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JP6947602B2 - Water treatment equipment and water treatment method - Google Patents
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JP6947602B2 - Water treatment equipment and water treatment method - Google Patents

Water treatment equipment and water treatment method Download PDF

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JP6947602B2
JP6947602B2 JP2017196919A JP2017196919A JP6947602B2 JP 6947602 B2 JP6947602 B2 JP 6947602B2 JP 2017196919 A JP2017196919 A JP 2017196919A JP 2017196919 A JP2017196919 A JP 2017196919A JP 6947602 B2 JP6947602 B2 JP 6947602B2
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圭一郎 福水
圭一郎 福水
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Organo Corp
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Description

本発明は、水生生物の飼育水を処理する水処理装置及び水処理方法に関する。 The present invention relates to a water treatment apparatus and a water treatment method for treating breeding water for aquatic organisms.

水族館や養殖場等で、水生生物を飼育する際に用いられる飼育水には、水生生物の飼育に伴い、通常、懸濁物質、有機物、アンモニア態窒素等が含まれる。そして、水生生物の飼育水中の懸濁物質等を除去することは、水生生物の健康を保持するために重要である。 The breeding water used for breeding aquatic organisms in aquariums, aquaculture farms, etc. usually contains suspended solids, organic matter, ammonia nitrogen, etc. in association with the breeding of aquatic organisms. It is important to remove suspended solids and the like in the breeding water of aquatic organisms in order to maintain the health of aquatic organisms.

例えば、特許文献1には、魚介類を飼育する閉鎖循環式養殖装置の飼育槽から抜き出した、残餌や糞及び飼育魚が排泄したアンモニア及び有機性排泄物などを含む飼育水から、懸濁物質や排泄物質を分離または分解処理する装置として、膜分離活性汚泥処理装置を備えた閉鎖循環式養殖装置を使用して養殖魚を飼育するにあたり、膜分離活性汚泥処理装置の曝気槽に粒子状活性炭を添加して運転する魚介類の飼育方法が提案されている。 For example, in Patent Document 1, suspended from breeding water containing residual feed, feces, ammonia excreted by breeding fish, organic excrement, etc., extracted from the breeding tank of a closed-circulation aquaculture device for breeding fish and shellfish. When breeding aquaculture fish using a closed circulation aquaculture device equipped with a membrane separation activated sludge treatment device as a device for separating or decomposing substances and excreted substances, particles are placed in the aeration tank of the membrane separation activated sludge treatment device. A method for raising fish and shellfish that is operated by adding activated charcoal has been proposed.

特開2011−130685号公報Japanese Unexamined Patent Publication No. 2011-130685

しかし、膜分離活性汚泥処理装置の場合、飼育水中に生息する細菌の繁殖や、飼育水中の有機物等により、膜の表面が汚染され、細孔が塞がれてしまうファウリングが生じる場合がある。 特に、アンモニア等のアンモニア態窒素が含まれる飼育水を処理しようとする場合、窒素が細菌の栄養源となり、ファウリングを助長してしまう可能性がある。なお、飼育水中のアンモニア濃度が高くなると、それ自体が魚等に毒性を示すため、除去することが望ましい。 However, in the case of a membrane separation activated sludge treatment device, the surface of the membrane may be contaminated by the growth of bacteria living in the breeding water, organic substances in the breeding water, etc., and fouling may occur in which the pores are blocked. .. In particular, when trying to treat breeding water containing ammoniacal nitrogen such as ammonia, nitrogen becomes a nutrient source for bacteria and may promote fouling. When the ammonia concentration in the breeding water becomes high, it is toxic to fish and the like, so it is desirable to remove it.

そこで、本発明の目的は、ファウリングを抑制し、飼育水を安定して処理することが可能な水処理装置及び水処理方法を提供することにある。 Therefore, an object of the present invention is to provide a water treatment apparatus and a water treatment method capable of suppressing fouling and stably treating breeding water.

本発明は、水生生物の飼育水を処理する水処理装置であって、前記飼育水が供給される反応槽と、前記反応槽内に浸漬され、前記飼育水をろ過する浸漬型ろ過膜と、前記反応槽内にオゾンを供給して、前記飼育水をオゾン処理するオゾン処理手段と、前記浸漬型ろ過膜によりろ過された前記処理水が貯留される処理水槽と、前記処理水槽内に貯留された前記処理水中に含まれる、前記オゾン処理により発生した過酸化物を分解処理する過酸化物分解処理手段と、前記処理水槽内に貯留された前記処理水を使用して、前記浸漬型ろ過膜を逆洗処理する逆洗処理手段と、を備え、前記浸漬型ろ過膜は、セラミック製ろ過膜であり、前記反応槽に供給される前記飼育水は、水生生物を飼育する水槽からの飼育水であり、前記過酸化物分解処理手段により過酸化物が分解処理された処理水を前記水槽に返送する返送手段を有する水処理装置である。 The present invention is a water treatment apparatus for treating breeding water of aquatic organisms, which comprises a reaction tank to which the breeding water is supplied, an immersion type filter membrane which is immersed in the reaction tank and filters the breeding water. An ozone treatment means for supplying ozone to the reaction tank to treat the breeding water with ozone, a treated water tank in which the treated water filtered by the immersion type filtration membrane is stored, and a treated water tank stored in the treated water tank. The immersion type filtration film is used by using the peroxide decomposition treatment means for decomposing the peroxide generated by the ozone treatment and the treated water stored in the treated water tank, which are contained in the treated water. The immersion type filter membrane is a ceramic filter membrane, and the breeding water supplied to the reaction tank is breeding water from a tank for breeding aquatic organisms. It is a water treatment apparatus having a return means for returning the treated water in which the peroxide is decomposed by the peroxide decomposition treatment means to the water tank.

