JP3660421B2 - Reservoir purification equipment - Google Patents

Reservoir purification equipment Download PDF

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Publication number
JP3660421B2
JP3660421B2 JP09769196A JP9769196A JP3660421B2 JP 3660421 B2 JP3660421 B2 JP 3660421B2 JP 09769196 A JP09769196 A JP 09769196A JP 9769196 A JP9769196 A JP 9769196A JP 3660421 B2 JP3660421 B2 JP 3660421B2
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Japan
Prior art keywords
water
purification
ozone treatment
ozone
stored
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JP09769196A
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Japanese (ja)
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JPH09253670A (en
Inventor
孝 河野
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Sumitomo Precision Products Co Ltd
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Sumitomo Precision Products Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明はプール、浴場、池等に貯溜されている水の浄化に使用される貯溜水浄化設備、特にオゾン処理を組み合わせた貯留水浄化設備に関し、更に詳しくは震災、渇水等の非常時にその貯溜水を飲料水に浄化できる機能を有するオゾン処理装置付きの貯溜水浄化設備に関する。
【0002】
【従来の技術】
プール、浴場、池等に貯溜されている水を浄化する浄化設備としては、濾過と消毒剤注入とを組み合わせた循環式が一般的であるが、最近では更に、浄化効果の向上を目的としてオゾン処理を組み合わせたものも使用されている。オゾン処理の特徴は、オゾンの強力な酸化殺菌作用により濁質および汚染物質を従来より大幅に減少させることができ、更には耐塩素性の微生物を殺菌、不活性化することも可能である。オゾン処理を組み合わせた従来の貯溜水浄化設備を図1に示す。
【0003】
プール、浴場、池等の貯水部1に貯溜された水は、主循環系統2により貯水部1の底部から取出され貯水部1の側部から貯水部1に戻される。主循環系統2には、ヘアキャッチャ3、循環ポンプ4および濾過器5が設けられている。これにより、貯水部1から取出された貯溜水は、ヘアキャッチャ3により大型の固形物質が除去され、循環ポンプ4で加圧された後、濾過器5で微細な固形物質が除去され、最後に塩素剤等で消毒されて貯水部1に戻される。
【0004】
このとき、濾過器5の上流側または下流側から貯溜水の一部が取出されてオゾン処理装置6に送られる。オゾン処理装置6は、オゾン発生器で発生したオゾンガスをエジェクタで貯溜水に注入し、その貯溜水をオゾン処理した後、ポンプ4の上流側に戻す。オゾン処理により溶解性の汚染物質の分解および耐塩素性の微生物の殺菌、不活性化が行われると共に、コロイド物質が凝集されて濾過器5に捕捉されやすい形態となる。
【0005】
【発明が解決しようとする課題】
このようなオゾン処理を組み合わせた従来の貯溜水浄化設備は、オゾン処理を組み合わせないものよりも浄化能力が格段に高いが、震災、渇水等の非常時に浄化水を飲料水として使用することはできない。なぜなら、プール、浴場、池等の循環浄化では、消毒のために塩素等の薬剤が注入され、プールではその濃度が厚生省基準で0.4mg/リットル以上に維持されるが、消毒副生成物の残留に関心がもたれていないため、消毒副生成物の濃度が水道水の水質基準値を超える場合が少なくないからである。
【0006】
このようなことから、貯溜水から飲料水を得ようとすると、非常用の専用浄化装置が必要になる。しかし、非常用の専用浄化装置は大型で高価である。また、浄化設備とメーカが異なるのが通例であるので、点検コストが嵩むという問題もある。
【0007】
本発明の目的は、震災、渇水等の非常時に貯溜水から飲料水を得ることができ、しかも浄化設備の大型化、コスト増大およびメンテナンス性の悪化を可及的に回避できるオゾン処理装置付きの貯留水浄化設備を提供することにある。
【0008】
【課題を解決するための手段】
