JPH038393Y2 - - Google Patents
Info
- Publication number
- JPH038393Y2 JPH038393Y2 JP1987173107U JP17310787U JPH038393Y2 JP H038393 Y2 JPH038393 Y2 JP H038393Y2 JP 1987173107 U JP1987173107 U JP 1987173107U JP 17310787 U JP17310787 U JP 17310787U JP H038393 Y2 JPH038393 Y2 JP H038393Y2
- Authority
- JP
- Japan
- Prior art keywords
- water
- ejector
- valve
- outside
- sterilizing
- 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.)
- Expired
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 86
- 230000001954 sterilising effect Effects 0.000 claims description 23
- 239000000126 substance Substances 0.000 claims description 23
- 241000894006 Bacteria Species 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 32
- 238000011045 prefiltration Methods 0.000 description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 238000000108 ultra-filtration Methods 0.000 description 8
- 230000000844 anti-bacterial effect Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000004659 sterilization and disinfection Methods 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- 239000008399 tap water Substances 0.000 description 4
- 235000020679 tap water Nutrition 0.000 description 4
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 244000063299 Bacillus subtilis Species 0.000 description 1
- 235000014469 Bacillus subtilis Nutrition 0.000 description 1
- 206010043376 Tetanus Diseases 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002510 pyrogen Substances 0.000 description 1
- 210000004215 spore Anatomy 0.000 description 1
- 210000003812 trophozoite Anatomy 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Water Treatments (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
本考案は、衛生状態を特に問題にする医療、薬
品、食品等を取扱う部門で水を殺菌して使うため
の通水装置とその殺菌装置に関するものである。[Detailed description of the invention] (Industrial application field) The present invention is a water passage device and its sterilizer for use in sterilizing water in departments that handle medical, pharmaceutical, food, etc. where hygiene is a particular issue. It is related to.
(従来の技術)
従来、水道の水を殺菌して外部に供給する通水
装置の殺菌方法としては、通水装置に熱湯を通水
して殺菌を行う方法と第9図に示すホルマリンに
よる殺菌方法がある。(Prior Art) Conventionally, methods for sterilizing tap water using a water passing device that sterilizes tap water and supplies it to the outside include a method of sterilizing water by passing boiling water through the water passing device, and a method of sterilizing water using formalin as shown in Fig. 9. There is a way.
(考案が解決しようとする問題点)
ここで、通水装置に熱湯を通して殺菌を行う方
法の場合、装置の耐熱条件により90℃前後の熱湯
しか使用できず、この程度の熱湯では病原性細菌
の栄養型しか殺せず、破傷風、ガス壊菌、枯草菌
の芽胞を完全に殺すことはできず、又、限外フイ
ルタを使用している場合、急熱、急冷によりフイ
ルターハウジングに歪みが発生し易いため、加
熱、冷却にかなりの技術と時間を必要とすると言
う欠点があり、又、第9図に示すホルマリンによ
る殺菌方法、即ち、開閉弁31を通して水道の水
を図示省略通水装置のプレフイルタへ供給すると
ともに、前記通水装置の殺菌に際して、開閉弁3
1を閉じて開閉弁32,33を開けることによ
り、原水の水道水をホルマリン貯水槽34内に入
れて貯水槽34内のホルマリンを通水装置のプレ
フイルタへ押出すホルマリンによる殺菌方法があ
るが、この場合、ホルマリン貯水槽34内のホル
マリンが水道の水で希釈されながら通水装置のプ
レフイルタへ供給されるためホルマリンの濃度管
理ができないと言う欠点があつた。(Problem that the invention aims to solve) In the case of the method of sterilizing by passing boiling water through a water flow device, only boiling water of around 90℃ can be used due to the heat resistance conditions of the device, and this level of boiling water can kill pathogenic bacteria. It only kills trophozoites and cannot completely kill spores of tetanus, gas sterilizers, and Bacillus subtilis.Also, if an ultrafilter is used, the filter housing is likely to become distorted due to rapid heating and cooling. Therefore, there is a drawback that heating and cooling require considerable skill and time, and the formalin sterilization method shown in FIG. At the same time as supplying water, when sterilizing the water passage device, the on-off valve 3
There is a formalin sterilization method in which raw tap water is put into the formalin water tank 34 by closing the valve 1 and opening the on-off valves 32 and 33, and the formalin in the water tank 34 is pushed out to the prefilter of the water passing device. In this case, the formalin in the formalin water tank 34 is supplied to the prefilter of the water passage device while being diluted with tap water, so there is a drawback that the concentration of formalin cannot be controlled.