また、前記水処理装置において、前記飼育水は海水であることが好ましい。 Further, in the water treatment apparatus, the breeding water is preferably seawater.

また、前記水処理装置において、前記飼育水は内陸型水族館の飼育水であることが好ましい。 Further, in the water treatment apparatus, it is preferable that the breeding water is the breeding water of an inland aquarium.

また、前記水処理装置において、前記過酸化物分解処理手段は、活性炭処理装置であることが好ましい。 Further, in the water treatment apparatus, the peroxide decomposition treatment means is preferably an activated carbon treatment apparatus.

また、本発明は、水生生物の飼育水を処理する水処理方法であって、前記飼育水が供給される反応槽内に浸漬された浸漬型ろ過膜により、前記飼育水をろ過するろ過工程と、前記反応槽内にオゾンを供給して、前記飼育水をオゾン処理するオゾン処理工程と、前記ろ過工程によりろ過された処理水を処理水槽に貯留する工程と、前記処理水槽に貯留された前記処理水中に含まれる、前記オゾン処理により発生した過酸化物を分解処理する過酸化物分解処理工程と、前記処理水槽内に貯留された前記処理水を使用して、前記浸漬型ろ過膜を逆洗処理する逆洗処理工程と、を備え、前記浸漬型ろ過膜は、セラミック製ろ過膜であり、前記反応槽に供給される前記飼育水は、水生生物を飼育する水槽からの飼育水であり、前記過酸化物分解処理工程により過酸化物が分解処理された処理水を前記水槽に返送する返送工程を有する水処理方法である。 Further, the present invention is a water treatment method for treating breeding water of aquatic organisms, which comprises a filtration step of filtering the breeding water by an immersion type filtration membrane immersed in a reaction tank to which the breeding water is supplied. An ozone treatment step of supplying ozone into the reaction tank and treating the breeding water with ozone, a step of storing the treated water filtered by the filtration step in the treated water tank, and the step of storing the treated water in the treated water tank. The immersion type filtration membrane is reversed by using the peroxide decomposition treatment step of decomposing the peroxide generated by the ozone treatment contained in the treated water and the treated water stored in the treated water tank. The immersion type filter membrane is a ceramic filter membrane, and the breeding water supplied to the reaction tank is breeding water from a tank for breeding aquatic organisms. It is a water treatment method including a return step of returning the treated water in which the peroxide is decomposed by the peroxide decomposition treatment step to the water tank.

また、前記水処理方法において、前記飼育水は海水であることが好ましい。 Further, in the water treatment method, the breeding water is preferably seawater.

また、前記水処理方法において、前記飼育水は内陸型水族館の飼育水であることが好ましい。 Further, in the water treatment method, it is preferable that the breeding water is the breeding water of an inland aquarium.

また、前記水処理方法において、前記過酸化物分解処理工程は、活性炭処理装置により、前記ろ過工程によりろ過された処理水中に含まれる、前記オゾン処理により発生した過酸化物を分解処理することが好ましい。 Further, in the water treatment method, in the peroxide decomposition treatment step, the peroxide generated by the ozone treatment contained in the treated water filtered by the filtration step can be decomposed by the activated carbon treatment apparatus. preferable.

本発明によれば、ファウリングを抑制し、飼育水を安定して処理することが可能となる。 According to the present invention, fouling can be suppressed and breeding water can be treated stably.

本実施形態に係る水処理装置の一例を示す概略構成図である。It is a schematic block diagram which shows an example of the water treatment apparatus which concerns on this embodiment. 本実施形態に係る水処理装置の他の一例を示す概略構成図である。It is a schematic block diagram which shows another example of the water treatment apparatus which concerns on this embodiment.

本発明の実施の形態について以下説明する。本実施形態は本発明を実施する一例であって、本発明は本実施形態に限定されるものではない。 Embodiments of the present invention will be described below. The present embodiment is an example of carrying out the present invention, and the present invention is not limited to the present embodiment.

図1は、本実施形態に係る水処理装置の一例を示す概略構成図である。図1に示す水処理装置1は、反応槽10、反応槽10内に浸漬された浸漬型膜モジュール12、オゾン処理装置14、処理水槽16、循環ポンプ18、吸引ポンプ20、配管22a,22b,22c、オゾン排出配管24、返送ポンプ26、逆洗ポンプ28、逆洗配管30を備えている。 FIG. 1 is a schematic configuration diagram showing an example of a water treatment apparatus according to the present embodiment. The water treatment device 1 shown in FIG. 1 includes a reaction tank 10, an immersion type film module 12 immersed in the reaction tank 10, an ozone treatment device 14, a treatment water tank 16, a circulation pump 18, a suction pump 20, and pipes 22a and 22b. It includes 22c, an ozone discharge pipe 24, a return pump 26, a backwash pump 28, and a backwash pipe 30.

