JPH0639371A - Water purifying system - Google Patents

Water purifying system

Info

Publication number
JPH0639371A
JPH0639371A JP4199869A JP19986992A JPH0639371A JP H0639371 A JPH0639371 A JP H0639371A JP 4199869 A JP4199869 A JP 4199869A JP 19986992 A JP19986992 A JP 19986992A JP H0639371 A JPH0639371 A JP H0639371A
Authority
JP
Japan
Prior art keywords
water
tank
circulation
septic tank
pump
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP4199869A
Other languages
Japanese (ja)
Inventor
Motoharu Sato
元春 佐藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanden Corp
Original Assignee
Sanden Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sanden Corp filed Critical Sanden Corp
Priority to JP4199869A priority Critical patent/JPH0639371A/en
Publication of JPH0639371A publication Critical patent/JPH0639371A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To supply high quality water from a water storage tank and extend the water purifying life by properly circulating water in a water storage tank to a first and a second purifying tanks having a filtering material and remove impurities contained in the storage water by the filtering material to purify the water. CONSTITUTION:A water purifying system is provided with tank 1 placed at a high place to store supplied water temporarily, a first circulating pipeline 11 of which each terminal part is connected with the tank, and a pump 12 installed near one connection terminal part. A first purifying tank 21 having a filtering material is installed in the outlet side of the pump, a second solenoid valve 16 is set in the outlet side of the first purifying tank 21, a second circulating route 31 is made to bypass between the outlet side of the pump 12 and the outlet side of the solenoid valve 16, and a second purifying tank 41 having a filtering material is installed in the second circulating route 31. In the case the solenoid valve 16 is closed and the pump 12 is operated, the water in the tank 1 at a high position is circulated to the second purifying tank 41 of the second circulating route 31 and in the case the solenoid valve 16 is opened, water is circulated to the first purifying tank 21 of the first circulating route 11 and impurities are removed by the built-in filtering material.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、マンション,オフィス
ビル等の建物に有用な浄水システムに関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purification system useful for buildings such as condominiums and office buildings.

【0002】[0002]

【従来の技術】マンション,オフィスビル等の建物で
は、その屋上等に設置された高置タンクにポンプを利用
して水道水を揚水し、該高置タンクから建物内の各部屋
の水栓に供水できるようにしている。
2. Description of the Related Art In buildings such as condominiums and office buildings, tap water is pumped to a high tank installed on the roof of the building, and the water is pumped from the high tank to the faucet of each room in the building. The water is available.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、高置タ
ンクから建物内の必要箇所に給水される水には、タンク
内で発生した錆の他に藻類や細菌等が混入し易く、水道
管から直接水栓に水を供給する場合に比べて不純物が多
く水質が悪化する欠点がある。
However, in addition to the rust generated in the tank, algae, bacteria, etc. are easily mixed in the water supplied from the elevated tank to the required place in the building, and the water is directly fed from the water pipe. Compared with the case where water is supplied to the faucet, there are many impurities and the water quality deteriorates.

【0004】本発明は上記事情に鑑みてなされたもの
で、その目的とするところは、高置タンク等の貯水タン
クから給水される水の浄化を適切に行なえる浄水システ
ムを提供することにある。
The present invention has been made in view of the above circumstances, and an object thereof is to provide a water purification system capable of appropriately purifying water supplied from a water storage tank such as an elevated tank. .

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、請求項1では、供給水を一次的に貯留する貯水タン
クと、貯水タンクに各端部を接続された第1循環管路
と、第1循環管路の一接続端寄りに介装されたポンプ
と、第1循環管路のポンプの出口側に介装された濾過材
内蔵の第1浄化槽と、第1循環管路の第1浄化槽の出口
側に介装された開閉弁と、第1循環管路のポンプの出口
側と開閉弁の出口側をバイパスする第2循環管路と、第
2循環管路に介装された濾過材内蔵の第2浄化槽とか
ら、浄水システムを構成している。
In order to achieve the above-mentioned object, in claim 1, a water storage tank for temporarily storing the supply water, and a first circulation pipe line having each end connected to the water storage tank are provided. A pump installed near one connection end of the first circulation line, a first septic tank containing a filter medium installed on the outlet side of the pump of the first circulation line, and a first circulation line An on-off valve installed on the outlet side of the septic tank, a second circulation line that bypasses the pump outlet side of the first circulation line and the outlet side of the on-off valve, and filtration installed on the second circulation line. A water purification system is composed of a second septic tank with a built-in material.

【0006】請求項2では、請求項1の浄水システムに
おいて、第1循環管路の開閉弁の出口側で且つ第2循環
管路との接続端よりも下流側に介装された第2の開閉弁
と、第2浄化槽内の水を排出する排水管路とを設けけい
る。
According to a second aspect of the present invention, in the water purification system of the first aspect, the second circulating pipe is provided on the outlet side of the opening / closing valve of the first circulating pipe line and on the downstream side of the connection end with the second circulating pipe line. An on-off valve and a drain pipe for discharging the water in the second septic tank are provided.

【0007】請求項3では、請求項1または2記載の浄
水システムにおいて、オゾン発生機のオゾン送出口を第
1循環管路に接続している。
According to a third aspect of the present invention, in the water purification system according to the first or second aspect, the ozone outlet of the ozone generator is connected to the first circulation line.

【0008】請求項4では、請求項1乃至3何れか1項
記載の浄水システムにおいて、第1浄化槽内に吸着剤を
配置すると共に、第1循環管路のポンプの出口側から流
路切換用の弁を介して分岐され第1浄化槽に至る再生管
路と、再生管路に介装されたヒ−タ付きの温水生成槽
と、第1浄化槽内の水を排出する排水管路とを設けてい
る。
According to a fourth aspect, in the water purification system according to any one of the first to third aspects, the adsorbent is arranged in the first septic tank, and the flow path is switched from the outlet side of the pump of the first circulation pipeline. A regeneration pipe branching through the valve to reach the first septic tank, a heater-equipped hot water generating tank interposed in the regeneration pipe, and a drain pipe for discharging water in the first septic tank ing.

【0009】請求項5では、請求項4記載の浄水システ
ムにおいて、紫外線を照射可能な殺菌ランプを第1浄化
槽内に配置すると共に、白金族系酸化物及び酸化物系セ
ラミックスを主成分とする触媒を殺菌ランプの周囲に配
設している。
According to a fifth aspect, in the water purification system according to the fourth aspect, a sterilizing lamp capable of irradiating ultraviolet rays is arranged in the first septic tank, and a catalyst containing a platinum group oxide and an oxide ceramic as a main component. Is arranged around the germicidal lamp.

【0010】[0010]

【作用】請求項1に係る浄水システムでは、開閉弁を閉
じた状態でポンプを作動させることにより貯水タンク内
の水を第2循環管路の第2浄化槽に、また開閉弁を開け
た状態でポンプを作動させることにより貯水タンク内の
水を第1循環管路の第1浄化槽に循環させることができ
る。循環時には夫々の浄化槽に内蔵された濾過材によっ
て貯留水に含まれる不純物が除去される。
In the water purification system according to the first aspect of the present invention, the pump is operated with the on-off valve closed to move the water in the water storage tank to the second septic tank of the second circulation line and with the on-off valve opened. By operating the pump, the water in the water storage tank can be circulated in the first septic tank of the first circulation line. At the time of circulation, impurities contained in the stored water are removed by the filter media contained in the respective septic tanks.

