WO2010002164A2 - Oxygenated water production device - Google Patents
Oxygenated water production device Download PDFInfo
- Publication number
- WO2010002164A2 WO2010002164A2 PCT/KR2009/003525 KR2009003525W WO2010002164A2 WO 2010002164 A2 WO2010002164 A2 WO 2010002164A2 KR 2009003525 W KR2009003525 W KR 2009003525W WO 2010002164 A2 WO2010002164 A2 WO 2010002164A2
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- WO
- WIPO (PCT)
- Prior art keywords
- oxygen
- rotating body
- case
- oxygen water
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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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
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
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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
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
-
- 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
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
- B01F23/23761—Aerating, i.e. introducing oxygen containing gas in liquids
- B01F23/237612—Oxygen
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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
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/272—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed axially between the surfaces of the rotor and the stator, e.g. the stator rotor system formed by conical or cylindrical surfaces
- B01F27/2721—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed axially between the surfaces of the rotor and the stator, e.g. the stator rotor system formed by conical or cylindrical surfaces provided with intermeshing elements
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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
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/27—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices
- B01F27/272—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed axially between the surfaces of the rotor and the stator, e.g. the stator rotor system formed by conical or cylindrical surfaces
- B01F27/2722—Mixers with stator-rotor systems, e.g. with intermeshing teeth or cylinders or having orifices with means for moving the materials to be mixed axially between the surfaces of the rotor and the stator, e.g. the stator rotor system formed by conical or cylindrical surfaces provided with ribs, ridges or grooves on one surface
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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
- C02F1/74—Treatment of water, waste water, or sewage by oxidation with air
Definitions
- the present invention relates to an oxygen water production apparatus, and more particularly, to an oxygen water production apparatus capable of containing a high concentration of oxygen in water.
- Oxygen water refers to water in which the amount of oxygen dissolved (ie dissolved oxygen) is greater than the average average dissolved oxygen (approximately 7 ppm at room temperature in air). As mentioned above, such oxygen water is beneficial to plants, animals or humans because the amount of oxygen contained in the water is higher than that of ordinary water.
- supplying oxygen water to a fishbowl or aquaculture farms not only contributes to the growth of fish growing in a fishbowl or aquaculture farms, but also purifies water that contains feces or other suspended solids as they grow. There is an advantage that can proceed faster by a high concentration of oxygen.
- oxygen water when used as drinking water, oxygen can be supplied to the body even through water, so it may be helpful to the elderly, who are uncomfortable breathing through the respiratory system.
- this advantageous oxygen water production apparatus produces oxygen water in two ways. One is to produce oxygen water by using an electrolysis method, and the other is to produce oxygen water by simultaneously pressurizing water and oxygen to a plurality of partitions in which fine pores are formed.
- the oxygen water production apparatus using the former method is expensive to manufacture and install, there is a problem that the generated oxygen is generated in the form of bubbles rather than dissolved in the water disappears into the atmosphere.
- the oxygen water producing apparatus using the latter method has an advantage of obtaining a relatively high concentration of dissolved oxygen, but requires a considerably high pressure to increase the concentration of oxygen.
- the latter oxygen water production apparatus has a problem that the amount of dissolved oxygen of the produced oxygen water drops sharply in the atmosphere (see FIG. 9), so it is difficult to be utilized in farms or agricultural products cultivators that require a large amount of oxygen water.
- the present invention is to solve the above problems, an object of the present invention is to provide an oxygen water production apparatus capable of producing oxygen water containing a relatively small amount of dissolved oxygen changes with time while containing a high concentration of dissolved oxygen.
- an oxygen water production apparatus for mixing a liquid containing water and a gas containing oxygen, the upper surface is open, the cylindrical case formed with an outlet;
- a cover coupled to an upper surface of the case and having a first inlet and a second inlet through which water, oxygen, or gas are respectively introduced;
- a rotating shaft rotatably installed in the case;
- a disk-shaped first rotating body installed at a predetermined interval on the rotating shaft and having a tooth-shaped protrusion formed on an outer surface thereof;
- a disc-shaped second rotating body provided at a predetermined interval on the rotating shaft, and having a tooth-shaped protrusion formed on an outer surface thereof and having a larger diameter than the first rotating body;
- a ring-shaped first fixing body installed at a predetermined interval on the inner side of the case, having a serrated protrusion formed on the inner side thereof, and having an inner diameter larger than an outer diameter of the first rotating body;
- a ring-shaped second stationary body installed at a predetermined interval on the inner side of the case
- the first rotating body and the second rotating body are respectively installed in succession of two or more sheets, and the first fixing body and the second fixing body are respectively the first rotating body and the second rotating body. It is preferable to be installed in the case so as to correspond to the installation position of the.