本発明の貯留水浄化設備は、プール、浴場、池等の貯水部に貯溜されている水を循環させながら固形物を除去して浄化し、更に消毒を行う貯留水浄化設備であって、前記貯水部に貯留されている水を当該貯水部から取り出して当該貯水部へ戻す主循環系統と、前記主循環系統より貯溜水を取入れオゾン処理して再び主循環系統に戻すオゾン処理装置とを具備しており、前記オゾン処理装置は前記オゾン処理を行う処理装置本体と、該処理装置本体に付設された浄化ユニットとからなり、該浄化ユニットは、前記処理装置本体内のオゾン処理部の下流側に、通常時に閉止されるバルブを介して接続されており、地震、渇水等の非常時に前記バルブが開放されることによりオゾン処理後の貯溜水を取入れて飲料水に浄化する構成である
【0009】
本発明の貯留水浄化設備を用いた場合、非常時以外のとき、すなわち通常時は、浄化設備において循環浄化される貯溜水をオゾン処理装置の処理装置本体に循環させることにより、オゾン処理を組み合わせた通常の循環浄化が行われる。非常時のときは処理装置本体でオゾン処理された貯溜水を浄化ユニットに送る。オゾン処理後の貯溜水、すなわちオゾン処理水は、オゾンの強力な殺菌作用で耐塩素性微生物が殺菌、不活性され、更に消毒副生成物も分解低減されている。そのため浄化ユニットでは、オゾン処理水中に含まれる溶存オゾンを分解し、且つオゾン処理水中に残存する消毒副生成物を低減除去する程度で、飲料水を得ることができる。かくして、貯溜水から飲料水が得られ、且つ浄化ユニットは簡易で安価なものとなる。
【0010】
溶存オゾンの分解および残存消毒副生成物の低減除去には、活性炭処理または紫外線処理を用いることができる。濁質の多い場合はメンブラフィルタ、UF膜、MF膜等の膜フィルタを組み合わせて、濁質の低減を図るのが望ましい。
【0011】
オゾン処理装置の処理装置本体においては、エジェクタを用いて貯溜水にオゾンガスを注入するのがよい。一般にオゾンガスの注入処理では、水量が一定を保つのが好ましい。この点から、貯溜水の取入れ部と戻し部との間をバルブ付きのバイパス管により直結し、該パイパス管に備わるバルブの開放により前記処理装置本体内の戻し部からオゾン処理部へ貯留水を送るように構成するのが望ましい。これにより、飲料水の需要量(供給水量)の増減に関係なく、バイパス管を通してオゾンガス処理部に所定水量の貯溜水を送ることができる。
【0012】
ここで取入れ部を主循環系統における浄化部の下流側に接続し、戻し部を前記浄化部の上流側に接続しておくと、前記浄化部が停止状態の場合も、浄化部上流側の戻し部からバイパス管を通して貯溜水をオゾン処理部に送り、更に浄化ユニットに送り続けることができる。
【0013】
【発明の実施の形態】
以下に本発明の実施の形態を図示例に基づいて説明する。図2は本発明を実施した貯留水浄化設備の一例について、そのオゾン処理装置の構造を示す系統図、図3は浄化ユニットの構成例を示す模式図である。
【0014】
本貯留水浄化設備は、図1に示した貯溜水浄化設備のオゾン処理装置6を、図2に示したオゾン処理装置に代えたものである。図2に示したオゾン処理装置は、処理装置本体10とこれに付設された浄化ユニット20とからなる。
【0015】
処理装置本体10は、従来のオゾン処理装置6と基本的に同じものであり、そのA点は図1中のA′点に、またB点は図1中のB′点にそれぞれ接続されている。この接続により、非常時以外のとき、すなわち通常時は、浄化設備の主循環系統2を流れる貯溜水が、濾過器5の上流側または下流側から取入れ弁11を介してオゾン処理装置に取入れられる。オゾン処理装置に取入れられた貯溜水は、加圧ポンプ12、エジェクタ13、気液分離塔14、逆止弁15を順に通り、戻り弁16より主循環系路2内のポンプ4の上流側に戻る。
【0016】
ここでエジェクタ13は、オゾン発生器17からオゾンガスを供給され、そのオゾンガスを貯溜水に注入する。気液分離塔14はオゾン分解塔14aを装備している。また、加圧ポンプ12およびオゾン発生器17は、非常時の停電に備えて非常用発電機19と接続されている。一方、取入れ弁11の下流側と戻り弁16の上流側との間は、流量調節弁18aを備えたバイパス管18により直結されている。
【0017】
浄化ユニット20は、気液分離塔14と逆止弁15との間に、流量調節弁21を介して接続されている。浄化ユニット20の内部は、図3(A)に示すように、活性炭カートリッジ22により導入水を濾過する構造であるが、図3(B)に示すように、紫外線発生器23により導入水を処理する構造でもよい。また、図3(C)(D)に示すように、これらに加えて膜フィルタ24を設ける構造でもよい。膜フィルタ24は、メンブラフィルタ、UF膜、MF膜等であり、濁質が多い場合にこれを低減除去する。
【0018】
次に、本貯留水浄化設備の運転方法について説明する。
【0019】
通常は、オゾン処理装置の処理装置本体10において、取入れ弁11および戻り弁16を開け、流量調節弁18aおよび21を閉じた状態で、加圧ポンプ12およびオゾン発生器17を通常電源により作動させる。これにより、貯留水浄化設備の主循環系路2を流れる貯溜水が、濾過器5の上流側または下流側から処理装置本体10に取入れられ、ここでオゾン処理されてポンプ4の上流側に戻る。かくして、浄化設備を循環する貯溜水に対して通常のオゾン処理が実施される。そして、このオゾン処理により、耐塩素性微生物が殺菌、不活性され、消毒副生成物が分解低減される。
