JPH0639372A - Water purification system - Google Patents
Water purification systemInfo
- Publication number
- JPH0639372A JPH0639372A JP4199871A JP19987192A JPH0639372A JP H0639372 A JPH0639372 A JP H0639372A JP 4199871 A JP4199871 A JP 4199871A JP 19987192 A JP19987192 A JP 19987192A JP H0639372 A JPH0639372 A JP H0639372A
- Authority
- JP
- Japan
- Prior art keywords
- water
- tank
- purification system
- septic tank
- pipe
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 176
- 238000000746 purification Methods 0.000 title claims abstract description 38
- 238000003860 storage Methods 0.000 claims abstract description 16
- 239000008400 supply water Substances 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims abstract description 3
- 239000003054 catalyst Substances 0.000 claims description 29
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 17
- 239000011224 oxide ceramic Substances 0.000 claims description 8
- 229910052574 oxide ceramic Inorganic materials 0.000 claims description 8
- 229910001924 platinum group oxide Inorganic materials 0.000 claims description 8
- 239000003463 adsorbent Substances 0.000 claims description 6
- 230000001678 irradiating effect Effects 0.000 claims description 3
- 230000001954 sterilising effect Effects 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- 241000195493 Cryptophyta Species 0.000 abstract description 10
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 abstract description 10
- 239000000428 dust Substances 0.000 abstract description 9
- 238000001179 sorption measurement Methods 0.000 description 21
- 238000011045 prefiltration Methods 0.000 description 14
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 13
- 150000004045 organic chlorine compounds Chemical class 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 11
- 241000894006 Bacteria Species 0.000 description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 229910052801 chlorine Inorganic materials 0.000 description 8
- 239000000460 chlorine Substances 0.000 description 8
- 230000008929 regeneration Effects 0.000 description 8
- 238000011069 regeneration method Methods 0.000 description 8
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 238000005086 pumping Methods 0.000 description 6
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titanium dioxide Inorganic materials O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 6
- 238000013032 photocatalytic reaction Methods 0.000 description 5
- 229910021536 Zeolite Inorganic materials 0.000 description 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 4
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical class ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 description 4
- 230000001172 regenerating effect Effects 0.000 description 4
- 239000010457 zeolite Substances 0.000 description 4
- 230000006870 function Effects 0.000 description 3
- 235000019645 odor Nutrition 0.000 description 3
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 3
- 150000001768 cations Chemical class 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 1
- 150000001804 chlorine Chemical class 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- QBWCMBCROVPCKQ-UHFFFAOYSA-N chlorous acid Chemical class OCl=O QBWCMBCROVPCKQ-UHFFFAOYSA-N 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- -1 hypochlorite ions Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000011403 purification operation Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Filtration Of Liquid (AREA)
- Water Treatment By Sorption (AREA)
Abstract
(57)【要約】
【目的】 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。
【構成】 供給水を一次的に貯留する貯水タンク1と、
貯水タンク1に各端部を接続された循環管路11と、循
環管路11に介装されたポンプ12と、循環管路11に
介装された濾過材内蔵の浄化槽21とから浄水システム
を構成しているので、ポンプ12を作動し貯水タンク1
内の水を浄化槽21に循環させることにより、該貯留水
に含まれるごみ,錆,藻類等を濾過材で除去できる。
(57) [Summary] [Purpose] To provide a water purification system capable of appropriately purifying water supplied from a storage tank such as an elevated tank. [Structure] A water storage tank 1 for temporarily storing supply water,
A water purification system is constructed from a circulation pipeline 11 having each end connected to the water storage tank 1, a pump 12 interposed in the circulation pipeline 11, and a septic tank 21 with a built-in filter medium interposed in the circulation pipeline 11. Since it is configured, the pump 12 is activated to operate the water storage tank 1
By circulating the water in the septic tank 21, dust, rust, algae, etc. contained in the stored water can be removed by a filter material.
