CN101119937A - Sterile water producing apparatus - Google Patents
Sterile water producing apparatus Download PDFInfo
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- CN101119937A CN101119937A CNA200580046539XA CN200580046539A CN101119937A CN 101119937 A CN101119937 A CN 101119937A CN A200580046539X A CNA200580046539X A CN A200580046539XA CN 200580046539 A CN200580046539 A CN 200580046539A CN 101119937 A CN101119937 A CN 101119937A
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- path
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- water
- clorox
- ingress pipe
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/45—Mixing liquids with liquids; Emulsifying using flow mixing
- B01F23/451—Mixing liquids with liquids; Emulsifying using flow mixing by injecting one liquid into another
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
- B01F25/3141—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit with additional mixing means other than injector mixers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
- B01F25/4316—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being flat pieces of material, e.g. intermeshing, fixed to the wall or fixed on a central rod
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Dispersion Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Accessories For Mixers (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
A sterile water producing apparatus that even when the operation interval of electromagnetic pump is long, is capable of causing the pH value and effective free hypochlorous acid concentration of produced sterile water to be constant at all times. First passage (16) for mixing of raw water with sodium hypochlorite is communicated with communication passage (50), and an opening of first introduction pipe (32) for discharging of sodium hypochlorite from first electromagnetic pump (26) is disposed inside the communication passage (50). Eddy (60) containing sodium hypochlorite is generated by the sodium hypochlorite discharged from the opening of first introduction pipe (32) and by the raw water flowing in the communication passage (50) from the first passage (16), and part of the eddy (60) is caused to protrude in the first passage (16). As a result, the sodium hypochlorite discharged from the first introduction pipe (32) rides the eddy (60) and within given period of time, is mixed with the raw water flowing through the first passage (16).
Description
Technical field
The present invention relates to be used for making the sterile water producing apparatus of powerful sterilization water by the water of tap water or well water etc.
Background technology
In the past, developed acid such as passing through in the former water of tap water or well water etc., to mix clorox and hydrochloric acid or acetate and a large amount of sterile water producing apparatus of making the sterilization water of bringing into play powerful sterilizing power.In this sterile water producing apparatus, possesses the mixing tank that is used to mix former water, clorox and acid, make 2 kinds of mixing waters by clorox and an amount of acid of measuring of the former water that imports the specified amount in the mixing tank being added an amount of metering respectively, mix this 2 kinds of mixing waters, thereby generate sterilization water (for example, with reference to patent documentation 1).
Patent documentation 1: the Japanese Patent spy opens the 2001-300547 communique
In the mixing tank in the past, when mixing clorox and acid among the Xiang Yuanshui, clorox may directly contact with acid, if clorox directly contacts with acid, pH is reduced to less than 4.5, then produces chlorine.Therefore in the mixing tank in the past, the troubled water according to clorox and acid can partly produce chlorine, must be arranged on from mixing tank and chlorine is discharged to the mechanism that the chlorine of discharging is handled outside the time.
Therefore, developed and made the mixing tank that does not produce chlorine when in former water, mixing clorox and acid.Adopt the mixing tank of the design that does not produce chlorine to be shown in Fig. 2 here.Mixing tank (mixing device) 10 has the shell 12 of cube shaped, and the inside of this shell 12 forms former water passage 14, from the interflow path 20 at this former water passage 14 ramose, first path 16 and alternate path 18, first path 16 and alternate path 18 interflow.In addition, shell 12 can adopt connection to substitute the form of cube shaped corresponding to the form of the pipeline of each path.The former water ingress pipe 22 that is connected with former water passage 14 is installed on the shell 12, and former water is imported into former water passage 14 from former water ingress pipe 22, and former water is divided into first path 16 and alternate path 18 from former water passage 14 and flows.Be equipped with on the shell 12 and collaborate the mixing tube 24 that path 20 is connected, the water that arrives interflow path 20 is discharged to the outside through mixing tube 24.