- the first rotating body, the second rotating body, the first fixing body, and the second fixing body may be disposed so that protrusions of adjacent members are shifted from each other.
- cover may be further provided with a gas micronization means to generate bubbles when mixing the liquid flowing through the first inlet and the gas flowing through the second inlet.
- gas atomization means is preferably a filter member provided in the second inlet.
- Oxygen water production apparatus of the present invention has the advantage that can produce a high concentration of oxygen water through a relatively simple structure.
- the oxygen water production apparatus of the present invention can not only continuously produce oxygen water, but also change the dissolved oxygen amount of oxygen water by changing the arrangement and arrangement number of the rotating body and the fixed body inside, It can be used in large farms or large agricultural fields that require high oxygen and high concentrations of oxygen.
- the oxygen water production apparatus of the present invention can dissolve the oxygen in the water in the form of micro bubbles through the gas micronization means, it is possible to increase the effect by the oxygen water.
- FIG. 1 is a block diagram of an oxygen water production apparatus according to the present invention.
- FIG. 2 is an exploded perspective view of the oxygen water production apparatus according to the first embodiment of the present invention.
- FIG. 3 is a longitudinal sectional view of the oxygen water production apparatus according to the first embodiment of the present invention.
- FIG. 4 is a cross-sectional view taken along the line A-A of FIG. 3.
- FIG 5 is an exploded perspective view of the oxygen water production apparatus according to the second embodiment of the present invention.
- FIG. 6 is an exploded perspective view of the oxygen water production apparatus according to the third embodiment of the present invention.
- FIG. 7 is an exploded perspective view of an oxygen water producing apparatus according to a fourth embodiment of the present invention.
- FIG. 8 is an exploded perspective view of the oxygen water production apparatus according to the fifth embodiment of the present invention.
- FIG. 9 is a cross-sectional view of the oxygen water producing apparatus shown in FIG.
- FIG. 10 is a cross-sectional view showing a state of use of the oxygen water production apparatus shown in FIG.
- FIG. 11 is an exploded perspective view of the oxygen water production apparatus according to the sixth embodiment of the present invention.
- FIG. 12 is a cross-sectional view of the oxygen water producing apparatus shown in FIG.
- FIG. 13 is a cross-sectional view of the oxygen water producing apparatus according to the seventh embodiment of the present invention.
- 15 is a chart showing the relationship between the internal pressure and the dissolved oxygen amount
- 17 is a chart showing the relationship between the rotational speed and the dissolved oxygen amount of the oxygen water production apparatus.
- control unit 4 122: second inlet
- cover 190 gas micronization means (or filter)
- FIG. 1 is a configuration diagram of an oxygen water production apparatus according to the present invention
- Figures 2 to 4 is a view of a first embodiment of the present invention.
- Oxygen water production apparatus 1 includes a cylindrical case 11, the first inlet 4 for supplying water and the second inlet for supplying oxygen gas to the upper surface (upper side in the drawing) of the case 11 (5) is formed, the drive means 2 is coupled to the bottom surface (down in the figure) of the case (11). The operation of the drive means 2 is controlled by the controller 3. The water and the oxygen gas supplied into the case 11 are mixed by the oxygen water producing apparatus 1, discharged through the outlet 7, and supplied to the necessary device 6.
- the driving means 2 is connected to the rotary shaft 12 located on the central axis of the case 11, and drives the rotary shaft 12 to rotate.
- the rotating body 13 is fixed around the rotating shaft 12, and when the rotating shaft 12 rotates by the drive means 2, the rotating body 13 also rotates together.
- the rotor 13 is formed with a plurality of protrusions 17 extending outward in the radial direction thereof.
- the rotor 13 is composed of a plurality of annular rotors 15 superimposed in the axial direction of the rotary shaft 12, each The rotating body 15 is formed with a hexahedral protrusion 17 extending outward in the radial direction thereof. Therefore, the rotating body 15 is formed in the shape of a gear having a tooth of a hexahedron shape.