【0011】請求項2に係る浄水システムでは、開閉弁
を開け、第2の開閉弁を閉じた状態でポンプを作動させ
ることにより、第2循環管路に水を逆流させて濾過材に
捕獲されている不純物を該濾過材から離脱させ、これら
を含んだ水を排水管路から外部に排出できる。
In the water purification system according to the second aspect of the present invention, the pump is operated with the opening / closing valve opened and the second opening / closing valve closed, whereby the water is made to flow backward through the second circulation pipe and is captured by the filter medium. The impurities contained therein can be separated from the filter material, and the water containing them can be discharged to the outside through the drainage pipe.

【0012】請求項3に係る浄水システムでは、第1循
環管路を流れる水にオゾンを混入させて、貯留水に含ま
れる細菌を死滅させることができる。
In the water purification system according to the third aspect, it is possible to kill the bacteria contained in the stored water by mixing ozone into the water flowing through the first circulation line.

【0013】請求項4に係る浄水システムでは、第1循
環管路への循環時に臭気や次亜塩素塩,有機塩素化合物
等を吸着剤で吸着して除去できると共に、弁切換えによ
って高置タンク内の貯留水を温水生成槽を通じて加温し
て浄化槽に送り込むことにより、吸着剤に吸着されてい
る次亜塩素塩及び有機塩素化合物を温水中に脱離させ、
これらを含んだ水を排水管路から外部に排出できる。
In the water purification system according to the fourth aspect, odors, hypochlorite, organic chlorine compounds, etc. can be adsorbed and removed by the adsorbent during circulation to the first circulation line, and the valve can be switched in the high tank. The stored water of is heated through the hot water generation tank and sent to the septic tank to desorb the hypochlorite and organic chlorine compounds adsorbed by the adsorbent into the hot water,
Water containing these can be discharged to the outside from the drainage pipe.

【0014】請求項5に係る浄水システムでは、請求項
4と同様の作用で温水中に脱離した次亜塩素塩及び有機
塩素化合物を触媒及び紫外線による光触媒反応によって
分解させ、分解分を含んだ水を排水管路から外部に排出
できる。
In the water purification system according to claim 5, the hypochlorous salt and the organic chlorine compound desorbed in warm water are decomposed by a catalyst and a photocatalytic reaction by ultraviolet rays by the same action as in claim 4, and the decomposed component is contained. Water can be discharged to the outside from the drain pipe.

【0015】[0015]

【実施例】図1には本発明を適用した浄水システムの概
略構成を示してある。同図において、1は高置タンク、
11は第1循環管路、21は第1浄化槽、31は第2循
環管路、41は第2浄化槽、51は再生管路、61は温
水生成槽である。
FIG. 1 shows a schematic structure of a water purification system to which the present invention is applied. In the figure, 1 is a high tank,
11 is a first circulation pipe, 21 is a first septic tank, 31 is a second circulation pipe, 41 is a second septic tank, 51 is a regeneration pipe, and 61 is a hot water production tank.

【0016】高置タンク1はマンション,オフィスビル
等の建物の屋上等に設置され、貯留水の水位を検知する
フロ−トスイッチ等の水位センサ2を内部に備えてい
る。また、高置タンク1の上面には建物の地下に至る揚
水管路3の一端が接続され、該揚水管路2の他端は地下
に配置された揚水用ポンプ4及び図示省略の受水タンク
を介して水道本管に接続されている。さらに、高置タン
ク1の側面下端には建物内の各部屋の水栓に至る給水管
路5の一端が接続され、該給水管路5の途中には塩素発
生機6の出口が混入用ポンプ7を介して接続されてい
る。
The high tank 1 is installed on the roof of a building such as a condominium or office building, and has a water level sensor 2 such as a float switch for detecting the water level of stored water therein. Further, one end of a pumping pipe line 3 reaching the underground of the building is connected to the upper surface of the elevated tank 1, and the other end of the pumping pipe line 2 is a pumping pump 4 arranged underground and a receiving tank (not shown). Is connected to the water mains via. Further, one end of a water supply pipe 5 leading to the water faucet of each room in the building is connected to the lower end of the side surface of the high tank 1, and the outlet of the chlorine generator 6 is provided in the middle of the water supply pipe 5 as a mixing pump. It is connected via 7.

【0017】上記の塩素発生機6は、図2にも示すよう
に、側面上端に入口6aを側面下端に出口6bを夫々有
する本体槽6cと、本体槽6c内の出口寄り位置に配置
された正電極6dと、本体槽6c内の入口寄り位置に配
置された負電極6eとから構成されている。また、本体
槽6cの入口6aには開閉弁を有する水道管Sが接続さ
れ、また出口6bにはポンプ7の入口が直接或いは中継
パイプ6fを介して接続されている。この塩素発生機6
では水道水を電気分解することにより次亜塩素酸イオン
(clO- ) を正電極6dの周辺で生成し、該イオン水
をポンプ7によって給水管路4内に送り込み供給水に混
入できる。詳しくは、給水管路5の流量に応じたポンプ
7の比例的な作動によって、給水管路5を流れる水に水
道基準相当の濃度(0.1ppm以上)で塩素を含有さ
せることができる。
As shown in FIG. 2, the chlorine generator 6 is arranged at a main body tank 6c having an inlet 6a at the upper end of the side surface and an outlet 6b at the lower end of the side surface, and a position near the outlet in the main body tank 6c. It is composed of a positive electrode 6d and a negative electrode 6e arranged at a position near the entrance in the main body tank 6c. A water pipe S having an on-off valve is connected to the inlet 6a of the main body tank 6c, and the inlet of the pump 7 is connected to the outlet 6b directly or via a relay pipe 6f. This chlorine generator 6
Then, by electrolyzing tap water, hypochlorite ions (clO ) are generated around the positive electrode 6d, and the ion water can be sent into the water supply pipe 4 by the pump 7 to be mixed with the supply water. More specifically, by proportionally operating the pump 7 according to the flow rate of the water supply pipeline 5, the water flowing through the water supply pipeline 5 can contain chlorine at a concentration (0.1 ppm or more) equivalent to the water supply standard.

【0018】第1循環管路11は、一端を高置タンク1
の側面下端に、また他端を高置タンク1の側面上端に夫
々接続されている。この第1循環管路11には下方の接
続端から順に、循環用ポンプ12と、開閉を可能とした
電磁式の3方切換弁(以下、第1電磁弁という)13
と、ベンチュリ管14と、逆止弁15と、後述する第1
浄化槽21と、電磁式の開閉弁16(以下、第2電磁弁
という)と、電磁式の開閉弁17(以下、第2電磁弁と
いう)が介装されている。また、逆止弁15と第1浄化
槽21の間には、電磁式の開閉弁18(以下、第4電磁
弁という)が介装された排水管路19が接続されてい
る。
The first circulation line 11 has one end with the elevated tank 1
Is connected to the lower end of the side surface and the other end is connected to the upper end of the side surface of the high tank 1. A circulation pump 12 and an electromagnetic three-way switching valve (hereinafter, referred to as a first electromagnetic valve) 13 that can be opened and closed are arranged in this first circulation line 11 in order from a lower connection end.
, Venturi pipe 14, check valve 15, and first described later
A septic tank 21, an electromagnetic opening / closing valve 16 (hereinafter referred to as a second electromagnetic valve), and an electromagnetic opening / closing valve 17 (hereinafter referred to as a second electromagnetic valve) are interposed. In addition, a drainage conduit 19 in which an electromagnetic on-off valve 18 (hereinafter referred to as a fourth electromagnetic valve) is interposed is connected between the check valve 15 and the first septic tank 21.