図1に示すオゾン処理装置14は、オゾン発生装置32、オゾン供給配管34、散気装置36を備えている。散気装置36は、反応槽10内に設置されている。オゾン発生装置32と散気装置36はオゾン供給配管34により接続されている。図1に示すオゾン処理装置14はオゾン処理手段の一例である。オゾン処理手段としては、オゾンを発生して、当該オゾンを反応槽10内に供給することができる構成であれば特に制限されるものではない。 The ozone treatment device 14 shown in FIG. 1 includes an ozone generator 32, an ozone supply pipe 34, and an air diffuser 36. The air diffuser 36 is installed in the reaction tank 10. The ozone generator 32 and the air diffuser 36 are connected by an ozone supply pipe 34. The ozone treatment device 14 shown in FIG. 1 is an example of ozone treatment means. The ozone treatment means is not particularly limited as long as it can generate ozone and supply the ozone into the reaction vessel 10.

図1に示す浸漬型膜モジュール12は、浸漬型ろ過膜38及び集水配管40を備えている。浸漬型ろ過膜38は、反応槽10内に設置されている。浸漬型ろ過膜38は単一でも複数でもよい。集水配管40は、浸漬型ろ過膜38の上端に設置されている。図1に示す浸漬型ろ過膜38は、例えば、その内部に膜を透過した処理水が流入する集水空間が形成されており、浸漬型ろ過膜38の上端に設置された集水配管40と連通している。図1に示す浸漬型膜モジュール12は一例であって、反応槽10内に浸漬される浸漬型ろ過膜38を備えるものであれば特に制限されるものではない。 The immersion type membrane module 12 shown in FIG. 1 includes an immersion type filtration membrane 38 and a water collecting pipe 40. The immersion type filtration membrane 38 is installed in the reaction tank 10. The immersion type filtration membrane 38 may be single or plural. The water collecting pipe 40 is installed at the upper end of the immersion type filtration membrane 38. The immersion type filtration membrane 38 shown in FIG. 1 has, for example, a water collection space in which treated water that has permeated the membrane flows into the immersion type filtration membrane 38, and has a water collection pipe 40 installed at the upper end of the immersion type filtration membrane 38. Communicating. The immersion type membrane module 12 shown in FIG. 1 is an example, and is not particularly limited as long as it includes the immersion type filtration membrane 38 immersed in the reaction vessel 10.

図1の水処理装置において、水槽41の出口と反応槽10の入口とが循環ポンプ18を介して配管22aにより接続されている。また、集水配管40の出口と処理水槽16の入口とが吸引ポンプ20を介して配管22bにより接続されている。また、処理水槽16の出口と水槽41の入口とが、返送ポンプ26を介して配管22cにより接続されている。また、処理水槽16の逆洗用出口と配管22bとは逆洗ポンプ28を介して逆洗配管30により接続されている。また、反応槽10にはオゾン排出配管24が接続されている。 In the water treatment apparatus of FIG. 1, the outlet of the water tank 41 and the inlet of the reaction tank 10 are connected by a pipe 22a via a circulation pump 18. Further, the outlet of the water collecting pipe 40 and the inlet of the treatment water tank 16 are connected by a pipe 22b via a suction pump 20. Further, the outlet of the treatment water tank 16 and the inlet of the water tank 41 are connected by a pipe 22c via a return pump 26. Further, the backwash outlet of the treatment water tank 16 and the pipe 22b are connected by the backwash pipe 30 via the backwash pump 28. Further, an ozone discharge pipe 24 is connected to the reaction tank 10.

図1の水処理装置1の動作について説明する。 The operation of the water treatment device 1 of FIG. 1 will be described.

水槽41内では、魚類等の水生生物が飼育水中で飼育されている。飼育水は、水族館等に設置される展示水槽、養殖用水槽、活魚水槽等の水槽水等が挙げられ、淡水でも海水でもよい。飼育水は、水生生物の飼育に伴い、通常、懸濁物質、有機物、アンモニア態窒素等が含まれる。 In the aquarium 41, aquatic organisms such as fish are bred in the breeding water. Examples of the breeding water include an exhibition tank installed in an aquarium, aquaculture tank, aquarium water such as a live fish tank, and the like, and may be fresh water or seawater. The breeding water usually contains suspended solids, organic matter, ammonia nitrogen and the like with the breeding of aquatic organisms.