【0020】
震災、渇水等の非常時で、且つ電源を確保できる場合は、取入れ弁11および流量調節弁21を開き、戻り弁16を閉じた状態で、浄水設備の主循環系路2を通常通り運転しながら、加圧ポンプ12およびオゾン発生器17を作動させる。これにより、主循環系路2を流れる貯溜水が濾過器5の上流側または下流側から取入れ弁11を通って処理装置本体10に取入れられ、通常通りのオゾン処理を受けた後、流量調節弁21を通って浄化ユニット20に送られ、ここで溶存オゾンが分解乃至は除去され、更に残存する消毒副生成物が水道水の水質基準値および監視項目指針の判定基準値以下に低減される。かくして、循環浄化水から飲料水が得られる。
【0021】
このとき、バイパス管18に設けた流量調節弁18aを開けば、オゾン処理された貯溜水(オゾン処理水)の一部がバイパス管18を通ってエジェクタ13に循環する。そのため、飲料水の需要量(供給水量)の増減に関係なく、エジェクタ13に所定量の水を供給し続けることができる。
【0022】
非常時で電源を確保できない場合は、主循環系路2内のポンプ3が停止するので、戻り弁16および流量調節弁18aを開け、取入れ弁11を閉じた状態で、非常用発電機19を作動させる。これにより、貯水部1内の貯溜水がヘアキャッチャ3の上流側から戻り弁16を通ってオゾン処理装置内へ直接導入される。そして、その導入水はバイパス管18を通ってオゾン処理部に送られ、更に浄化ユニット20に送られることにより、飲料水となる。このときも、流量調節弁18aの開度調節を行うことにより、エジェクタ13に所定水量を供給することができる。
【0023】
電源を確保できるにもかかわらず、主循環系路2内のポンプ3や濾過部4が破損している場合も、戻り弁16および流量調節弁18aを開け、取入れ弁11を閉じることにより、貯溜水から飲料水を生成することができる。
【0024】
【発明の効果】
以上に説明した通り、本発明の貯留水浄化設備は、貯留水をオゾン処理するオゾン処理装置がオゾン処理を行う処理装置本体と共に、オゾン処理水を飲料水に浄化する浄化ユニットを備え、且つその浄化ユニットが簡易で安価なため、震災、渇水等の非常時に飲料水を確保できるにもかかわらず、浄化設備の大型化およびコスト増を可及的に回避することができる。また、飲料水を生成する部分がオゾン処理装置と同一メーカとなるので、メンテナンス性の悪化も回避される。
【0025】
処理装置本体における貯溜水の取入れ部と戻り部との間をバルブ付きのバイパス管により直結した場合は、飲料水の需要量(供給水量)の増減に関係なく、バイパス管を通して処理装置本体内のオゾン処理部に所定量の水を送ることができる。
【0026】
貯溜水の取入れ部を主循環系統における浄化部の下流側に接続し、戻し部を前記浄化部の上流側に接続した場合は、前記浄化部が停止状態の場合も、浄化部上流側の戻し部からバイパス管を通して貯溜水を処理装置本体内のオゾン処理部および浄化ユニットに直接送ることができるので、飲料水の生成を続けることができる。
【図面の簡単な説明】
【図1】 オゾン処理を組み合わせた従来の貯溜水浄化設備の構成を示す系統図である。
【図2】 本発明を実施した貯留水浄化設備の1例について、そのオゾン処理装置の構造を示す系統図である。
【図3】 浄化ユニットの構成例を示す模式図である。
【符号の説明】
1 貯水部
2 主循環系統
3 ヘアキャッチャ
4 循環ポンプ
5 濾過器
6 オゾン処理装置
10 処理装置本体
11 取入れ弁
12 加圧ポンプ
13 エジェクタ
14 気液分離塔
15 逆止弁
16 戻り弁
17 オゾン発生器
18 バイパス管
19 非常用発電機
20 浄化ユニット
22 活性炭カートリッジ
23 紫外線発生器
24 膜フィルタ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to storage water purification equipment used for purification of water stored in pools, baths, ponds, etc. , in particular , stored water purification equipment combined with ozone treatment, and more particularly in the event of an emergency such as an earthquake disaster or drought. The present invention relates to a stored water purification facility with an ozone treatment device having a function of purifying stored water into drinking water.