Import clorox from first electromagnetic pump 26 through first connecting path 28, first vacuum breaker 30 and first ingress pipe 32 midway at first path 16.Be opened on the entad in the cross section of first path 16 for the front end opening that makes the clorox of deriving from first ingress pipe 32 drop into first path, 16, the first ingress pipes 32 reliably by the running of first electromagnetic pump 26.Import acid such as hydrochloric acid or acetate from second electromagnetic pump 34 through second connecting path 36, second vacuum breaker 38 and second ingress pipe 40 midway at alternate path 18.The front end opening that acid such as hydrochloric acid of deriving from second ingress pipe 40 for the running that makes by second electromagnetic pump 34 or acetate drop into alternate path 18, the second ingress pipes 40 reliably is opened on the entad in the cross section of alternate path.
The aperture position of first path, 16 internal ratios, first ingress pipe 32 more downstream side (interflow path 20 sides) possess agitator 42, the aperture position of alternate path 18 internal ratios second ingress pipe 40 more downstream side (interflow path 20 sides) possess agitator 44.In addition, the inside of mixing tube 24 also possesses agitator 46. Agitator 42,44,46 further mixes the mixing water of former water and soup, and its material uses can be by the material of acid corrosion.Agitator 42,44,46 uses shape for example shown in Figure 3, but its shape is not limited to shape shown in Figure 3.
As above in the mixing tank 10 of Gou Chenging, import the former water of former water passage 14 from former water ingress pipe 22, half of its import volume is imported into first path 16, its import volume remaining half be imported into alternate path 18.In first path 16, the clorox of deriving from first ingress pipe 32 is added to the former water by it, and former then water and clorox mix by agitator 42, make the mixing water of former water and clorox.In the alternate path 18, the acid of deriving from second ingress pipe 40 is added to the former water by it, and former then water and acid mix by agitator 44, make the mixing water of former water and acid.The mixing water of the mixing water of former water and clorox and former water and acid is by interflow path 20 interflow, and former then water, clorox and acid mix by the agitator in the mixing tube 24 46, and formation can be killed the sterilization water of various bacterium.Then, sterilization water is discharged to the outside from mixing tube 24.
In the mixing tank 10 shown in Figure 2, as the clorox of soup with directly do not contact as acid such as the hydrochloric acid of soup or acetate.That is, clorox is diluted by former water, and acid is also diluted by former water, and diluted clorox and diluted acid are mixed by the agitator in the mixing tube 24 46.Clorox and acid are all diluted, can not produce chlorine because of the mixing between the dilution water.As mentioned above, by using mixing tank shown in Figure 2 10, can under the state that does not produce chlorine, mix former water, clorox and acid and generation sterilization water.
As the method that in former water, drops into clorox and acid, as shown in Figure 2, the central position that the front end opening of first ingress pipe 32 is opened on the passage sections of first path 16 is arranged, the front end opening of second ingress pipe 40 is opened on the method for central position of the passage sections of alternate path 18.Input clorox and acid have other method among the Xiang Yuanshui, and other method is shown in Fig. 4 and Fig. 5.Fig. 4 and Fig. 5 represent to drop into to first path 16 from first ingress pipe 32 example of clorox.At first path 16 connecting path 50 that is connected in vertical direction with this first path 16 is set midway.The valve 52 that is formed by the pliability material that is generally known as duckbill valve is installed at the peristome front end of first ingress pipe 32.This valve 52 is the shape of the tubular with end face 54, is formed with the jet orifice 56 of slit-shaped on the end face 54.After this valve 52 was installed on the peristome of first ingress pipe 32, (than the peristome position of first ingress pipe 32 more on the front) formed and accumulates space 58 in the inside of valve 52.
The end face 54 of this valve 52 be disposed at from the enough inside of the connecting path 50 of inboard of the link position of first path 16.First electromagnetic pump 26 (second electromagnetic pump 34) turns round off and on, and at the running intermittence of first electromagnetic pump 26, the jet orifice 56 of valve 52 is closed, and clorox can not sprayed from valve 52.On the other hand, during 26 runnings of first electromagnetic pump, the clorox extruding of sending from first electromagnetic pump 26 lodges in the clorox that accumulates in the space 58, opens the jet orifice 56 of valve 52, and clorox is sprayed from this jet orifice 56.Clorox relies on the jet power of blowing loophole 56 to arrive first path 16, and former water and clorox mix in first path 16.That is, borrow the gesture of first electromagnetic pump 26 and valve 52 to be ejected in first path 16, the jet orifice 56 (peristome of first ingress pipe 32) of valve 52 is disposed at the inner side of connecting path 50 in order to make clorox.