- each of the rotors 15 is positioned so that the protrusions 17 are located between the protrusions 17 of the rotors 15 adjacent in the axial direction of the rotary shaft 12, that is, the adjacent rotors.
- the projections 17 of the whole 15 are arranged to be shifted from each other.
- a key groove 19 is formed at a predetermined position of each rotating body 15 to form a key formed on one side of the rotating shaft 12. Can be matched with (21).
- the fixed body 14 is fixed to the inner surface of the case 11.
- the fixture 14 is composed of a plurality of annular fixtures 16 superimposed in the axial direction of the rotary shaft 12, each of the fixtures 16 extends inward in the radial direction A hexahedral shaped projection 18 is formed.
- each fixture 16 is positioned such that the projections 18 are located between the projections 18 of the adjacent fixtures 16 in the axial direction of the rotation axis 12, that is, the adjacent heights.
- the projections 18 of the stagnation 16 are arranged to be offset from each other.
- the key groove 20 is formed at a predetermined position of each fixture 16, the key formed on one side of the case 11 Can be matched with (22).
- the protrusion 18 may not be formed on the intermediate plate 16a which is one of the fixing bodies 16.
- the intermediate plate 16a where no protrusions are formed, it is possible to cause a difference in pressure between the suction side and the discharge side above and below the intermediate plate 16a, so that water and oxygen gas can be sufficiently mixed at the suction side.
- the intermediate plate 16a can be any of the fixtures 16, but is preferably a fixture 16 near the middle.
- the intermediate plate 16a is shown as one, you may form two or more as needed.
- the rotary body 13 and the fixed body 14 is formed of a plurality of plates, the projections 17, 18 are formed to be hexahedral, but is not limited to this, the rotary body 13 ) And the fixing body 14 may each be formed in an integral cylindrical shape, and the protrusions 17 and 18 may have different shapes.
- the second embodiment of the present invention is formed in an integral cylindrical shape having a hole penetrating the center of the rotor 23 and the fixture 24, respectively.
- a plurality of hexahedral protrusions 27 extending radially outward are formed to be arranged in the circumferential direction and the axial direction.
- the fixed body 24 is formed such that a plurality of hexahedral protrusions 28 extending inward in the radial direction thereof are arranged in the circumferential direction and the axial direction.
- the third embodiment of the present invention has a cylindrical shape in which the rotating body 33 and the fixing body 34 have a hole passing through the center thereof, and the rotating body 33 has a radially outer side thereof.
- a plurality of hemispherical protrusions 37 extending toward each other are formed to be arranged in the circumferential direction and the axial direction.
- the fixing body 34 is formed such that the protrusions 38 having the same shape as in the second embodiment are arranged in the circumferential direction and the axial direction.
- the concave portion 49 may be formed in the rotating body 43 instead of the protruding portion. That is, by forming a plurality of concave portions 49 extending in the radial direction on the rotating body 43 so that the portions except the concave portions 49 protrude relatively outward in the radial direction, the protruding portion is a projection ( 47). As a result, vortices can be generated by the projections 47 formed by the recesses 49 of the rotating body 43 and the protrusions 48 of the fixing body 44, so that stable oxygen water can be produced.
- FIG. 8 is an exploded perspective view of the oxygen water production apparatus according to the fifth embodiment of the present invention
- Figure 9 is a cross-sectional view of the oxygen water production apparatus shown in Figure 8
- Figure 10 is the oxygen water production apparatus shown in FIG. Is a cross-sectional view showing the state of use.
- Oxygen water production apparatus 100 according to a fifth embodiment of the present invention, as shown in Figure 8, the case 110, the cover 120, a plurality of first rotating body 140, a plurality of second It includes the whole 150, a plurality of first fixing body 160, a plurality of second fixing body 170, the driving means 180.
- the case 110 is a generally cylindrical member and accommodates a plurality of rotors 140 and 150 and a plurality of fixtures 160 and 170.
- the upper surface 112 of the case 110 is open so that these members can be easily installed and detached, and the side of the case 110, more specifically, the lower side of the case 110 may discharge material to the outside of the case 110.
- a discharge port 114 is formed.