Description
【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循環管路と、循環
管路に介装されたポンプと、循環管路に介装された濾過
材内蔵の浄化槽とから、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 supply water, a circulation pipeline having each end connected to the water storage tank, and a circulation pipeline. A water purification system is composed of a pump installed in the water tank and a septic tank with a built-in filter media installed in the circulation pipeline.
【0006】請求項2では、請求項1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循環管路に
接続している。According to a second aspect, in the water purification system according to the first aspect, the ozone outlet of the ozone generator is connected to the circulation pipe line.
【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、浄化槽内に吸着剤を配置すると共
に、循環管路のポンプ出口側から流路切換用の弁を介し
て分岐され浄化槽に至るバイパス管路と、バイパス管路
に介装されたヒ−タ付きの温水生成槽と、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 third aspect of the present invention, in the water purification system according to the first or second aspect, an adsorbent is arranged in the septic tank, and the adsorbent is branched from the pump outlet side of the circulation pipe through a passage switching valve to the septic tank. There are provided a bypass pipeline, a hot water generating tank with a heater interposed in the bypass pipeline, and a drain pipeline for discharging water in the septic tank.
【0008】請求項4では、請求項3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 fourth aspect of the present invention, in the water purification system according to the third aspect, a sterilizing lamp capable of irradiating ultraviolet rays is arranged in the septic tank, and the catalyst containing platinum group oxides and oxide ceramics as main components is sterilized. It is arranged around the lamp.
【0009】[0009]
【作用】請求項1に係る浄水システムでは、ポンプを作
動し貯水タンク内の水を浄化槽に循環させることによ
り、該貯留水に含まれるごみ,錆,藻類等を濾過材で除
去できる。In the water purification system according to the first aspect, by operating the pump to circulate the water in the water storage tank to the septic tank, dust, rust, algae and the like contained in the water storage can be removed by the filter medium.
【0010】請求項2に係る浄水システムでは、循環管
路を流れる水にオゾンを混入することにより、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 second aspect, bacteria contained in the stored water can be killed by mixing ozone into the water flowing through the circulation pipeline.
【0011】請求項3に係る浄水システムでは、弁切換
えによって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、脱離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 the third aspect of the present invention, the water in the water storage tank is heated by the valve switching through the hot water generation tank and sent to the purification tank, whereby the hypochlorite and the organic chlorine compound adsorbed by the adsorbent are provided. Can be desorbed in warm water, and the water containing the desorbed water can be discharged to the outside from the drain pipe.
【0012】請求項4に係る浄水システムでは、請求項
3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 4, the hypochlorous salt and the organochlorine compound desorbed in warm water are decomposed by a catalyst and a photocatalytic reaction by ultraviolet rays by the same action as in claim 3, and the decomposed component is contained. Water can be discharged to the outside from the drain pipe.
【0013】[0013]
【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は循環管路、21は浄化槽、31はバイパス管路、
41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 circulation line, 21 is a septic tank, 31 is a bypass line,
Reference numeral 41 is a hot water production tank.
【0014】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及び受水タンク(図示省
略)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 elevated tank 1 is installed on a rooftop of a building such as a condominium or an 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 pipeline 3 that reaches the basement of the building is connected to the upper surface of the elevated tank 1, and the other end of the pumping pipeline 2 is a pumping pump 4 and a receiving tank (not shown in the figure) that are disposed underground. ) 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.
【0015】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 in 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.
【0016】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、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、後述する浄化槽21と、電磁式の開閉弁16
(以下、第2電磁弁という)が介装されている。また、
逆止弁15と浄化槽21の間には、電磁式の開閉弁17
(以下、第3電磁弁という)が介装された排水管路18
が接続されている。The circulation line 11 has one end connected to the lower end of the side surface of the high tank 1 and the other end 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 solenoid valve) 13, a venturi pipe 14, a check valve 15, a septic tank 21 described later, and an electromagnetic on-off valve 16
(Hereinafter, referred to as a second solenoid valve) is provided. Also,
An electromagnetic on-off valve 17 is provided between the check valve 15 and the septic tank 21.
