JP7089859B2 - Water treatment equipment and water treatment method - Google Patents

Water treatment equipment and water treatment method Download PDF

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JP7089859B2
JP7089859B2 JP2017215667A JP2017215667A JP7089859B2 JP 7089859 B2 JP7089859 B2 JP 7089859B2 JP 2017215667 A JP2017215667 A JP 2017215667A JP 2017215667 A JP2017215667 A JP 2017215667A JP 7089859 B2 JP7089859 B2 JP 7089859B2
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圭一郎 福水
響介 山田
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Organo Corp
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Description

本発明は、水生生物を飼育する水槽から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 from an aquarium for breeding aquatic organisms.

水生生物が飼育されている水槽内の飼育水は、ランニングコスト低減等の観点から、飼育水を循環して用いられる場合がある。従来、飼育水を循環利用する場合、飼育水の循環経路に砂ろ過を設置して、飼育水を砂ろ過によりろ過処理して、飼育水中の懸濁物質等を除去することが行われている。 The breeding water in the aquarium in which aquatic organisms are bred may be used by circulating the breeding water from the viewpoint of reducing running costs and the like. Conventionally, when the breeding water is recycled, sand filtration is installed in the circulation route of the breeding water, and the breeding water is filtered by sand filtration to remove suspended solids and the like in the breeding water. ..

例えば、特許文献1には、飼育水をろ過工程を通じて循環浄化する方法であって、ろ過工程は、上部に砂以外の生物付着担体を充填した生物付着担体層と、下部に砂を充填した砂層とを有する複層ろ過層に、飼育水を下降流で通液する方法が開示されている。 For example, Patent Document 1 describes a method of circulating and purifying breeding water through a filtration step, in which the filtration step includes a biological attachment carrier layer in which a biological attachment carrier other than sand is filled in the upper part and a sand layer in which sand is filled in the lower part. Disclosed is a method of passing breeding water in a downward flow through a multi-layer filtration layer having the above.

特開2015-23841号公報JP-A-2015-23841

ところで、飼育水の懸濁物質等を効率的に除去するには、砂ろ過より、ろ過膜を用いた膜ろ過処理が好適である。しかし、膜ろ過処理の場合、飼育水をろ過膜に通液するためのポンプ動力等が影響して、装置の運転に掛かる電力消費量が増大し、ひいてはランニングコストが増加する場合がある。 By the way, in order to efficiently remove suspended solids and the like in breeding water, membrane filtration treatment using a filtration membrane is preferable to sand filtration. However, in the case of membrane filtration treatment, the power consumption of the pump for passing the breeding water through the filtration membrane may affect the power consumption required for operating the device, which may lead to an increase in running cost.

そこで、本発明の目的は、装置の運転に掛かる電力消費量を抑えながら、砂ろ過より飼育水中の懸濁物質を効率的に除去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である。 Therefore, an object of the present invention is to provide a water treatment device and a water treatment method capable of efficiently removing suspended solids in breeding water by sand filtration while suppressing the power consumption required for the operation of the device. Is.

本発明は、水生生物を飼育する水槽からの飼育水を限外ろ過膜又は精密ろ過膜を用いてろ過する膜ろ過手段を有し、前記膜ろ過手段によりろ過した処理水の少なくとも一部を前記水槽に返送する水処理装置であって、前記水槽からの前記飼育水を貯留する貯留槽、前記貯留槽に設置される水位計、前記水槽内の飼育水を前記貯留槽に送液する循環ポンプ、及び前記水位計により計測された前記貯留槽内の水位に基づいて、前記循環ポンプの稼働・停止を制御する制御部を有し、前記膜ろ過手段は、前記水槽より高い位置に設置され、前記貯留槽は、前記膜ろ過手段より高い位置に設置され、前記貯留槽からの前記飼育水を、重力により前記膜ろ過手段に通液する水処理装置である。 The present invention has a membrane filtration means for filtering the breeding water from a water tank for breeding aquatic organisms using an extraneous filtration membrane or a precision filtration membrane, and at least a part of the treated water filtered by the membrane filtration means is described above. A water treatment device that returns to the water tank, a storage tank that stores the breeding water from the water tank, a water level gauge installed in the storage tank, and a circulation pump that sends the breeding water in the water tank to the storage tank. , And a control unit that controls the operation / stop of the circulation pump based on the water level in the storage tank measured by the water level gauge, and the membrane filtration means is installed at a position higher than the water tank. The storage tank is a water treatment device that is installed at a position higher than the membrane filtration means and allows the breeding water from the storage tank to pass through the membrane filtration means by gravity.

また、上記水処理装置において、前記水槽からの前記飼育水を貯留する貯留槽を有し、前記膜ろ過手段は、前記水槽より高い位置に設置され、前記貯留槽は、前記膜ろ過手段より高い位置に設置され、前記貯留槽からの飼育水を、重力により前記膜ろ過手段に通液することが好ましい。 Further, the water treatment apparatus has a storage tank for storing the breeding water from the water tank, the membrane filtration means is installed at a position higher than the water tank, and the storage tank is higher than the membrane filtration means. It is preferable that the breeding water installed at the position is passed through the membrane filtration means by gravity.

