CN1955123A - Functional water and manufacturing method and device thereof - Google Patents

Abstract

A kind of functional water (the water for beverage) is prepared from the purified water through adding vitamins, minerals and amino acids, dissolving O2 in it, filling it in containers and sealing. Its apparatus is also disclosed.

Description

Function water and manufacture method thereof and manufacturing installation

Technical field

The function water that the present invention relates to a kind of high density ground dissolving aerobic with and manufacture method and manufacturing installation.

Background technology

In recent years, people have proposed the function water of various materials as high density ground dissolving aerobic, and one of them is exactly a sweet water.Oxygen also can be by drinking this class sweet water from picked-ups such as stomach or intestines except being ingested from lung, and confirm to have following effect when picked-up oxygen: the decomposition of the alcohol that is contained in the promotion wine is in case stay liquor-saturated; Prevent from the oxygen supply ability of health each several part to be reduced because of the carbon monoxide that cigarette is contained; Improve the discharge of the old refuse of metabolism promotion; The lactic acid decomposition that generates when promoting motion prevents fatigue.

And, with regard to above-mentioned sweet water, the for example known spy of having opens the disclosed product of 2001-292748 communique, this sweet water is, after obtaining deep seawater it is adjusted to the salt concentration of regulation from the deep-sea, make oxygen be dissolved in this water, make the molten storage of oxygen bring up to 25～30mg/l, the water after this oxygen dissolution process is filled in the back sealing obtains in the bottle from 6～8mg/l.Like this, because molten storage height of oxygen and deep seawater contain various natural mineral substance, so be its commodity value height of sweet water of purpose as improving health.

In addition, be dissolved in regard to the method for water (sweet water), for example, as the spy opens the disclosed sweet water of flat 10-314561 communique,, oxygen be dissolved in this water by air or the oxygen that utilizes oxygen generator unit to generate are led in water with regard to making oxygen.

But, above-mentioned existing beverage water, when Kaifeng during bottle, the sweet water ingress of air in this bottle, dissolved oxygen is released in the air, so the molten storage of oxygen reduce along with the process of time, be reduced at short notice with the oxygen dissolution process before equal level.

Therefore, must once all drink the sweet water in the bottle or throw away do not drunk that part of after the bottle of Kaifeng, through after the certain hour, even drink remaining sweet water, because the molten storage of oxygen reduces, so be difficult to obtain effect as described above, can not only drink the amount of drinking wanted when drinking.

Like this, the problem of the function water of representatives such as above-mentioned sweet water is, even the molten storage of oxygen of just having carried out after the oxygen dissolution process is many, when it is placed in the atmosphere, the molten storage of oxygen be reduced to along with the process of time with the oxygen dissolution process before equal level.

Summary of the invention

The present invention finishes in view of above truth, though its objective is provide a kind of just carried out the molten storage of oxygen after the oxygen dissolution process many and be placed on the molten storage of oxygen in the atmosphere also be difficult to the function water that reduces with and manufacture method and manufacturing installation.

In order to reach a kind of function water that the present invention relates to of above-mentioned purpose, it is the function water of the oxygen more than the dissolving nature concentration of ordinary dissolution in former water, it is characterized in that, the molten storage of oxygen of just having carried out after the oxygen dissolution process is 25～70mg/l, afterwards, under the state in being placed on atmosphere, remain on more than the 15mg/l through the molten storage of oxygen after 24 hours.

In addition, this function water also can contain at least a among VITAMIN, mineral substance, amino acid or the medicine, fills and is sealed in the movable container.

Such function water, the molten storage of oxygen after just carrying out the oxygen dissolution process is the high density of 25～70mg/l, and, contact even be placed in the atmosphere and with atmosphere, as long as the elapsed time is in 24 hours, the molten storage of oxygen still remains on the above many like this states of 15mg/l, so for example when it is used as sweet water, to fill, after sealing the movable container Kaifeng of this sweet water, the molten storage of oxygen still keeps high state, when wanting to drink this sweet water (function water), can only drink the amount of drinking wanted, and, even whenever drink, also can absorb the oxygen of the abundant amount that obtains effect as described above.Therefore, drinking of this sweet water becomes easy.In addition, through the molten storage of oxygen after 24 hours more preferably more than the 35mg/l.

In addition, this function water also can be used for the raw material of pharmaceuticals or makeup etc. except that sweet water, for example, when being used in medicament for the eyes or eyewash, astringent, also can obtain absorbing oxygen and promoting the metabolic effect of this part from eye or skin surface.In addition, this is one of suitable purposes of this function water, and its purposes is not limited thereto.

Like this, even the molten storage of oxygen also is difficult to reduce under the state of function water of the present invention in being positioned over atmosphere, so can further improve the commodity value of this function water.In addition, if this function water contains at least a among VITAMIN, mineral substance, amino acid or the medicine, just can become the function water of the commodity value that further improves this function water.

And this function water can use following manufacture method suitably to make.

That is to say that this manufacture method is: the oxygen of pressurization is supplied in the encloses container body, make this encloses container body inside become the above oxygen atmosphere of normal atmosphere; Simultaneously, former water is spued in the above-mentioned encloses container body, in above-mentioned encloses container body, flow down, make it and the oxygen gas-to-liquid contact, generate the function water that is dissolved with 25～70mg/l oxygen with membranaceous by making the former water that is spued; Then, in above-mentioned encloses container body, take out the function water that generates.

Utilize this manufacture method, in the encloses container body inside of oxygen pressure being brought up to more than the normal atmosphere, former water is flowed down with membranaceous, contact with oxygen from the both sides of moisture film, generation has the function water of following feature, 6～the 8mg/l of the molten storage of the oxygen of this former water before this processing brings up to the hyperoxia concentration of 25～70mg/l, even and under the state in being positioned over atmosphere through 24 hours, the molten storage of oxygen still remain on 15mg/l above, more preferably remain on more than the 35mg/l.This is considered to: because under the highly compressed oxygen atmosphere, when water molecules contacts with oxygen molecule, their a part of ionization, this water molecules and oxygen molecule by ionic linkage become the bonded state, oxygen is dissolved in the former water, so generated the function water that hyperoxia concentration and the molten storage of oxygen are difficult to reduce by this class ionic linkage.Then, in above-mentioned encloses container body, take out the function water that generates.

In addition, above-mentioned manufacture method preferably purifies above-mentioned former water by contrary saturation process, and the former water supply after purifying is arrived in the above-mentioned encloses container body; In addition, former water supply after after preferably adding at least a among VITAMIN, mineral substance, amino acid or the medicine in the above-mentioned former water this interpolation being handled is in above-mentioned encloses container body, or, former water supply after after adding at least a among VITAMIN, mineral substance, amino acid or the medicine in the former water after the above-mentioned purification this interpolation being handled is in above-mentioned encloses container body, perhaps, with at least a the adding to the function water of in above-mentioned encloses container body, taking out among VITAMIN, mineral substance, amino acid or the medicine; In addition, the function water of taking out can also be filled in the movable container back sealing in above-mentioned encloses container body, perhaps, at least a function water of having added among VITAMIN, mineral substance, amino acid or the medicine be filled in back sealing in the movable container.