[0002]
[Prior art]
As a purification system for purifying water stored in pools, baths, ponds, etc., a circulation system combining filtration and disinfectant injection is generally used, but recently, ozone has been further improved for the purpose of improving the purification effect. A combination of treatments is also used. The characteristic of ozone treatment is that turbidity and pollutants can be greatly reduced by the strong oxidative sterilization action of ozone, and further, chlorine-resistant microorganisms can be sterilized and inactivated. A conventional stored water purification facility combined with ozone treatment is shown in FIG.
[0003]
The water stored in the water storage unit 1 such as a pool, a bathhouse, or a pond is taken out from the bottom of the water storage unit 1 by the main circulation system 2 and returned to the water storage unit 1 from the side of the water storage unit 1. The main circulation system 2 is provided with a hair catcher 3, a circulation pump 4 and a filter 5. Thus, the stored water taken out from the water storage unit 1 is removed from the large solid material by the hair catcher 3 and pressurized by the circulation pump 4, and then the fine solid material is removed by the filter 5. It is disinfected with a chlorine agent and returned to the water storage unit 1.
[0004]
At this time, a part of the stored water is taken out from the upstream side or the downstream side of the filter 5 and sent to the ozone treatment device 6. The ozone treatment device 6 injects ozone gas generated by an ozone generator into stored water using an ejector, and ozone-treats the stored water, and then returns it to the upstream side of the pump 4. Ozone treatment decomposes soluble pollutants and sterilizes and inactivates chlorine-resistant microorganisms, and colloidal substances are aggregated and easily trapped in the filter 5.
[0005]
[Problems to be solved by the invention]
Conventional stored water purification equipment combined with ozone treatment has a much higher purification capacity than those without ozone treatment, but it is not possible to use purified water as drinking water in the event of an emergency such as an earthquake or drought. Can not. This is because in circulation purification of pools, baths, ponds, etc., chemicals such as chlorine are injected for disinfection, and the concentration in the pool is maintained at 0.4 mg / liter or more by the Ministry of Health and Welfare, Because there is no interest in the residue, the concentration of disinfection by-products often exceeds the water quality standard value of tap water.
[0006]
For this reason, in order to obtain drinking water from the stored water, an emergency dedicated purification device is required. However, an emergency dedicated purification device is large and expensive. Moreover, since it is customary that the purification equipment and the manufacturer are different, there is a problem that the inspection cost increases.
[0007]
The object of the present invention is to provide drinking water from the stored water in the event of an emergency such as an earthquake disaster or drought, and with an ozone treatment device that can avoid the increase in the size of purification equipment, the increase in cost, and the deterioration of maintainability as much as possible It is to provide the stored water purification equipment .
[0008]
[Means for Solving the Problems]
The stored water purification equipment of the present invention is a stored water purification equipment that removes and purifies solids while circulating water stored in a water storage section such as a pool, a bath, and a pond , and further disinfects, A main circulation system for taking out water stored in the water storage unit from the water storage unit and returning the water to the water storage unit; and an ozone treatment device that takes in the stored water from the main circulation system and returns it to the main circulation system again. The ozone treatment apparatus comprises a treatment apparatus main body for performing the ozone treatment and a purification unit attached to the treatment apparatus main body, and the purification unit is downstream of the ozone treatment section in the treatment apparatus main body. a is connected via a valve that is closed during normal, it is configured to purify an earthquake, incorporate a reservoir water after ozonation by the valve in an emergency drought or the like is opened to drinking water.