(問題を解決するための手段)
本考案は、水供給源からの水を該水内に含まれ
る菌等を滅菌除去して外部に滅菌水を供給する通
水装置において、外部に供給される水の量を水供
給源側水の圧力変動に対して一定に保持する定流
量弁と、通水によつて吸込み口に吸込み力を発生
させるエジエクタと、前記通水装置の殺菌用薬液
を容れた薬液タンクとのそれぞれを備え、水供給
源からの水を外部に供給する通水路上に前記定流
量弁とエジエクタとを直列に接続し、かつ、前記
エジエクタの吸込み口に薬液吸込み可能に前記薬
液タンクを接続した通水装置用殺菌装置にある。(Means for solving the problem) The present invention is a water flow device that sterilizes and removes bacteria contained in water from a water supply source and supplies sterilized water to the outside. A constant flow valve that maintains the amount of water constant against pressure fluctuations of water on the water supply source side, an ejector that generates suction force at the suction port by passing water, and a sterilizing chemical solution in the water passing device. The constant flow valve and the ejector are connected in series on a water passageway for supplying water from a water supply source to the outside, and the chemical solution is capable of being sucked into the suction port of the ejector. It is located in a sterilizer for water flow equipment connected to a chemical tank.
(作用・効果)
このように構成された通水装置用殺菌装置の場
合、水供給源からの水は互いに直列に接続された
定流量弁とエジエクタを通るとともに、エジエク
タを通る水によつて薬液タンク内の殺菌用薬液、
例えばホルマリンが水に混入して通水装置の通水
路全体に供給される結果、通水装置のフイルタを
含む通水路全体が有効に殺菌され、しかも、薬液
タンク内の殺菌用薬液がエジエクタを通して水と
混合する量は、通水源の水圧変動にかかわらず定
流量弁により水量に比例する結果、薬液タンク内
の殺菌用薬液が水に混入する濃度を一定にして常
に安定した殺菌効果を得ることができる。(Function/Effect) In the case of the sterilizer for water passing device configured as described above, water from the water supply source passes through the constant flow valve and the ejector which are connected in series with each other, and the water passing through the ejector converts the chemical solution into Sterilizing chemical solution in the tank,
For example, formalin mixes with water and is supplied to the entire water channel of the water passing device, so that the entire water channel including the filter of the water passing device is effectively sterilized, and the sterilizing chemical solution in the chemical tank is passed through the ejector to the water. As a result of the constant flow valve, the amount of water to be mixed with water is proportional to the amount of water regardless of fluctuations in the water pressure of the water supply source.As a result, the concentration of the sterilizing chemical solution in the chemical solution tank mixed into the water is kept constant, and a stable sterilizing effect can always be obtained. can.
(実施例)
次に、本考案の一実施例の構成を第1図〜第8
図によつて説明する。(Example) Next, the configuration of an example of the present invention is shown in Figures 1 to 8.
This will be explained using figures.
水供給源に接続される外部配管口1は、定圧弁
2と定流量弁3と電磁開閉弁4とプレフイルタ
5、この場合、ある程度粗い粒子の混入物を除去
するプレフイルタ5と、限外濾過フイルタ6、こ
の場合、肉眼で見えない微粒子、細菌、パイロジ
エンを除去する限外濾過フイルタ6とを介して外
部に殺菌後の水をシヤワー状に放出する防菌蛇口
7、この場合、第5図、第6図に示すように、
Ag含有溶解性ガラス8を詰めた網状格納袋9を
板材に多数の孔10を明けたシヤワー板11と皿
ビス12を介して蛇口本体13に取付けた防菌蛇
口7、或は、第7図に示すように、活性炭をウレ
タンフオームに含浸吸着させたシート状の吸着体
にAgを添着したAg添着活性炭シート14を蛇口
本体13に取付けた防菌蛇口15に接続され、か
つ、定流量弁3と電磁開閉弁4との間と電磁開閉
弁4とプレフイルタ5との間には開閉弁16を介
してエジエクタ17が接続され、エジエクタ17
の吸込み口18には開閉弁19を介してホース2
0が接続され、該ホース20先端部に取付けられ
たストレーナ21は殺菌用薬液の例えばホルマリ
ンを容れた薬液タンク22に挿入されている。 An external piping port 1 connected to a water supply source includes a constant pressure valve 2, a constant flow valve 3, an electromagnetic shutoff valve 4, and a prefilter 5, in this case, a prefilter 5 for removing contaminants of coarse particles to some extent, and an ultrafiltration filter. 6. In this case, an antibacterial faucet 7 that discharges sterilized water in the form of a shower to the outside through an ultrafiltration filter 6 that removes fine particles, bacteria, and pyrogens invisible to the naked eye; in this case, FIG. As shown in Figure 6,
An antibacterial faucet 7 in which a mesh storage bag 9 filled with Ag-containing soluble glass 8 is attached to a faucet main body 13 via a shower plate 11 with many holes 10 in the plate material and countersunk screws 12, or FIG. As shown in the figure, an Ag-impregnated activated carbon sheet 14 in which Ag is impregnated on a sheet-like adsorbent in which activated carbon is impregnated and adsorbed into urethane foam is connected to an antibacterial faucet 15 that is attached to a faucet body 13, and a constant flow valve 3 An ejector 17 is connected between the electromagnetic on-off valve 4 and the electromagnetic on-off valve 4 and the prefilter 5 via an on-off valve 16.