And this manufacture method can preferably utilize following manufacturing installation to implement.

That is, this manufacturing installation possesses: the oxygen dissolution process equipment portion of the oxygen systematic function water in former water more than the dissolving nature concentration of ordinary dissolution; With, will be filled in the filling treatment facility portion of back sealing in the movable container by the function water that this oxygen dissolution process equipment portion generates,

Above-mentioned oxygen dissolution process equipment portion possesses: the encloses container body; Have and be connected in the intravital supply-pipe of above-mentioned encloses container, oxygen supplied in the above-mentioned encloses container body, make this encloses container body inside become the oxygen supply unit of the oxygen atmosphere more than the normal atmosphere by this supply-pipe; Have one distolaterally be connected in the above-mentioned encloses container body, in this encloses container body with upper and lower to configuration and formed first water service pipe of discharge opening in the upper surface, from the discharge opening of this first water service pipe to the spue water supply unit of above-mentioned former water of the top-direction of above-mentioned encloses container body; Be connected in the above-mentioned encloses container body, will be stored in the above-mentioned functions water supply of this encloses container body bottom to the second outside water service pipe; From the outstanding to the inside first system stream unit of the inner face of above-mentioned encloses container body and/or from the outstanding laterally second tabular system stream unit of an end-side outer peripheral surface of above-mentioned first water service pipe,

Above-mentioned oxygen dissolution process equipment section is constituted as: the top-direction of above-mentioned former water from above-mentioned discharge opening to above-mentioned closed container body spued; Simultaneously; Make the former water that spues from this discharge opening and flow along the outer peripheral face of the inner peripheral surface of above-mentioned closed container body and/or above-mentioned first feed pipe; Flow down to the inner space of above-mentioned closed container body from the jag of above-mentioned first stream unit processed and/or second stream unit processed; Thereby make above-mentioned former water carry out gas-liquid contact in above-mentioned closed container body inside with oxygen and generate above-mentioned functions water

Above-mentioned filling treatment facility portion will be filled in back sealing in the above-mentioned movable container from the function water that second water service pipe of above-mentioned oxygen dissolution process equipment portion is supplied with.

Utilize this manufacturing installation at first in oxygen dissolution process equipment portion, to generate function water from former water.Particularly, utilize the oxygen supply unit oxygen to be supplied in the encloses container body by supply-pipe, after this encloses container body inside becomes the above oxygen atmosphere of normal atmosphere, by the water supply unit former water (water before the oxygen dissolving) is supplied in first water service pipe, after in logical this first water service pipe of the former current that are supplied to, spued the encloses container body from its discharge opening in.

The former water that is spued sprays to top-direction with water spray shape (is the radial of center with the discharge opening), after impacting with the inner face of encloses container bodies such as top surface or inner peripheral surface, along this inner face flow or the internal space that drops to the encloses container body of rebounding in or flow along the periphery of first water service pipe, then, controlled it along the former water of periphery mobile of the inner face of encloses container body or first water service pipe respectively by each system stream unit and flow, to the internal space of above-mentioned encloses container body, flow down with film like and waterfall shape overhang from this each system stream unit.

And, flow through the bottom that the intravital former water of encloses container is stored in the encloses container body, but oxygen is dissolved in this former water that is in contact with it in the flow process in this class oxygen atmosphere.Generate function water thus with following feature, promptly, the molten storage of the oxygen of this former water is brought up to the hyperoxia concentration of 25～70mg/l from 6 preceding～8mg/l of this processing, even and under the state in being positioned over atmosphere through 24 hours, the molten storage of oxygen still can remain on above 15mg/l, more preferably remains on more than the 35mg/l.

Then, be stored in the encloses container body function water (oxygen dissolving after water) since the oxygen pressure of encloses container body inside to be fed into encloses container from second water service pipe external, the function water that is supplied to is filled in back sealing in the movable container by filling treatment facility portion.Made the function water that is filled, is sealed in the movable container like this.

In addition, above-mentioned manufacturing installation also possesses the contrary saturation process equipment portion that purifies above-mentioned former water, the water supply unit of above-mentioned oxygen dissolution process equipment portion preferably is constituted as, the former water that purifies by above-mentioned contrary saturation process equipment portion is spued from the discharge opening of above-mentioned first water service pipe, in addition, above-mentioned manufacturing installation also has VITAMIN, mineral substance, at least a interpolation treatment facility portion that adds in the above-mentioned former water among amino acid or the medicine, the water supply unit of above-mentioned oxygen dissolution process equipment portion is constituted as, the former water handled by above-mentioned interpolation treatment facility portion is spued from the discharge opening of above-mentioned first water service pipe, above-mentioned manufacturing installation also has VITAMIN, mineral substance, at least a interpolation treatment facility portion that adds in the former water that purified by above-mentioned contrary saturation process equipment portion among amino acid or the medicine, above-mentioned water supply unit is constituted as the former water handled by above-mentioned interpolation treatment facility portion is spued from the discharge opening of above-mentioned first water service pipe, above-mentioned manufacturing installation also has VITAMIN, mineral substance, at least a among amino acid or the medicine added the interpolation treatment facility portion from the function water that second water service pipe of above-mentioned oxygen dissolution process equipment portion is supplied with to, and above-mentioned filling treatment facility quality award from the ministry choosing is constituted as the function water filling of handling by above-mentioned interpolation treatment facility portion, be sealed in the above-mentioned movable container.

Like this, utilize these functional water making method and manufacturing installations, spray former water from discharge opening and increase this former water and contact area oxygen with radial, simultaneously, by the first system stream unit or the second system stream unit control flowing along the former water of periphery mobile of the inner face of encloses container body or first water service pipe, former water is flowed down to the internal space of above-mentioned encloses container body with film like or the waterfall shape overhang from this system stream unit, former water is contacted with oxygen from the two sides side of moisture film, in addition, owing to also improved the oxygen pressure of encloses container body inside, so more oxygen is dissolved in this former water effectively, can generates as described above hyperoxia concentration and the molten storage of the oxygen function water that is difficult to reduce effectively.

As above being described in detail, even under the state of function water of the present invention in being positioned over atmosphere, if before the time, still can keep the state of hyperoxia concentration, so can improve the value added of this function water through afore mentioned rules.In addition, if make this function water contain VITAMIN, mineral substance, amino acid or medicine, just can further improve the value added of this function water.

In addition, if utilize functional water making method of the present invention and manufacturing installation, just can suitably make function water as described above.

Description of drawings

Fig. 1 is the functional diagram of expression manufacturing as the concise and to the point formation of the sweet water manufacturing installation of the sweet water of the function water of one embodiment of the present invention.

Fig. 2 is the sectional drawing of concise and to the point formation of the oxygen dissolution process equipment of expression present embodiment.

Fig. 3 is the sectional drawing along the arrow A among Fig. 2-A direction.

Fig. 4 is the sectional drawing along the arrow B among Fig. 2-B direction.

Fig. 5 is the sectional drawing along the arrow C among Fig. 2-C direction.

Fig. 6 is the mobile explanatory view that is used for illustrating the water of present embodiment.