また、上記水処理装置において、前記膜ろ過手段を逆洗する逆洗手段を有し、前記貯留槽内の前記飼育水の水位が所定水位以上に達した際に、前記逆洗手段により前記膜ろ過手段を逆洗することが好ましい。 Further, the water treatment apparatus has a backwashing means for backwashing the membrane filtration means, and when the water level of the breeding water in the storage tank reaches a predetermined water level or higher, the backwashing means causes the membrane. It is preferable to backwash the filtration means.

また、上記水処理装置において、前記水槽内の飼育水の一日当たりの循環回数は、6回/日以上であることが好ましい。 Further, in the water treatment apparatus, the number of times of circulation of the breeding water in the aquarium per day is preferably 6 times / day or more.

また、本発明は、限外ろ過膜又は精密ろ過膜を有する膜ろ過手段により、水生生物を飼育する水槽からの飼育水をろ過する膜ろ過工程を有し、前記膜ろ過工程によりろ過した処理水の少なくとも一部を前記水槽に返送する水処理方法であって、前記膜ろ過工程では、前記飼育水を、重力により前記膜ろ過手段に通液する水処理方法である。 Further, the present invention has a membrane filtration step of filtering breeding water from a water tank for breeding aquatic organisms by a membrane filtration means having an ultrafiltration membrane or a precision filtration membrane, and the treated water filtered by the membrane filtration step. It is a water treatment method in which at least a part of the above is returned to the water tank, and in the membrane filtration step, the breeding water is passed through the membrane filtration means by gravity.

また、前記水処理方法において、前記膜ろ過手段を前記水槽より高い位置に設置し、前記水槽からの前記飼育水を貯留する貯留槽を前記膜ろ過手段より高い位置に設置し、前記膜ろ過工程では、前記貯留槽からの飼育水を、重力により前記膜ろ過手段に通液することが好ましい。 Further, in the water treatment method, the membrane filtration means is installed at a position higher than the water tank, and the storage tank for storing the breeding water from the water tank is installed at a position higher than the membrane filtration means. Then, it is preferable to pass the breeding water from the storage tank through the membrane filtration means by gravity.

また、前記水処理方法において、前記貯留槽内の前記飼育水の水位が所定水位以上に達した際に、前記膜ろ過手段を逆洗する逆洗工程を有することが好ましい。 Further, in the water treatment method, it is preferable to have a backwashing step of backwashing the membrane filtration means when the water level of the breeding water in the storage tank reaches a predetermined water level or higher.

また、上記水処理方法において、前記水槽内の飼育水の一日当たりの循環回数を6回/日以上とすることが好ましい。 Further, in the above water treatment method, it is preferable that the number of circulations of the breeding water in the aquarium per day is 6 times / day or more.

本発明によれば、装置の運転に掛かる電力消費量を抑えながら、砂ろ過より飼育水中の懸濁物質を効率的に除去することが可能となる。 According to the present invention, it is possible to efficiently remove suspended solids in breeding water by sand filtration while suppressing the power consumption required for operating the apparatus.

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、貯留槽10、膜ろ過手段としての限外ろ過膜または精密ろ過膜を有する膜ろ過装置12、処理水槽14、循環ポンプ16、配管18a,18b,18c,18d、逆洗ポンプ20、逆洗配管22a,22b、制御部24を備えている。図1に示す貯留槽10には水位計26が設置されている。 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 storage tank 10, a membrane filtration device 12 having an ultrafiltration membrane or a microfiltration membrane as a membrane filtration means, a treatment water tank 14, a circulation pump 16, and pipes 18a, 18b, 18c, 18d. , The backwash pump 20, the backwash pipes 22a and 22b, and the control unit 24 are provided. A water level gauge 26 is installed in the storage tank 10 shown in FIG.

図1に示す水処理装置1では、水生生物が飼育される水槽28より高い位置に処理水槽14及び膜ろ過装置12が設置され、膜ろ過装置12より高い位置に貯留槽10が設置されている。すなわち、膜ろ過装置12と貯留槽10との間には、膜ろ過装置12と貯留槽10との位置の差による水頭差が生じている。なお、図1に示す水処理装置1では、処理水槽14(膜ろ過装置12)と水槽28との間には、処理水槽14(膜ろ過装置12)と水槽28との位置の差による水頭差が生じている。 In the water treatment device 1 shown in FIG. 1, the treatment water tank 14 and the membrane filtration device 12 are installed at a position higher than the water tank 28 in which aquatic organisms are bred, and the storage tank 10 is installed at a position higher than the membrane filtration device 12. .. That is, a head difference occurs between the membrane filtration device 12 and the storage tank 10 due to the difference in position between the membrane filtration device 12 and the storage tank 10. In the water treatment device 1 shown in FIG. 1, there is a head difference between the treated water tank 14 (film filtration device 12) and the water tank 28 due to the difference in position between the treated water tank 14 (film filtration device 12) and the water tank 28. Has occurred.