【0019】上記のベンチュリ管14は、図3にも示す
ように、中央に向かって徐々に断面径が小さくなる管材
から成り、最小径部分に導入孔14aを有している。ま
た、ベンチュリ管14の導入孔14aには、無声放電式
等のオゾン発生機20の出口が直接或いは中継パイプ1
4bを介して接続されている。このベンチュリ管14で
はオゾン発生機20で生成されたオゾン(O3 )を導入
孔14aを通じてベンチュリ管14内に送り込んで循環
水に混入できる。
As shown in FIG. 3, the Venturi pipe 14 is made of a pipe material whose cross-sectional diameter gradually decreases toward the center and has an introduction hole 14a in the minimum diameter portion. In addition, the inlet of the venturi pipe 14 is directly connected to the outlet of the ozone generator 20 of the silent discharge type or the relay pipe 1
It is connected via 4b. In the venturi pipe 14, ozone (O3) generated by the ozone generator 20 can be sent into the venturi pipe 14 through the introduction hole 14a and mixed into the circulating water.

【0020】第1浄化槽21は、図4にも示すように、
下面中央に入口22aを上面中央に出口22bを夫々有
し、また側面下端に温水導入口22cを有する本体槽2
2と、本体槽22の温水導入口22cよりも上方に配置
された整流板23と、整流板23の上側に配置されたプ
レフィルタ24と、プレフィルタ24の上側に配置され
た吸着層25と、吸着層25の上側に配置された有底筒
状の触媒層26と、触媒層26の内側中央に配置された
UVランプ27とから構成されている。吸着層25は繊
維状或いは粒状活性炭から形成され、また触媒層26は
有底筒状に成形されたゼオライトの表面に触媒となる白
金族系酸化物及び酸化物系セラミックスの複合物を担持
させて形成されその周面部分には多数の孔(図示省略)
が設けられている。尚、白金族系酸化物としてはPt,
Rd,Ru等の酸化物等が、また酸化物系セラミックス
としてはルチル型或いはアナタ−ゼ型の酸化チタン等が
夫々使用される。この第1浄化槽21における機能詳細
は後述する。
The first septic tank 21 is, as shown in FIG.
Main body tank 2 having inlet 22a at the center of the lower surface, outlet 22b at the center of the upper surface, and hot water inlet 22c at the lower end of the side surface
2, a rectifying plate 23 arranged above the hot water inlet 22c of the main body tank 22, a prefilter 24 arranged above the rectifying plate 23, and an adsorption layer 25 arranged above the prefilter 24. The bottomed cylindrical catalyst layer 26 is arranged above the adsorption layer 25, and the UV lamp 27 is arranged in the center of the inside of the catalyst layer 26. The adsorption layer 25 is formed of fibrous or granular activated carbon, and the catalyst layer 26 is formed by supporting a complex of platinum group oxide and oxide ceramics, which is a catalyst, on the surface of zeolite shaped into a bottomed cylinder. A large number of holes (not shown) formed in the peripheral surface
Is provided. The platinum group oxide is Pt,
Oxides such as Rd and Ru are used, and as oxide-based ceramics, rutile type or anatase type titanium oxide is used. The functional details of the first septic tank 21 will be described later.

【0021】第2循環管路31は、一端を第1循環管路
11の循環用ポンプ12と第1電磁弁13との間に接続
され、また他端を第1循環管路11の第2電磁弁16と
第2電磁弁17の間に接続され、第1循環管路11をバ
イパスしている。この第2循環管路31には、循環用ポ
ンプ12側の接続端から順に電磁式の開閉弁32(以
下、第5電磁弁という)と、後述する第2浄化槽41が
介装されている。また、第2浄化槽41と第5電磁弁3
2との間には、電磁式の開閉弁33(以下、第6電磁弁
という)が介装された排水管路34が接続されている。
The second circulation line 31 has one end connected between the circulation pump 12 of the first circulation line 11 and the first electromagnetic valve 13, and the other end connected to the second circulation line of the first circulation line 11. It is connected between the solenoid valve 16 and the second solenoid valve 17, and bypasses the first circulation line 11. An electromagnetic opening / closing valve 32 (hereinafter referred to as a fifth electromagnetic valve) and a second septic tank 41, which will be described later, are provided in this second circulation pipeline 31 in order from the connection end on the circulation pump 12 side. In addition, the second septic tank 41 and the fifth solenoid valve 3
A drain pipe line 34 in which an electromagnetic on-off valve 33 (hereinafter, referred to as a sixth electromagnetic valve) is interposed is connected between the first and second terminals.

【0022】第2浄化槽41は、図5にも示すように、
下面中央に入口42aを有する下部材42と、上面中央
に出口43aを有し下部材42に着脱可能に螺着された
上部材43と、上・下部材42,43内にその周縁を挟
着されたストレ−ナ44とから構成されている。
The second septic tank 41, as shown in FIG.
A lower member 42 having an inlet 42a at the center of the lower surface, an upper member 43 having an outlet 43a at the center of the upper surface and being detachably screwed to the lower member 42, and its peripheral edge sandwiched between the upper and lower members 42, 43. And a strainer 44 that has been formed.

【0023】再生管路51は、一端を第1電磁弁13の
出口ポ−トに、また他端を第1浄化槽21の温水導入口
22cに接続されている。この再生管路51には後述す
る温水生成槽61が介装されている。
One end of the regeneration pipe line 51 is connected to the outlet port of the first electromagnetic valve 13, and the other end is connected to the hot water inlet port 22c of the first septic tank 21. A hot water production tank 61, which will be described later, is interposed in the regeneration pipeline 51.

【0024】温水生成槽61は、図4にも示すように、
上面中央に入口62aを下面中央に出口62bを夫々有
する本体槽62と、本体層62の周面に付設されたパネ
ル状の電熱ヒ−タ63と、本体層62の内壁に設けられ
たサ−ミスタ等の温度センサ64と、本体層62内に配
置されたフロ−トスイッチ等の水位センサ65とから構
成されている。この温水生成槽61における機能詳細は
後述する。
The hot water producing tank 61, as shown in FIG.
A main body tank 62 having an inlet 62a at the center of the upper surface and an outlet 62b at the center of the lower surface, a panel-shaped electric heater 63 attached to the peripheral surface of the main body layer 62, and a server provided on the inner wall of the main body layer 62. It is composed of a temperature sensor 64 such as a mister and a water level sensor 65 such as a float switch arranged in the main body layer 62. The functional details of this hot water production tank 61 will be described later.