Fig. 7 is the sectional drawing of concise and to the point formation of the oxygen dissolution process equipment of expression other embodiment of the present invention.

Fig. 8 is the sectional drawing along the arrow D-D direction among Fig. 7.

Fig. 9 is the water mobile explanatory view that is used for illustrating other embodiment of the present invention.

Figure 10 is the orthographic plan of the concise and to the point formation of the 2nd system stream plate of expression other embodiment of the present invention etc.

Figure 11 is the sectional drawing of the concise and to the point formation of the 2nd system stream plate of expression other embodiment of the present invention etc.

Figure 12 is the sectional drawing of concise and to the point formation of the system stream unit etc. of expression other embodiment of the present invention.

Embodiment

Below, based on the description of drawings preferred embodiment of the present invention.Fig. 1 is the functional diagram of expression manufacturing as the concise and to the point formation of the sweet water manufacturing installation of the sweet water of the function water of one embodiment of the present invention, Fig. 2 is the sectional drawing of concise and to the point formation of the oxygen dissolution process device of expression present embodiment, Fig. 3 is the sectional drawing of the arrow A-A direction among Fig. 2, Fig. 4 is the sectional drawing of the arrow B-B direction among Fig. 2, Fig. 5 is the sectional drawing of the arrow C-C direction among Fig. 2, and Fig. 6 is the explanatory view that is used for illustrating the current of present embodiment.

The sweet water as an example of function water in this example except high density ground dissolving aerobic, also contains VITAMIN, mineral substance and amino acid etc., is filled and is sealed in to have in the long-pending bottle (movable container) of specified content.In addition, the oxygen molten storage of this sweet water after just carrying out the oxygen dissolution process is 25～70mg/l, and remain on more than the 15mg/l, more preferably remain on more than the 35mg/l through the molten storage of oxygen after 24 hours under the state in being positioned over atmosphere, promptly, the molten storage of oxygen under the air-tight state is 25～70mg/l, even and bottle Kaifeng is back through 24 hours, the molten storage of oxygen also remains on more than 15 (35) mg/l.

And, this class sweet water can use sweet water manufacturing installation 1 shown in Figure 1 and suitably make, this sweet water manufacturing installation 1 as shown in Figure 1, its formation is to have purification apparatus 11, interpolation treatment facility 15, oxygen dissolution process equipment 20 and fill treatment facility 16, raw water (the former water of beverage) is handled in this treatment facility 11,15,20,16 successively, made the sweet water that is filled in the bottle.

Above-mentioned purification apparatus 11 is by the first filtration treatment portion 12, the second filtration treatment portion 13 and contrary saturation process portion 14 constitute, the first filtration treatment portion 12 is constituted as by appropriate filters and removes rubbish or dust etc. from the former water of beverage, the second filtration treatment portion 13 is constituted as by carbon filter adsorbs from the former water of handling with the first filtration treatment portion 12 of beverage and removes halogen compounds such as three methine halides, and contrary saturation process portion 14 is constituted as by the contrary film that soaks into from each filtration treatment portion 12, remove in the former water of 13 beverages of handling and fail with this handling part 12,13 impurity of removing (for example Dioxins (dioxin) or environmental hormone etc.).

Above-mentioned interpolation treatment facility 15 is constituted as VITAMIN, mineral substance and amino acid etc. is added in the sweet water that the contrary saturation process portion 14 with purification apparatus 11 handled.

Above-mentioned oxygen dissolution process equipment 20 is constituted as, and oxygen is dissolved in adding in the former water of beverage that treatment facility 15 handled generates sweet water, as Fig. 2～shown in Figure 5, possesses: form cylindric and have the container body 21 of enclosed space; Oxygen is supplied to oxygen supply portion 22 in the container body 21; The pressure detector of the oxygen pressure of detection receptacle body 21 inside (not diagram); With the water supply portion 23 of the former water supply of beverage in the container body 21; The sweet water of container body 21 inside is supplied to outside water service pipe (the 3rd water service pipe) 24; Be disposed at first, second and the 3rd system stream plate 25,26,27 of upper position in the container body 21; The water level detecting portion 28 of the water level in the detection receptacle body 21.

The outstanding spherical flexure plane to foreign side is formed on the top of said vesse body 21, is connected with the inside and outside vapor pipe 29 of connection container body 21 on this top, and this vapor pipe 29 is provided with the vent valve 29a that is controlled so as to closing condition usually.In addition, the following quilt of container body 21 is positioned on the suitable installation parts 30, and by its support.

Above-mentioned oxygen supply portion 22 comprises: the oxygen supply source 22a that supplies with oxygen, with one distolaterally be connected in oxygen supply source 22a and another distolateral supply-pipe 22b that is connected in the first water service pipe 23a described later and adjust the supply valve 22c that supplies to the oxygen flow in the container body 21 from oxygen supply source 22a by supply-pipe 22b; By the supply-pipe 22b and the first water service pipe 23a oxygen is supplied in the container body 21, make container body 21 inside become the above oxygen atmosphere of normal atmosphere.In addition, the aperture of supply valve 22c is adjusted to, and makes by the detected force value of above-mentioned pressure detector (not diagram) or by above-mentioned water level detecting portion 28 detected water levels and remains on certain value substantially.

Above-mentioned water supply portion 23 possesses: axis is provided with along the vertical direction, be configured in simultaneously with container body 21 coaxial positions on, the top surface of upper surface and container body 21 is predetermined distance and be configured in the first water service pipe 23a of the upper side of container body 21 at interval; The periphery injection of one distolateral calm body 21 is arrived in the container body 21, and is connected in the upper end of the above-mentioned first water service pipe 23a and the second water service pipe 23b between the bottom; Another that is connected in the second water service pipe 23b is distolateral, and by each water service pipe 23b, 23a the interior pumping unit 23e of container body 21 etc. is arrived in the former water supply of handling with above-mentioned interpolation treatment facility 15 of beverage.

The above-mentioned first water service pipe 23a possesses and is opened on its upper surface and towards the spue discharge opening 23c of the former water of beverage of above-mentioned top-direction, the other parts (inside diameter D 1) that the internal diameter of this discharge opening 23c is formed than the first water service pipe 23a are little.In addition, it is distolateral that the bottom of the first water service pipe 23a is connected to another of above-mentioned supply-pipe 22b, and the lower surface of this first water service pipe 23a is suitably sealed by sealing element 22d.

Being provided with among the above-mentioned second water service pipe 23b does not have illustrated reverse checkvalve, by this reverse checkvalve (do not have diagram) prevent to supply to the adverse current of the former water of beverage in the container body 21 or the oxygen leakage supplied with from supply-pipe 22b to the outside.

The bottom periphery injection of one distolateral calm body 21 of above-mentioned the 3rd water service pipe 24 is in its inside, and the sweet water (water of dissolving aerobic) that utilizes the oxygen pressure of these container body 21 inside will be stored in the bottom of container body 21 inside supplies to outside the container body 21.In addition, it is identical or less than the inside diameter D 1 of the first and second water service pipe 23a, 23b that the 3rd water service pipe 24 is constituted as its inside diameter D 2, has to be opened on the above-mentioned end face and to be used for sweet water is supplied to outside suction port 24a.