The announcement of invention
The running of first electromagnetic pump 26 and second electromagnetic pump 34 has the situation that becomes very long according to the dilute strength of each mixing water at interval.Make under the situation of cl concn reduction, the running of first electromagnetic pump 26 that extends at interval; Make under the situation of pH value rising, the running of second electromagnetic pump 34 that extends at interval.In addition, if the flow of former water tails off, then the running of first electromagnetic pump 26 at interval and all to be proportional to flow elongated at the running of second electromagnetic pump 34 interval.Here, be that example describes with first electromagnetic pump 26.Under the situation that the running of first electromagnetic pump 26 is grown at interval, exported to from the 1st time clorox the 2nd time clorox by till deriving long at interval in, by unmixed clorox in the former water of first path 16, produce the state that the mixing water that approaches former water arrives interflow path 20.Similarly, under the situation that the running of second electromagnetic pump 34 is grown at interval,, produce the state that the mixing water that approaches former water arrives interflow path 20 by unmixed acid in the former water of alternate path 18.Its result is, mixing water (sterilization water) the discontinuous ground of discharging from mixing tube 24 generates the different mixing water of pH value, perhaps generate the effectively free different off and on mixing water of hypochlorous acid concentration that produces by clorox and sour mixing off and on, existence becomes and can't generate the sterilization water of constant pH value and the effectively free hypochlorous acid concentration of constant.
Under the situation that the running of first electromagnetic pump 26 and second electromagnetic pump 34 is grown at interval, when as shown in Figure 2 the front end opening of first ingress pipe 32 and second ingress pipe 40 being opened on the kernel of section position of first path 16 and alternate path 18 and as shown in Figure 4 valve 52 is installed on the front end of first ingress pipe 32 (second ingress pipe 40) and with the position configuration of this valve 52 in apart from the inner side of first path 16 (alternate path 18) connecting path 50 far away the time, has all that the pH value of the sterilization water that is generated and effective hypochlorous acid concentration of dissociating are inconstant asks.
The present invention finishes in view of the above-mentioned problems, even its purpose is to provide the running of electromagnetic pump long at interval, also can make the pH value of the sterilization water that is generated and the hypochlorous acid concentration constant sterile water producing apparatus always that effectively dissociates.
The present invention to achieve these goals derives clorox through first ingress pipe from first electromagnetic pump to first path, in aforementioned first path, make the mixing water of former water and clorox, acid is derived to alternate path through second ingress pipe from second electromagnetic pump, in aforementioned alternate path, make the mixing water of former water and acid, the mixing water of former water and clorox mixed with the mixing water of former water and acid and generate the sterile water producing apparatus of sterilization water, wherein, setting is connected in the connecting path of aforementioned first path, the peristome of aforementioned first ingress pipe is disposed in the aforementioned connecting path, make to produce whirlpool by former water and clorox, and make the part of the whirlpool of this generation protrude in aforementioned first passage side at the link position of aforementioned first path and aforementioned connecting path.The present invention will be made as B and the maximum of the passage sections of aforementioned connecting path be made as under the situation of D from the peristome of aforementioned first ingress pipe distance with link position aforementioned first path in the aforementioned connecting path, make 1/3D≤B≤2.5D, the pressure that the pressure of former water that will be by aforementioned first path is made as P and will exports to the clorox in the aforementioned connecting path from the peristome of aforementioned first ingress pipe is made as under the situation of P ', makes 1/8P '≤P＜P '.
The present invention derives clorox through first ingress pipe from first electromagnetic pump to first path, in aforementioned first path, make the mixing water of former water and clorox, acid is derived to alternate path through second ingress pipe from second electromagnetic pump, in aforementioned alternate path, make the mixing water of former water and acid, the mixing water of former water and clorox mixed with the mixing water of former water and acid and generate the sterile water producing apparatus of sterilization water, wherein, setting is connected in the connecting path of aforementioned alternate path, the peristome of aforementioned second ingress pipe is disposed in the aforementioned connecting path, make to produce whirlpool by former water and acid, and make the part of the whirlpool of this generation protrude in aforementioned alternate path side at the link position of aforementioned alternate path and aforementioned connecting path.The present invention will be made as B and the maximum of the passage sections of aforementioned connecting path be made as under the situation of D from the peristome of aforementioned second ingress pipe distance with link position aforementioned alternate path in the aforementioned connecting path, make 1/3D≤B≤2.5D, the pressure that the pressure of former water that will be by aforementioned alternate path is made as P and will exports to the acid in the aforementioned connecting path from the peristome of aforementioned second ingress pipe is made as under the situation of P ', makes 1/8P '≤P＜P '.
