物濾過槽2との間で飼育水1を交換することで飼育水1に懸濁物除去処理を施す。図2に示すように、上述した生物濾過槽2には、濾材6を挟む流路を形成するようにして流入口10と排出口5が設けられ、循環水路13を介して飼育水槽14から流れてきた飼育水1は、生物濾過槽2に流入口10から流入されて排出口5から排出する過程で濾材6を通過する。   Moreover, the foam separation apparatus 3 to which the circulating water channel 13 described above is not directly connected performs suspension removal processing on the breeding water 1 by exchanging the breeding water 1 with the biological filtration tank 2. As shown in FIG. 2, the biological filtration tank 2 described above is provided with an inlet 10 and an outlet 5 so as to form a flow path sandwiching the filter medium 6, and flows from the breeding water tank 14 through the circulation water channel 13. The raised breeding water 1 passes through the filter medium 6 in the process of flowing into the biological filtration tank 2 from the inlet 10 and discharging from the outlet 5.

生物濾過槽2の上方への開放部を流入口10として活用するこの実施の形態において、生物濾過槽2には、底部を連通させて生物濾過槽2を2つの区画に仕切る縦方向の仕切り26が設けられ、この仕切り26で仕切られたより広い一方の区画の上方への開放部が流入口10として機能し、他方の区画の上部に上述した排出口5が形成される。濾材6は、泡沫分離装置3による懸濁物除去処理前の飼育水1の流入を考慮し、飼育水1中の懸濁物4が通過できる間隙8を形成するサイズの粒状体の多数で構成され、上記一方の区画内を水平方向に塞ぐようにして配置されて網22で支持され、生物濾過槽2の高さ方向中間部に保持される。これにより飼育水1は、生物濾過槽2の一方の区画に上方から流入されると、濾材6を通過して下方に移動し、仕切り26を越えて他方の区画側に移動した後、今度は上方に移動して排出口5から排出される。   In this embodiment in which the upward opening portion of the biological filtration tank 2 is utilized as the inflow port 10, the biological filtration tank 2 has a vertical partition 26 that communicates the bottom and partitions the biological filtration tank 2 into two compartments. The upper opening of one of the wider compartments partitioned by the partition 26 functions as the inflow port 10, and the discharge port 5 described above is formed in the upper part of the other compartment. In consideration of the inflow of the breeding water 1 before the suspension removal process by the foam separation device 3, the filter medium 6 is composed of a large number of granular materials having a size that forms a gap 8 through which the suspension 4 in the breeding water 1 can pass. Then, it is arranged so as to block the inside of the one section in the horizontal direction, is supported by the net 22, and is held at the intermediate portion in the height direction of the biological filtration tank 2. As a result, when the breeding water 1 flows into one section of the biological filtration tank 2 from above, the breeding water 1 moves downward through the filter medium 6, moves over the partition 26 to the other section side, and this time. It moves upward and is discharged from the discharge port 5.

上述した生物濾過槽2と飼育水1を交換する泡沫分離装置3は、取水部12によって上記濾材6の下方、すなわち濾材6を既に通過した飼育水1を生物濾過槽2から中空部23の底部に取り込み、この中空部23内で泡沫分離処理してから排水部11によって濾材6の上方、すなわち流入口10から生物濾過槽2内に流入されて濾材6を通過する前の飼育水1に加えるようにして処理済水を生物濾過槽2に帰還させる。上記中空部23は有底の略円筒形状に形成され、取水部12は、略水平に延びて生物濾過槽2の低い位置とエアレータ9の散気部8aに隣接する泡沫分離装置3の中空部23の低い位置とを接続し、また、排水部11は、略水平に延びて生物濾過槽2の高い位置と泡沫分離装置3の中空部23の高い位置を接続する。   The foam separation device 3 for exchanging the biological filtration tank 2 and the breeding water 1 described above has the intake part 12 below the filter medium 6, that is, the breeding water 1 that has already passed through the filter medium 6 from the biological filtration tank 2 to the bottom of the hollow part 23. In the hollow portion 23, foam separation is performed, and then the drainage portion 11 is added to the breeding water 1 before being passed through the filter medium 6 by flowing into the biological filtration tank 2 from above the filter medium 6, that is, from the inlet 10. In this way, the treated water is returned to the biological filtration tank 2. The hollow part 23 is formed in a substantially cylindrical shape with a bottom, and the water intake part 12 extends substantially horizontally, and is a hollow part of the foam separation device 3 adjacent to the low position of the biological filtration tank 2 and the diffuser part 8a of the aerator 9. The drainage part 11 extends substantially horizontally and connects the high position of the biological filtration tank 2 and the high position of the hollow part 23 of the foam separation device 3.