図1の水処理装置1において、水槽28の出口と貯留槽10の入口とが循環ポンプ16を介して配管18aにより接続されている。また、貯留槽10の出口と膜ろ過装置12の一次側とが配管18bにより接続され、膜ろ過装置12の二次側と処理水槽14の入口とが配管18cにより接続されている。また、処理水槽14の出口と水槽28の入口とが配管18dにより接続されている。また、処理水槽14の逆洗用出口と膜ろ過装置12の2次側とは逆洗ポンプ20を介して逆洗配管22aにより接続され、膜ろ過装置12の一次側には逆洗配管22bが接続されている。 In the water treatment device 1 of FIG. 1, the outlet of the water tank 28 and the inlet of the storage tank 10 are connected by a pipe 18a via a circulation pump 16. Further, the outlet of the storage tank 10 and the primary side of the membrane filtration device 12 are connected by a pipe 18b, and the secondary side of the membrane filtration device 12 and the inlet of the treatment water tank 14 are connected by a pipe 18c. Further, the outlet of the treatment water tank 14 and the inlet of the water tank 28 are connected by a pipe 18d. Further, the backwash outlet of the treatment water tank 14 and the secondary side of the membrane filtration device 12 are connected by the backwash pipe 22a via the backwash pump 20, and the backwash pipe 22b is connected to the primary side of the membrane filtration device 12. It is connected.

制御部24は、水位計26及び各ポンプと電気的に接続されている。制御部24は、貯留槽10の水位計26により計測された水位に基づいて、各ポンプの稼働・停止を制御する機能を有する。 The control unit 24 is electrically connected to the water level gauge 26 and each pump. The control unit 24 has a function of controlling the operation / stop of each pump based on the water level measured by the water level meter 26 of the storage tank 10.

本実施形態に係る水処理装置1の動作について説明する。 The operation of the water treatment apparatus 1 according to the present embodiment will be described.

水槽28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、懸濁物質等が含まれる。 In the aquarium 28, 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. Breeding water usually contains suspended solids and the like with the breeding of aquatic organisms.

水槽28内の飼育水は、循環ポンプ16により配管18aを通して貯留槽10に貯留される。貯留槽10内の飼育水は、重力(水頭差)により、配管18bを通り、膜ろ過装置12に通液され、飼育水中の懸濁物質等が限外ろ過膜や精密ろ過膜によりろ過される(膜ろ過工程)。懸濁物質等がろ過された処理水は、配管18cを通して処理水槽14に貯留される。また、処理水槽14内の処理水の少なくとも一部は、配管18dを通して水槽28に返送され、水槽28内の飼育水として循環利用される。図1に示す水処理装置1では、膜ろ過装置12から処理水槽14、処理水槽14から水槽28への処理水の供給も、水頭差により行われている。 The breeding water in the water tank 28 is stored in the storage tank 10 through the pipe 18a by the circulation pump 16. The breeding water in the storage tank 10 passes through the pipe 18b and is passed through the membrane filtration device 12 by gravity (water head difference), and suspended substances and the like in the breeding water are filtered by an ultrafiltration membrane or a microfiltration membrane. (Membrane filtration process). The treated water from which suspended solids and the like have been filtered is stored in the treated water tank 14 through the pipe 18c. Further, at least a part of the treated water in the treated water tank 14 is returned to the water tank 28 through the pipe 18d and recycled as breeding water in the water tank 28. In the water treatment device 1 shown in FIG. 1, the treated water is also supplied from the membrane filtration device 12 to the treated water tank 14 and from the treated water tank 14 to the water tank 28 due to the head difference.

このように、図1に示す水処理装置1では、水槽28からの飼育水を限外ろ過膜や精密ろ過膜を有する膜ろ過装置12により、水槽28からの飼育水をろ過しているため、砂ろ過によるろ過と比べて、飼育水中の懸濁物質等を効率的に除去することが可能となる。 As described above, in the water treatment device 1 shown in FIG. 1, the breeding water from the water tank 28 is filtered by the membrane filtration device 12 having an ultrafiltration membrane or a microfiltration membrane. Compared with filtration by sand filtration, it is possible to efficiently remove suspended substances and the like in breeding water.

また、図1に示す水処理装置1のように、膜ろ過装置12への飼育水の通液を重力(水頭差)により行うことで、膜ろ過装置12への飼育水の通液を重力(水頭差)を利用せずに行った場合と比較して、以下に例示するように、循環ポンプ16の電力消費量が削減される。 Further, as in the water treatment device 1 shown in FIG. 1, the breeding water is passed through the membrane filtering device 12 by gravity (head difference), so that the breeding water is passed through the membrane filtering device 12 by gravity (difference). As illustrated below, the power consumption of the circulation pump 16 is reduced as compared with the case where the water head difference is not used.