- a key 116 protruding toward the radial center of the case 110 is formed in the case 110 so that the plurality of fixing members 160 and 170 may be firmly fixed without moving.
- a valve for adjusting the flow rate and discharge time of the oxygen water discharged from the case 110 may be installed.
- the cover 120 is a member for sealing the open upper surface 112 of the case 110 and is coupled to the upper portion of the case 110 by fastening means such as bolts and nuts.
- the cover 120 is formed with a first inlet 122 and a second inlet 124 for supplying a liquid (especially water) and a gas (especially oxygen) to the inside of the case 110. That is, the first inlet 122 is connected to the tank (not shown) storing the liquid, and the second inlet 124 is connected to the tank (not shown) storing the gas.
- each of the inlets (122, 124) may be provided with a valve for adjusting the flow rate.
- an airtight member for example, rubber packing
- airtightness between the two members may be further installed at the edge of the cover 120 or the contact surface of the cover 120 and the case 110.
- the rotating shaft 130 is installed in the center of the case 110 along the longitudinal direction of the case 110.
- One end of the rotation shaft 130 protrudes through the bottom of the case 110, and the other end extends to a range not departing from the upper surface of the case 110 in the case 110.
- the key 132 is formed in the rotation shaft 130 along the longitudinal direction of the rotation shaft 130. The key 132 rotates the rotary shafts 140 and 150 to the rotary shaft 130 so that the plurality of rotary bodies 140 and 150 installed on the rotary shaft 130 can be integrally rotated with the rotary shaft 130. Serve as an anchor.
- the rotating shaft 130 and the coupling portion of the case 110 that is, the bottom surface of the case 110 through which the rotating shaft 130 penetrates the case 110
- the bearing and the airtight member are installed to prevent the material contained in the case 110 from leaking to the interface between the rotation shaft 130 and the case 110.
- This configuration is known to those of ordinary skill in the art, so a detailed description thereof will be omitted.
- the first rotating body 140 is a generally thin disk-shaped member, and has a plurality of protrusions 142 protruding at regular intervals along the circumferential direction. In the center of the first rotating body 140, a hole 143 into which the rotating shaft 130 is fitted and a key groove 144 into which the key 132 of the rotating shaft 130 is inserted are formed.
- the first rotatable body 140 formed as described above has a form of a cog wheel with a hole 143 in the center as a whole, and is installed at regular intervals along the longitudinal direction of the rotating shaft 130.
- the second rotating body 150 is a disk-shaped member having a diameter d2 that is thinner than the first rotating body 140 but larger than the diameter d1 of the first rotating body 140, and has a circumferential direction around the second rotating body 150. It has a plurality of protrusions 152 protruding at regular intervals. Like the first rotating body 140, a hole 153 into which the rotating shaft 130 is fitted and a key groove 154 into which the key 132 of the rotating shaft 130 is inserted are formed at the center of the second rotating body 150, respectively. do.
- the second rotating body 150 formed as described above forms a larger and thinner cogwheel than the first rotating body 140 and is installed at a predetermined interval along the longitudinal direction of the rotating shaft 130 (in FIG. 9 in this embodiment). As shown in the installation between the first rotating body 140).
- the second rotating body 150 may be disposed such that the protrusions 152 of the second rotating body 150 are shifted from the protrusions 142 of the first rotating body 140 adjacent to each other.
- the first fixing body 160 is a generally thin ring-shaped member, and has a plurality of protrusions 162 protruding at regular intervals along the inner surface.
- the inner surface of the first fixing body 160 is formed with a key groove 164 into which the key 116 of the case 110 is fitted.
- the first fixing body 160 formed as described above forms a ring shape having teeth on the inner surface as a whole, and is installed at predetermined intervals along the longitudinal direction of the case 110.
- the inner diameter of the first fixing body 160 (the diameter of the virtual circle formed by the plurality of protrusions 162; D1) of the first rotating body 140, so that the first rotating body 140 can be inserted It is larger than the outer diameter (the diameter of the imaginary circle which many protrusion 142 makes; d1).
- the deviation between the inner diameter D1 of the first fixing body 160 and the outer diameter d1 of the first rotating body 140 is 3 to 7 mm.
- the inner diameter (D1) of the first fixing body 160, the second rotating body 150, so that the gap formed between the rotating body (140, 150) and the fixing body (160, 170) can be optimized It is better to be equal to or larger than the outer diameter d2 of (see FIG. 9).