水槽41内の飼育水は、循環ポンプ18により配管22aを通して反応槽10に供給される。また、配管22bに設置された吸引ポンプ20によって、浸漬型ろ過膜38に吸引圧力が付与されると、反応槽10内の飼育水が、浸漬型ろ過膜38によりろ過される(ろ過工程)。これにより、飼育水中の懸濁物質等は、浸漬型ろ過膜38により除去され、浸漬型ろ過膜38を透過した処理水は、膜内の内部空間(二次側(処理水側))、集水配管40、配管22bを通り、処理水槽16に供給される。 The breeding water in the water tank 41 is supplied to the reaction tank 10 through the pipe 22a by the circulation pump 18. Further, when a suction pressure is applied to the immersion type filtration film 38 by the suction pump 20 installed in the pipe 22b, the breeding water in the reaction tank 10 is filtered by the immersion type filtration film 38 (filtration step). As a result, suspended solids and the like in the breeding water are removed by the immersion type filtration membrane 38, and the treated water that has permeated through the immersion type filtration membrane 38 collects in the internal space (secondary side (treated water side)) in the membrane. It is supplied to the treatment water tank 16 through the water pipe 40 and the pipe 22b.

また、反応槽10には、オゾン発生装置32で発生させたオゾンが、オゾン供給配管34、散気装置36を通して供給され、反応槽10内の飼育水がオゾン処理される(オゾン処理工程)。なお、排オゾンは、オゾン排出配管24を通して排出される。 Further, ozone generated by the ozone generator 32 is supplied to the reaction tank 10 through the ozone supply pipe 34 and the air diffuser 36, and the breeding water in the reaction tank 10 is treated with ozone (ozone treatment step). The discharged ozone is discharged through the ozone discharge pipe 24.

オゾン処理は、反応槽10内の飼育水とオゾンとを接触させる処理であり、これにより、飼育水中の微生物や有機物等が分解処理される。また、飼育水中に、ハロゲン化物イオンが含まれている場合、以下に説明するように、ハロゲン化物イオンとオゾンとの反応により生成したハロゲンオキソ酸等の過酸化物により、アンモニア等のアンモニア態窒素が分解処理される。なお、飼育水は、海水や淡水が用いられるため、通常ハロゲン化物イオンが含まれる。 The ozone treatment is a treatment in which the breeding water in the reaction tank 10 is brought into contact with ozone, whereby microorganisms, organic substances and the like in the breeding water are decomposed. When the breeding water contains a halide ion, as described below, a peroxide such as a halogen oxo acid generated by the reaction between the halide ion and ozone causes ammonia nitrogen such as ammonia. Is disassembled. Since seawater and fresh water are used as the breeding water, halide ions are usually contained.

以下に、オゾン処理によるアンモニア態窒素の分解反応の一例を説明する。 An example of the decomposition reaction of ammonia nitrogen by ozone treatment will be described below.

下記式1に示すように、飼育水に含まれるハロゲン化物イオンとオゾンとの反応により、過酸化物である次亜ハロゲン酸(HXO)等のハロゲンオキソ酸が発生する。 As shown in the following formula 1, a halogen oxo acid such as hypohalogenate (HXO), which is a peroxide, is generated by the reaction between the halide ion contained in the breeding water and ozone.

[式1]
+ O → O + OX
OX + HO → HXO + OH
(ここで、Xは、塩化物イオン(Cl)、臭化物イオン(Br)、ヨウ化物イオン(I)等のハロゲン化物イオンであり、Xは、Cl,Br,I等のハロゲンである。)
[Equation 1]
X + O 3 → O 2 + OX
OX + H 2 O → HXO + OH
(Here, X is a halide ion such as chloride ion (Cl ), bromide ion (Br ), iodide ion (I ), and X is a halogen such as Cl, Br, I. be.)

が塩化物イオンの場合、下記式2に示すように、飼育水に含まれる塩化物イオンとオゾンとの反応により、過酸化物である次亜塩素酸(HClO)等のハロゲンオキソ酸が発生する。 When X is a chloride ion, as shown in the following formula 2, a halogen oxo acid such as hypochlorous acid (HClO), which is a peroxide, is generated by the reaction between the chloride ion contained in the breeding water and ozone. appear.

[式2]
Cl + O → O + OCl
OCl + HO → HClO + OH
[Equation 2]
Cl - + O 3 → O 2 + OCl -
OCl + H 2 O → HClO + OH

また、Xが臭化物イオンの場合、下記式3に示すように、飼育水に含まれる臭化物イオンとオゾンとの反応により、過酸化物である次亜臭素酸(HBrO)等のハロゲンオキソ酸が発生する。
[式3]
Br + O → O + OBr
OBr + HO → HBrO + OH
When X is a bromide ion, as shown in the following formula 3, halogen oxo acids such as hypobromous acid (HBrO), which is a peroxide, are generated by the reaction between the bromide ion contained in the breeding water and ozone. appear.
[Equation 3]
Br + O 3 → O 2 + OBr
OBr + H 2 O → HBr O + OH

そして、下記式4に示すように、発生させた次亜ハロゲン酸等のハロゲンオキソ酸により、飼育水に含まれるアンモニア態窒素が分解される。 Then, as shown in the following formula 4, the generated halogen oxo acid such as hypochlorous acid decomposes the ammonia nitrogen contained in the breeding water.