The drainage pipe 18 in which (hereinafter, referred to as a third solenoid valve) is interposed
Are connected.
【0017】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19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19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. Further, the outlet of the ozone generator 19 of a silent discharge type or the like is directly introduced into the introduction hole 14a of the venturi pipe 14 or the relay pipe 1
It is connected via 4b. In the venturi pipe 14, ozone (O3) generated by the ozone generator 19 can be sent into the venturi pipe 14 through the introduction hole 14a and mixed into the circulating water.
【0018】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22
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U
V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,R
d,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。この浄化槽21における機能詳細は後述
する。As shown in FIG. 4, the septic tank 21 has an inlet 22a at the center of the lower surface and an outlet 22b at the center of the upper surface,
Further, the main body tank 22 having a hot water inlet 22c at the lower end of the side
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, A bottomed cylindrical catalyst layer 26 disposed on the upper side of the adsorption layer 25, and a U disposed on the inner center of the catalyst layer 26.
It is composed of a V lamp 27. 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 in a bottomed cylinder. A large number of holes (not shown) are provided in the peripheral surface portion of the formed hole. The platinum group oxides are Pt and R
Oxides such as d and Ru are used, and rutile type or anatase type titanium oxide is used as the oxide ceramics. Details of the function of the septic tank 21 will be described later.
【0019】バイパス管路31は一端を第1電磁弁13
の出口ポ−トに、また他端を浄化槽21の温水導入口2
2cに接続されている。このバイパス管路31には温水
生成槽41が介装されている。One end of the bypass line 31 has the first solenoid valve 13
Of the septic tank 21 to the outlet port of
2c is connected. A hot water production tank 41 is provided in the bypass pipe 31.
【0020】温水生成槽41は、図4にも示すように、
上面中央に入口42aを下面中央に出口42bを夫々有
する本体槽42と、本体層42の周面に付設されたパネ
ル状の電熱ヒ−タ43と、本体層42の内壁に設けられ
たサ−ミスタ等の温度センサ44と、本体層42内に配
置されたフロ−トスイッチ等の水位センサ45とから構
成されている。この温水生成槽41における機能詳細は
後述する。The hot water producing tank 41, as shown in FIG.
A main body tank 42 having an inlet 42a in the center of the upper surface and an outlet 42b in the center of the lower surface, a panel-shaped electric heater 43 attached to the peripheral surface of the main body layer 42, and a server provided on the inner wall of the main body layer 42. It is composed of a temperature sensor 44 such as a mister and a water level sensor 45 such as a float switch arranged in the main body layer 42. The functional details of this hot water production tank 41 will be described later.
【0021】図5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、51はマイク
ロコンピュ−タ構成の制御部、52は運転スイッチ、5
3乃至55は第1乃至第3電磁弁13,16,17の駆
動部、56は揚水用ポンプ4の駆動部、57は循環用ポ
ンプ12の駆動部、58は塩素発生機6用の駆動部、5
9は混入用ポンプ7の駆動部、60はオゾン発生機19
の駆動部、61はUVランプ27の駆動部、62は電熱
ヒ−タ43の駆動部であり、2は高置タンク1の水位セ
ンサ、44は温水生成層41の温度センサ、45は温水
生成層41の水位センサである。FIG. 5 shows an electric system circuit relating to the water purification system shown in FIG. In the figure, 51 is a control unit having a microcomputer configuration, 52 is an operation switch, 5
Reference numerals 3 to 55 are drive units for the first to third solenoid valves 13, 16, 17; 56 is a drive unit for the pump 4 for pumping water; 57 is a drive unit for the circulation pump 12; and 58 is a drive unit for the chlorine generator 6. 5,
Reference numeral 9 is a drive unit of the mixing pump 7, and 60 is an ozone generator 19.