【0025】図6には図1に示した浄水システムに係る
電気系回路を示してある。同図において、71はマイク
ロコンピュ−タ構成の制御部、72は運転スイッチ、7
3乃至78は第1乃至第6電磁弁13,16乃至18,
32,33の駆動部、79は揚水用ポンプ4の駆動部、
80は循環用ポンプ12の駆動部、81は塩素発生機6
の駆動部、82は混入用ポンプ7の駆動部、83はオゾ
ン発生機20用の駆動部、84はUVランプ27の駆動
部、85は電熱ヒ−タ63の駆動部であり、2は高置タ
ンク1の水位センサ、64は温水生成層61の温度セン
サ、65は温水生成層61の水位センサである。
FIG. 6 shows an electric system circuit relating to the water purification system shown in FIG. In the figure, 71 is a control unit having a microcomputer configuration, 72 is an operation switch, and 7
3 to 78 are first to sixth solenoid valves 13, 16 to 18,
32 and 33 drive parts, 79 is a drive part of the pump 4 for pumping water,
80 is a drive part of the circulation pump 12, 81 is a chlorine generator 6
Drive unit for the mixing pump 7, 83 drive unit for the ozone generator 20, 84 drive unit for the UV lamp 27, 85 drive unit for the electrothermal heater 63, and 2 is a high drive unit. The water level sensor of the stationary tank 1, 64 is a temperature sensor of the hot water generating layer 61, and 65 is a water level sensor of the hot water generating layer 61.

【0026】上記の制御部71はCPUとプログラムを
格納したメモリ等を具備しており、運転スイッチ72,
水位センサ2,温度センサ64及び水位センサ65の操
作信号及び検知信号に基づき、プログラムに従って各駆
動部73乃至85に制御信号を送出する。
The control unit 71 has a CPU and a memory storing a program, and the like.
Based on the operation signals and detection signals of the water level sensor 2, the temperature sensor 64, and the water level sensor 65, a control signal is sent to each of the drive units 73 to 85 according to a program.

【0027】ここで、図1に示した浄水システムにおけ
る浄水動作を図7乃至図9を参照して説明する。尚、図
7乃至図9での図示を省略したが、高置タンク1内の貯
留水の水位は、水位センサ2の検知信号に基づく揚水用
ポンプ4の断続作動によって所定の高水位に近づくよう
に制御される。また、高置タンク1から給水管路5に送
り込まれる水には、塩素発生機6からポンプ7を介して
所定濃度の塩素が混入される。
Here, the water purification operation in the water purification system shown in FIG. 1 will be described with reference to FIGS. 7 to 9. Although not shown in FIGS. 7 to 9, the water level of the stored water in the high tank 1 approaches a predetermined high water level by the intermittent operation of the pump 4 for pumping water based on the detection signal of the water level sensor 2. Controlled by. Further, the water sent from the elevated tank 1 to the water supply pipe 5 is mixed with chlorine of a predetermined concentration from the chlorine generator 6 via the pump 7.

【0028】運転スイッチ72がオン操作されると、ま
ず、第3電磁弁17及び第5電磁弁32が開かれ、他の
電磁弁13,16,18,33が閉じられて、循環用ポ
ンプ12が作動される(図7のs1乃至s3)。これに
より、高置タンク1内の貯留水が図1の破線矢印に従っ
て第2循環管路31を循環し、第2浄化槽41内に送り
込まれた循環水はストレ−ナ44で比較的大きなごみ,
錆,藻類等を除去される。この循環は所定時間ts、例
えば1分間だけ継続して行なわれる(図6のs4)。
When the operation switch 72 is turned on, first, the third solenoid valve 17 and the fifth solenoid valve 32 are opened and the other solenoid valves 13, 16, 18, 33 are closed, and the circulation pump 12 is closed. Are operated (s1 to s3 in FIG. 7). As a result, the stored water in the high tank 1 circulates through the second circulation pipeline 31 according to the broken line arrow in FIG. 1, and the circulating water sent into the second septic tank 41 is relatively large dust in the strainer 44.
Removes rust and algae. This circulation is continuously performed for a predetermined time ts, for example, 1 minute (s4 in FIG. 6).

【0029】時間経過後は、第1電磁弁13が第1浄化
槽21側に切換えられ、第2電磁弁16が開かれると共
に、第5電磁弁32が閉じられる。また、オゾン発生機
20が作動され、UVランプ27が点灯される(図6の
s5乃至s7)。
After a lapse of time, the first electromagnetic valve 13 is switched to the first septic tank 21 side, the second electromagnetic valve 16 is opened, and the fifth electromagnetic valve 32 is closed. Further, the ozone generator 20 is activated and the UV lamp 27 is turned on (s5 to s7 in FIG. 6).

【0030】これにより、高置タンク1内の貯留水が図
1の実線矢印に従って第1循環管路11を循環し、ベン
チュリ管14位置では循環水にオゾンが混入され、該オ
ゾンによって細菌が死滅する。また、第1浄化槽21内
に送り込まれた循環水は、プレフィルタ24で上記より
も小さなごみ,錆,藻類等を除去されると共に、吸着層
25及び触媒層26で臭気や次亜塩素塩,有機塩素化合
物等を吸着されて除去され、さらにUVランプ27から
の紫外線によって細菌が死滅する。本例では、活性炭か
ら成る吸着層25でトリハロメタン等の有機塩素化合物
が主に吸着され、またゼオライト及び触媒から成る触媒
層26で次亜塩素塩及び陽イオンが主に吸着される。
As a result, the stored water in the high tank 1 circulates through the first circulation line 11 in accordance with the solid line arrow in FIG. 1, ozone is mixed into the circulating water at the position of the venturi pipe 14, and the ozone kills the bacteria. To do. Further, the circulating water sent into the first septic tank 21 is subjected to removal of dust, rust, algae and the like smaller than the above by the pre-filter 24, and at the same time, the adsorption layer 25 and the catalyst layer 26 remove odor and hypochlorous salt, The organic chlorine compound or the like is adsorbed and removed, and the ultraviolet rays from the UV lamp 27 kill bacteria. In this example, an organic chlorine compound such as trihalomethane is mainly adsorbed by the adsorption layer 25 made of activated carbon, and hypochlorite and cations are mainly adsorbed by the catalyst layer 26 made of zeolite and a catalyst.

【0031】高置タンク1の水位センサ2の信号から得
られる貯留水の水位Lが設定水位Ls以上で、且つ単位
時間当りの水位変化量△Aが設定値Aよりも小さくなる
と、つまり建物内における水の消費量が少なく或いは零
になると、オゾン発生機20が停止されると共に、第1
電磁弁13が温水生成槽41側に切換えられ、第2電磁
弁16が閉じられる(図7のs8、図8のs9,s1
0)。これにより、高置タンク1内の貯留水が図1の1
点鎖線矢印に従って再生管路51を通じ温水生成槽61
に送り込まれる。
When the water level L of the stored water obtained from the signal of the water level sensor 2 of the high tank 1 is equal to or higher than the set water level Ls and the water level change amount ΔA per unit time is smaller than the set value A, that is, in the building When the water consumption in the water is low or becomes zero, the ozone generator 20 is stopped and the first
The solenoid valve 13 is switched to the hot water production tank 41 side, and the second solenoid valve 16 is closed (s8 in FIG. 7, s9, s1 in FIG. 8).
0). As a result, the stored water in the high tank 1 is
Hot water generation tank 61 through the regeneration pipe line 51 according to the dashed line arrow
Sent to.

【0032】温水生成槽61内の水位Fが設定水位Fs
まで上昇すると、循環用ポンプ12が停止され、電熱ヒ
−タ63への通電が開始される(図8のs11乃至s1
3)。そして、電熱ヒ−タ63の加熱により温水生成槽
61内の水温が設定水温Ts、例えば70〜80℃にな
ると電熱ヒ−タ63への通電が停止され、第4電磁弁1
8が開かれる(図8のs14乃至s16)。
The water level F in the warm water production tank 61 is the set water level Fs.
When the temperature rises, the circulation pump 12 is stopped, and energization of the electric heat heater 63 is started (s11 to s1 in FIG. 8).
3). Then, when the water temperature in the hot water generation tank 61 reaches the set water temperature Ts, for example, 70 to 80 ° C. by heating the electric heat heater 63, the electricity supply to the electric heat heater 63 is stopped, and the fourth solenoid valve 1
8 is opened (s14 to s16 in FIG. 8).