[0009]
When the stored water purification equipment of the present invention is used, in other than emergency , that is, in normal time , combined with ozone treatment by circulating the stored water circulated and purified in the purification equipment to the treatment equipment body of the ozone treatment equipment. Normal circulation purification is performed. In the event of an emergency, the stored water that has been subjected to ozone treatment by the treatment device body is sent to the purification unit. The stored water after the ozone treatment, that is, the ozone-treated water, is sterilized and inactivated by chlorine-resistant microorganisms due to the strong sterilization action of ozone, and further, disinfection by-products are also decomposed and reduced. Therefore, in the purification unit, drinking water can be obtained to such an extent that dissolved ozone contained in the ozone-treated water is decomposed and disinfection by-products remaining in the ozone-treated water are reduced and removed. Thus, drinking water is obtained from the stored water, and the purification unit is simple and inexpensive.
[0010]
Activated carbon treatment or ultraviolet treatment can be used for decomposition of dissolved ozone and reduction and removal of residual disinfection by-products. When there is a lot of turbidity, it is desirable to reduce the turbidity by combining membrane filters such as a membrane filter, UF membrane, and MF membrane.
[0011]
In the processing apparatus main body of the ozone processing apparatus, it is preferable to inject ozone gas into the stored water using an ejector. In general, in the ozone gas injection process, it is preferable that the amount of water is kept constant. From this point, the storage water intake part and the return part are directly connected by a bypass pipe with a valve, and the stored water is supplied from the return part in the main body of the treatment apparatus to the ozone treatment part by opening the valve provided in the bypass pipe. It is desirable to configure to send . Thereby, it is possible to send a predetermined amount of stored water to the ozone gas processing section through the bypass pipe regardless of increase or decrease of the demand amount (supply water amount) of drinking water.
[0012]
Here, if the intake unit is connected to the downstream side of the purification unit in the main circulation system and the return unit is connected to the upstream side of the purification unit, even if the purification unit is stopped, the return of the upstream side of the purification unit is returned. The stored water can be sent from the part to the ozone treatment part through the bypass pipe, and further sent to the purification unit.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 2 is a system diagram showing the structure of the ozone treatment apparatus for one example of the stored water purification equipment embodying the present invention, and FIG. 3 is a schematic diagram showing an example of the configuration of the purification unit.
[0014]
In this stored water purification facility, the ozone treatment device 6 of the stored water purification facility shown in FIG. 1 is replaced with the ozone treatment device shown in FIG. The ozone treatment apparatus shown in FIG. 2 includes a treatment apparatus main body 10 and a purification unit 20 attached thereto.
[0015]
The processing apparatus main body 10 is basically the same as the conventional ozone processing apparatus 6, and its point A is connected to point A 'in FIG. 1, and point B is connected to point B' in FIG. Yes. Due to this connection, in times other than emergency, that is, in normal times, the stored water flowing through the main circulation system 2 of the purification equipment is taken into the ozone treatment apparatus from the upstream side or the downstream side of the filter 5 through the intake valve 11. . The stored water taken into the ozone treatment device passes through the pressurizing pump 12, the ejector 13, the gas-liquid separation tower 14, and the check valve 15 in this order, and from the return valve 16 to the upstream side of the pump 4 in the main circulation path 2. Return.
[0016]
Here, the ejector 13 is supplied with ozone gas from the ozone generator 17 and injects the ozone gas into the stored water. The gas-liquid separation tower 14 is equipped with an ozonolysis tower 14a. The pressurizing pump 12 and the ozone generator 17 are connected to an emergency generator 19 in preparation for a power failure in an emergency. On the other hand, the downstream side of the intake valve 11 and the upstream side of the return valve 16 are directly connected by a bypass pipe 18 having a flow rate adjusting valve 18a.