, 61 is a drive unit for the UV lamp 27, 62 is a drive unit for the electric heater 43, 2 is a water level sensor of the high tank 1, 44 is a temperature sensor of the hot water generation layer 41, and 45 is hot water generation. Water level sensor for layer 41.
【0022】上記の制御部51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52,
水位センサ2,温度センサ44及び水位センサ45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53乃至61に制御信号を送出する。The control unit 51 has a CPU and a memory storing programs, and the like.
Based on the operation signal and the detection signal of the water level sensor 2, the temperature sensor 44, and the water level sensor 45, a control signal is sent to each of the drive units 53 to 61 according to a program.
【0023】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6を参照して説明する。尚、図6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。Now, the water purification operation in the water purification system shown in FIG. 1 will be described with reference to FIG. Although not shown in FIG. 6, the water level of the stored water in the high tank 1 is controlled to approach 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. It 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.
【0024】運転スイッチ52がオン操作されると、第
1電磁弁13が浄化槽21側に切換えられ、第2電磁弁
16が開かれ、また第3電磁弁17が閉じられる。これ
と共にオゾン発生機19が作動され、UVランプ27が
点灯されて、循環用ポンプ12が作動される(図6のs
1乃至s5)。When the operation switch 52 is turned on, the first solenoid valve 13 is switched to the septic tank 21 side, the second solenoid valve 16 is opened, and the third solenoid valve 17 is closed. Along with this, the ozone generator 19 is operated, the UV lamp 27 is turned on, and the circulation pump 12 is operated (s in FIG. 6).
1 to s5).
【0025】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循環管路11に送り込まれて循環
する。ベンチュリ管14位置では循環管路11を流れる
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、入口22aから浄化槽21内に送り込まれた
循環水は、プレフィルタ24でごみ,錆,藻類等を除去
され、また吸着層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U
V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 is sent to the circulation pipeline 11 and circulated according to the solid line arrow in FIG. At the position of the venturi pipe 14, ozone is mixed into the water flowing through the circulation pipe 11, and the ozone kills the bacteria. Further, the circulating water sent into the septic tank 21 from the inlet 22a is subjected to removal of dust, rust, algae, etc. by the prefilter 24, and odors, hypochlorite, organic chlorine compounds, etc. are adsorbed by the adsorption layer 25 and the catalyst layer 26. Is absorbed and removed, and further U
Ultraviolet rays from the V lamp 27 kill the 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.
【0026】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19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6のs6乃至s8)。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
循環管路11からバイパス管路31を通じて温水生成槽
41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 19 is stopped and the first
The electromagnetic valve 13 is switched to the hot water production tank 41 side, and the second electromagnetic valve 16 is closed (s6 to s8 in FIG. 6). As a result, the stored water in the high tank 1 is sent from the circulation pipeline 11 to the hot water production tank 41 through the bypass pipeline 31 according to the broken line arrow in FIG.
【0027】温水生成槽41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43への通電が開始される(図6のs9乃至s1
1)。そして、電熱ヒ−タ43の加熱により温水生成槽
41内の水温が設定水温Ts、例えば70〜80℃にな
ると電熱ヒ−タ43への通電が停止され、第3電磁弁1
7が開かれる(図6のs12乃至s14)。The water level F in the warm water production tank 41 is the set water level Fs.
When the temperature rises to 0, the circulation pump 12 is stopped, and energization to the electric heating heater 43 is started (s9 to s1 in FIG. 6).
1). Then, when the water temperature in the hot water generation tank 41 reaches the set water temperature Ts, for example, 70 to 80 ° C. by heating the electric heat heater 43, the electric power supply to the electric heat heater 43 is stopped, and the third solenoid valve 1
7 is opened (s12 to s14 in FIG. 6).
【0028】これにより、浄化槽21内の水が入口22
aから排水管路18を通じて排水され、これに伴って温
水生成槽41内の温水が図1の1点鎖線矢印に従って浄
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18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18を通じて外部に排出される。As a result, the water in the septic tank 21 enters the inlet 22.