水槽28からの飼育水を、重力(水頭差)を利用せずに、限外ろ過膜や精密ろ過膜を有する膜ろ過装置に通液する場合、飼育水が限外ろ過膜又は精密ろ過膜を通過する分のポンプ動力が必要となる。例えば、10m水槽に対し、循環回数を6回/日とした時、重力を利用しない場合の循環ポンプの電力消費量は、以下の通りとなる。 When the breeding water from the water tank 28 is passed through a membrane filtration device having an ultrafiltration membrane or a microfiltration membrane without using gravity (water head difference), the breeding water uses the ultrafiltration membrane or the microfiltration membrane. The pump power required to pass through is required. For example, when the number of circulations is 6 times / day for a 10 m 3 water tank, the power consumption of the circulation pump when gravity is not used is as follows.

<重力利用しない場合>
限外ろ過の圧力損失を0.2MPa(閉塞時考慮)、循環流量を2.5m/h(=6回/日)、配管による圧力損失を0.1MPa、必要ポンプ能力として流量を2.5m/h及び揚程を30m(0.3MPa相当)とすると、循環ポンプ(例えば、グルンドフォス製CRN1-8)の電力消費量は、0.75kWである。さらに、循環ポンプの稼働時間を24(h/日)、365(日/年)とすると、0.75(kW)×24(h/日)×365(日/年)=6.6MWh/年となる。
<When not using gravity>
The pressure loss of ultrafiltration is 0.2 MPa (considering when blocked), the circulation flow rate is 2.5 m 3 / h (= 6 times / day), the pressure loss due to piping is 0.1 MPa, and the flow rate is 2. Assuming 5 m 3 / h and a lift of 30 m (corresponding to 0.3 MPa), the power consumption of the circulation pump (for example, CRN1-8 manufactured by Grundfoss) is 0.75 kW. Further, assuming that the operating time of the circulation pump is 24 (h / day) and 365 (day / year), 0.75 (kW) x 24 (h / day) x 365 (day / year) = 6.6 MWh / year. Will be.

一方、本実施形態のように、水槽28からの飼育水を、重力(水頭差)により限外ろ過膜や精密ろ過膜を有する膜ろ過装置12に通液する場合、循環ポンプ16の動力は、所定の水頭差が生じるまで、飼育水を引き上げる分のポンプ動力で足りる。例えば、前述と同様に、10m水槽に対し、循環回数を6回/日とした時、重力を利用する場合の循環ポンプの電力消費量は、以下の通りとなる。 On the other hand, when the breeding water from the water tank 28 is passed through the membrane filtration device 12 having an ultrafiltration membrane or a microfiltration membrane by gravity (head difference) as in the present embodiment, the power of the circulation pump 16 is Pump power is sufficient to pull up the breeding water until a given head difference occurs. For example, as described above, when the number of circulations is 6 times / day for a 10 m 3 water tank, the power consumption of the circulation pump when gravity is used is as follows.

<重力利用する場合>
循環流量を2.5m/h(=6回/日)、配管による圧力損失を0.1MPa、限外ろ過の圧力損失を水頭差にて充当し、必要ポンプ能力として流量を2.5m/h及び揚程10m(0.1MPa相当)とすると、循環ポンプ(例えば、グルンドフォス製CRN1-8)の電力消費量は、0.55kWである。さらに、循環ポンプの稼働時間を24(h/日)、365(日/年)とすると、0.55(kW)×24(h/日)×365(日/年)=4.8MWh/年となる。
<When using gravity>
The circulation flow rate is 2.5 m 3 / h (= 6 times / day), the pressure loss due to piping is 0.1 MPa, the pressure loss of ultrafiltration is applied by the head difference, and the flow rate is 2.5 m 3 as the required pump capacity. Assuming / h and a lift of 10 m (corresponding to 0.1 MPa), the power consumption of the circulation pump (for example, CRN1-8 manufactured by Grundfoss) is 0.55 kW. Further, assuming that the operating time of the circulation pump is 24 (h / day) and 365 (day / year), 0.55 (kW) x 24 (h / day) x 365 (day / year) = 4.8 MWh / year. Will be.

このように、膜ろ過装置12への飼育水の通液を重力(水頭差)により通液することで、循環ポンプの電力消費量が削減される。これにより、装置の運転に掛かる電力消費量が抑えられ、ひいてはランニングコストの増大を抑えることが可能となる。膜ろ過装置12へ飼育水を通液する際の水頭差(図1で言えば、貯留槽10と膜ろ過装置12との位置の差)は、膜ろ過装置12に用いられる限外ろ過膜や精密ろ過膜の性能等にもよるが、膜の圧力損失を考慮して、例えば、1m~30mの範囲であることが好ましく、5m~20mの範囲であることが好ましい。 In this way, the power consumption of the circulation pump is reduced by passing the breeding water through the membrane filtration device 12 by gravity (head difference). As a result, the power consumption required for operating the device can be suppressed, and eventually the increase in running cost can be suppressed. The water head difference (difference in position between the storage tank 10 and the membrane filtration device 12 in FIG. 1) when the breeding water is passed through the membrane filtration device 12 is the ultrafiltration membrane used in the membrane filtration device 12. Although it depends on the performance of the microfiltration membrane and the like, in consideration of the pressure loss of the membrane, for example, it is preferably in the range of 1 m to 30 m, and preferably in the range of 5 m to 20 m.