Above-mentioned first, second and the 3rd system stream plate 25,26,27 constitute by the dull and stereotyped of configuration separated by a certain interval on above-below direction and for the cyclic parts, the first system stream plate 25 is, when its periphery was fixed on the top inner peripheral surface of container body 21 by intercalation, inner circumferential surface was embedded in the upper end of the first water service pipe 23a outward; The second system stream plate 26 is that inner circumferential surface is scheduled the upper end of the first water service pipe 23a by outer build-in, and is configured in the below of the first system stream plate 25; The 3rd system stream plate 27 is that its periphery is fixed in the top inner peripheral surface of container body 21 by intercalation, and is configured in the below of the second system stream plate 26.

The above-mentioned first system stream plate 25 possesses four communicating pores 25a that are opened on its about fan-shaped, control is along flow (the flowing of the former water of control beverage) of the top surface of the former water of periphery mobile beverage of the inner peripheral surface of container body 21 or the first water service pipe 23a, impact container body 21 and the former water of beverage that rebounds, makes it to flow down to the internal space of container body 21 with film like and waterfall shape each communicating pores 25a from this first system stream plate 25.

The above-mentioned second system stream plate 26, its periphery (end edge) forms the zigzag shape, flowing of the former water of beverage of former water of beverage that control is flowed down by the first system stream plate, 25 system streams or each communicating pores 25a that passes through the first system stream plate 25 makes it to flow down to the internal space of container body 21 from the peripheral part (overhang) that this second system flows plate 26 with film like and waterfall shape.

Above-mentioned the 3rd system stream plate 27, inner circumferential surface (end edge) forms the zigzag shape, flowing of the former water of beverage of former water of beverage that control is flowed down by the first system stream plate 25 or the second system stream plate, 26 system streams or each communicating pores 25a by the first system stream plate 25 makes it to flow down to the internal space of container body 21 with film like and the waterfall shape interior perimembranous (overhang) from the 3rd system stream plate 27.

Above-mentioned water level detecting portion 28 is made by photopermeability materials such as glass or resins, comprising: length direction is attached to the ingress pipe 28a on the periphery of container body 21 along the vertical direction; With, two water level sensor 28b, 28c to be set up in parallel up and down near container body 21 peripherys the ingress pipe 28a.

Are communicated with in the upper end of above-mentioned ingress pipe 28a and bottom and the container body 21, the liquid level position in this ingress pipe 28a is according to container body 21 interior water levels and lifting, and above-mentioned water level sensor 28b, 28c detect above-mentioned liquid level position.

Utilize this water level detecting portion 28, liquid level position when the water level in the container body 21 rises in the ingress pipe 28a also rises, and when its water level sensor 28b by upside detected, the water level that is judged as in the container body 21 surpassed the upper limit, the aperture of supply valve 22c is adjusted, and increases the oxygen feed rate.Thus, the oxygen pressure in the container body 21 uprises, and the supply quantitative change that supplies to the outside is many, and the water levels in the container body 21 descend.

On the other hand, liquid level when the water level in the container body 21 descends in the ingress pipe 28a also descends, and when its water level sensor 28c by downside detected, the water level that is judged as in the container body 21 surpassed lower limit, the aperture of supply valve 22c is adjusted, and reduces the oxygen feed rate.Thus, the oxygen pressure step-down in the container body 21 supplies to outside feed rate and tails off, and the water level in the container body 21 rises.

Like this, utilize this oxygen dissolution process equipment 20, at first, by the supply-pipe 22b and the first water service pipe 23a oxygen is supplied in the container body 21 from oxygen supply source 22a, container body 21 inside become the above oxygen atmosphere of normal atmosphere.

Then, when utilizing pumping unit 23e with adding the former water of beverage (oxygen dissolves preceding water) that treatment facility 15 handled when supplying to the second water service pipe 23b, after in the logical second water service pipe 23b of the former current of the beverage that is supplied to, in the first water service pipe 23a with the oxygen mix of supplying with by supply-pipe 22b, circulate in this first water service pipe 23a while being in contact with one another, 23c is spued with oxygen from its discharge opening.

The former water of beverage that is spued sprays (with reference to Fig. 6 arrow C 1) with water spray shape (is the radial of center with discharge opening 23c) to top-direction, because the internal diameter of discharge opening 23c is littler than the internal diameter of the other parts of the first water service pipe 23a, so the former water of the beverage that is ejected pressure when spuing uprises and its flow velocity accelerates, and comes out with large-scale radial wild-flowing.

Then, top surface or inner peripheral surface from the former water slug of beverage of discharge opening 23c ejection to container body 21, or flow to below (reference arrow C2) or rebound (not have diagram) or flow to below (not illustrating) along the periphery of the first water service pipe 23a along this top surface or inner peripheral surface, then, it flows by 25 controls of the first system stream plate, flows down (reference arrow C3 and C4) with film like and waterfall shape from this first communicating pores 25a that makes stream plate 25 to the internal space of container body 21.

Then, the former water of beverage that is flowed down by the first system stream plate, 25 system streams or rebound and the former water of beverage of each the communicating pores 25a by the first system stream plate 25, it flows by 26 controls of the second system stream plate, with film like and waterfall shape, the peripheral part that flows plate 26 from this second system flows down (reference arrow C5) to the internal space of container body 21.

Afterwards, the former water of beverage that is flowed down by the first system stream plate 25 or the second system stream plate, 26 system streams or rebound and the former water of beverage of each the communicating pores 25a by the first system stream plate 25, it flows by 27 controls of the 3rd system stream plate, to the internal space of container body 21, flow down (reference arrow C6) with film like and waterfall shape from the interior perimembranous that the 3rd system flows plate 27, and be stored in the bottom of container body 21.

And, in the first water service pipe 23a and in the flow process in the container body 21 of so former water of beverage, the oxygen that touches the former water of this beverage is dissolved in wherein.

Generate the sweet water with following feature thus, that is: the molten storage of oxygen is brought up to the hyperoxia concentration of 25～70mg/l from 6 preceding～8mg/l of this processing; Even and back, bottle Kaifeng still remains on more than the 15mg/l, more preferably remains on more than the 35mg/l through 24 hours molten storages of oxygen.This is considered to: under the high pressure oxygen atmosphere, when water molecules contacts with oxygen molecule, their a part of ionization, this water molecules and oxygen molecule become the bonded state by ionic linkage is dissolved in the water oxygen, so, can obtain the function water that the molten storage of hyperoxia concentration and oxygen is difficult to reduce by this class ionic linkage.

Then, the sweet water (water after the oxygen dissolving) that is stored in container body 21 passes through the oxygen pressure of container body 21 inside, is fed into outside (above-mentioned filling treatment facility 16) from the 3rd water service pipe 24.

Be stored in the water level of the sweet water in the container body 21, when surpassing its upper limit or detect by water level detecting portion 28 in limited time down, when water level surpass last in limited time, the liquid level position in the ingress pipe 28a is detected by the water level sensor 28b of upside; When water level surpasses down in limited time, by the level switch 28c detection of downside.