また、上記泡沫分離装置3として上述した生物濾過槽2による生物濾過処理に比べて処理能力の低い小型のものを用いるこの実施の形態において、生物濾過処理と泡沫分離処理のそれぞれの処理時間の違いを考慮した上で、上述したポンプ25とエアレータ9によるエアリフトのそれぞれの送水力が適宜調整される。すなわち、生物濾過槽2から排出口5を通って飼育水槽14に戻される飼育水1について、単に一度泡沫分離処理が施されたものよりも水質を良好にし、溶存酸素量を高めるには、排出口5を通る単位時間当たりの水量よりも、取水部12によって泡沫分離装置3に引き込まれる単位時間当たりの水量が多ければ足りる。この実施の形態においては、生物濾過槽2よりも比較的処理能力が低く、かつ、処理時間が短い泡沫分離装置3に取水部12によって生物濾過槽2の排出口5から排出されるよりも速い流速で飼育水1を引き込むことにより、単位時間当たりで生物濾過処理される水量よりも泡沫分離処理される水量を増大させ、生物濾過槽2から排出口5を通って飼育水槽14に戻る飼育水1に対して実質的に十分な泡沫分離処理を確保する。   Moreover, in this embodiment using the small thing with a low processing capability compared with the biological filtration process by the biological filtration tank 2 mentioned above as the said foam separation apparatus 3, the difference of each processing time of a biological filtration process and a foam separation process In consideration of the above, the water supply forces of the air lift by the pump 25 and the aerator 9 described above are appropriately adjusted. That is, for the breeding water 1 returned from the biological filtration tank 2 through the discharge port 5 to the breeding tank 14, in order to improve the water quality and increase the amount of dissolved oxygen compared to the case where the foam separation process is performed once, It is sufficient that the amount of water per unit time drawn into the foam separation device 3 by the water intake unit 12 is larger than the amount of water per unit time passing through the outlet 5. In this embodiment, the processing capacity is relatively lower than that of the biological filtration tank 2 and the processing time is shorter than that of the foam separation device 3 being discharged from the outlet 5 of the biological filtration tank 2 by the water intake unit 12. By pulling the breeding water 1 at a flow rate, the amount of water that is subjected to foam separation treatment is increased from the amount of water that is subjected to biological filtration treatment per unit time, and the breeding water that returns from the biological filtration tank 2 to the breeding tank 14 through the discharge port 5. A substantially sufficient foam separation process for 1 is ensured.

したがって飼育水処理装置は、飼育水1を飼育水槽14と生物濾過槽2等との間で循環させる主循環系27と、この主循環系27内の生物濾過槽2に対して泡沫分離装置3との間での飼育水1を循環させる副循環系28とを有し、副循環系28によって主循環系27を循環する飼育水1に生物濾過処理工程と同時に懸濁物除去処理工程を行い、飼育水槽14から汚れた飼育水1を常時取り込むと同時に、浄化された飼育水1を継続供給する。また、副循環系28が主循環系27よりも循環流の流速、流量を高く設定され、生物濾過処理される濾過処理対象水は、副循環系28を循環する泡沫分離処理済水によって溶存酸素量が増大されるとともに流速が速められ、かつ、懸濁物4の含有量が低減され、これによって濾材6に付着する微生物への酸素供給量を増大させて硝化処理効率が高められる。   Therefore, the breeding water treatment apparatus includes a main circulation system 27 that circulates the breeding water 1 between the breeding water tank 14 and the biological filtration tank 2 and the like, and a foam separation device 3 for the biological filtration tank 2 in the main circulation system 27. And a sub-circulation system 28 for circulating the breeding water 1 between them, and the suspension-removing process step is performed simultaneously with the biological filtration process step on the breeding water 1 circulating through the main circulation system 27 by the sub-circulation system 28. The contaminated breeding water 1 is always taken in from the breeding water tank 14, and at the same time, the purified breeding water 1 is continuously supplied. The subcirculation system 28 is set to have a higher circulation flow velocity and flow rate than the main circulation system 27, and the filtration target water to be biologically filtered is dissolved oxygen by the foam-separated water circulating through the subcirculation system 28. As the amount is increased, the flow rate is increased, and the content of the suspension 4 is reduced, thereby increasing the amount of oxygen supplied to the microorganisms adhering to the filter medium 6 and increasing the nitrification efficiency.