[0017]
The purification unit 20 is connected between the gas-liquid separation tower 14 and the check valve 15 via a flow rate adjustment valve 21. The purification unit 20 has a structure in which the introduced water is filtered by the activated carbon cartridge 22 as shown in FIG. 3 (A), but the introduced water is treated by the ultraviolet ray generator 23 as shown in FIG. 3 (B). It may be a structure. Moreover, as shown to FIG.3 (C) (D), the structure which provides the membrane filter 24 in addition to these may be sufficient. The membrane filter 24 is a membrane filter, UF membrane, MF membrane or the like, and reduces and removes this when there is a lot of turbidity.
[0018]
Next, an operation method of the stored water purification facility will be described.
[0019]
Normally, in the processing apparatus main body 10 of the ozone processing apparatus , the pressurizing pump 12 and the ozone generator 17 are operated by a normal power source with the intake valve 11 and the return valve 16 opened and the flow rate adjusting valves 18a and 21 closed. . As a result, the stored water flowing through the main circulation system path 2 of the stored water purification facility is taken into the processing apparatus main body 10 from the upstream side or the downstream side of the filter 5, where it is ozone treated and returns to the upstream side of the pump 4. . Thus, ordinary ozone treatment is performed on the stored water circulating through the purification equipment. And by this ozone treatment, chlorine-resistant microorganisms are sterilized and inactivated, and disinfection by-products are decomposed and reduced.
[0020]
In the event of an emergency such as an earthquake disaster or drought, and when the power supply can be secured, the main circulation system 2 of the water purification facility is operated as usual with the intake valve 11 and the flow control valve 21 open and the return valve 16 closed. Meanwhile, the pressurizing pump 12 and the ozone generator 17 are operated. As a result, the stored water flowing through the main circulation path 2 is taken into the processing apparatus main body 10 through the intake valve 11 from the upstream side or the downstream side of the filter 5 and is subjected to normal ozone treatment. 21 is sent to the purification unit 20 where the dissolved ozone is decomposed or removed, and the remaining disinfection by-products are reduced below the water quality standard value of the tap water and the judgment standard value of the monitoring item guide. Thus, drinking water is obtained from the circulating purified water.
[0021]
At this time, if the flow rate adjustment valve 18 a provided in the bypass pipe 18 is opened, a part of the ozone-treated stored water (ozone-treated water) circulates through the bypass pipe 18 to the ejector 13. Therefore, it is possible to continue supplying a predetermined amount of water to the ejector 13 regardless of increase or decrease in the demand amount (supply water amount) of drinking water.
[0022]
If the power supply cannot be secured in an emergency, the pump 3 in the main circulation system 2 stops, so that the emergency generator 19 is opened with the return valve 16 and the flow rate control valve 18a open and the intake valve 11 closed. Operate. Thereby, the stored water in the water storage part 1 is directly introduced into the ozone treatment apparatus from the upstream side of the hair catcher 3 through the return valve 16. Then, the introduced water is sent to the ozone treatment section through the bypass pipe 18 and further sent to the purification unit 20 to become drinking water. Also at this time, the predetermined amount of water can be supplied to the ejector 13 by adjusting the opening degree of the flow control valve 18a.
[0023]
Even when the power supply can be secured and the pump 3 and the filtration unit 4 in the main circulation system 2 are damaged, the return valve 16 and the flow rate control valve 18a are opened, and the intake valve 11 is closed. Drinking water can be generated from the water.
[0024]
【The invention's effect】
As described above, the stored water purification equipment of the present invention includes a purification unit that purifies ozone treated water into drinking water together with a treatment apparatus main body in which an ozone treatment apparatus that ozone treats stored water performs ozone treatment, and Since the purification unit is simple and inexpensive, it is possible to avoid the increase in the size and cost of the purification facility as much as possible, although drinking water can be secured in the event of an emergency such as an earthquake or drought. Moreover, since the part which produces | generates drinking water becomes the same manufacturer as an ozone treatment apparatus, the deterioration of maintainability is also avoided.
[0025]
When the storage water intake part and the return part in the main body of the treatment device are directly connected by a bypass pipe with a valve, the inside of the main body of the treatment device is passed through the bypass pipe regardless of the increase or decrease in the amount of demand for drinking water (supply water amount) . A predetermined amount of water can be sent to the ozone treatment unit .