[式4]
HXO + NH → NHX + H
3HXO + 2NH → 2N + 3HX + 3H
(ここで、Xは、Cl,Br,I等のハロゲンである。)
[Equation 4]
HXO + NH 3 → NH 2 X + H 2 O
3HXO + 2NH 3 → 2N 2 + 3HX + 3H 2 O
(Here, X is a halogen such as Cl, Br, I, etc.)

特に、XがBrの場合、発生させた次亜臭素酸により、飼育水に含まれるアンモニア態窒素が分解され易い(下記式5参照)。 In particular, when X is Br, the generated hypobromous acid easily decomposes the ammonia nitrogen contained in the breeding water (see the following formula 5).

[式5]
HBrO + NH → NHBr + H
3HBrO + 2NH → 2N + 3HBr + 3H
[Equation 5]
HBrO + NH 3 → NH 2 Br + H 2 O
3HBrO + 2NH 3 → 2N 2 + 3HBr + 3H 2 O

このように、図1に示す水処理装置1では、反応槽10内に浸漬した浸漬型ろ過膜38により飼育水をろ過して、飼育水中の懸濁物質等を除去するだけでなく、反応槽10内の飼育水をオゾン処理して、飼育水中に生息する細菌、有機物、アンモニア態窒素等を分解する。したがって、細菌、有機物、アンモニア態窒素等により、浸漬型ろ過膜38の表面が汚染されて、細孔が塞がれてしまうファウリングが抑制されるため、飼育水の安定処理が可能となる。 As described above, in the water treatment apparatus 1 shown in FIG. 1, not only the breeding water is filtered by the immersion type filtration membrane 38 immersed in the reaction tank 10 to remove suspended solids and the like in the breeding water, but also the reaction tank is used. The breeding water in No. 10 is treated with ozone to decompose bacteria, organic substances, ammonium nitrogen, etc. that live in the breeding water. Therefore, the surface of the immersion filtration membrane 38 is contaminated by bacteria, organic substances, ammonia nitrogen, and the like, and fouling that closes the pores is suppressed, so that stable treatment of the breeding water becomes possible.

図1に示す水処理装置1において、処理水槽16に貯留された処理水の一部は、返送ポンプ26により配管22cを通して水槽41に返送されるが、処理水槽16が水槽41よりも上部にある場合は、返送ポンプを使わずに、自然流下によって返送してもよい。なお、処理水は、水槽41に返送せれずに、水処理装置1の系外へ排出されてもよい。 In the water treatment apparatus 1 shown in FIG. 1, a part of the treated water stored in the treated water tank 16 is returned to the water tank 41 through the pipe 22c by the return pump 26, but the treated water tank 16 is above the water tank 41. In that case, it may be returned by natural flow without using a return pump. The treated water may be discharged to the outside of the system of the water treatment device 1 without being returned to the water tank 41.

浸漬型ろ過膜38の洗浄が必要になった場合には、逆洗処理を行うことが好ましい。例えば、循環ポンプ18及び吸引ポンプ20を停止した後、逆洗ポンプ28を稼働させて、処理水槽16内の処理水の少なくとも一部を逆洗水として、逆洗配管30、配管22b、集水配管40を通して、浸漬型ろ過膜38の内部空間(二次側)に供給し、浸漬型ろ過膜38の一次側に透過させる。逆洗を行うタイミングは、特に制限されるものではなく、例えば、予め定めた一定の時間間隔で実施しても良いし、予め定めた一定のろ過水量の間隔で実施しても良い。 When it becomes necessary to wash the immersion type filtration membrane 38, it is preferable to perform a backwash treatment. For example, after stopping the circulation pump 18 and the suction pump 20, the backwash pump 28 is operated so that at least a part of the treated water in the treated water tank 16 is backwashed, and the backwash pipe 30, the pipe 22b, and the water collecting water are collected. It is supplied to the internal space (secondary side) of the immersion type filtration membrane 38 through the pipe 40 and permeates through the primary side of the immersion type filtration membrane 38. The timing of backwashing is not particularly limited, and for example, it may be carried out at predetermined fixed time intervals or at predetermined fixed intervals of the amount of filtered water.

図1に示す水処理装置1において、処理水槽16は必須の構成ではないが、浸漬型ろ過膜38に対する逆洗工程を実施する点等において、処理水槽16を設置することが望ましい。 In the water treatment apparatus 1 shown in FIG. 1, the treatment water tank 16 is not an indispensable configuration, but it is desirable to install the treatment water tank 16 in terms of carrying out a backwashing step on the immersion type filtration membrane 38.

浸漬型膜モジュール12によるろ過は、吸引ポンプ20による吸引式のろ過処理に制限されるものではなく、反応槽10の水位と処理水槽16の水位との水位差によるサイホン作用を利用したサイホン式のろ過処理等でもよい。 Filtration by the immersion type membrane module 12 is not limited to the suction type filtration process by the suction pump 20, but is a siphon type using the siphon action due to the water level difference between the water level of the reaction tank 10 and the water level of the treatment water tank 16. It may be filtered or the like.