Like this, when water level surpasses certain limit and by water level sensor 28b, when 28c detects, adjust the aperture of supply valve 22c and adjust the oxygen feed rate, thus, the oxygen pressure adjustment of adjusting in the container body 21 supply to outside feed rate, and the oxygen in the container body 21 and the ratio of sweet water are maintained within a certain range.

In addition, first and the second water service pipe 23a, 23b and the 3rd water service pipe 24 are formed: the inside diameter D 2 of the 3rd water service pipe 24 is same as or less than the inside diameter D 1 of the first and second water service pipe 23a, 23b, so the sweet water in the container body 21 is difficult to be fed into outside (sweet water is stored in the container body 21 easily), the oxygen pressure of container body 21 inside is enhanced higher pressure.

In addition, when oxygen was dissolved in the former water of beverage, the gases such as nitrogen that originally contain (being dissolved with) were emitted from the former water of this beverage according to the Henry rule, so the oxygen concn in the container body 21 reduces gradually, the oxygen meltage of the former water of beverage reduces.Therefore, the oxygen concentration in the container body 21 should maintain more than the certain value, regularly the gases such as nitrogen in the amount discharge container body 21.

Particularly, at first, close supply valve 22c and stop oxygen being supplied in the container body 21, afterwards, the vent valve 29a that opens vapor pipe 29 makes the 21 inside and outside connections of container body.Thus, container body 21 gas inside pressure are reduced to the pressure that equates with normal atmosphere, and the sweet water that is stored in the container body 21 can not supply to the outside from the 3rd water service pipe 24.

Then, further supply with the former water of beverage in container body 21, the water level in this container body 21 is risen, the gas in the container body 21 is discharged to container body 21 outsides from vapor pipe 29 from each water service pipe 23a, 23b.

As described above, make oxygen be dissolved in the former water of beverage by oxygen dissolution process equipment 20 and generate sweet water, then, above-mentioned filling treatment facility 16 will be filled in the bottle interior back sealing of specified volume by the sweet water that the 3rd water service pipe 24 of this oxygen dissolution process equipment 20 is supplied with.

If utilize the sweet water manufacturing installation 1 of structure like this, at first,, handle, purify the former water of beverage successively with the order of the first filtration treatment portion 12, the second filtration treatment portion 13 and contrary saturation process portion 14 by purification apparatus 11; Then, VITAMIN, mineral substance and amino acid etc. are added in the former water of beverage that purified with purification apparatus 11 by adding treatment facility 15; Then, by oxygen dissolution process equipment 20,, generate the sweet water of high density ground dissolving aerobic with adding the former water of beverage that treatment facility 15 has added VITAMIN, mineral substance and amino acid etc.; Then, the sweet water that will be generated in oxygen dissolution process equipment 20 by filling treatment facility 16 is filled in back sealing in the bottle, makes bottled drink water.

Like this, sweet water molten storage of oxygen under sealed state of the present embodiment of being made by this sweet water manufacturing installation 1 is a high density, in addition, even back, bottle Kaifeng contacts with air, the back, Kaifeng is at the state that also kept hyperoxia concentration through the afore mentioned rules time in the past, so when wanting to drink this sweet water, want the amount of drinking with regard to drinkable, simultaneously, even whenever drink the oxygen that also can absorb the abundant amount that can access effect as described above.Thus, this sweet water is suitable to be drunk, and can further improve its commodity value.

In addition, since be with purification apparatus 11 purifications, almost do not sneak into the former water of beverage of impurity, and be to make, so can further improve commodity value by the former water of beverage that has added VITAMIN, mineral substance and amino acid etc. with interpolation treatment facility 15.

In addition, above-mentioned sweet water manufacturing installation 1 also has the advantage of the following stated except that can suitably making this class sweet water.

That is, with the former water of radial ejection beverage, increase the contact area of former water of this beverage and oxygen from discharge opening 23c; Simultaneously,, the former water of this beverage is flowed down to the internal space of container body 21 from this each system stream plate 25,26,27 with film like and waterfall shape, the former water of beverage is contacted with oxygen from the both sides of moisture film by flowing of the former water of each system stream plate 25,26,27 control beverage; In addition, also improve the oxygen pressure of container body 21 inside; So, more oxygen is dissolved in the former water of this beverage effectively, can generate the sweet water that hyperoxia concentration as described above and the molten storage of oxygen are difficult to reduce effectively.

In addition, though in container body 21, be provided with each system stream plate 25,26,27, but the falling flow and can not be subjected to their restriction of the former water of beverage, so when can handle the former water of a large amount of beverages effectively, when gases such as discharge nitrogen, water level in the container body 21 is risen rapidly, promptly discharge this gas.

In addition, will be with the former water supply of the beverage that purification apparatus 11 purified to container body 21, owing to foreign body obstruction first systems such as not having rubbish flows each communicating pores 25a of plate 25 or the gap between each system stream plate 25,26,27, so there is no need to remove the operation of foreign matter, can reduce maintenance cost, simultaneously, there is no need to make the structure of container body 21 become removable reservoir, therefore can simplify the resistance to air loss of structure, reduction manufacturing cost and the raising container body 21 of container body 21 in order to remove foreign matter.

In addition,, the flow state of the former water of beverage is changed, improve the frequency of exposure of former water of this beverage and oxygen by a plurality of systems stream plates 25,26,27 being set to increase the system stream number of times of the former water of beverage, thus, dissolved oxygen more effectively.

In addition, owing to form the periphery of the second system stream plate 26 and the inner peripheral surface of the 3rd system stream plate 27 with the zigzag shape, so extended the girth of this periphery and inner peripheral surface, increased the former water of beverage that flows down from the second system stream plate 26 and the 3rd system stream plate 27 with film like and waterfall shape surface-area, increased the contact area of former water of beverage and oxygen, more oxygen is dissolved in the former water of this beverage.

In addition, owing to make the top of container body 21 form outstanding laterally spherical flexure plane, so can make the former water of beverage that spues from discharge opening 23c, impact container body 21 tops flow to the first system stream plate, 25 sides along this top inner surface, it flows and makes it to flow down in the internal space of container body 21 by these first system stream plate, 25 controls, can improve the oxygen meltage of the former water of this beverage.

In addition, the upper surface of the first water service pipe 23a is configured in upper side in the container body 21, upper side in container body 21 makes the former water of beverage spue from discharge opening 23c, so can make from discharge opening 23c and spue the back, can further improve the oxygen meltage of the former water of this beverage until being stored in mobile distance lengthening container body 21 bottoms, the former water of beverage.

In addition, the inside diameter D 2 of the 3rd water service pipe 24 is constituted as identical or less than the inside diameter D 1 of the first and second water service pipe 23a, 23b, so the sweet water that is difficult to be stored in the container body 21 supplies to the outside, can further improve the oxygen pressure in the container body 21, can make more oxygen be dissolved in the former water of the beverage that flows in this oxygen atmosphere effectively.

In addition, even the oxygen pressure in the container body 21 rises because of any reason, water level in the container body 21 also is difficult to descend, and makes the oxygen in the container body 21 leak into outside unfavorable condition from the 3rd water service pipe 24 so can prevent this water level from dropping to the suction port 24a that is lower than the 3rd water service pipe 24 effectively.

