JP2542292B2 - Purification method for fish tank water - Google Patents
Purification method for fish tank waterInfo
- Publication number
- JP2542292B2 JP2542292B2 JP3053796A JP5379691A JP2542292B2 JP 2542292 B2 JP2542292 B2 JP 2542292B2 JP 3053796 A JP3053796 A JP 3053796A JP 5379691 A JP5379691 A JP 5379691A JP 2542292 B2 JP2542292 B2 JP 2542292B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- ozone
- seawater
- tank
- 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.)
- Expired - Fee Related
Links
Landscapes
- Farming Of Fish And Shellfish (AREA)
- Physical Water Treatments (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は水族館や養魚場等に使用
される魚類水槽の水槽水浄化方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying aquarium water of a fish tank used in aquariums, fish farms and the like.
【0002】[0002]
【従来の技術】魚類水槽においては、魚類の排泄物や残
餌からアンモニアが生じ、これが魚類の呼吸障害を引き
起こすことから、その除去が重要な課題とされている。
そのため、魚類水槽の浄化は、アンモニアの除去を主眼
に考えられ、一般的には生物学的濾過法が採用されてい
る。また、一部では、これにオゾンによる処理を組合せ
た魚類水槽水の浄化も試みられている。2. Description of the Related Art In a fish tank, ammonia is produced from excretions and residual food of fish, which causes respiratory disorders of fish. Therefore, its removal is an important issue.
Therefore, the purification of the fish tank is considered mainly to remove ammonia, and the biological filtration method is generally adopted. In addition, some attempts have been made to purify fish tank water by combining this with ozone treatment.
【0003】[0003]
【発明が解決しようとする課題】生物学的濾過法による
魚類水槽水の浄化においては、水槽水が濾過砂に通され
て、微細な有機懸濁物が水槽水から除去されると共に、
水槽水中のアンモニアが魚類に無害な硝酸塩に酸化され
る。しかし、浄化の基本形態が緩速濾過のため、装置が
大規模になるのを避け得ず、また、炉床の細菌群が環境
的不安定要素(例えば塩分、水温、溶存酸素、溶解性有
機物など)に対して極めて敏感であるため、望ましい硝
化割合を保証することが難しい。更に、流行性病原菌の
突発を完全に抑えることも難しい。In the purification of fish aquarium water by biological filtration, the aquarium water is passed through filter sand to remove fine organic suspensions from the aquarium water, and
Ammonia in the aquarium water is oxidized to nitrate, which is harmless to fish. However, since the basic form of purification is slow filtration, it is unavoidable that the equipment becomes large-scale, and the bacterial groups in the hearth also have environmental instability factors (for example, salt, water temperature, dissolved oxygen, soluble organic matter). It is difficult to guarantee the desired nitrification rate. Furthermore, it is difficult to completely suppress the outbreak of epidemic pathogens.
【0004】これに対し、オゾンによる処理を組合せた
場合には、その強力な酸化作用により処理速度が上が
り、装置が小型化されると共に、その強力な細菌作用に
より病原菌の発生をも効果的に抑えることができる。し
かし、オゾンは単体ではアンモニアに対する分解効果が
小さい。そのようなこともあり、オゾンによる浄化効果
を得ようとすると、かなりの注入量が必要となり、溶存
オゾンが水槽内に流入するのを避け得なくなる。溶存オ
ゾンは、それ自体が魚類に有害であるだけでなく、種々
の酸化性物質を生成し、水槽内の魚類を死滅に至らしめ
る危険性がある。On the other hand, when the treatment with ozone is combined, the treatment speed is increased by the strong oxidizing action, the apparatus is miniaturized, and the strong bacterial action effectively causes the generation of pathogenic bacteria. Can be suppressed. However, ozone alone has a small decomposition effect on ammonia. Due to such circumstances, in order to obtain a purifying effect by ozone, a considerable injection amount is required, and it becomes inevitable that dissolved ozone will flow into the water tank. Dissolved ozone is not only harmful to fish itself, but also produces various oxidative substances, and there is a risk of killing fish in the aquarium.
【0005】本発明の目的は、これからの問題を解決し
た高効率で且つ安全性の高い魚類水槽水の浄化方法を提
供することにある。An object of the present invention is to provide a highly efficient and highly safe method for purifying fish tank water that solves the problems hereafter.