浸漬型ろ過膜38の材質は、例えば、アルミナ、シリカ、チタニア、ジルコニア、ムライト、スピネル、又はこれらの混合物等のセラミック製材料、ポリフッ化ビニリデン(PVDF)、ポリ塩化ビニル(PVC)、ポリエーテルサルフォン(PES)、セルロースアセテート(CA)等の有機物製材料等が挙げられる。浸漬型ろ過膜38は、オゾン耐性、強靭性、低い通水差圧によるろ過が可能である点で、セラミック製ろ過膜であることが好ましい。 The material of the immersion type filtration film 38 is, for example, a ceramic material such as alumina, silica, titania, zirconia, mullite, spinel, or a mixture thereof, polyvinylidene fluoride (PVDF), polyvinyl chloride (PVC), polyether monkey. Examples thereof include organic materials such as phone (PES) and cellulose acetate (CA). The immersion type filtration membrane 38 is preferably a ceramic filtration membrane in that it has ozone resistance, toughness, and can be filtered with a low water flow differential pressure.

浸漬型ろ過膜38の形状は、例えば、管状、平膜状、中空糸膜状、スパイラル状等が挙げられる。浸漬型ろ過膜38の種類は、例えば、限外ろ過膜(UF膜)、精密ろ過膜(MF膜)等が挙げられる。そして、浸漬型ろ過膜38の材質、形状、種類の組み合わせについては、浸漬型ろ過膜38のオゾン耐性、強靭性、ろ過フラックスの低下を抑制する点で、セラミック製で、平膜状の精密ろ過膜であることが好ましい。 Examples of the shape of the immersion type filtration membrane 38 include a tubular shape, a flat membrane shape, a hollow fiber membrane shape, and a spiral shape. Examples of the type of the immersion type filtration membrane 38 include an ultrafiltration membrane (UF membrane) and a microfiltration membrane (MF membrane). Regarding the combination of the material, shape, and type of the immersion type filtration membrane 38, it is made of ceramic and has a flat membrane-like precision filtration in that it suppresses the ozone resistance, toughness, and decrease of the filtration flux of the immersion type filtration membrane 38. It is preferably a membrane.

図2は、本実施形態に係る水処理装置の他の一例を示す概略構成図である。図2に示す水処理装置2において、図1に示す水処理装置1と同様の構成については同一の符号を付し、その説明を省略する。図2に示す水処理装置2は、図1に示す水処理装置1の構成に加え、過酸化物分解処理手段としての活性炭処理装置42、配管22d、返送ポンプ44を備える。活性炭処理装置42としては、例えば、活性炭が充填された活性炭充填塔等である。 FIG. 2 is a schematic configuration diagram showing another example of the water treatment apparatus according to the present embodiment. In the water treatment apparatus 2 shown in FIG. 2, the same reference numerals are given to the same configurations as those of the water treatment apparatus 1 shown in FIG. 1, and the description thereof will be omitted. The water treatment device 2 shown in FIG. 2 includes an activated carbon treatment device 42, a pipe 22d, and a return pump 44 as peroxide decomposition treatment means, in addition to the configuration of the water treatment device 1 shown in FIG. The activated carbon treatment device 42 is, for example, an activated carbon packed tower filled with activated carbon.

図2の水処理装置2において、処理水槽16の出口と活性炭処理装置42の入口とが、返送ポンプ26を介して配管22cにより接続されている。また、活性炭処理装置42の出口と水槽41の入口とが、返送ポンプ44を介して配管22dにより接続されている。なお、重力を使った活性炭処理装置42への通水が可能な場合、返送ポンプ26と返送ポンプ44を除くことができる。 In the water treatment device 2 of FIG. 2, the outlet of the treatment water tank 16 and the inlet of the activated carbon treatment device 42 are connected by a pipe 22c via a return pump 26. Further, the outlet of the activated carbon treatment device 42 and the inlet of the water tank 41 are connected by a pipe 22d via a return pump 44. If water can be passed through the activated carbon treatment device 42 using gravity, the return pump 26 and the return pump 44 can be removed.

浸漬型ろ過膜38によりろ過された処理水は、処理水槽16に貯留された後、返送ポンプ26により、配管22cを通して、活性炭処理装置42に供給される。活性炭処理装置42に供給される処理水中には、前述したオゾン処理により発生したハロゲンオキソ酸等の過酸化物が含まれている場合があるが、ハロゲンオキソ酸等の過酸化物は、活性炭処理装置42により分解される(過酸化物分解処理工程)。過酸化物が分解処理された処理水は、返送ポンプ44により、配管22dを通して水槽に返送される(返送工程)。 The treated water filtered by the immersion type filtration membrane 38 is stored in the treated water tank 16 and then supplied to the activated carbon treatment device 42 through the pipe 22c by the return pump 26. The treated water supplied to the activated charcoal treatment apparatus 42 may contain a peroxide such as halogen oxo acid generated by the above-mentioned ozone treatment, but the peroxide such as halogen oxo acid is treated with activated carbon. It is decomposed by the apparatus 42 (peroxide decomposition treatment step). The treated water in which the peroxide has been decomposed is returned to the water tank through the pipe 22d by the return pump 44 (return step).