In addition, former water of mixing drink and oxygen also make it to be in contact with one another, oxygen is dissolved in the former water of beverage, and meanwhile make it in the first water service pipe 23a to discharge opening 23c side flow, so can be effectively and oxygen is dissolved in the former water of beverage.

In addition, the internal diameter of discharge opening 23c is constituted as the internal diameter less than the other parts of the first water service pipe 23a, so pressure in the time of can improving the former water of beverage and spue and improve its flow velocity, make the former water of beverage that spues from discharge opening 23c with wider radial distribution, can be more effectively and make oxygen be dissolved in the former water of beverage in large quantities, or can be more effectively and make in large quantities in the first water service pipe 23a and be dissolved in the former water of this beverage with the former water blended of beverage oxygen.

In addition, with the first water service pipe 23a be configured in container body 21 co-axial positions on, flow down in container body 21 so can make from the former water homodisperse of the beverage ground that discharge opening 23c spues, can carry out this processing effectively.

More than, one embodiment of the present invention has been described, but the concrete mode that the present invention can adopt is not subjected to any restriction of this mode.

For example, in last example, make oxygen be dissolved in the former water of beverage and used oxygen dissolution process equipment 20 when generating sweet water, but be not limited thereto, also can use as Fig. 7～oxygen dissolution process equipment 40 shown in Figure 9.In addition, Fig. 7 is the sectional drawing of concise and to the point formation of the oxygen dissolution process equipment of expression other embodiment of the present invention, and Fig. 8 is the sectional drawing along the arrow D-D direction among Fig. 7, and Fig. 9 is the explanatory view that is used for illustrating the current of other embodiment of the present invention.

As shown in Figure 7, above-mentioned oxygen dissolution process equipment 40 is the equipment that is different from oxygen supply portion 22, water supply portion 23, the 3rd water service pipe 24 and each system stream plate 25,26,27 in the above-mentioned oxygen dissolution process equipment 20, for the component part mark same-sign identical, omit its detailed description with oxygen dissolution process equipment 20.

As Fig. 7 and shown in Figure 8, above-mentioned oxygen dissolution process equipment 40 possesses: said vesse body 21, with oxygen supply to the oxygen supply portion 41 in the container body 21, above-mentioned pressure detector (not have diagram), with the water supply portion 42 of the former water supply of beverage in the container body 21, the sweet waters in the container body 21 are supplied to outside water service pipe (second water service pipe) 43, are disposed at first and second of upper position in the container body 21 and make plate 44,45 and the above-mentioned water level detecting portion 28 of flowing.

Above-mentioned oxygen supply portion 41 comprises: above-mentioned oxygen supply source 22a; One distolateral oxygen supply source 22a, another distolateral supply-pipe 41a that is connected in the top of container body 21 of being connected in; Above-mentioned supply valve 22c; The vent valve 41b that connection container body 21 is inside and outside.Usually, supply valve 22c Be Controlled is in the state of opening with the aperture of regulation, and vent valve 41b Be Controlled is in closing state.

Above-mentioned water supply portion 42 possesses: the bottom periphery of a distolateral calm body 21, is bent to the L word shape at the central part of container body 21 and prolongs the first water service pipe 42a that is provided with to the top of this container body 21 to its inside by injection; With, be connected in another distolateral said pump device 23e of the first water service pipe 42a.

The above-mentioned first water service pipe 42a possess in its above-mentioned end (upper end) and the container body 21 top surface at a distance of the predetermined distance configuration, at the discharge opening 42b of this upper surface opening, the top-direction opening of this discharge opening 42b in container body 21 is to this top-direction former water of beverage that spues.In addition, not shown reverse checkvalve is arranged at the first water service pipe 42a, prevents to supply to the adverse current of the former water of beverage in the container body 21 by this reverse checkvalve (not having diagram).

Above-mentioned second water service pipe 43, the bottom periphery of the distolateral calm body 21 of one is arrived its inside by injection, in container body 21, bend to the L word shape and prolong setting to the bottom surface of this container body 21 direction, by the oxygen pressure of these container body 21 inside, the sweet water (water of dissolving aerobic) that is stored in container body 21 inner bottom parts is supplied to container body 21 outsides.

In addition, second water service pipe 43 possesses: the bottom surface of its above-mentioned end (lower end) and container body 21 at a distance of the predetermined distance configuration, this lower surface opening, be used for sweet water is supplied to outside suction port 43a.In addition, second water service pipe 43 is constituted as that its inside diameter D 2 is same as or less than the inside diameter D 1 of the first water service pipe 42a.

The above-mentioned first system stream plate 44 is made of flat board and cyclic parts, its periphery is fixed on the top inner peripheral surface of container body 21 by intercalation, and be configured in about equal height position, the upper end of the first water service pipe 42a on, control is along the former water of inner peripheral surface mobile beverage of container body 21 or impact the top of container body 21 and the flowing of the former water of beverage that rebounds, and makes it to flow down to the internal space of container body 21 with film like and waterfall shape interior perimembranous from this first system stream plate 44.

The above-mentioned second system stream plate 45 is made of flat board and cyclic parts equally, inner circumferential surface is fixed on the upper end side periphery of the first water service pipe 42a by intercalation, and be configured in the below of the first system stream plate 44, control is along the former water of periphery mobile beverage of the first water service pipe 42a or impact the top of container body 21 and the flowing of the former water of beverage that rebounds, and makes it to flow down to the internal space of container body 21 with film like and waterfall shape peripheral part from this second system stream plate 45.

Like this, utilize this oxygen dissolution process equipment 40, at first, by oxygen supply portion 41 oxygen is supplied in the container body 21, container body 21 inside become the above oxygen atmosphere of normal atmosphere.Then, when utilizing pumping unit 23e with the former water of beverage (oxygen dissolving before water) when supplying to the first water service pipe 42a, in the logical first water service pipe 23a of the former current of the beverage that is supplied to after, spued in the container body 21 by this discharge opening 42b.

The former water of beverage that is spued sprays (with reference to Fig. 9 arrow C 11) with water spray shape (is the radial of center with discharge opening 42b) to top-direction, impact the top surface or the inner peripheral surface of container body 21, perhaps flow to below (reference arrow C12) or rebound (not have diagram) or along the periphery of the first water service pipe 42a mobile (reference arrow C13) downwards along this top surface or inner peripheral surface.

Along the former water of inner peripheral surface mobile beverage of container body 21,,, to the internal space of container body 21, flow down (reference arrow C14) from this first interior perimembranous of making stream plate 44 with film like and waterfall shape afterwards by the first system stream plate, 44 system streams; Along the former water of periphery mobile beverage of the first water service pipe 42a,, to the internal space of container body 21, flow down (reference arrow C15) from this second peripheral part of making stream plate 45 with film like and waterfall shape by the second system stream plate, 45 system streams.

In addition, the major part of the above-mentioned former water of beverage that rebounds, it does not flow by each system stream plate 44,45 control, flows down in the internal space of container body 21.

So, flowing down the bottom that the former water of beverage in the oxygen atmosphere is stored in container body 21, the former water of the beverage of storage (water after the oxygen dissolving, that is, sweet water) is filled treatment facility 16 because of the oxygen pressure of container body 21 inside is fed into from second water service pipe 43.