また、図1に示す水処理装置1では、膜ろ過装置12からの処理水を重力(水頭差)により水槽28へ返送しているので、飼育水の循環に必要な循環ポンプ16の電力消費量はさらに削減される。 Further, in the water treatment device 1 shown in FIG. 1, since the treated water from the membrane filtration device 12 is returned to the water tank 28 by gravity (head difference), the power consumption of the circulation pump 16 required for circulation of the breeding water is consumed. Will be further reduced.

ところで、図1に示す水処理装置1において、膜ろ過工程を継続すると、飼育水中の懸濁物質等が限外ろ過膜や精密ろ過膜の膜面に堆積して、ろ過膜の細孔が閉塞するファウリングが引き起こされる場合があるので、逆洗工程を実施することが好ましい。例えば、循環ポンプ16を停止した後、逆洗ポンプ20を稼働させて、処理水槽14内の処理水の少なくとも一部を逆洗水として、逆洗配管22aを通して膜ろ過装置12の2次側から1次側に通液させて、ろ過膜を洗浄する(逆洗工程)。そして、膜ろ過装置12の一次側の逆洗排水を逆洗配管22bから排出する。 By the way, in the water treatment apparatus 1 shown in FIG. 1, when the membrane filtration step is continued, suspended substances and the like in the breeding water are deposited on the membrane surface of the ultrafiltration membrane and the microfiltration membrane, and the pores of the filtration membrane are closed. It is preferable to carry out a backwashing step as it may cause fouling. For example, after stopping the circulation pump 16, the backwash pump 20 is operated to use at least a part of the treated water in the treated water tank 14 as backwash water, and the backwash pipe 22a is passed through the secondary side of the membrane filtration device 12. The filtration membrane is washed by passing the liquid through the primary side (backwashing step). Then, the backwash drainage on the primary side of the membrane filtration device 12 is discharged from the backwash pipe 22b.

通常、懸濁物質等が限外ろ過膜や精密ろ過膜の膜面に堆積していくと、ろ過膜を通過する飼育水量が減少するため、貯留槽10内の飼育水の水位が上昇する。したがって、逆洗工程は、貯留槽10内の飼育水の水位が所定水位以上に達した際に実施することが望ましい。図1に示す水処理装置1では、例えば、貯留槽10に設置された水位計26により計測された水位データが制御部24に送信され、制御部24により、送信された水位データと予め設定した所定値とが比較される。そして、水位データが所定値以上である場合に、制御部24により、各ポンプの稼働・停止が制御され、前述した逆洗工程が実施される。なお、所定値は適宜設定されればよい。 Normally, when a suspended substance or the like is deposited on the membrane surface of an ultrafiltration membrane or a microfiltration membrane, the amount of breeding water passing through the filtration membrane decreases, so that the water level of the breeding water in the storage tank 10 rises. Therefore, it is desirable to carry out the backwashing step when the water level of the breeding water in the storage tank 10 reaches a predetermined water level or higher. In the water treatment apparatus 1 shown in FIG. 1, for example, the water level data measured by the water level gauge 26 installed in the storage tank 10 is transmitted to the control unit 24, and is preset with the transmitted water level data by the control unit 24. The predetermined value is compared. Then, when the water level data is equal to or higher than a predetermined value, the control unit 24 controls the operation / stop of each pump, and the backwashing step described above is carried out. The predetermined value may be set as appropriate.

また、逆洗工程は、所定時間毎に行ってもよい。すなわち、膜ろ過工程を所定時間行った後に、逆洗工程を所定時間行うというサイクルを繰り返してもよい。また、このサイクルの膜ろ過工程中に、貯留槽10内の飼育水の水位が所定水位以上に達した際には、逆洗工程を実施することが好ましい。 Further, the backwashing step may be performed at predetermined time intervals. That is, the cycle of performing the membrane filtration step for a predetermined time and then performing the backwashing step for a predetermined time may be repeated. Further, when the water level of the breeding water in the storage tank 10 reaches a predetermined water level or higher during the membrane filtration step of this cycle, it is preferable to carry out the backwashing step.