浸漬型ろ過膜38によりろ過された処理水中の過酸化物の濃度が高くなると、生態等に影響を及ぼすことが懸念されるが、図2に示すように、浸漬型ろ過膜38の後段に活性炭処理装置42を設置することにより、過酸化物が分解されるため、水槽41に返送せずに、系外へ排出しても、生体への影響を低減することが可能となる。また、過酸化物が分解された処理水を水槽41へ返送しても、水生生物への影響を低減することが可能となる。さらには、ランニングコストの削減にも繋がることとなる。 If the concentration of peroxide in the treated water filtered by the immersion type filtration film 38 becomes high, there is a concern that it may affect the ecology, etc., but as shown in FIG. 2, activated carbon is placed after the immersion type filtration film 38. By installing the treatment device 42, the peroxide is decomposed, so that the influence on the living body can be reduced even if the peroxide is discharged to the outside of the system without being returned to the water tank 41. Further, even if the treated water in which the peroxide is decomposed is returned to the water tank 41, the influence on aquatic organisms can be reduced. Furthermore, it will lead to reduction of running cost.

過酸化物分解手段としては、活性炭処理装置42の他に、例えば、Pd担持担体、酸化チタン、白金等の過酸化物分解触媒を充填した充填塔等が挙げられ、コスト等の観点から活性炭処理装置42が好ましい。 Examples of the peroxide decomposition means include a filling tower filled with a peroxide-supporting carrier, a peroxide decomposition catalyst such as titanium oxide and platinum, and the like in addition to the activated carbon treatment apparatus 42, and the activated carbon treatment is performed from the viewpoint of cost and the like. Device 42 is preferred.

本実施形態の水処理装置は、水生生物を飼育する際に用いられる飼育水を処理するために、水族館や養殖場等で使用されるものであるが、特に、内陸型水族館での使用が好適である。また、本実施形態の水処理装置は、水生生物の飼育水の処理のうち、特に、アンモニア態窒素を含む海水の処理に適している。海水には臭化物イオンが通常含まれるため、本実施形態の水処理装置において、浸漬型ろ過膜が浸漬された反応槽内の海水をオゾン処理することで、海水中のアンモニア態窒素を容易に分解することができる。なお、生物処理によりアンモニア態窒素を分解(硝化及び脱窒)しようとする場合、まず、好気性生物処理によりアンモニア態窒素を硝酸にした後、嫌気性生物処理により硝酸を窒素ガスへ還元して水中から窒素を除去するのが通常である。すなわち、生物処理を用いる場合、好気条件の硝化槽と嫌気条件の脱窒槽を必要とするため、広い設置スペースが必要となる。しかし、本実施形態に係る水処理装置では、アンモニア態窒素の分解(硝化及び脱窒)を一つの槽(反応槽10)で行うことができるため、省スペース化が可能となる。 The water treatment device of the present embodiment is used in an aquarium, a farm, or the like for treating the breeding water used for breeding aquatic organisms, and is particularly suitable for use in an inland aquarium. Is. Further, the water treatment apparatus of the present embodiment is particularly suitable for the treatment of seawater containing ammonia nitrogen among the treatments of breeding water for aquatic organisms. Since seawater usually contains bromide ions, the water treatment apparatus of the present embodiment can easily decompose ammonia nitrogen in seawater by ozone-treating the seawater in the reaction vessel in which the immersion type filtration membrane is immersed. can do. When attempting to decompose (nitrify and denitrify) ammonia nitrogen by biological treatment, first, ammonia nitrogen is converted to nitric acid by aerobic biological treatment, and then nitric acid is reduced to nitric acid by anaerobic biological treatment. It is normal to remove nitrogen from the water. That is, when biological treatment is used, a nitrification tank under aerobic conditions and a denitrification tank under anaerobic conditions are required, so that a large installation space is required. However, in the water treatment apparatus according to the present embodiment, decomposition (nitrification and denitrification) of ammonia nitrogen can be performed in one tank (reaction tank 10), so that space can be saved.

1,2 水処理装置、10 反応槽、12 浸漬型膜モジュール、14 オゾン処理装置、16 処理水槽、18 循環ポンプ、20 吸引ポンプ、22a〜22d 配管、24 オゾン排出配管、26,44 返送ポンプ、28 逆洗ポンプ、30 逆洗配管、32 オゾン発生装置、34 オゾン供給配管、36 散気装置、38 浸漬型ろ過膜、40 集水配管、41 水槽、42 活性炭処理装置。 1,2 water treatment equipment, 10 reaction tanks, 12 immersion type membrane module, 14 ozone treatment equipment, 16 treatment water tanks, 18 circulation pumps, 20 suction pumps, 22a to 22d pipes, 24 ozone discharge pipes, 26,44 return pumps, 28 backwash pump, 30 backwash pipe, 32 ozone generator, 34 ozone supply pipe, 36 air diffuser, 38 immersion type filter membrane, 40 water collection pipe, 41 water tank, 42 activated charcoal treatment equipment.