Like this, also can obtain the effect same with this oxygen dissolution process equipment 40 with above-mentioned oxygen dissolution process equipment 20, that is: can be with the former water of beverage from discharge opening 42b with radial ejection, simultaneously, can make along the former water of periphery mobile beverage of the inner peripheral surface of container body 21 and the first water service pipe 42a to flow down from each system stream plate 44,45, so can generate the sweet water etc. that high density ground has dissolved oxygen with film like and waterfall shape.

In addition, in above-mentioned oxygen dissolution process equipment 40, the above-mentioned second system stream plate 45 also can be constituted as Figure 10 and the described second system stream plate 46 of Figure 11.

As Figure 10 and shown in Figure 11, the above-mentioned second system stream plate 46 is formed dull and stereotyped and rectangular-shaped, simultaneously, its periphery is formed the zigzag shape, possess a plurality of communicating pores 46a that connect its inside and outside and the insert opening 46b that forms at central part, make the former water of beverage with film like and waterfall shape when peripheral part flows down, the former water of beverage is dripped from communicating pores 46a with a plurality of drops.

It is on the concentric(al) circles at center that above-mentioned communicating pores 46a is formed on insert opening 46b, is formed on inboard communicating pores 46a and the communicating pores 46a that is formed on outside intersection setting respectively on the position of circumferential direction with departing from.

In addition, the second system stream plate 46 is, the inner peripheral surface of insert opening 46b is scheduled on the upper end side periphery of the first water service pipe 42a by outer build-in, four bights are supported by the inner peripheral surface of container body 21, on the top position that is configured in the first system stream plate 44 at a distance of predetermined distance, between periphery and container body 21 inner peripheral surfaces, form gap 46c.

In the oxygen dissolution process equipment of the second system stream plate 46 that possesses this spline structure and the first system stream plate 44, as following, the former water of beverage flows in the container body 21.

Promptly, with the former water of the radial beverage that is ejected (reference arrow C21) after impact the top surface or the inner peripheral surface of container body 21, perhaps along this top or inner peripheral surface flows downwards (reference arrow C22) or rebound (not diagram), perhaps along the periphery of the first water service pipe 42a flow downwards (reference arrow C23).

So, along the former water of periphery mobile beverage of the first water service pipe 42a or the former water of beverage that rebounds, by second system stream plate 46 systems flowing thereafter, and flow down with film like and waterfall shape peripheral part from this second system stream plate 46, perhaps with a plurality of drops from the communicating pores 46a of the second system stream plate 46 drip (reference arrow C24).

On the other hand, along the former water of inner peripheral surface mobile beverage of container body 21, rebound and by former water of the beverage of gap 46c and the former water of beverage that flows down by the second system stream plate, 46 systems, flow by the first system stream plate, 44 systems, and flow down (reference arrow C25) from this first interior perimembranous of making stream plate 44 with film like and waterfall shape.

Even constitute like this and dispose each system stream plate 44,46, the former water of beverage that spues from discharge opening 42b is flowed down from interior perimembranous or the peripheral part that each system flows plate 44,46 with film like and waterfall shape, simultaneously, also can make it to drip with a plurality of drops from communicating pores 46a, so can generate the sweet water of high density ground dissolving aerobic etc., can obtain and above-mentioned same effect.

In addition, as shown in figure 12, in above-mentioned oxygen dissolution process equipment 20, even the tubular system stream unit 31 of both ends of the surface opening is disposed at the end face of container body 21 with its axis direction direction along the vertical direction, also can with spued from discharge opening 23c, along the former water of this end face mobile beverage, by system stream unit 31 system stream, and make it to the internal space of container body 21, to flow down with film like and waterfall shape bottom from this system stream unit 31.In addition, though not shown, this equally also is applicable to above-mentioned oxygen dissolution process equipment 40.

In addition, this moment is in orthographic plan, if form the inner peripheral surface of above-mentioned system stream unit 31 with the zigzag shape, as described above, can extend this inner peripheral surface girth, can increase from the surface-area of the former water of beverage that flows down of system stream unit 31, can increase the contact area with oxygen, more oxygen is dissolved in the former water of this beverage.

In addition, in last example, the allocation position of each system stream plate 25,26,27,44,45,46 is not particularly limited, but on the upper position of preferred disposition in container body 21.For example, system stream plate 25,45,46 is disposed at the upper end of water service pipe 23a, 42a, or be disposed in scope less than about 3 times of inner diameter values of discharge opening 23c, 42b, be positioned at this upper end below the position on, in addition, preferably will make stream plate 27,44 and be configured in the top position that is higher than discharge opening 23c, 42b.

Like this, from each system stream plate 25,26,27,44,45,46 flow down the back, arrive to the water surface of the sweet water of storing at container body 21 to fall distance variable long, so can make the former water of more oxygen and beverage contact and be dissolved in the former water of beverage.

In addition, the position relation about between each system stream plate 25,26,27,44,45,46 can be configured in the either party upper side or lower side, in addition, also can be arranged on the position of about equal height.

And about the shape of each system stream plate 25,26,27,44,45,46, for example, the shape of the shape of periphery or inner peripheral surface, communicating pores 25a, 46a or formation position etc. also are not particularly limited.Form the periphery of zigzag shape (spination) or the shape of inner peripheral surface, also can use slick curve-like, or rectangle is wavy, or the wavy combination of these spinations, curve-like and rectangle replaces this zigzag shape.

In addition, the configured number of each system stream plate 25,26,27,44,45,46 is without any qualification, both can be part or all the structure that this each system stream plate 25,26,27,44,45,46 is not set, also can be the multistage structure that is provided with more than last example.

In addition, the upper surface of water service pipe 23a, 42a preferably is arranged on the upper side in the container body 21, the upper side of the former water of beverage in container body 21 spued, so it is back, elongated until the mobile distance of the former water of beverage that is stored in container body 21 bottoms to be spued from discharge opening 23c, 42b, can further improve the oxygen meltage of sweet water.

In addition, in last example, water service pipe 23a, 23b, a 42a are arranged in the container body 21, but many water service pipe 23a, 23b, 42a also can be set.In addition, the inside diameter D 1 of water service pipe 23a, 23b, 42a other parts except that the part of discharge opening 23c are formed fixed inner diameter, and the inside diameter D 2 of water service pipe 24,43 forms fixed inner diameter, but these internal diameters also can form in the mode of suitable variation.

In addition, in last example, the top of container body 21 is formed outstanding laterally spherical flexure plane, be not limited thereto, though not shown but also can form outstanding to the inside spherical flexure plane.Like this, can make the former water of beverage that impacts container body 21 end faces along the inner peripheral surface side of this end face to container body 21, that is, the first system stream plate, 25,44 side flow can be flowed down by these first system stream unit, 25,44 system streams, so can improve the oxygen meltage of sweet water.

In addition, in last example, in adding treatment facility 15, VITAMIN, mineral substance and amino acid etc. are added in the former water of beverage, but be not limited thereto, also can add other composition except that these VITAMIN, mineral substance and amino acid.