なお、以上においては飼育水槽14から懸濁物4を除去することなく生物濾過槽2に直接飼育水1を導入し、生物濾過槽2を経由して泡沫分離装置3によって飼育水1に懸濁物除去処理を施す場合を示したが、飼育水1を滞留させるなどすれば、例えば、泡沫分離装置3を経由して生物濾過槽2に飼育水1を導入し、生物濾過槽2と泡沫分離装置3との間で飼育水1の交換を繰り返した後、泡沫分離装置3から循環させることなども可能である。また、生物濾過槽2内の濾材6を通過し、あるいは濾材6を通過する前の飼育水1を泡沫分離装置3との間で交換するに際しては、泡沫分離装置3の取水部12、排水部11によって生物濾過槽2自体に対して直接取水、排水するほか、例えば、生物濾過槽2の上流、下流の循環水路13に取水部12、排水部11を接続して行うことも可能である。   In the above, the breeding water 1 is directly introduced into the biological filtration tank 2 without removing the suspension 4 from the breeding tank 14 and suspended in the breeding water 1 by the foam separation device 3 via the biological filtration tank 2. Although the case where the thing removal process is performed has been shown, if the breeding water 1 is retained, for example, the breeding water 1 is introduced into the biological filtration tank 2 via the foam separation device 3, and the biological filtration tank 2 and the foam separation are performed. It is also possible to circulate from the foam separator 3 after repeating the exchange of the breeding water 1 with the device 3. Moreover, when exchanging the breeding water 1 before passing through the filtering medium 6 in the biological filtration tank 2 or before passing through the filtering medium 6 with the foam separating apparatus 3, a water intake section 12 and a drain section of the foam separating apparatus 3 are used. In addition to directly taking water from and draining the biological filtration tank 2 by 11, for example, it is possible to connect the water intake part 12 and the drainage part 11 to the circulation channel 13 upstream and downstream of the biological filtration tank 2.

飼育水の処理手順を示すフローチャートである。It is a flowchart which shows the processing procedure of breeding water. 生物濾過処理と泡沫分離処理の流れを示す図である。It is a figure which shows the flow of a biofiltration process and a foam separation process.

符号の説明Explanation of symbols

1 飼育水
2 生物濾過槽
3 泡沫分離装置
4 懸濁物
5 排出口
6 濾材
7 泡沫
8 間隙
9 エアレータ
10 流入口
11 排水部
12 取水部
13 循環水路
14 飼育水槽
DESCRIPTION OF SYMBOLS 1 Breeding water 2 Biological filtration tank 3 Foam separator 4 Suspension 5 Outlet 6 Filter medium 7 Foam 8 Gap 9 Aerator 10 Inlet 11 Drainage part 12 Water intake part 13 Circulation channel 14 Breeding tank 14

Claims (5)