[0026]
When the storage water intake part is connected to the downstream side of the purification part in the main circulation system and the return part is connected to the upstream side of the purification part, the return of the upstream part of the purification part even when the purification part is stopped Since the stored water can be directly sent from the unit to the ozone processing unit and the purification unit in the processing apparatus main body through the bypass pipe, the production of drinking water can be continued.
[Brief description of the drawings]
FIG. 1 is a system diagram showing a configuration of a conventional stored water purification facility combined with ozone treatment.
FIG. 2 is a system diagram showing the structure of an ozone treatment apparatus for one example of a stored water purification facility embodying the present invention.
FIG. 3 is a schematic diagram showing a configuration example of a purification unit.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Water storage part 2 Main circulation system 3 Hair catcher 4 Circulation pump 5 Filter 6 Ozone processing apparatus 10 Processing apparatus main body 11 Intake valve 12 Pressurization pump 13 Ejector 14 Gas-liquid separation tower 15 Check valve 16 Return valve 17 Ozone generator 18 Bypass pipe 19 Emergency generator 20 Purification unit 22 Activated carbon cartridge 23 Ultraviolet generator 24 Membrane filter

Claims (3)

プール、浴場、池等の貯水部に貯溜されている水を循環させながら固形物を除去して浄化し、更に消毒を行う貯留水浄化設備であって、前記貯水部に貯留されている水を当該貯水部から取り出して当該貯水部へ戻す主循環系統と、前記主循環系統より貯溜水を取入れオゾン処理して再び主循環系統に戻すオゾン処理装置とを具備しており、前記オゾン処理装置は前記オゾン処理を行う処理装置本体と、該処理装置本体に付設された浄化ユニットとからなり、該浄化ユニットは、前記処理装置本体内のオゾン処理部の下流側に、通常時に閉止されるバルブを介して接続されており、地震、渇水等の非常時に前記バルブが開放されることによりオゾン処理後の貯溜水を取入れて飲料水に浄化する構成であることを特徴とする貯留水浄化設備A storage water purification facility that removes and purifies solids while circulating water stored in a water storage section such as a pool, bathhouse, pond, etc. , and further disinfects the water stored in the water storage section. A main circulation system that is taken out from the water storage unit and returned to the water storage unit; and an ozone treatment device that takes in the stored water from the main circulation system and returns it to the main circulation system by ozone treatment. The treatment apparatus main body that performs the ozone treatment, and a purification unit attached to the treatment apparatus main body, the purification unit has a valve that is normally closed on the downstream side of the ozone treatment section in the treatment apparatus main body. The stored water purification equipment is configured to take in the stored water after ozone treatment and purify it into drinking water by opening the valve in the event of an emergency such as an earthquake or drought . 前記処理装置本体における貯溜水の取入れ部と戻し部との間をバルブ付きのバイパス管により直結し、該パイパス管に備わるバルブの開放により前記処理装置本体内の戻し部からオゾン処理部へ貯留水を送るように構成したことを特徴とする請求項1に記載の貯留水浄化設備Between the inlet portion and the return portion of the reservoir water in the processing apparatus main body is directly connected by a bypass pipe with a valve, the accumulated water by opening the valve provided in the bypass pipe from the return portion of the processing apparatus main body to the ozone treatment unit accumulated water purification installation according to claim 1, characterized by being configured to send. 前記貯溜水の取入れ部を、前記主循環系統における浄化部の下流側に接続し、戻し部を前記浄化部の上流側に接続したことを特徴とする請求項2に記載の貯留水浄化設備 Wherein the intake portion of the reservoir water, the main circulation connected to the downstream side of the purifier in the system, the accumulated water purification installation according to claim 2, characterized in that connecting the return portion upstream of the purifier.
JP09769196A 1996-03-26 1996-03-26 Reservoir purification equipment Expired - Fee Related JP3660421B2 (en)

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Application Number Priority Date Filing Date Title
JP09769196A JP3660421B2 (en) 1996-03-26 1996-03-26 Reservoir purification equipment

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CN102030400A (en) * 2010-10-28 2011-04-27 昆山科技大学 Method for treating liquid ozone by using carbon-containing materials
CN109205761A (en) * 2017-06-30 2019-01-15 上海轻工业研究所有限公司 The recirculating cooling water system and ozone the controlling of injecting quantity device and method of ozone treatment

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