【0033】これにより、第1浄化槽21内の水が入口
22aから排水管路19を通じて排水され、これに伴っ
て温水生成槽61内の温水が図1の2点鎖線矢印に従っ
て第1浄化槽21内に取り込まれ、吸着層25及び触媒
層26に吸着されている次亜塩素塩及び有機塩素化合物
が温水中に脱離し、これらが触媒層26の白金族系酸化
物及び酸化物系セラミックスの複合物(触媒)に接触し
つつ紫外線を浴びて光触媒反応によって分解され、分解
分を含んだ温水が排水管路19を通じて外部に排出され
る。また、この際、プレフィルタ24に捕獲されている
ごみ,錆,藻類等も水流によって離脱し、上記の分解分
と共に排水管路19を通じて外部に排出される。第4電
磁弁18は温水生成槽61内の温水が排水管路19から
完全に排出されるまで所定時間tsだけ継続して開かれ
る(図8のs17)。
As a result, the water in the first septic tank 21 is drained from the inlet 22a through the drainage conduit 19, and along with this, the hot water in the hot water producing tank 61 follows the two-dot chain line arrow in FIG. The hypochlorite and the organic chlorine compound that are taken into the adsorption layer 25 and adsorbed on the adsorption layer 25 and the catalyst layer 26 are desorbed in warm water, and these are the platinum group-based oxide and oxide-based ceramic composite of the catalyst layer 26. While being in contact with the (catalyst), it is exposed to ultraviolet rays and decomposed by a photocatalytic reaction, and hot water containing the decomposed component is discharged to the outside through the drainage conduit 19. Further, at this time, dust, rust, algae and the like captured by the pre-filter 24 are also separated by the water flow, and are discharged to the outside through the drainage conduit 19 together with the above-mentioned decomposed components. The fourth solenoid valve 18 is continuously opened for a predetermined time ts until the hot water in the hot water producing tank 61 is completely discharged from the drainage pipe 19 (s17 in FIG. 8).

【0034】時間経過後は、第1電磁弁13が第1浄化
槽21側に切換えられ、第2電磁弁16が開かれると共
に、第3電磁弁17及び第4電磁弁18が閉じれられ、
第6電磁弁33が開かれる。また、オゾン発生機20が
作動され、UVランプ27が点灯される(図9のs18
乃至s21)。
After a lapse of time, the first solenoid valve 13 is switched to the first septic tank 21 side, the second solenoid valve 16 is opened, and the third solenoid valve 17 and the fourth solenoid valve 18 are closed,
The sixth solenoid valve 33 is opened. Further, the ozone generator 20 is activated and the UV lamp 27 is turned on (s18 in FIG. 9).
Through s21).

【0035】これにより、高置タンク1内の貯留水が図
1の3点鎖線矢印に従って第1循環管路11に循環し、
上記と同様の浄化,殺菌作用を受けた後に第1循環管路
11から第2循環管路31に流れ込んで第2浄化槽41
を逆流し、ストレ−ナ44に捕獲されているごみ,錆,
藻類等が水流によって離脱し、これらを含んだ水が排水
管路34を通じて外部に排出される。この循環は所定時
間ts、例えば1分間だけ継続して行なわれる(図9の
s22)。時間経過後は第3電磁弁17を開き、第6電
磁弁を閉じて(図9のs23)、ステップs8に戻り運
転スイッチ72がオフ操作されるまで同様の手順が繰り
返される。
As a result, the stored water in the high tank 1 circulates in the first circulation line 11 in accordance with the three-dot chain line arrow in FIG.
After being subjected to the same purification and sterilization action as described above, it flows into the second circulation pipeline 31 from the first circulation pipeline 11 and enters the second purification tank 41.
Backflow, and the dust, rust, and the like captured by the strainer 44
Algae and the like are separated by the water flow, and the water containing these is discharged to the outside through the drainage pipe 34. This circulation is continuously performed for a predetermined time ts, for example, 1 minute (s22 in FIG. 9). After the lapse of time, the third solenoid valve 17 is opened, the sixth solenoid valve is closed (s23 in FIG. 9), the process returns to step s8, and the same procedure is repeated until the operation switch 72 is turned off.

【0036】このように上述の浄水システムによれば、
高置タンク1内の貯留水を第1浄化槽21及び第2浄化
槽41に循環させることにより、該貯留水に含まれるご
み,錆,藻類等をプレフィルタ24及びストレ−ナ44
で、また臭気や次亜塩素塩,有機塩素化合物等を吸着層
25及び触媒層26で夫々除去して、浄化された良質の
水を高置タンク1から建物内の各部屋に常に供給でき
る。
Thus, according to the above water purification system,
By circulating the stored water in the elevated tank 1 to the first septic tank 21 and the second septic tank 41, dust, rust, algae and the like contained in the stored water are pre-filter 24 and strainer 44.
Further, odor, hypochlorite, organic chlorine compounds, etc. are removed by the adsorption layer 25 and the catalyst layer 26, respectively, and purified high-quality water can be constantly supplied from the elevated tank 1 to each room in the building.

【0037】また、ポンプ始動時に高置タンク1内の貯
留水を所定時間第2浄化槽41に先に循環させてから第
1浄化槽21に循環させ浄化するようにしているので、
貯留水を直接第1浄化槽21に送り込む場合に比べて該
浄化槽21の目詰りや機能低下を防止でき、浄化寿命を
向上させることができる。
In addition, when the pump is started, the stored water in the high tank 1 is circulated in the second septic tank 41 for a predetermined time first, and then circulated in the first septic tank 21 for purification.
As compared with the case where the stored water is directly sent to the first septic tank 21, it is possible to prevent clogging and functional deterioration of the septic tank 21, and it is possible to improve the purification life.

【0038】さらに、第1浄化槽21に貯留水を循環さ
せる際に第3電磁弁17を閉じることにより、第2循環
管路31に水を逆流させてストレ−ナ44に捕獲されて
いるごみ,錆,藻類等を該ストレ−ナ44から離脱さ
せ、これらを含んだ水を排水管路から外部に排出できる
ので、ストレ−ナ44の捕獲能力を回復させて第2浄化
槽41における浄化機能を継続して良好に発揮できる。
Further, when the stored water is circulated in the first septic tank 21, the third solenoid valve 17 is closed to cause the water to flow backward through the second circulation pipe line 31 and the dust trapped in the strainer 44, Rust, algae, etc. can be separated from the strainer 44, and water containing these can be discharged to the outside from the drainage pipe, so that the trapping ability of the strainer 44 is restored and the purifying function in the second septic tank 41 is continued. Can be demonstrated well.

【0039】さらにまた、第1浄化槽21への循環時に
はオゾンの混入及び紫外線照射によって循環水中の細菌
を死滅させて、無菌状態の水を供給できる。
Furthermore, during circulation to the first septic tank 21, bacteria in the circulating water can be killed by mixing ozone and irradiating ultraviolet rays, and aseptic water can be supplied.