The water is discharged from a through the drainage pipe 18, and accordingly, the hot water in the hot water producing tank 41 is taken into the septic tank 21 according to the one-dot chain line arrow in FIG. 1, and is adsorbed by the adsorption layer 25 and the catalyst layer 26. Chlorite salts and organic chlorine compounds are desorbed in warm water, and these are decomposed by photocatalytic reaction by being exposed to ultraviolet rays while contacting the composite (catalyst) of the platinum group oxide and oxide ceramics of the catalyst layer 26, Hot water containing the decomposed components is discharged to the outside through the drainage pipe 18. At this time, dust, rust, and the like captured by the pre-filter 24
The algae and the like are also separated by the water flow, and are discharged to the outside through the drainage pipe 18 together with the decomposed components.
【0029】第3電磁弁17は温水生成槽41内の温水
が排水管路18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6のs15)。時間経過後は
ステップs1に戻り運転スイッチ52がオフ操作される
まで上記の手順が繰り返される。The third electromagnetic valve 17 has a predetermined time ts until the hot water in the hot water producing tank 41 is completely discharged from the drainage pipe 18.
Only it is continuously opened (s15 in FIG. 6). After the lapse of time, the process returns to step s1 and the above procedure is repeated until the operation switch 52 is turned off.
【0030】このように上述の浄水システムによれば、
第1電磁弁13を浄化槽21側に切換え第2電磁弁16
を開いた状態で循環用ポンプ11を作動し、高置タンク
1内の貯留水を浄化槽21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
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,
The first solenoid valve 13 is switched to the septic tank 21 side, and the second solenoid valve 16
The circulating pump 11 is operated in the open state to circulate the stored water in the high tank 1 to the septic tank 21 to remove dust, rust, algae and the like contained in the stored water from the pre-filter 24.
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.
【0031】また、上記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
状態の水を建物内の各部屋に供給できる。Further, during the above circulation, bacteria in the circulating water can be killed by mixing ozone and irradiating with ultraviolet rays, and aseptic water can be supplied to each room in the building.
【0032】さらに、第1電磁弁13を浄化槽21側に
切換え第2電磁弁16を開いた状態で循環用ポンプ11
を作動し、高置タンク1内の貯留水を温水生成槽41に
送り込んで加温して該温水を浄化槽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上記の浄化
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,
藻類等を離脱させて、プレフィルタ24の捕獲能力も回
復できる。Further, with the first electromagnetic valve 13 switched to the septic tank 21 side and the second electromagnetic valve 16 opened, the circulation pump 11
Is operated to feed the stored water in the high-place tank 1 to the hot water generation tank 41 to heat it and feed the hot water to the purification tank 21, whereby the hypochlorous salt adsorbed in the adsorption layer 25 and the catalyst layer 26 is adsorbed. Also, since the organic chlorine compound can be desorbed in warm water to restore the adsorption capacity of each layer 25, 26 and can be regenerated, replacement of the adsorption layer 25 and the catalyst layer 26 becomes unnecessary, and the above-mentioned purification function can be continued and improved satisfactorily. Can be demonstrated. Also, at the time of this regeneration, dust, rust,
The capturing ability of the pre-filter 24 can be restored by removing algae or the like.
【0033】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, since the hypochlorite salt and the organic chlorine compound desorbed in the warm water can be decomposed by the catalyst of the catalyst layer 26 and the photocatalytic reaction by the ultraviolet rays of the UV lamp 27, harmful substances are directly discharged to the outside. Can be prevented.
【0034】図7には浄化槽の他の例を示してある。同
図には浄化槽71の他に温水生成槽41を示してある
が、該温水生成槽41の構成は上記のものと同様であ
る。FIG. 7 shows another example of the septic tank. In the figure, a hot water production tank 41 is shown in addition to the septic tank 71, but the configuration of the hot water production tank 41 is the same as that described above.