By mixing device of the present invention, can mix always all clorox or the acid of equivalent in the path that Yu Yuanshui passes through from based on the exporting under the long situation in the 2nd time the interval of derivation of the clorox of the 1st time of electromagnetic pump running or acid.Thus, can obtain in former water, to mix the mixing water of clorox and with the mixing water of constant concentration mixing acid in former water with constant concentration.Therefore, under the long at interval situation of the running of electromagnetic pump, also can generate the sterilization water of the effectively free hypochlorous acid concentration of constant pH value and constant always.
The simple declaration of accompanying drawing
Fig. 1 is the sectional view of an embodiment of the major portion of expression sterile water producing apparatus of the present invention.
Fig. 2 is the perspective, cut-away view of the mixing tank in the past that uses in the sterile water producing apparatus.
Fig. 3 is the stereographic map of the agitator that uses among Fig. 1 and Fig. 2.
Fig. 4 is for being installed on valve the major portion sectional view of the state behind the peristome of ingress pipe.
Fig. 5 is the stereographic map of valve.
The explanation of symbol
10 mixing tanks
12 shells
16 first paths
18 alternate paths
26 first electromagnetic pumps
32 first ingress pipes
34 second electromagnetic pumps
40 second ingress pipes
50 connecting paths
60 whirlpools
The best mode that carries out an invention
Below, the present invention will be described based on accompanying drawing.Fig. 1 is the sectional view of an embodiment of the major portion of expression sterile water producing apparatus of the present invention.Among Fig. 1, represent same parts with the Ref. No. that the Ref. No. shown in Fig. 2 and Fig. 4 is same.In addition, among Fig. 1, expression drops into clorox the example of first path 16 from first ingress pipe 32.The present invention is not for using the device of Fig. 4 and valve 52 shown in Figure 5, and the peristome of first ingress pipe 32 is disposed at the inside of connecting path 50.Here, shell 12 is under the situation of pipeline, and connecting path 50 adopts the rounded section of diameter D.Connecting path 50 better is the path of the cross section circle of employing and first path, 16 same diameter D, but is not limited thereto.In the sterile water producing apparatus, generally use the pipeline of the inner diameter d about 10mm≤D≤36mm, the pipeline about D=22mm particularly, but the size of inside diameter D is not limited thereto.In addition, it all is the situation of square-section that the connecting path 50 and first path 16 are also arranged, under this situation, with big limit as D.In addition, the distance with the position of the front end opening of in the connecting path 50 and the link position first path 16 and first ingress pipe 32 is made as B.Among the present invention, the peristome of first ingress pipe 32 is disposed at the inside of connecting path 50 with the condition of 1/3D≤B≤2.5D.
In addition, among the present invention, if will be made as P with the pressure of the former water that passes through first path 16 in the link position of connecting path 50, the pressure that will export to the clorox in the connecting path 50 from the peristome of first ingress pipe 32 is made as P ', then is set at 1/8P '≤P＜P '.
When the peristome of first ingress pipe 32 being disposed at the inside of connecting path 50 with the condition of 1/3D≤B≤2.5D, be set at 1/8P '≤P＜P ', from first ingress pipe 32 export to the clorox of inside of connecting path 50 connecting path 50 with link position first path 16 near produce the whirlpool 60 that has mixed former water.This whirlpool 60 exports to connecting path 50 and the clorox that directly do not arrive first path 16 forms by the part of the former water that passes through first path 16 that enters connecting path 50 with from first ingress pipe 32.The shape of this whirlpool 60 forms elliptical shape or forms different therewith shapes according to the length of B.By will being arranged in the scope of 1/3D≤B≤2.5D apart from B, the part (half of whirlpool 60 sizes is following) of the whirlpool 60 that is formed by clorox and former water protrudes in first path 16.By adopting the scope of 1/8P '≤P＜P ', make the clorox of deriving directly not arrive first path 16 from first ingress pipe 32.