In addition, it is constituted as: VITAMIN, mineral substance and amino acid etc. are added in the former water of beverage that purified with purification apparatus 11 by adding treatment facility 15; But be not limited thereto, also can be constituted as: oxygen is dissolved in the former water of the beverage that purified with purification apparatus by oxygen dissolution process equipment, generate sweet water, afterwards, by adding treatment facility VITAMIN, mineral substance and amino acid etc. are added in this sweet water, then, be filled in back sealing in the bottle by the sweet water of filling after treatment facility is handled this interpolation.

In addition, the structure of oxygen dissolution process equipment 20,40, it only is the expression of the structure of an example, be not limited to above-mentioned structure, in addition, based on Fig. 6, Fig. 9 and Figure 11 and the flowing of the former water of beverage of explanation (C1～C6, C11～C15, C21～C25) be an example just also, and such flowing naturally changes according to the discharge-amount of the former water of beverage or the pressure that spues etc.

In addition, in last example, enumerate the example of sweet water as function water, but be not limited thereto, this function water also can be used as the raw material of pharmaceuticals or makeup etc., for example when being used in medicament for the eyes or eyewash, astringent, also can obtain absorbing the metabolic effect that oxygen promotes this part from the surface of eye or skin.

So, when this function water during as the raw material of pharmaceuticals or makeup etc., for example be dissolved in the former water that purified with above-mentioned purification apparatus 11 with above-mentioned oxygen dissolution process equipment 20,40 with making the oxygen high density, systematic function water, the function water that generates directly can be supplied to the production line of pharmaceuticals or makeup, maybe the function water that generates can be filled in the suitable movable container and supply with.

In addition, can also medicine be added in this function water to make medicament for the eyes or eyewash, astringent etc. with adding treatment facility 15.

Claims (15)

1. a function water has been dissolved the oxygen more than the natural concentration of ordinary dissolution in former water, it is characterized in that,

The molten storage of oxygen of just having carried out after the oxygen dissolution process is 25～70mg/l, afterwards, remains on more than the 15mg/l through the molten storage of oxygen after 24 hours under the state in being positioned over atmosphere.

2. function water as claimed in claim 1 is characterized in that,

Contain at least a among VITAMIN, mineral substance, amino acid or the medicine.

3. function water as claimed in claim 1 or 2 is characterized in that,

Be filled, be sealed in the movable container.

4. a functional water making method is characterized in that,

The oxygen of pressurization is supplied in the encloses container body, make this encloses container body inside become the above oxygen atmosphere of normal atmosphere, simultaneously,

Former water is spued in the described encloses container body, in described encloses container body, flows down,, generate the function water of the oxygen that is dissolved with 25～70mg/l with the oxygen gas-to-liquid contact with membranaceous by making the former water that is spued,

Then, in described encloses container body, take out the function water that generates.

5. functional water making method as claimed in claim 4 is characterized in that,

Purify described former water by contrary saturation process, the former water supply after purifying is arrived in the described encloses container body.

6. functional water making method as claimed in claim 4 is characterized in that,

After adding at least a among VITAMIN, mineral substance, amino acid or the medicine in the described former water, this is added former water supply after handling in described encloses container body.

7. functional water making method as claimed in claim 5 is characterized in that,

After adding at least a among VITAMIN, mineral substance, amino acid or the medicine in the former water after the described purification, this is added former water supply after handling in described encloses container body.

8. as claim 4 or 5 described functional water making methods, it is characterized in that,

With at least a the adding to the function water of in described encloses container body, taking out among VITAMIN, mineral substance, amino acid or the medicine.

9. as each described functional water making method of claim 4～7, it is characterized in that,

The function water that to take out in the described encloses container body is filled in back sealing in the movable container.

10. functional water making method as claimed in claim 8 is characterized in that,

At least a function water of having added among VITAMIN, mineral substance, amino acid or the medicine is filled in back sealing in the movable container.

11. a functional water manufacturing apparatus is characterized in that,

Possess: the oxygen dissolution process equipment portion of the oxygen systematic function water in former water more than the dissolving nature concentration of ordinary dissolution; With, the function water of utilizing this oxygen dissolution process equipment portion to generate is filled in the filling treatment facility portion that the back seals in the movable container,

Described oxygen dissolution process equipment portion possesses: the encloses container body; Have and be connected in the intravital supply-pipe of described encloses container, oxygen supplied in the described encloses container body, make this encloses container body inside become the oxygen supply unit of the oxygen atmosphere more than the normal atmosphere by this supply-pipe; Have one distolaterally be connected in the described encloses container body, in this encloses container body with upper and lower to configuration and formed first water service pipe of discharge opening in the upper surface, from the discharge opening of this first water service pipe to the spue water supply unit of described former water of the top-direction of described encloses container body; Be connected in the described encloses container body, and the described function water that will be stored in bottom this encloses container body supplies to the second outside water service pipe; From the outstanding to the inside first system stream unit of the inner face of described encloses container body and/or from the outstanding laterally second tabular system stream unit of an end-side outer peripheral surface of described first water service pipe,

Described oxygen dissolution process equipment section is constituted as: the top-direction of described former water from described discharge opening to described closed container body spued; Simultaneously; The former water that spues from this discharge opening and flow along the outer peripheral face of the inner peripheral surface of described closed container body and/or described first feed pipe is flowed down to the inner space of described closed container body from the jag of described first stream unit processed and/or second stream unit processed; Thereby make described former water carry out gas-liquid contact in described closed container body inside with oxygen and generate described function water

Described filling treatment facility portion is constituted as: the function water that will be supplied to from second water service pipe of described oxygen dissolution process equipment portion is filled in back sealing in the described movable container.

12. functional water manufacturing apparatus as claimed in claim 11 is characterized in that,

Also possess the contrary saturation process equipment portion that purifies described former water,

The water supply unit of described oxygen dissolution process equipment portion is constituted as, and the former water that purifies by described contrary saturation process equipment portion is spued from the discharge opening of described first water service pipe.

13. functional water manufacturing apparatus as claimed in claim 11 is characterized in that,

Also possess at least a interpolation treatment facility portion that adds in the described former water among VITAMIN, mineral substance, amino acid or the medicine,

The water supply unit of described oxygen dissolution process equipment portion is constituted as, and the former water handled by described interpolation treatment facility portion is spued from the discharge opening of described first water service pipe.

14. functional water manufacturing apparatus as claimed in claim 12 is characterized in that,

Also possess at least a interpolation treatment facility portion that adds in the former water that purified by described contrary saturation process equipment portion among VITAMIN, mineral substance, amino acid or the medicine,

The water supply unit of described oxygen dissolution process equipment portion is constituted as, and the former water handled by described interpolation treatment facility portion is spued from the discharge opening of described first water service pipe.

15. as claim 11 or 12 described functional water manufacturing apparatus, it is characterized in that,

Also possess and add at least a among VITAMIN, mineral substance, amino acid or the medicine to from the function water that second water service pipe of described oxygen dissolution process equipment portion is supplied to interpolation treatment facility portion,

Described filling treatment facility portion is constituted as, and the function water of handling by described interpolation treatment facility portion is filled in back sealing in the described movable container.

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