【0035】この浄化槽71は、下面中央に入口72a
を下面一側に出口72bを夫々有し、また側面下端に温
水導入口72cを有する本体槽72と、本体層72の中
央に入口72に及んで配置された筒状の案内通路73
と、本体槽72の温水導入口72cよりも上方に配置さ
れた環状の吸着層74と、吸着層74の上側に配置され
た環状のプレフィルタ75と、プレフィルタ75の上側
に配置された環状の整流板76と、案内通路73の内面
に配置された筒状の触媒層77と、触媒層77の内側中
央に配置されたUVランプ78とから構成されている。
吸着層74は繊維状或いは粒状活性炭から形成され、ま
た触媒層77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 71 has an inlet 72a at the center of the lower surface.
, A main body tank 72 having outlets 72b on one side of the lower surface, and a hot water inlet 72c at the lower end of the side surface, and a cylindrical guide passage 73 arranged in the center of the main body layer 72 extending to the inlet 72.
An annular adsorption layer 74 arranged above the hot water inlet 72c of the main body tank 72, an annular pre-filter 75 arranged above the adsorption layer 74, and an annular arrangement arranged above the pre-filter 75. The flow control plate 76, the tubular catalyst layer 77 arranged on the inner surface of the guide passage 73, and the UV lamp 78 arranged in the center of the inside of the catalyst layer 77.
The adsorption layer 74 is formed of fibrous or granular activated carbon, and the catalyst layer 77 is formed by supporting a complex of platinum group oxide and oxide ceramics on the surface of zeolite shaped like 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.
【0036】浄化時に入口72aから浄化槽72内に送
り込まれた循環水は、案内通路73,整流板76,プレ
フィルタ75,吸着層74の順で流れて出口72bから
送り出される。この流通過程ではUVランプ78からの
紫外線によって細菌が死滅すると共に、吸着層74及び
触媒層77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75でごみ,錆,藻類等を除去さ
れる。上記の浄化槽21と同様に、活性炭から成る吸着
層75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77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 72a into the septic tank 72 at the time of purification flows in the order of the guide passage 73, the straightening plate 76, the prefilter 75, and the adsorption layer 74, and is sent out from the outlet 72b. In this distribution process, bacteria are killed by the ultraviolet rays from the UV lamp 78, and odor, hypochlorite, organic chlorine compounds, etc. are adsorbed by the adsorption layer 74 and the catalyst layer 77, and dust, rust, algae, etc. are adsorbed by the prefilter 75. Is removed. Similar to the septic tank 21, the organic chlorine compound such as trihalomethane is mainly adsorbed in the adsorption layer 75 made of activated carbon, and the hypochlorite salt is made in the catalyst layer 77 made of zeolite, platinum group oxide and oxide ceramics. And cations are mainly adsorbed.
【0037】また、再生時に温水導入口72cから浄化
槽71内に送り込まれた温水は、吸着層74,プレフィ
ルタ75,整流板76,案内通路73の順で流れて入口
72bから送り出される。この流通過程では、吸着層7
4及び触媒層77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77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75に付着され
ているごみ,錆,藻類等が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 71 from the hot water inlet 72c during regeneration flows in the order of the adsorption layer 74, the prefilter 75, the straightening plate 76, and the guide passage 73, and is sent out from the inlet 72b. In this distribution process, the adsorption layer 7
4 and the hypochlorite salt and the organic chlorine compound adsorbed on the catalyst layer 77 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 77. Meanwhile, it is exposed to ultraviolet rays and decomposed by a photocatalytic reaction. Further, at this time, dust, rust, algae and the like attached to the pre-filter 75 are separated and discharged together with the decomposed components.