The hose 2 is connected to the suction port 18 of the
A strainer 21 attached to the tip of the hose 20 is inserted into a chemical tank 22 containing a sterilizing chemical, such as formalin.
次に、本実施例の作用について説明する。 Next, the operation of this embodiment will be explained.
このように構成された通水装置23用殺菌装置
24における通常の水使用状態、即ち、電磁開閉
弁4オンで開、開閉弁16,19が閉の状態にお
いて、水供給源からの水はエジエクタ17を通ら
ずに通水装置23のプレフイルタ5と限外濾過フ
イルタ6のみを通つて外部に供給されるため、通
水に薬液タンク22内の殺菌用薬液の例えばホル
マリンが混入することはなく、殺菌された水が防
菌蛇口7或は15から外部にシヤワー状に放出さ
れ、このシヤワーの放出・停止は電磁開閉弁4の
オン・オフによつて適宜制御することができ、
又、シヤワーの放出が停止しても、防菌蛇口7或
は15内のAg含有溶解性ガラス8、或は、Agと
ともに活性炭を吸着させたウレタンホームの活性
炭シート14によつて、外部から通水装置23内
への菌を侵入が防止される。 In the normal water use state in the sterilizer 24 for the water passage device 23 configured in this way, that is, in the state where the solenoid on-off valve 4 is open and the on-off valves 16 and 19 are closed, water from the water supply source is transferred to the ejector. Since the water is supplied to the outside through only the prefilter 5 and ultrafiltration filter 6 of the water flow device 23 without passing through 17, the water does not mix with the sterilizing chemical solution in the chemical tank 22, such as formalin. Sterilized water is discharged to the outside from the antibacterial faucet 7 or 15 in the form of a shower, and the discharge and stop of this shower can be controlled as appropriate by turning on and off the electromagnetic on-off valve 4.
In addition, even if the shower stops discharging, the flow from the outside is maintained by the Ag-containing soluble glass 8 in the antibacterial faucet 7 or 15, or by the activated carbon sheet 14 made of urethane foam that adsorbs activated carbon along with Ag. Bacteria are prevented from entering the water device 23.
次に、電磁開閉弁4のオフ状態で通水装置23
のプレフイルタ5と限外濾過フイルタ6を通る通
水路上流位置の開閉弁16とエジエクタ17の吸
込み口18部分の開閉弁19を開にすると、水供
給源からの水はエジエクタ17と通水装置23の
プレフイルタ5と限外濾過フイルタ6を通つて防
菌蛇口7或は15から外部に放出されるととも
に、エジエクタ17を通る水によつて薬液タンク
22内の殺菌用薬液、例えばホルマリンが水に混
入し、通水装置23のプレフイルタ5と限外濾過
フイルタ6を含む通水路全体が有効に殺菌され、
しかも、薬液タンク22内の殺菌用薬液がエジエ
クタ17を通して水と混合する量は、水量に比例
し、この場合、定流量弁3によつて流量を一定に
している結果、一層、薬液タンク22内の殺菌用
薬液の例えばホルマリンが水に混入する濃度を通
水源の水圧変動及び各フイルタ5,6の目詰まり
による背圧の増大にかかわらず一定にして常に安
定した殺菌効果を得るこことができる。このよう
に一定濃度のホルマリン液が通水装置23内に充
満した状態において、開閉弁16を一旦閉じてホ
ルマリン液を通水装置23内に滞留させて十分に
殺菌した後、開閉弁19を閉じた状態で開閉弁1
6を開けることによつて、通水装置23内のホル
マリン液を外部に押出し洗浄することができる。 Next, the water flow device 23 is turned off with the electromagnetic on-off valve 4 turned off.
When the on-off valve 16 at the upstream position of the water passage passing through the pre-filter 5 and the ultrafiltration filter 6 and the on-off valve 19 at the suction port 18 of the ejector 17 are opened, water from the water supply source flows through the ejector 17 and the water passage device 23. The sterilizing chemical solution, such as formalin, in the chemical tank 22 is mixed into the water by the water passing through the ejector 17 and being discharged to the outside from the antibacterial faucet 7 or 15 through the prefilter 5 and ultrafiltration filter 6. Then, the entire passageway including the prefilter 5 and ultrafiltration filter 6 of the water passage device 23 is effectively sterilized.