【0040】さらにまた、高置タンク1内の貯留水を温
水生成槽61に送り込んで加温して該温水を第1浄化槽
21に送り込むことにより、吸着層25及び触媒層26
に吸着されている次亜塩素塩及び有機塩素化合物を温水
中に脱離させて各層25,26の吸着能力を回復させて
再生できるので、吸着層25及び触媒層26の交換を不
要にして第1浄化槽21における浄化機能を継続して良
好に発揮できる。また、この再生時には同時にプレフィ
ルタ24に付着されているごみ,錆,藻類等を水流によ
って離脱させて、プレフィルタ24の捕獲能力も回復で
きる。
Furthermore, the water stored in the high tank 1 is sent to the hot water production tank 61 to be heated and sent to the first purification tank 21, whereby the adsorption layer 25 and the catalyst layer 26 are supplied.
Since the hypochlorite and the organic chlorine compound adsorbed on the can be desorbed in warm water to restore the adsorption capacity of each layer 25, 26 and regenerated, the adsorption layer 25 and the catalyst layer 26 need not be replaced. The purification function in the 1 septic tank 21 can be continuously and satisfactorily exhibited. Further, at the time of this regeneration, the dust, rust, algae, etc. attached to the pre-filter 24 are simultaneously removed by the water flow, so that the capturing ability of the pre-filter 24 can be restored.

【0041】さらにまた、温水中に脱離した次亜塩素塩
及び有機塩素化合物を触媒層26の触媒及びUVランプ
27の紫外線による光触媒反応によって分解させること
ができるので、有害物質がそのまま外部に排出されるこ
とを防止できる。
Furthermore, the hypochlorous salt and the organic chlorine compound desorbed in the warm water can be decomposed by the photocatalytic reaction of the catalyst of the catalyst layer 26 and the ultraviolet rays of the UV lamp 27, so that harmful substances are directly discharged to the outside. Can be prevented.

【0042】図10には第1浄化槽の他の例を示してあ
る。同図には第1浄化槽91の他に温水生成槽61を示
してあるが、該温水生成槽61の構成は上記のものと同
様である。
FIG. 10 shows another example of the first septic tank. In the figure, a hot water production tank 61 is shown in addition to the first septic tank 91, but the configuration of the hot water production tank 61 is the same as that described above.

【0043】この浄化槽91は、下面中央に入口92a
を下面一側に出口92bを夫々有し、また側面下端に温
水導入口92cを有する本体槽92と、本体層92の中
央に入口92に及んで配置された筒状の案内通路93
と、本体槽92の温水導入口92cよりも上方に配置さ
れた環状の吸着層94と、吸着層94の上側に配置され
た環状のプレフィルタ95と、プレフィルタ95の上側
に配置された環状の整流板96と、案内通路93の内面
に配置された筒状の触媒層97と、触媒層97の内側中
央に配置されたUVランプ98とから構成されている。
吸着層94は繊維状或いは粒状活性炭から形成され、ま
た触媒層97は有底筒状に成形されたゼオライトの表面
に白金族系酸化物及び酸化物系セラミックスの複合物を
担持させて形成されている。尚、白金族系酸化物とした
はPt,Rd,Ru等の酸化物等が、また酸化物系セラ
ミックスとしてはルチル型或いはアナタ−ゼ型の酸化チ
タン等が夫々使用される。
The septic tank 91 has an inlet 92a at the center of the lower surface.
And a main body tank 92 each having an outlet 92b on one side of the lower surface and a hot water inlet 92c at the lower end of the side surface, and a cylindrical guide passage 93 arranged in the center of the main body layer 92 extending to the inlet 92.
A ring-shaped adsorption layer 94 arranged above the hot water inlet 92c of the main body tank 92, a ring-shaped prefilter 95 arranged above the adsorption layer 94, and a ring arranged above the prefilter 95. Of the straightening plate 96, a cylindrical catalyst layer 97 arranged on the inner surface of the guide passage 93, and a UV lamp 98 arranged in the center of the inside of the catalyst layer 97.
The adsorption layer 94 is formed of fibrous or granular activated carbon, and the catalyst layer 97 is formed by supporting a composite of platinum group oxide and oxide ceramics on the surface of zeolite shaped into a bottomed cylinder. There is. As the platinum group oxide, oxides such as Pt, Rd and Ru are used, and as the oxide ceramics, rutile type or anatase type titanium oxide and the like are used.

【0044】浄化時に入口92aから浄化槽92内に送
り込まれた循環水は、案内通路93,整流板96,プレ
フィルタ95,吸着層94の順で流れて出口92bから
送り出される。この流通過程ではUVランプ98からの
紫外線によって細菌が死滅すると共に、吸着層94及び
触媒層97で臭気や次亜塩素塩,有機塩素化合物等を吸
着され、プレフィルタ95でごみ,錆,藻類等を除去さ
れる。上記の第1浄化槽21と同様に、活性炭から成る
吸着層95ではトリハロメタン等の有機塩素化合物が主
に吸着され、またゼオライト,白金族系酸化物及び酸化
物系セラミックスから成る触媒層97では次亜塩素塩及
び陽イオンが主に吸着される。
The circulating water sent from the inlet 92a into the septic tank 92 at the time of purification flows in the order of the guide passage 93, the straightening plate 96, the prefilter 95, and the adsorption layer 94, and is sent out from the outlet 92b. In this distribution process, bacteria are killed by the ultraviolet rays from the UV lamp 98, odors, hypochlorite, organic chlorine compounds, etc. are adsorbed by the adsorption layer 94 and the catalyst layer 97, and dust, rust, algae, etc. are adsorbed by the prefilter 95. Is removed. Similar to the above-mentioned first septic tank 21, an organic chlorine compound such as trihalomethane is mainly adsorbed in the adsorption layer 95 made of activated carbon, and a hypochlorite is formed in the catalyst layer 97 made of zeolite, platinum group oxide and oxide ceramics. Chlorine salts and cations are mainly adsorbed.

【0045】また、再生時に温水導入口92cから浄化
槽91内に送り込まれた温水は、吸着層94,プレフィ
ルタ95,整流板96,案内通路93の順で流れて入口
92bから送り出される。この流通過程では、吸着層9
4及び触媒層97に吸着されている次亜塩素塩及び有機
塩素化合物が温水中に脱離し、これらが触媒層97の白
金族系酸化物及び酸化物系セラミックスの複合物(触
媒)に接触しつつ紫外線を浴びて光触媒反応によって分
解される。また、この際、プレフィルタ95に捕獲され
ているごみ,錆,藻類等が水流によって離脱し上記の分
解分と共に排出される。
The hot water sent into the septic tank 91 from the hot water inlet 92c during regeneration flows in the order of the adsorption layer 94, the prefilter 95, the straightening plate 96, and the guide passage 93, and is sent out from the inlet 92b. In this distribution process, the adsorption layer 9
4 and the hypochlorite salt and the organic chlorine compound adsorbed on the catalyst layer 97 are desorbed in warm water, and these come into contact with the platinum group-based oxide and oxide-based ceramic composite (catalyst) of the catalyst layer 97. Meanwhile, it is exposed to ultraviolet rays and decomposed by a photocatalytic reaction. At this time, dust, rust, algae and the like captured by the pre-filter 95 are separated by the water flow and are discharged together with the decomposed components.