【0038】尚、上述の実施例では、浄化槽を具備した
浄水回路に、バイパス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できる。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
再生を開始するようにしたものを示したが、該再生は夜
間または所定時間毎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、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。In the above-mentioned embodiment, the water purification circuit having the septic tank and the regenerating circuit consisting of the bypass pipe and the hot water producing tank are shown. However, even if the regenerating circuit is excluded, the high tank is installed. Of course, the stored water in the inside can be purified, and even if the ozone generator and the Venturi tube are excluded, if the UV lamp in the septic tank is turned on, it can be sterilized by ultraviolet rays. Further, although the one in which the regeneration is started when the consumption of water in the building is low or reaches zero is shown, the regeneration may be performed at night or at every predetermined time. Alternatively, it may be started when the electrical conductivity of water, which is proportional to the concentration of bacteria, exceeds a predetermined range. Further, the electric heat heater of the hot water production tank may be another heat source or a device utilizing waste heat.
【0039】[0039]
【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浄化槽に循環さ
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。As described above in detail, according to the water purification system of claim 1, the water in the water storage tank is circulated to the septic tank to remove dust, rust, algae, etc. contained in the water storage. It is possible to supply high quality purified water from the water storage tank.
【0040】請求項2に係る浄水システムによれば、上
記の循環時にオゾンの混入して循環水中の細菌を死滅さ
せることができ、無菌状態の水を供給できる。According to the water purification system of the second aspect, ozone can be mixed during the above circulation to kill bacteria in the circulating water, and aseptic water can be supplied.
【0041】請求項3に係る浄水システムによれば、弁
切換えによって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
させて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上記の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 third aspect, the water in the water storage tank is heated by the valve switching through the hot water generation tank and sent to the purification tank, so that the hypochlorite salt and the organic matter adsorbed by the adsorbent are discharged. Since the chlorine compound can be desorbed in warm water to recover its adsorption capacity and can be regenerated, it is not necessary to replace the adsorbent and the above-mentioned purification function can be continuously exerted well.
【0042】請求項4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 4, 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に示した浄化槽及び温水生成槽の断面図4 is a cross-sectional view of the septic tank and the hot water production tank shown in FIG.
【図5】浄水システムの電気系回路のブロック図FIG. 5: Block diagram of electric circuit of water purification system
【図6】浄水制御のフロ−チャ−ト[Fig. 6] Flow chart for water purification control
【図7】浄化槽の他の例を示す断面図FIG. 7 is a cross-sectional view showing another example of the septic tank.
1…高置タンク、3…揚水管路、5…給水管路、11…
循環管路、12…循環用ポンプ、18…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…バイパス管路、41
…温水生成槽、43…電熱ヒ−タ、51…制御部、53
〜62…駆動部、71…浄化層、74…吸着層、75…
プレフィルタ、77…触媒層、78…UVランプ。1 ... High tank, 3 ... Pumping pipeline, 5 ... Water supply pipeline, 11 ...
Circulation pipeline, 12 ... Circulation pump, 18 ... Drainage pipeline, 21
... Purification layer, 24 ... Pre-filter, 25 ... Adsorption layer, 26 ...
Catalyst layer, 27 ... UV lamp, 31 ... Bypass conduit, 41
... Warm water generation tank, 43 ... Electric heat heater, 51 ... Control unit, 53
-62 ... drive part, 71 ... purification layer, 74 ... adsorption layer, 75 ...
Pre-filter, 77 ... Catalyst layer, 78 ... UV lamp.
【手続補正書】[Procedure amendment]
【提出日】平成4年11月12日[Submission date] November 12, 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】0038[Correction target item name] 0038
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0038】尚、上述の実施例では、浄化槽を具備した
浄水回路に、バイパス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できる。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
再生を開始するようにしたものを示したが、該再生は夜
間または所定時間毎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、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。In the above-mentioned embodiment, the water purification circuit having the septic tank and the regenerating circuit consisting of the bypass pipe and the hot water producing tank are shown. However, even if the regenerating circuit is excluded, the high tank is installed. Of course, the stored water in the inside can be purified, and even if the ozone generator and the Venturi tube are excluded, if the UV lamp in the septic tank is turned on, it can be sterilized by ultraviolet rays. Further, although the one in which the regeneration is started when the consumption of water in the building is low or reaches zero is shown, the regeneration may be performed at night or at every predetermined time. Alternatively, it may be started when the electrical conductivity of water, which is proportional to the concentration of bacteria, exceeds a predetermined range. Furthermore, electric heater other heat sources and a heat device or the like using a rather good are also septic tank detachment means for the regeneration of the hot water production tank
Instead of the hot water but it may also be using superheated steam as.