水槽28内の飼育水の一日当たりの循環回数は、6回/日以上であることが好ましく、6回/日~24回/日であることがより好ましい。水槽28内の飼育水の循環回数とは、1日当たりに、水槽28内の飼育水が循環経路(配管18a~d)を通る回数であり、以下の式により表される。
循環回数(回/日)=24h/日×循環流量(m/h)÷水槽容積(m
The number of times of circulation of the breeding water in the aquarium 28 per day is preferably 6 times / day or more, and more preferably 6 times / day to 24 times / day. The number of times the breeding water in the water tank 28 is circulated is the number of times that the breeding water in the water tank 28 passes through the circulation route (pipes 18a to 18d) per day, and is expressed by the following formula.
Number of circulations (times / day) = 24h / day x circulation flow rate (m 3 / h) ÷ water tank volume (m 3 )

水槽28内の飼育水の一日当たりの循環回数を6回/日以上とすることで、飼育水中の懸濁物質等を効率的に除去することが可能であり、水槽28内の飼育水を清澄な状態に維持することが容易となる。一般的に、懸濁物質の除去には砂ろ過装置が用いられ、清澄な状態を維持するためには循環回数を24回以上とする必要があるが、本願では、砂ろ過装置よりもろ過精度が高い膜ろ過装置であるので、従来の砂ろ過装置よりも少ない循環回数で清澄な状態を維持することが可能となる。さらに、膜ろ過装置12への飼育水の通液を重力(水頭差)により行う図1に示す水処理装置1では、水槽28内の飼育水の一日当たりの循環回数を6回/日以上としても、循環ポンプ16の電力消費量が抑えられる。 By setting the number of circulations of the breeding water in the aquarium 28 per day to 6 times / day or more, it is possible to efficiently remove suspended solids and the like in the breeding water, and the breeding water in the aquarium 28 is clarified. It becomes easy to maintain the state. Generally, a sand filtration device is used to remove suspended substances, and in order to maintain a clear state, the number of circulations must be 24 or more, but in the present application, the filtration accuracy is higher than that of the sand filtration device. Since it is a membrane filtration device with a high value, it is possible to maintain a clear state with a smaller number of circulations than a conventional sand filtration device. Further, in the water treatment device 1 shown in FIG. 1 in which the breeding water is passed through the membrane filtration device 12 by gravity (head difference), the number of circulations of the breeding water in the water tank 28 per day is set to 6 times / day or more. However, the power consumption of the circulation pump 16 can be suppressed.

図1に示す水処理装置1では、膜ろ過装置12を水槽28より高い位置に設置し、貯留槽10を膜ろ過装置12より高い位置に設置する設置形態としたが、膜ろ過装置12への飼育水の通液を重力(水頭差)により通液することが可能な設置形態であれば、上記に制限されるものではない。図での説明は省略するが、例えば、水生生物が飼育される水槽28より低い位置に貯留槽10が設置され、貯留槽10より低い位置に膜ろ過装置12及び処理水槽14が設置される設置形態でもよい。このような構成によっても、膜ろ過装置12と貯留槽10との間には、膜ろ過装置12と貯留槽10との位置の差による水頭差が生じるため、貯留槽10内の飼育水は、重力(水頭差)により、膜ろ過装置12に通液され、飼育水中の懸濁物質等が限外ろ過膜や精密ろ過膜によりろ過される(膜ろ過工程)。なお、懸濁物質等が除去された処理水は、水槽28より低い位置にあるため、循環ポンプ16により水槽28に返送する必要がある。 In the water treatment device 1 shown in FIG. 1, the membrane filtration device 12 is installed at a position higher than the water tank 28, and the storage tank 10 is installed at a position higher than the membrane filtration device 12. It is not limited to the above as long as it is an installation form in which the liquid of breeding water can be passed by gravity (water head difference). Although the description in the figure is omitted, for example, the storage tank 10 is installed at a position lower than the water tank 28 in which aquatic organisms are bred, and the membrane filtration device 12 and the treatment water tank 14 are installed at a position lower than the storage tank 10. It may be in the form. Even with such a configuration, a water head difference occurs between the membrane filtration device 12 and the storage tank 10 due to the difference in the positions of the membrane filtration device 12 and the storage tank 10, so that the breeding water in the storage tank 10 is used. Due to gravity (water head difference), the liquid is passed through the membrane filtration device 12, and suspended substances and the like in the breeding water are filtered by an ultrafiltration membrane or a microfiltration membrane (membrane filtration step). Since the treated water from which the suspended solids and the like have been removed is located at a position lower than the water tank 28, it is necessary to return it to the water tank 28 by the circulation pump 16.