【0006】[0006]
【課題を解決するための手段】本発明の浄化方法は、魚
類水槽内の海水または海水とほぼ同程度に臭素を添加し
た真水を水槽から導出し、導出した水槽水の流れにエジ
エクタにてオゾンガスを注入して水中に次亜臭素酸イオ
ンを反応生成せしめ、次いで、その水槽水を気液分離し
て未反応オゾンを除去した後、前記次亜臭素酸イオンと
アンモニアとの分解反応を促進させる二酸化マンガン触
媒濾材に通過させて水槽へ還流させることを特徴として
なる。According to the purification method of the present invention, seawater in a fish tank or fresh water to which bromine is added to approximately the same level as seawater is drawn out from the tank, and the derived tank water flow
Hypobromous acid in water by injecting ozone gas in the effector Io
The emissions reacted product and then, after removing the unreacted ozone in the gas-liquid separating the aquarium water and the hypobromite ion
It is characterized in that it is passed through a manganese dioxide catalyst filter medium that promotes a decomposition reaction with ammonia and then refluxed to a water tank.
【0007】[0007]
【作用】本発明の浄化方法においては、魚類水槽から導
出された水槽水は、二酸化マンガン触媒濾材へと流れる
途中で、エジエクタにより注入されるオゾンにより脱色
殺菌されると共に、水槽水中に含まれる臭素イオンが式
1の反応により酸化されて次亜臭素酸イオン(OB
r−)を生成する。次亜臭素酸イオンが溶解した水槽水
は、未反応オゾンを除去された後、二酸化マンガン触媒
濾材を通過する。このとき、式2により水槽水中のアン
モニアの分解反応か促進され、また、式3に示す溶存オ
ゾンの分解反応も進む。In the purifying method of the present invention, the aquarium water derived from the fish aquarium flows to the manganese dioxide catalyst filter medium.
Along the way, ozone is injected by an ejecta to decolorize and sterilize, and bromine ions contained in the aquarium water are oxidized by the reaction of Formula 1 to form hypobromite ions (OB
r − ) is generated. The aquarium water in which the hypobromite ions have been dissolved passes through the manganese dioxide catalyst filter medium after the unreacted ozone is removed. At this time, the decomposition reaction of ammonia in the aquarium water is promoted by the formula 2, and the decomposition reaction of dissolved ozone shown in the formula 3 also proceeds.
【0008】[0008]
【式1】O3 +Br- →O2 +OBr- [Formula 1] O 3 + Br − → O 2 + OBr −
【0009】[0009]
【式2】 NH4 + +OBr- →NH2 Br +H2 O 2NH2 Br +OBr- →N2 ↑+3Br- +H2 O+2H+ [Equation 2] NH 4 + + OBr - → NH 2 Br + H 2 O 2NH 2 B r + OBr - → N 2 ↑ + 3Br - + H 2 O + 2H +
【0010】[0010]
【式3】O3 →O2 [Formula 3] O 3 → O 2
【0011】なお、オゾンと二酸化マンガンとを組合せ
た水処理は特開昭59−139991号公報に開示され
ているが、ここに示された水処理は、浄水場における水
道水の浄化であり、処理水に臭素が含まれない点で本発
明とは本質的に異なり、従って、アンモニアに対する分
解効果が小さく、溶存オゾンや酸化性物質の生成および
除去についても何ら考慮してしない。A water treatment in which ozone and manganese dioxide are combined is disclosed in Japanese Patent Laid-Open No. 59-139991, but the water treatment shown here is purification of tap water in a water purification plant. The treated water is essentially different from the present invention in that it does not contain bromine, and therefore has a small decomposition effect on ammonia, and no consideration is given to the production and removal of dissolved ozone and oxidizing substances.
【0012】[0012]
【実施例】以下に本発明の実施例を図面に基づいて説明
する。図1は本発明の浄化方法を実施するのに適した浄
化システムの模式図である。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic diagram of a purification system suitable for carrying out the purification method of the present invention.
【0013】魚類水槽1には海水が収容されている。水
槽1内の海水は、循環ポンプ2により水槽1から汲み出
されてエジェクタ3に送られる。エジェクタ3では、オ
ゾン発生機4で発生されたオゾンガスが海水に注入され
る。オゾンガスが注入された海水は、反応促進濾過装置
5内へ上方から注入される。濾過装置5の上部は気液分
離部6である。濾過装置5の気液分離部6では、オゾン
ガスが注入された海水から、未反応オゾンが気液分離さ
れる。海水から分離された未反応オゾンは、濾過装置5
外へ排出され、排オゾン分解装置7で分解される。未反
応オゾンが除去された海水は、濾過装置5内に収容され
た二酸化マンガン濾材8を通過して水槽1へ還流され
る。The fish tank 1 contains seawater. The seawater in the water tank 1 is pumped out of the water tank 1 by the circulation pump 2 and sent to the ejector 3. In the ejector 3, the ozone gas generated by the ozone generator 4 is injected into seawater. The seawater into which the ozone gas has been injected is injected into the reaction promoting filter device 5 from above. The gas-liquid separating section 6 is located above the filtering device 5. In the gas-liquid separation unit 6 of the filter device 5, unreacted ozone is separated into gas and liquid from the seawater into which ozone gas is injected. The unreacted ozone separated from the seawater is filtered by the filtration device 5
It is discharged to the outside and decomposed by the exhaust ozone decomposing device 7. The seawater from which unreacted ozone has been removed passes through the manganese dioxide filter medium 8 contained in the filtration device 5 and is returned to the water tank 1.