Claims (4)
と、 貯水タンクに各端部を接続された循環管路と、 循環管路に介装されたポンプと、 循環管路に介装された濾過材内蔵の浄化槽とから成る、 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 circulation pipe having each end connected to the water storage tank, a pump installed in the circulation pipe, and a circulation pipe installed in the circulation pipe. A water purification system, which comprises a septic tank with a built-in filter material.
に接続した、 ことを特徴とする請求項1記載の浄水システム。2. The water purification system according to claim 1, wherein an ozone outlet of the ozone generator is connected to a circulation line.
岐され浄化槽に至るバイパス管路と、 バイパス管路に介装されたヒ−タ付きの温水生成槽と、 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または2記載の浄水システ
ム。3. An adsorbent is arranged in the septic tank, and a bypass pipe branching from the pump outlet side of the circulation pipe through a passage switching valve to the septic tank and a bypass pipe are provided. 3. The water purification system according to claim 1 or 2, further comprising: a hot water generating tank with a heater, and a drainage pipe for discharging water in the septic tank.
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3記載の浄水システム。4. A sterilizing lamp capable of irradiating ultraviolet rays is arranged in a septic tank, and a catalyst containing platinum group oxide and oxide ceramics as main components is arranged around the sterilizing lamp. The water purification system according to claim 3.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4199871A JPH0639372A (en) | 1992-07-27 | 1992-07-27 | Water purification system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4199871A JPH0639372A (en) | 1992-07-27 | 1992-07-27 | Water purification system |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0639372A true JPH0639372A (en) | 1994-02-15 |
Family
ID=16415020
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4199871A Pending JPH0639372A (en) | 1992-07-27 | 1992-07-27 | Water purification system |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0639372A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU723763B3 (en) * | 1999-11-03 | 2000-09-07 | Noel Wright | Cooling solution filter apparatus and method |
AU737786B2 (en) * | 1999-11-03 | 2001-08-30 | Noel Wright | Cooling solution filter apparatus and method |
US6766822B2 (en) * | 1998-09-29 | 2004-07-27 | International Water-Guard Industries, Inc. | Method of water distribution and apparatus therefor |
WO2018221088A1 (en) * | 2017-05-30 | 2018-12-06 | パナソニックIpマネジメント株式会社 | Water purification system |
CN109928460A (en) * | 2018-07-26 | 2019-06-25 | 中国科学院水生生物研究所 | A kind of portable planktonic organism enrichment facility |
CN113277633A (en) * | 2021-05-10 | 2021-08-20 | 郑州三财通工贸有限公司 | Combined stainless steel water supply tank without horizontal seal |
-
1992
- 1992-07-27 JP JP4199871A patent/JPH0639372A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6766822B2 (en) * | 1998-09-29 | 2004-07-27 | International Water-Guard Industries, Inc. | Method of water distribution and apparatus therefor |
AU723763B3 (en) * | 1999-11-03 | 2000-09-07 | Noel Wright | Cooling solution filter apparatus and method |
AU737786B2 (en) * | 1999-11-03 | 2001-08-30 | Noel Wright | Cooling solution filter apparatus and method |
WO2018221088A1 (en) * | 2017-05-30 | 2018-12-06 | パナソニックIpマネジメント株式会社 | Water purification system |
CN109928460A (en) * | 2018-07-26 | 2019-06-25 | 中国科学院水生生物研究所 | A kind of portable planktonic organism enrichment facility |
CN113277633A (en) * | 2021-05-10 | 2021-08-20 | 郑州三财通工贸有限公司 | Combined stainless steel water supply tank without horizontal seal |
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