貯留槽10及び膜ろ過装置12の設置形態としては、膜ろ過装置12を水槽28より高い位置に設置し、貯留槽10を膜ろ過装置12より高い位置に設置する設置形態の方が、貯留槽10を水槽28より低い位置に設置し、膜ろ過装置12を貯留槽10より低い位置に設置する設置形態より、建築躯体への過重負荷軽減の点で好ましい。近年、水族館等が商業施設などのテナントとして運営されることがあり、水処理設備が高層階へ分配される場合がある。貯留槽10を水槽28より低い位置に設置し、膜ろ過装置12を貯留槽10より低い位置に設置する設置形態では、飼育水槽などの容積が大きい水槽28を、容量の小さい貯留槽10や膜ろ過装置12より高層階に設置せざるを得ない場合がある。この場合には、建築躯体への過剰負荷を考慮し、設計強度を強化する必要があり、建築躯体へのコストアップが生じる虞がある。 As for the installation form of the storage tank 10 and the membrane filtration device 12, the installation form in which the membrane filtration device 12 is installed at a position higher than the water tank 28 and the storage tank 10 is installed at a position higher than the membrane filtration device 12 is the storage tank. It is preferable to install the membrane filtration device 12 at a position lower than the water tank 28 and the membrane filtration device 12 at a position lower than the storage tank 10 in terms of reducing the overload on the building frame. In recent years, aquariums and the like may be operated as tenants such as commercial facilities, and water treatment facilities may be distributed to higher floors. In the installation mode in which the storage tank 10 is installed at a position lower than the water tank 28 and the membrane filtration device 12 is installed at a position lower than the storage tank 10, the water tank 28 having a large volume such as a breeding water tank is replaced with a storage tank 10 or a membrane having a small capacity. It may have to be installed on a higher floor than the filtration device 12. In this case, it is necessary to strengthen the design strength in consideration of the excessive load on the building frame, and there is a possibility that the cost to the building frame will increase.

本実施形態の水処理装置1において、貯留槽10は必須の構成ではないが、貯留槽10内の飼育水の水位から、膜ろ過装置12に対する逆洗工程の実施タイミングを決定する点等において、貯留槽10を設置することが望ましい。なお、貯留槽10が無くても、配管18aにより水頭差が形成される位置まで飼育水を引き上げれば、重力(水頭差)により膜ろ過装置12に飼育水を通液することは可能である。 In the water treatment device 1 of the present embodiment, the storage tank 10 is not an indispensable configuration, but the timing of carrying out the backwashing step for the membrane filtration device 12 is determined from the water level of the breeding water in the storage tank 10 and the like. It is desirable to install a storage tank 10. Even if there is no storage tank 10, if the breeding water is pulled up to a position where a head difference is formed by the pipe 18a, the breeding water can be passed through the membrane filtration device 12 by gravity (head difference). ..

本実施形態の水処理装置1において、処理水槽14は必須の構成ではないが、膜ろ過装置12に対する逆洗工程を実施する点等において、処理水槽14を設置することが望ましい。 Although the treated water tank 14 is not an essential configuration in the water treatment device 1 of the present embodiment, it is desirable to install the treated water tank 14 in terms of carrying out a backwashing step for the membrane filtration device 12.

膜ろ過装置12としては、限外ろ過膜(UF膜)または精密ろ過膜(MF膜)を有するものであればよく、特に制限はない。 The membrane filtration device 12 may be any as long as it has an ultrafiltration membrane (UF membrane) or a microfiltration membrane (MF membrane), and is not particularly limited.

本実施形態に係る水処理装置1は、オゾン発生装置を備えるオゾン処理装置や活性炭処理装置を循環経路中(配管18a~18d)に設置してもよい。水槽28内の飼育水には、水生生物の飼育に伴い、懸濁物質以外にも有機物やアンモニア態窒素等が含まれる場合があるが、上記オゾン処理装置や活性炭処理装置等を設置することで、有機物やアンモニア態窒素等を効率的に処理することができるため、より清澄な飼育水を水槽28に返送することが可能となる。 In the water treatment device 1 according to the present embodiment, an ozone treatment device or an activated carbon treatment device including an ozone generator may be installed in the circulation path (pipes 18a to 18d). The breeding water in the water tank 28 may contain organic substances, ammonia nitrogen, etc. in addition to suspended solids due to the breeding of aquatic organisms. Since organic matter, ammonium nitrogen, and the like can be efficiently treated, clearer breeding water can be returned to the water tank 28.

本実施形態の水処理装置1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。内陸型水族館は、複数階からなる建物である場合が多いため、貯留槽10や膜ろ過装置12を各階に分散させて配置すれば、膜ろ過装置12へ飼育水を通液するための水頭差を容易に形成することができる。なお、貯留槽10や膜ろ過装置12を各階に分散させて配置することができない場合には、例えば、所定の高さを有する台座等に貯留槽10を載置して、膜ろ過装置12へ飼育水を通液するための水頭差を確保すればよい。 The water treatment device 1 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 used in an inland aquarium. Suitable. Since inland aquariums are often buildings consisting of multiple floors, if the storage tank 10 and the membrane filtration device 12 are distributed and arranged on each floor, the head difference for passing breeding water to the membrane filtration device 12 Can be easily formed. If the storage tank 10 and the membrane filtration device 12 cannot be distributed and arranged on each floor, for example, the storage tank 10 is placed on a pedestal or the like having a predetermined height and placed on the membrane filtration device 12. It suffices to secure a head difference for passing the breeding water.