Moreover, the amount of the sterilizing chemical in the chemical tank 22 mixed with water through the ejector 17 is proportional to the amount of water, and in this case, as the flow rate is kept constant by the constant flow valve 3, even more A stable sterilizing effect can be obtained by keeping the concentration of sterilizing chemicals such as formalin mixed in water constant regardless of fluctuations in water pressure at the water source or increases in back pressure due to clogging of the filters 5 and 6. . With the formalin solution at a certain concentration filling the water passing device 23 in this manner, the on-off valve 16 is temporarily closed to allow the formalin solution to remain in the water passing device 23 for sufficient sterilization, and then the on-off valve 19 is closed. On-off valve 1
By opening 6, the formalin solution in the water passage device 23 can be pushed out to the outside for cleaning.
なお、本実施例のプレフイルタ5と限外濾過フ
イルタ6は紫外線を用いた殺菌装置に代えること
ができる。 Note that the prefilter 5 and ultrafiltration filter 6 of this embodiment can be replaced with a sterilization device using ultraviolet rays.
第1図は本考案の一実施例の装置全体を示す略
体正面図、第2図はその右側面図、第3図はその
平面図、第4図はその配管図、第5図はその菌蛇
口7の破断正面図、第6図は第5図の裏面図、第
7図はその菌蛇口15の破断正面図、第8図は通
水圧の変動にともなう薬液吸い上げ特性を示す動
作特性図、第9図は従来の実施例の説明図であ
る。
4……電磁開閉弁、5……プレフイルタ、6…
…限外濾過フイルタ、16……開閉弁、17……
エジエクタ、22……薬液タンク、23……通水
装置、24……殺菌装置。
Fig. 1 is a schematic front view showing the entire device according to an embodiment of the present invention, Fig. 2 is its right side view, Fig. 3 is its plan view, Fig. 4 is its piping diagram, and Fig. 5 is its FIG. 6 is a cutaway front view of the bacteria faucet 7, FIG. 6 is a back view of FIG. , FIG. 9 is an explanatory diagram of a conventional embodiment. 4... Solenoid on-off valve, 5... Pre-filter, 6...
...Ultrafiltration filter, 16... Opening/closing valve, 17...
Ejector, 22... Chemical tank, 23... Water passage device, 24... Sterilization device.
Claims (1)
菌除去して外部に滅菌水を供給する通水装置にお
いて、外部に供給される水の量を水供給源側水の
圧力変動に対して一定に保持する定流量弁と、通
水によつて吸込み口に吸込み力を発生させるエジ
エクタと、前記通水装置の殺菌用薬液を容れた薬
液タンクとのそれぞれを備え、水供給源からの水
を外部に供給する通水路上に前記定流量弁とエジ
エクタとを直列に接続し、かつ、前記エジエクタ
の吸込み口に薬液吸込み可能に前記薬液タンクを
接続することを特徴とする通水装置用殺菌装置。 In a water flow device that sterilizes water from a water supply source to remove bacteria, etc. contained in the water and supplies sterilized water to the outside, the amount of water supplied to the outside is adjusted to fluctuations in the pressure of the water on the water supply source side. A constant flow valve that maintains the water at a constant level, an ejector that generates a suction force at the suction port by passing water, and a chemical tank that contains a sterilizing chemical solution for the water passing device. The constant flow valve and the ejector are connected in series on a water passageway for supplying water to the outside, and the chemical liquid tank is connected to the suction port of the ejector so as to be capable of sucking the chemical liquid. Sterilizer for use.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1987173107U JPH038393Y2 (en) | 1987-11-12 | 1987-11-12 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1987173107U JPH038393Y2 (en) | 1987-11-12 | 1987-11-12 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0177895U JPH0177895U (en) | 1989-05-25 |
JPH038393Y2 true JPH038393Y2 (en) | 1991-02-28 |
Family
ID=31465043
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1987173107U Expired JPH038393Y2 (en) | 1987-11-12 | 1987-11-12 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH038393Y2 (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4413338Y1 (en) * | 1965-05-18 | 1969-06-03 | ||
JPS5088853A (en) * | 1973-12-12 | 1975-07-16 |
-
1987
- 1987-11-12 JP JP1987173107U patent/JPH038393Y2/ja not_active Expired
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4413338Y1 (en) * | 1965-05-18 | 1969-06-03 | ||
JPS5088853A (en) * | 1973-12-12 | 1975-07-16 |
Also Published As
Publication number | Publication date |
---|---|
JPH0177895U (en) | 1989-05-25 |
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