飼育水を懸濁物除去処理するとともに、好気性の微生物により硝化処理する飼育水処理方法であって、
前記微生物を収容する生物濾過槽に流入された飼育水を泡沫分離装置に引き込み、泡沫分離処理により懸濁物を除去するとともに溶存酸素量を高めた後、前記生物濾過槽に戻して好気性の微生物の硝化作用を促進させる飼育水処理方法。
It is a breeding water treatment method in which breeding water is treated for removing suspended matter and nitrified by aerobic microorganisms,
The breeding water that has flowed into the biological filtration tank containing the microorganisms is drawn into a foam separation device, the suspension is removed by foam separation treatment and the dissolved oxygen amount is increased, and then returned to the biological filtration tank to return to the aerobic A breeding water treatment method for promoting nitrification of microorganisms.
前記硝化処理は、流入されるとともに泡沫分離装置から帰還される飼育水を生物濾過槽に形成される排出口から排出する途上で微生物が付着する濾材に通過させてなされ、
前記泡沫分離処理は、発生する泡沫によって前記排出口に流れ込む排出流よりも強い水流を生じさせて生物濾過槽の濾材を通過した飼育水を排出口に比べて優先的に泡沫分離装置に引き込むことによりなされる請求項1記載の飼育水処理方法。
The nitrification treatment is performed by passing the breeding water that is introduced and returned from the foam separation device through a filter medium to which microorganisms adhere on the way to discharge from the discharge port formed in the biological filtration tank,
In the foam separation process, the generated water causes a stronger water flow than the discharge flow flowing into the discharge port, and the breeding water that has passed through the filter medium of the biological filtration tank is preferentially drawn into the foam separation device compared to the discharge port. The breeding water treatment method according to claim 1, which is performed by:
飼育水に含まれた懸濁物を通過させる間隙を形成する濾材によって好気性の微生物を保持し、流入された飼育水を微生物により硝化処理する生物濾過槽と、
該生物濾過槽から飼育水を引き込み、エアレータからのエアレーションにより懸濁物除去処理するとともに溶存酸素量を高めて前記生物濾過槽に帰還させる泡沫分離装置とを有する飼育水処理装置。
A biological filtration tank that retains aerobic microorganisms by a filter medium that forms a gap through which a suspension contained in the breeding water passes, and nitrifies the fed breeding water with microorganisms;
A breeding water treatment apparatus comprising: a foam separation device that draws breeding water from the biological filtration tank, removes suspended matter by aeration from an aerator, and returns the amount of dissolved oxygen to the biological filtration tank.
前記生物濾過槽には、飼育水を流入する流入口、および該流入口から流入されるとともに泡沫分離装置の排水部から排出されて硝化微生物が付着する濾材を通過した飼育水を排出する排出口が形成され、
前記泡沫分離装置には、エアレーションによって水流を生じさせて生物濾過槽の濾材を通過した飼育水を取り込む取水部が形成される請求項3記載の飼育水処理装置。
The biological filtration tank has an inlet through which breeding water flows, and an outlet through which the breeding water that has flowed from the inlet and discharged from the drainage part of the foam separation device and passed through the filter medium to which nitrifying microorganisms adhere is discharged. Formed,
The breeding water treatment apparatus according to claim 3, wherein the foam separation device is formed with a water intake portion that takes in breeding water that has passed through the filter medium of the biological filtration tank by generating a water flow by aeration.
請求項3記載の飼育水処理装置の生物濾過槽に循環水路を介して接続され、循環処理により収容する飼育水の水質が浄化管理された飼育水槽を備える閉鎖循環式の飼育システム。   A closed circulation type breeding system comprising a breeding water tank connected to the biological filtration tank of the breeding water treatment apparatus according to claim 3 through a circulation channel and whose quality of the breeding water stored by the circulation treatment is purified and managed.
JP2007232985A 2007-09-07 2007-09-07 Breeding water treatment method, breeding water treatment device, and breeding system Expired - Fee Related JP4960182B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011194368A (en) * 2010-03-23 2011-10-06 Chugoku Electric Power Co Inc:The Nitrification tank and wastewater treatment system
JP2017077511A (en) * 2015-10-19 2017-04-27 王子ホールディングス株式会社 Water treatment system and method
CN114524529A (en) * 2022-03-11 2022-05-24 重庆工商大学 Intelligent aeration control system and method

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JPH01265837A (en) * 1988-04-15 1989-10-23 Nichipura Kaiyo Setsubi Kk Raising device of aquatic animal
JPH02234620A (en) * 1989-03-07 1990-09-17 Yanmar Diesel Engine Co Ltd Container device for live fish
JP2002191257A (en) * 2000-12-25 2002-07-09 Matsushita Electric Works Ltd Apparatus for cleaning apparatus for cultivating fish and shellfish

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01265837A (en) * 1988-04-15 1989-10-23 Nichipura Kaiyo Setsubi Kk Raising device of aquatic animal
JPH02234620A (en) * 1989-03-07 1990-09-17 Yanmar Diesel Engine Co Ltd Container device for live fish
JP2002191257A (en) * 2000-12-25 2002-07-09 Matsushita Electric Works Ltd Apparatus for cleaning apparatus for cultivating fish and shellfish

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011194368A (en) * 2010-03-23 2011-10-06 Chugoku Electric Power Co Inc:The Nitrification tank and wastewater treatment system
JP2017077511A (en) * 2015-10-19 2017-04-27 王子ホールディングス株式会社 Water treatment system and method
CN114524529A (en) * 2022-03-11 2022-05-24 重庆工商大学 Intelligent aeration control system and method

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