【0014】このような浄化方法によれば、まず、海水
にオゾンが加えられることにより、海水が脱色殺菌され
ると共に、海水中の臭素イオンが次亜臭素酸イオンに酸
化される。次いで、海水から未反応オゾンが除去された
後、その海水が二酸化マンガン濾材8を通過する。その
際に、海水中の溶存オゾンが分解されると共に、上記次
亜臭素酸イオンを介して、アンモニアの分解反応が促進
される。According to such a purification method, first, ozone is added to seawater to decolorize and sterilize the seawater and oxidize bromine ions in the seawater to hypobromite ions. Next, after the unreacted ozone is removed from the seawater, the seawater passes through the manganese dioxide filter medium 8. At that time, dissolved ozone in seawater is decomposed, and the decomposition reaction of ammonia is promoted through the hypobromite ion.
【0015】このとき、オゾンは水槽1の外で海水に加
えられ、しかも、海水が水槽1へ還流される前に、海水
から未反応オゾンが除去され、且つ海水中の溶存オゾン
が除去される。そのため、オゾンおよび酸化性物質が水
槽1内へ侵入するおそれがなく、充分な安全性が確保さ
れると共に、多量のオゾン使用によってオゾンによる処
理効率を上げることができる。また、アンモニアに対し
ては、オゾンは単体では分解能力が小さいが、海水中の
臭素を媒体とすることにより、高い分解効率を示し、そ
の多量使用とあいまって優れた浄化能力を発揮するよう
になる。なお、水槽水が海水ではなく真水の場合は、こ
れに臭素イオンを添加するとことにより同様の効果を挙
げることができる。At this time, ozone is added to the seawater outside the water tank 1, and before the seawater is returned to the water tank 1, unreacted ozone is removed from the seawater and dissolved ozone in the seawater is removed. . Therefore, there is no risk of ozone and oxidizing substances entering the water tank 1, sufficient safety is ensured, and the use efficiency of ozone can be improved by using a large amount of ozone. Also, for ammonia, ozone has a small decomposition ability by itself, but by using bromine in seawater as a medium, it shows high decomposition efficiency, so that it can exhibit excellent purification ability in combination with its large use. Become. When the aquarium water is not seawater but fresh water, the same effect can be obtained by adding bromine ions to this.
【0016】図1の浄化システムにおいて、本発明の浄
化方法の有効性を調査した結果を表1に示す。原水(水
槽内の海水)中の臭素イオン濃度は50〜60g/m3
であった。OBr−と溶存オゾンは全酸化性物質として
定量した。表1からわかるように、システム入口水と濾
過装置入口水との間にアンモニア量の差がなく、オゾン
のみではアンモニア分解効果が小さい。しかし、濾過装
置出口水ではアンモニア量が低下している。そして、そ
の浄化効果はオゾン注入量を多くするほど増加し、多量
のオゾンを注入した場合も溶存オゾンおよび酸化性物質
の流出がない。これにより、原水が二酸化マンガン触媒
濾材を通過する間に、原水中の次亜臭素酸イオンとアン
モニアとの分解反応が、著しく促進されていることが判
明した。 Table 1 shows the results of investigation of the effectiveness of the purification method of the present invention in the purification system of FIG. The bromine ion concentration in raw water (seawater in the aquarium) is 50 to 60 g / m 3.
Met. OBr − and dissolved ozone were quantified as total oxidizing substances. As can be seen from Table 1, there is no difference in the amount of ammonia between the system inlet water and the filter inlet water, and the ozone decomposition effect is small only with ozone. However, the amount of ammonia in the outlet water of the filter is low. The purification effect increases as the ozone injection amount increases, and even when a large amount of ozone is injected, dissolved ozone and oxidizing substances do not flow out. As a result, the raw water becomes a manganese dioxide catalyst.
During passage through the filter medium, hypobromite ions and anions in raw water
It was found that the decomposition reaction with monia was significantly accelerated.
Revealed.