Protrude in first path 16 by a part that makes the whirlpool 60 that contains clorox, the part of clorox that running by first electromagnetic pump 26 (with reference to Fig. 2) exports to the inside of connecting path 50 from first ingress pipe 32 is mixed in the former water by first path 16, and it most forms whirlpool 60 and residues in the connecting path 50.Then, in the time before the running next time of first electromagnetic pump 26, whirlpool 60 contained clorox progressively are mixed in the former water that flows through first path 16 with whirlpool 60.At this moment, by 1st time the clorox of first electromagnetic pump 26 in first ingress pipe 32 exports to connecting path 50 the 2nd time clorox almost all was mixed in former water by first path 16 before first ingress pipe 32 is derived.Thus, the blending ratio that can make former water and clorox constant mixing water always.
Regulate above-mentioned length apart from B at interval by the running according to first electromagnetic pump 26, the clorox of the 1st derivation can all drop into before the 2nd time is derived and be mixed in the former water that flows through first path 16.Satisfy 1/3D≤B≤2.5D when as previously mentioned, a part that contains the whirlpool of clorox protrudes in first path 16.B is during less than 1/2D, most protruding in first path 16 of the whirlpool 60 of clorox, so from exporting to before the 2nd time the derivation of clorox of the 1st time clorox, all clorox of deriving for the 1st time just are mixed in the former water that flows through first path 16, produce the state that only former water flows through in first path 16.On the other hand, B is during greater than 2.5D, and from the 1st time clorox no show first path 16 that first ingress pipe 32 is derived, before the derivation of the 2nd time clorox, the 1st time clorox all is not mixed in the former water that flows through first path 16.Thus, produce the problem that to make the mixing water of former water and clorox equalization in first path 16.
In addition, P is less than 1/8P ' time, and the clorox of deriving from first ingress pipe 32 arrives first path 16, and P can't guarantee the derived quantity of clorox greater than P ' time, so the scope of P is made as 1/8P '≤P＜P '.
In addition, among Fig. 1, the structure that will be mixed in the former water that flows through first path 16 from the clorox that first electromagnetic pump 26 is derived is illustrated, and the structure that will be mixed in from the acid that second electromagnetic pump 34 (with reference to Fig. 2) is derived the former water that flows through alternate path 18 also is same (1/3D≤B≤2.5D, 1/8P '≤P＜P ').In the sterile water producing apparatus, the running that has first electromagnetic pump 26 that only extends at interval reduce the situation of effective free chloro concentration and the running of second electromagnetic pump 34 that only extends at interval and the situation of reduction pH value.Therefore, have only to be used in and derive the situation at the position of clorox, only be used in by second electromagnetic pump 34 and second ingress pipe 40 and derive the situation at position of acid and the situation that is used in two positions by first electromagnetic pump 26 and first ingress pipe 26.
Claims (4)
1. sterile water producing apparatus, it is that clorox is derived to first path through first ingress pipe from first electromagnetic pump, in aforementioned first path, make the mixing water of former water and clorox, acid is derived to alternate path through second ingress pipe from second electromagnetic pump, in aforementioned alternate path, make the mixing water of former water and acid, the mixing water of former water and clorox mixed with the mixing water of former water and acid and generate the sterile water producing apparatus of sterilization water, it is characterized in that, setting is connected in the connecting path of aforementioned first path, the peristome of aforementioned first ingress pipe is disposed in the aforementioned connecting path, make to produce whirlpool by former water and clorox, and make the part of the whirlpool of this generation protrude in aforementioned first passage side at the link position of aforementioned first path and aforementioned connecting path.
2. sterile water producing apparatus as claimed in claim 1, it is characterized in that, to be made as B and the maximum of the passage sections of aforementioned connecting path be made as under the situation of D from the peristome of aforementioned first ingress pipe distance with link position aforementioned first path in the aforementioned connecting path, make 1/3D≤B≤2.5D, the pressure that the pressure of former water that will be by aforementioned first path is made as P and will exports to the clorox in the aforementioned connecting path from the peristome of aforementioned first ingress pipe is made as under the situation of P ', makes 1/8P '≤P＜P '.