Claims (8)

水生生物の飼育水を処理する水処理装置であって、
前記飼育水が供給される反応槽と、前記反応槽内に浸漬され、前記飼育水をろ過する浸漬型ろ過膜と、前記反応槽内にオゾンを供給して、前記飼育水をオゾン処理するオゾン処理手段と、前記浸漬型ろ過膜によりろ過された前記処理水が貯留される処理水槽と、前記処理水槽内に貯留された前記処理水中に含まれる、前記オゾン処理により発生した過酸化物を分解処理する過酸化物分解処理手段と、前記処理水槽内に貯留された前記処理水を使用して、前記浸漬型ろ過膜を逆洗処理する逆洗処理手段と、を備え
前記浸漬型ろ過膜は、セラミック製ろ過膜であり、
前記反応槽に供給される前記飼育水は、水生生物を飼育する水槽からの飼育水であり、前記過酸化物分解処理手段により過酸化物が分解処理された処理水を前記水槽に返送する返送手段を有することを特徴とする水処理装置。
A water treatment device that treats breeding water for aquatic organisms.
A reaction tank to which the breeding water is supplied, an immersion type filtration membrane that is immersed in the reaction tank and filters the breeding water, and ozone that supplies ozone into the reaction tank to treat the breeding water with ozone. Decomposes the peroxide generated by the ozone treatment contained in the treatment means, the treated water tank in which the treated water filtered by the immersion type filtration membrane is stored, and the treated water stored in the treated water tank. The peroxide decomposition treatment means to be treated and the backwash treatment means for backwashing the immersion type filtration film using the treated water stored in the treated water tank are provided .
The immersion type filtration membrane is a ceramic filtration membrane.
The breeding water supplied to the reaction tank is breeding water from a water tank for breeding aquatic organisms, and the treated water obtained by decomposing the peroxide by the peroxide decomposition treatment means is returned to the water tank. A water treatment apparatus characterized by having means.
前記飼育水は海水であることを特徴とする請求項1に記載の水処理装置。The water treatment apparatus according to claim 1, wherein the breeding water is seawater. 前記飼育水は内陸型水族館の飼育水であることを特徴とする請求項1又は2に記載の水処理装置。The water treatment apparatus according to claim 1 or 2, wherein the breeding water is breeding water of an inland aquarium. 前記過酸化物分解処理手段は、活性炭処理装置であることを特徴とする請求項1〜3のいずれか1項に記載の水処理装置。 The water treatment apparatus according to any one of claims 1 to 3, wherein the peroxide decomposition treatment means is an activated carbon treatment apparatus. 水生生物の飼育水を処理する水処理方法であって、
前記飼育水が供給される反応槽内に浸漬された浸漬型ろ過膜により、前記飼育水をろ過するろ過工程と、
前記反応槽内にオゾンを供給して、前記飼育水をオゾン処理するオゾン処理工程と、
前記ろ過工程によりろ過された処理水を処理水槽に貯留する工程と、
前記処理水槽に貯留された前記処理水中に含まれる、前記オゾン処理により発生した過酸化物を分解処理する過酸化物分解処理工程と、
前記処理水槽内に貯留された前記処理水を使用して、前記浸漬型ろ過膜を逆洗処理する逆洗処理工程と、を備え
前記浸漬型ろ過膜は、セラミック製ろ過膜であり、
前記反応槽に供給される前記飼育水は、水生生物を飼育する水槽からの飼育水であり、前記過酸化物分解処理工程により過酸化物が分解処理された処理水を前記水槽に返送する返送工程を有することを特徴とする水処理方法。
It is a water treatment method that treats the breeding water of aquatic organisms.
A filtration step of filtering the breeding water by an immersion type filtration membrane immersed in the reaction tank to which the breeding water is supplied, and
An ozone treatment step of supplying ozone into the reaction vessel and treating the breeding water with ozone,
A step of storing the treated water filtered by the filtration step in a treated water tank, and a step of storing the treated water in the treated water tank.
A peroxide decomposition treatment step for decomposing the peroxide generated by the ozone treatment contained in the treated water stored in the treated water tank, and
A backwashing treatment step of backwashing the immersion type filtration membrane using the treated water stored in the treated water tank is provided .
The immersion type filtration membrane is a ceramic filtration membrane.
The breeding water supplied to the reaction tank is breeding water from a water tank for breeding aquatic organisms, and the treated water in which the peroxide is decomposed by the peroxide decomposition treatment step is returned to the water tank. A water treatment method characterized by having a step.
前記飼育水は海水であることを特徴とする請求項5に記載の水処理方法。The water treatment method according to claim 5, wherein the breeding water is seawater. 前記飼育水は内陸型水族館の飼育水であることを特徴とする請求項5又は6に記載の水処理方法。The water treatment method according to claim 5 or 6, wherein the breeding water is breeding water of an inland aquarium. 前記過酸化物分解処理工程は、活性炭処理装置により、前記ろ過工程によりろ過された処理水中に含まれる、前記オゾン処理により発生した過酸化物を分解処理することを特徴とする請求項5〜7のいずれか1項に記載の水処理方法。 The peroxide decomposition treatment process, the activated carbon treatment apparatus, according to claim 5-7, wherein the filtration contained in the treated water which has been filtered by step, characterized by decomposing peroxide generated by the ozone treatment The water treatment method according to any one of the above.
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