【0017】[0017]
【表1】 [Table 1]
【0018】[0018]
【発明の効果】以上の説明から明らかなように、本発明
の魚類水槽水の浄化方法は、オゾンを多量使用した場合
も水槽への溶存オゾンおよび酸化性物質の侵入がなく、
安全性に著しく優れる。また、オゾン単体では分解効果
の小さいアンモニアに対しても分解反応を促進し、オゾ
ンの多量使用が可能なこととあいまって浄化能力に著し
く優れる。従って、小型かつ高性能で処理速度が速く、
しかも安全性に優れた浄化システムが提供される。As is clear from the above description, the method for purifying fish tank water according to the present invention does not cause dissolved ozone and oxidizing substances to enter the tank even when a large amount of ozone is used.
Remarkably excellent in safety. In addition, ozone alone promotes the decomposition reaction even with respect to ammonia, which has a small decomposition effect, and, in combination with the possibility of using a large amount of ozone, the cleaning performance is remarkably excellent. Therefore, it is small, high-performance, fast in processing speed ,
Moreover, a purification system with excellent safety is provided.
【図面の簡単な説明】[Brief description of drawings]
【図1】本発明の浄化方法を実施するのに適した浄化シ
ステムの模式図である。FIG. 1 is a schematic diagram of a purification system suitable for carrying out the purification method of the present invention.
1 魚類水槽 3 エジェクタ 4 オゾン発生機 5 濾過装置 6 気液分離部 8 二酸化マンガン濾材 1 Fish Tank 3 Ejector 4 Ozone Generator 5 Filtration Device 6 Gas-Liquid Separation Section 8 Manganese Dioxide Filter Media
Claims (1)
度に臭素を添加した真水を水槽から導出し、導出した水
槽水の流れにエジエクタにてオゾンガスを注入して水中
に次亜臭素酸イオンを反応生成せしめ、次いで、その水
槽水を気液分離して未反応オゾンを除去した後、前記次
亜臭素酸イオンとアンモニアとの分解反応を促進させる
二酸化マンガン触媒濾材に通過させて水槽へ還流させる
ことを特徴とする魚類水槽水の浄化方法。1. Sea water in a fish tank, or fresh water containing bromine added to about the same level as sea water is discharged from the water tank, and ozone gas is injected into the stream of the discharged water by an Ejecta machine to make it into water.
A hypobromous acid ion reacted product and then, after removing the unreacted ozone in the gas-liquid separating the aquarium water, the following
Method of purifying fish aquarium water, characterized in that the decomposition reaction of the bromite ion and ammonia is passed through a manganese dioxide catalyst filtering medium Ru is promoted is refluxed to the water tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3053796A JP2542292B2 (en) | 1991-02-25 | 1991-02-25 | Purification method for fish tank water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3053796A JP2542292B2 (en) | 1991-02-25 | 1991-02-25 | Purification method for fish tank water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04267829A JPH04267829A (en) | 1992-09-24 |
JP2542292B2 true JP2542292B2 (en) | 1996-10-09 |
Family
ID=12952784
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3053796A Expired - Fee Related JP2542292B2 (en) | 1991-02-25 | 1991-02-25 | Purification method for fish tank water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2542292B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002335811A (en) * | 2001-05-17 | 2002-11-26 | Tacmina Corp | Culturing seawater circulating unit |
JP5854502B2 (en) * | 2011-11-21 | 2016-02-09 | 株式会社アクルス | Ozone sterilizer |
CN108849692A (en) * | 2018-06-12 | 2018-11-23 | 伊婕 | A kind of raising fish and shrimp case and application method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59139991A (en) * | 1983-01-31 | 1984-08-11 | Suido Kiko Kk | Colored water disposal |
JPH01288395A (en) * | 1988-05-16 | 1989-11-20 | Ebara Jitsugyo Kk | Ozone purifying device of water tank |
JPH03181391A (en) * | 1989-12-08 | 1991-08-07 | Mitsubishi Electric Corp | Water treating device for decomposition ammoniacal nitrogen |
-
1991
- 1991-02-25 JP JP3053796A patent/JP2542292B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59139991A (en) * | 1983-01-31 | 1984-08-11 | Suido Kiko Kk | Colored water disposal |
JPH01288395A (en) * | 1988-05-16 | 1989-11-20 | Ebara Jitsugyo Kk | Ozone purifying device of water tank |
JPH03181391A (en) * | 1989-12-08 | 1991-08-07 | Mitsubishi Electric Corp | Water treating device for decomposition ammoniacal nitrogen |
Also Published As
Publication number | Publication date |
---|---|
JPH04267829A (en) | 1992-09-24 |
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