【0046】尚、上述の実施例では第2浄化槽内にスト
レ−ナを配置したものを示したが、ストレ−ナはプレフ
ィルタ等の他の濾過材であってもよい。また、第1浄化
槽側の循環浄水回路に再生管路及び温水生成槽から成る
再生回路を組み付けたものを示したが、再生回路を除外
したシステム構成でも高置タンク内の貯留水の浄化を行
なえることは勿論であり、またオゾン発生機及びベンチ
ュリ管を除外しても浄化槽内のUVランプを点灯してお
けば紫外線によって殺菌を行なうことが可能である。さ
らに、ポンプ始動時に第2浄化槽への循環を先に開始す
るようにしたものを示したが、該循環はポンプ運転中に
所定時間毎に行なうようにしてもよい。さらにまた、建
物内における水の消費量が少なく或いは零になった際に
第1浄化槽の吸着層等の再生を開始し、この後に第2浄
化槽のストレ−ナの再生を行なうようにしたものを示し
たが、両再生は夜間または所定時間毎に、しかも別々に
行なうようにしてもよく、また重金属イオンや細菌の濃
度に比例する水の導電率が所定範囲を越えた際に開始す
るようにしてもよい。さらにまた、温水生成槽の電熱ヒ
−タは他の熱源や排熱を利用した装置等であってもよ
い。
Although the strainer is disposed in the second septic tank in the above-mentioned embodiment, the strainer may be another filtering material such as a prefilter. Also, the circulation water purification circuit on the side of the first septic tank is shown with a regeneration circuit composed of a regeneration pipe and a hot water generation tank, but the system configuration without the regeneration circuit can also purify the stored water in the high tank. Of course, even if the ozone generator and the Venturi tube are excluded, if the UV lamp in the septic tank is turned on, the sterilization can be performed by ultraviolet rays. Further, although the one in which the circulation to the second septic tank is started first when the pump is started is shown, the circulation may be performed at every predetermined time during the pump operation. Furthermore, when the amount of water consumed in the building is low or has become zero, the regeneration of the adsorption layer of the first septic tank and the like is started, and then the strainer of the second septic tank is regenerated. As shown, both regenerations may be performed at night or at predetermined time intervals and separately, and should be started when the conductivity of water, which is proportional to the concentration of heavy metal ions or bacteria, exceeds a predetermined range. May be. Furthermore, the electric heat heater of the hot water producing tank may be another heat source or a device utilizing waste heat.

【0047】[0047]

【発明の効果】以上詳述したように請求項1に係る浄水
システムによれば、貯水タンク内の水を第1浄化槽及び
第2浄化槽に適宜循環させることにより、該貯留水に含
まれる不純物を濾過材で除去して浄化された良質の水を
貯水タンクから供給できる。また、貯水タンク内の水を
第2浄化槽に先に循環させてから第1浄化槽に循環させ
浄化することができるので、貯留水を直接第1浄化槽に
送り込む場合に比べて該浄化槽の目詰りや機能低下を防
止でき、浄化寿命を向上させることができる。
As described above in detail, according to the water purification system of the first aspect, the water contained in the water storage tank is appropriately circulated to the first septic tank and the second septic tank to remove impurities contained in the stored water. High-quality water that has been purified by removing it with a filter material can be supplied from a water storage tank. Further, since the water in the water storage tank can be circulated through the second septic tank first and then circulated to the first septic tank for purification, clogging of the septic tank can be prevented as compared with the case where the stored water is directly sent to the first septic tank. It is possible to prevent functional deterioration and improve the purification life.

【0048】請求項2に係る浄水システムによれば、第
2循環管路に水を逆流させて濾過材に捕獲されている不
純物を該濾過材から離脱させ、これらを含んだ水を排水
管路から外部に排出できるので、濾過材の捕獲能力を回
復させて第2浄化槽における浄化機能を継続して良好に
発揮できる。
According to the water purification system of the second aspect, the water is made to flow backward through the second circulation pipe to separate the impurities captured by the filter medium from the filter medium, and the water containing them is drained. Since it can be discharged from the outside to the outside, it is possible to restore the trapping ability of the filter medium and continue to exert the purifying function in the second septic tank well.

【0049】請求項3に係る浄水システムによれば、第
1浄化槽への循環時にオゾンを混入して循環水中の細菌
を死滅させることができ、無菌状態の水を建物内の各部
屋に供給できる。
According to the water purification system of the third aspect, ozone can be mixed during the circulation to the first septic tank to kill the bacteria in the circulation water, and aseptic water can be supplied to each room in the building. .

【0050】請求項4に係る浄水システムによれば、貯
水タンク内の水を温水生成槽を通じて加温して浄化槽に
送り込むことにより、吸着剤に吸着されている次亜塩素
塩及び有機塩素化合物を温水中に脱離させその吸着能力
を回復させて再生できるので、吸着剤の交換を不要にし
て第1浄化槽における浄化機能を継続して良好に発揮で
きる。
According to the water purification system of the fourth aspect, the water in the water storage tank is heated through the hot water generation tank and sent to the purification tank to remove the hypochlorite salt and the organic chlorine compound adsorbed by the adsorbent. Since the adsorbent can be desorbed in warm water to recover its adsorption capacity and can be regenerated, the adsorbent need not be replaced, and the purifying function in the first septic tank can be continuously exerted well.

【0051】請求項5に係る浄水システムによれば、上
記再生時に温水中に脱離した次亜塩素塩及び有機塩素化
合物を触媒及び紫外線による光触媒反応によって分解で
きるので、有害物質がそのまま外部に排出されることを
防止できる。
According to the water purification system of claim 5, the hypochlorite and the organic chlorine compound desorbed in the warm water at the time of the regeneration can be decomposed by the photocatalytic reaction by the catalyst and the ultraviolet rays, so that the harmful substances are directly discharged to the outside. Can be prevented.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明を適用した浄水システムの概略構成図FIG. 1 is a schematic configuration diagram of a water purification system to which the present invention is applied.

【図2】図1に示した塩素発生機の断面図FIG. 2 is a sectional view of the chlorine generator shown in FIG.

【図3】図1に示したベンチュリ管の断面図FIG. 3 is a sectional view of the Venturi tube shown in FIG.

【図4】図1に示した第1浄化槽及び温水生成槽の断面
FIG. 4 is a cross-sectional view of the first septic tank and the hot water producing tank shown in FIG.

【図5】図1に示した第2浄化槽の断面図5 is a cross-sectional view of the second septic tank shown in FIG.

【図6】浄水システムの電気系回路のブロック図FIG. 6 is a block diagram of an electric circuit of the water purification system.

【図7】浄水制御のフロ−チャ−ト[Figure 7] Flow chart for water purification control

【図8】浄水制御のフロ−チャ−ト[Figure 8] Flow chart for water purification control

【図9】浄水制御のフロ−チャ−ト[Fig. 9] Flow chart for water purification control

【図10】第1浄化槽の他の例を示す断面図FIG. 10 is a cross-sectional view showing another example of the first septic tank.