1 水処理装置、10 貯留槽、12 膜ろ過装置、14 処理水槽、16 循環ポンプ、18a~18d 配管、20 逆洗ポンプ、22a,22b 逆洗配管、24 制御部、26 水位計、28 水槽。
1 water treatment device, 10 storage tank, 12 membrane filtration device, 14 treatment water tank, 16 circulation pump, 18a-18d piping, 20 backwash pump, 22a, 22b backwash piping, 24 control unit, 26 water level gauge, 28 water tank.

Claims (7)

水生生物を飼育する水槽からの飼育水を限外ろ過膜又は精密ろ過膜を用いてろ過する膜ろ過手段を有し、前記膜ろ過手段によりろ過した処理水の少なくとも一部を前記水槽に返送する水処理装置であって、
前記水槽からの前記飼育水を貯留する貯留槽、前記貯留槽に設置される水位計、前記水槽内の飼育水を前記貯留槽に送液する循環ポンプ、及び前記水位計により計測された前記貯留槽内の水位に基づいて、前記循環ポンプの稼働・停止を制御する制御部を有し、
前記膜ろ過手段は、前記水槽より高い位置に設置され、前記貯留槽は、前記膜ろ過手段より高い位置に設置され、前記貯留槽からの前記飼育水を、重力により前記膜ろ過手段に通液することを特徴とする水処理装置。
It has a membrane filtration means that filters the breeding water from the aquatic tank that breeds aquatic organisms using an ultrafiltration membrane or a microfiltration membrane, and returns at least a part of the treated water filtered by the membrane filtration means to the tank. It is a water treatment device
A storage tank for storing the breeding water from the water tank, a water level gauge installed in the storage tank, a circulation pump for sending the breeding water in the water tank to the storage tank, and the storage measured by the water level gauge. It has a control unit that controls the operation / stop of the circulation pump based on the water level in the tank.
The membrane filtration means is installed at a position higher than the water tank, the storage tank is installed at a position higher than the membrane filtration means, and the breeding water from the storage tank is passed through the membrane filtration means by gravity. A water treatment device characterized by
前記膜ろ過手段を逆洗する逆洗手段を有し、
前記貯留槽内の前記飼育水の水位が所定水位以上に達した際に、前記逆洗手段により前記膜ろ過手段を逆洗することを特徴とする請求項に記載の水処理装置。
It has a backwashing means for backwashing the membrane filtration means.
The water treatment apparatus according to claim 1 , wherein when the water level of the breeding water in the storage tank reaches a predetermined water level or higher, the membrane filtration means is backwashed by the backwashing means.
前記水槽内の飼育水の一日当たりの循環回数は、6回/日以上であることを特徴とする請求項1~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 2 , wherein the number of times of circulation of the breeding water in the aquarium per day is 6 times / day or more. 限外ろ過膜又は精密ろ過膜を有する膜ろ過手段により、水生生物を飼育する水槽からの飼育水をろ過する膜ろ過工程を有し、前記膜ろ過工程によりろ過した処理水の少なくとも一部を前記水槽に返送する水処理方法であって、
前記膜ろ過工程では、前記飼育水を、重力により前記膜ろ過手段に通液することを特徴とする水処理方法。
It has a membrane filtration step of filtering the breeding water from a water tank for breeding aquatic organisms by a membrane filtration means having an ultrafiltration membrane or a precision filtration membrane, and at least a part of the treated water filtered by the membrane filtration step is described above. It is a water treatment method that returns to the water tank.
In the membrane filtration step, a water treatment method comprising passing the breeding water through the membrane filtration means by gravity.
前記膜ろ過手段を前記水槽より高い位置に設置し、前記水槽からの前記飼育水を貯留する貯留槽を前記膜ろ過手段より高い位置に設置し、
前記膜ろ過工程では、前記貯留槽からの飼育水を、重力により前記膜ろ過手段に通液することを特徴とする請求項4に記載の水処理方法。
The membrane filtration means is installed at a position higher than the aquarium, and the storage tank for storing the breeding water from the aquarium is installed at a position higher than the membrane filtration means.
The water treatment method according to claim 4, wherein in the membrane filtration step, the breeding water from the storage tank is passed through the membrane filtration means by gravity.
前記貯留槽内の前記飼育水の水位が所定水位以上に達した際に、前記膜ろ過手段を逆洗する逆洗工程を有することを特徴とする請求に記載の水処理方法。 The water treatment method according to claim 5 , further comprising a backwashing step of backwashing the membrane filtration means when the water level of the breeding water in the storage tank reaches a predetermined water level or higher. 前記水槽内の飼育水の一日当たりの循環回数を6回/日以上とすることを特徴とする請求項5~のいずれか1項に記載の水処理方法。 The water treatment method according to any one of claims 5 to 6 , wherein the number of times of circulation of the breeding water in the aquarium per day is 6 times / day or more.
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