3. sterile water producing apparatus, it is that clorox is derived to first path through first ingress pipe from first electromagnetic pump, in aforementioned first path, make the mixing water of former water and clorox, acid is derived to alternate path through second ingress pipe from second electromagnetic pump, in aforementioned alternate path, make the mixing water of former water and acid, the mixing water of former water and clorox mixed with the mixing water of former water and acid and generate the sterile water producing apparatus of sterilization water, it is characterized in that, setting is connected in the connecting path of aforementioned alternate path, the peristome of aforementioned second ingress pipe is disposed in the aforementioned connecting path, make to produce whirlpool by former water and acid, and make the part of the whirlpool of this generation protrude in aforementioned alternate path side at the link position of aforementioned alternate path and aforementioned connecting path.
4. sterile water producing apparatus as claimed in claim 3, it is characterized in that, to be made as B and the maximum of the passage sections of aforementioned connecting path will be made as under the situation of D from the peristome of aforementioned second ingress pipe distance with link position aforementioned alternate path in the aforementioned connecting path, make 1/3D≤B≤2.5D, the pressure that the pressure of former water that will be by aforementioned alternate path is made as P and will exports to the acid in the aforementioned connecting path from the peristome of aforementioned second ingress pipe is made as under the situation of P ', makes 1/8P '≤P＜P '.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005008634 | 2005-01-17 | ||
| JP008634/2005 | 2005-01-17 | ||
| PCT/JP2005/023108 WO2006075475A1 (en) | 2005-01-17 | 2005-12-16 | Sterile water producing apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101119937A true CN101119937A (en) | 2008-02-06 |
| CN101119937B CN101119937B (en) | 2010-12-01 |
Family
ID=36677506
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200580046539XA Active CN101119937B (en) | 2005-01-17 | 2005-12-16 | Sterile water producing apparatus |
Country Status (5)
| Country | Link |
|---|---|
| JP (1) | JP4388550B2 (en) |
| KR (1) | KR101256015B1 (en) |
| CN (1) | CN101119937B (en) |
| TW (1) | TW200628176A (en) |
| WO (1) | WO2006075475A1 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR200455554Y1 (en) * | 2009-07-25 | 2011-09-15 | (주) 디엔디전자 | Mixer for disinfectant generator by electrolysis |
| JP7020850B2 (en) * | 2017-10-06 | 2022-02-16 | Ckd株式会社 | Liquid dilution mixer |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5436304A (en) * | 1977-08-25 | 1979-03-17 | Miura Kogyo Kk | Production of emulsion fuel |
| JPH06312189A (en) * | 1993-03-05 | 1994-11-08 | Tatsuo Okazaki | Electrolytic sterilized water making apparatus |
| JP4828012B2 (en) | 2000-05-12 | 2011-11-30 | 東亜ディーケーケー株式会社 | Disinfection water generation method and apparatus |
| JP3719589B2 (en) | 2001-04-23 | 2005-11-24 | ソニー株式会社 | Disinfection water production equipment |
| JP3703758B2 (en) | 2001-11-30 | 2005-10-05 | ソニー株式会社 | Disinfection water production apparatus and production method |
| JP4150533B2 (en) * | 2002-05-10 | 2008-09-17 | 岡▲崎▼ 美惠子 | Disinfection water production equipment |
-
2005
- 2005-12-16 WO PCT/JP2005/023108 patent/WO2006075475A1/en not_active Application Discontinuation
- 2005-12-16 JP JP2006515435A patent/JP4388550B2/en active Active
- 2005-12-16 KR KR1020077016072A patent/KR101256015B1/en active IP Right Grant
- 2005-12-16 CN CN200580046539XA patent/CN101119937B/en active Active
- 2005-12-27 TW TW094146801A patent/TW200628176A/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| KR20070104354A (en) | 2007-10-25 |
| TW200628176A (en) | 2006-08-16 |
| WO2006075475A1 (en) | 2006-07-20 |
| JPWO2006075475A1 (en) | 2008-06-12 |
| CN101119937B (en) | 2010-12-01 |
| KR101256015B1 (en) | 2013-04-18 |
| JP4388550B2 (en) | 2009-12-24 |
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