【符号の説明】[Explanation of symbols]

1…高置タンク、3…揚水管路、5…給水管路、11…
第1循環管路、12…循環用ポンプ、13…第1電磁
弁、16…第2電磁弁、17…第3電磁弁、19…排水
管路、21…浄化層、24…プレフィルタ、25…吸着
層、26…触媒層、27…UVランプ、31…第2循環
管路、41…第2浄化槽、44…ストレ−ナ、51…再
生管路、61…温水生成槽、63…電熱ヒ−タ、71…
制御部、73〜85…駆動部、91…浄化層、94…吸
着層、95…プレフィルタ、97…触媒層、98…UV
ランプ。
1 ... High tank, 3 ... Pumping pipeline, 5 ... Water supply pipeline, 11 ...
1st circulation pipeline, 12 ... Circulation pump, 13 ... 1st solenoid valve, 16 ... 2nd solenoid valve, 17 ... 3rd solenoid valve, 19 ... Drainage pipeline, 21 ... Purification layer, 24 ... Prefilter, 25 Adsorption layer, 26 ... Catalyst layer, 27 ... UV lamp, 31 ... Second circulation line, 41 ... Second septic tank, 44 ... Strainer, 51 ... Regeneration line, 61 ... Hot water generation tank, 63 ... Electrothermal heat -Ta, 71 ...
Control part, 73-85 ... Drive part, 91 ... Purification layer, 94 ... Adsorption layer, 95 ... Prefilter, 97 ... Catalyst layer, 98 ... UV
lamp.

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成4年11月16日[Submission date] November 16, 1992

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0046[Correction target item name] 0046

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0046】尚、上述の実施例では第2浄化槽内にスト
レーナを配置したものを示したが、ストレーナはプレフ
ィルタ等の他の濾過材であってもよい。また、第1浄化
槽側に循環浄水回路に再生管路及び温水生成槽から成る
再生回路を組み付けたものを示したが、再生回路を除外
したシステム構成でも高置タンク内の貯留水の浄化を行
なえることは勿論であり、またオゾン発生機及びベンチ
ュリ管を除外しても浄化槽内のUVランプを点灯してお
けば紫外線によって殺菌を行なうことが可能である。さ
らに、ポンプ始動時に第2浄化槽への循環を先に開始す
るようにしたものを示したが、該循環はポンプ運転中に
所定時間毎に行なうようにしてもよい。さらにまた、建
物内における水の消費量が少なく或いは零になった際に
第1浄化槽の吸着層等の再生を開始し、この後に第2浄
化槽のストレーナの再生を行なうようにしたものを示し
たが、両再生は夜間または所定時間毎に、しかも別々に
行なうようにしてもよく、また重金属イオンや細菌の濃
度に比例する水の導電率が所定範囲を越えた際に開始す
るようにしてもよい。さらにまた、温水生成槽の電熱ヒ
ータは他の熱源や排熱を利用した装置等であってもよ
く、また浄化槽の再生のための脱離手段として温水に代
えて過熱蒸気を利用してもよい。
Although the strainer is arranged in the second septic tank in the above-mentioned embodiment, the strainer may be another filtering material such as a prefilter. Also, the circulation water purification circuit on the side of the first septic tank is shown with a regeneration circuit consisting of a regeneration pipe and a hot water generation tank, but the system configuration without the regeneration circuit can also purify the stored water in the high tank. Of course, even if the ozone generator and the Venturi tube are excluded, if the UV lamp in the septic tank is turned on, the sterilization can be performed by ultraviolet rays. Further, although the one in which the circulation to the second septic tank is started first when the pump is started is shown, the circulation may be performed at every predetermined time during the pump operation. Furthermore, when the consumption of water in the building is low or zero, regeneration of the adsorption layer of the first septic tank etc. is started, and then the strainer of the second septic tank is regenerated. However, both regenerations may be performed at night or at predetermined time intervals and separately, and may be started when the conductivity of water proportional to the concentration of heavy metal ions or bacteria exceeds a predetermined range. Good. Furthermore, the electric heater of the hot water producing tank may be another heat source or a device using waste heat.
In addition, hot water is used as a desorption means for regenerating the septic tank.
Ete but it may also be using superheated steam.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 供給水を一次的に貯留する貯水タンク
と、 貯水タンクに各端部を接続された第1循環管路と、 第1循環管路の一接続端寄りに介装されたポンプと、 第1循環管路のポンプの出口側に介装された濾過材内蔵
の第1浄化槽と、 第1循環管路の第1浄化槽の出口側に介装された開閉弁
と、 第1循環管路のポンプの出口側と開閉弁の出口側をバイ
パスする第2循環管路と、 第2循環管路に介装された濾過材内蔵の第2浄化槽とか
ら成る、 ことを特徴とする浄水システム。
1. A water storage tank for temporarily storing supply water, a first circulation pipe having each end connected to the water storage tank, and a pump interposed near one connection end of the first circulation pipe. A first septic tank with a built-in filter medium installed on the outlet side of the pump of the first circulation line; an on-off valve installed on the outlet side of the first septic tank of the first circulation line; and a first circulation A purified water comprising: a second circulation pipe that bypasses the outlet side of the pump and the outlet side of the on-off valve of the pipe line; and a second septic tank with a built-in filter media interposed in the second circulation pipe. system.
【請求項2】 第1循環管路の開閉弁の出口側で且つ第
2循環管路との接続端よりも下流側に介装された第2の
開閉弁と、 第2浄化槽内の水を排出する排水管路とを設けた、 ことを特徴とする請求項1記載の浄水システム。
2. A second opening / closing valve provided on the outlet side of the opening / closing valve of the first circulation pipeline and on the downstream side of a connection end with the second circulation pipeline, and water in the second septic tank. The water purification system according to claim 1, further comprising: a drainage pipe for discharging.
【請求項3】 オゾン発生機のオゾン送出口を第1循環
管路に接続した、 ことを特徴とする請求項1または2記載の浄水システ
ム。
3. The water purification system according to claim 1 or 2, wherein an ozone outlet of the ozone generator is connected to the first circulation line.
【請求項4】 第1浄化槽内に吸着剤を配置すると共
に、第1循環管路のポンプの出口側から流路切換用の弁
を介して分岐され第1浄化槽に至る再生管路と、 再生管路に介装されたヒ−タ付きの温水生成槽と、 第1浄化槽内の水を排出する排水管路とを設けた、 ことを特徴とする請求項1乃至3何れか1項記載の浄水
システム。
4. A regeneration conduit, in which an adsorbent is disposed in the first septic tank, and a branch pipe is branched from the outlet side of the pump of the first circulation conduit via a valve for switching the passage to the first septic tank, The hot water production tank with a heater interposed in the pipeline, and a drainage pipeline for discharging the water in the first septic tank are provided. Water purification system.
【請求項5】 紫外線を照射可能な殺菌ランプを第1浄
化槽内に配置すると共に、 白金族系酸化物及び酸化物系セラミックスを主成分とす
る触媒を殺菌ランプの周囲に配設した、 ことを特徴とする請求項4記載の浄水システム。
5. A sterilization lamp capable of irradiating ultraviolet rays is arranged in the first septic tank, and a catalyst containing platinum group oxide and oxide ceramics as main components is arranged around the sterilization lamp. The water purification system according to claim 4, which is characterized.
JP4199869A 1992-07-27 1992-07-27 Water purifying system Pending JPH0639371A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4199869A JPH0639371A (en) 1992-07-27 1992-07-27 Water purifying system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4199869A JPH0639371A (en) 1992-07-27 1992-07-27 Water purifying system

Publications (1)

Publication Number Publication Date
JPH0639371A true JPH0639371A (en) 1994-02-15

Family

ID=16414993

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4199869A Pending JPH0639371A (en) 1992-07-27 1992-07-27 Water purifying system

Country Status (1)

Country Link
JP (1) JPH0639371A (en)

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