- the second fixing body 170 is a ring-shaped member thicker than the first fixing body 160 and has a plurality of protrusions 162 protruding at regular intervals along the inner surface.
- the inner side of the second fixing body 170 is formed with a key groove 174 into which the key 116 of the case 110 is fitted.
- the second fixing body 170 formed as described above forms a ring shape having teeth on the inner surface as a whole, and is installed at regular intervals along the longitudinal direction of the case 110 (as shown in FIG. 9 in the present embodiment). 1 is installed between the fixing body 160).
- the second fixing body 170 may be disposed such that the protrusions 172 of the second fixing body 170 are displaced from the protrusions 162 of the first fixing body 160 adjacent to each other.
- the inner diameter of the second fixing body 170 (the diameter of the virtual circle formed by the plurality of protrusions 172; D2) of the second rotating body 150, so that the second rotating body 150 can be inserted It is larger than the outer diameter (the diameter of the imaginary circle which many protrusions 152 make; d2).
- the deviation between the inner diameter D2 of the second fixing body 170 and the outer diameter d2 of the second rotating body 150 is 3 to 7 mm.
- the driving means 180 is a member for rotating the rotation shaft 130 and is installed below the case 110.
- the driving means 180 is preferably a motor having a transmission that enables high speed rotation of the rotation shaft 130 and changes the rotation speed of the rotation shaft 130.
- the rotation shaft 130 may be a driving shaft of the driving means 180.
- reference numeral 148 which is not described, is a means for preventing separation of the rotating bodies 140 and 150 by being coupled to the end of the rotating shaft 130.
- the reference numeral 148 is composed of a crown member and a nut so that the mixing of water and oxygen can be made more smoothly, in some cases it may be composed of only a simple nut.
- the first rotating body 140 and the second rotating body 150 are alternately installed on the rotating shaft 130, and the first fixed body 160 is provided.
- the second fixing body 170 are alternately installed in the case 110 to accommodate the first rotating body 140 and the second rotating body 150 therein.
- the inner diameter of the first fixing body 160 A flow path through which the fluid can flow is formed despite being greater than or equal to the outer diameter of the second rotating body 150.
- the oxygen water production apparatus 100 When the oxygen water production apparatus 100 operates, water and oxygen (gas) are supplied into the case 110 through the first inlet 122 and the second inlet 124, respectively, and the driving means 180.
- the rotating shaft 130 is rotated at a high speed (preferably 4000 rpm).
- water and oxygen supplied to the inside of the case 110 pass through between the rotating bodies 140 and 150 rotating at high speed and the stationary fixtures 160 and 170 (particularly between the protrusions).
- the fluid in which the water and the oxygen are mixed that is, the oxygen water
- the oxygen water is continuously produced by the continuous collision of water and oxygen passing between the plurality of rotors 140 and 150 rotating at high speed and the stationary fixtures 160 and 170. Therefore, according to the present invention, it is possible to continuously produce a relatively high concentration of oxygen water.
- FIG. 11 is an exploded perspective view of the oxygen water production apparatus according to the sixth embodiment of the present invention
- Figure 12 is a cross-sectional view of the combined oxygen water production apparatus shown in FIG.
- Oxygen water production apparatus 100 has a difference from the fifth embodiment in the arrangement structure of the rotating body (140, 150) and the stationary body (160, 170).
- the same components as those of the fifth embodiment have the same reference numerals, and detailed descriptions of these components will be omitted.
- the oxygen water producing apparatus 100 of the present embodiment has a structure in which the first rotating body 140 and the second rotating body 150 of the same size are arranged in succession, respectively, as shown in FIGS. 11 and 12.
- the continuously installed rotors 140 and 150 are disposed to be offset from the protrusions 142 and 152 of the rotors 140 and 150 adjacent to the protrusions 142 and 152 (up and down).
- This arrangement also applies to the stationary fixtures 160, 170 installed in series.
- the present embodiment made as described above has a structure in which the rotating bodies 140 and 150 of the same size and the fixing bodies 160 and 170 of the same size are continuously arranged, so that the fluid introduced into the case 110 (especially , Water) is smoother than the first embodiment.
- the continuous rotating bodies 140 and 150 and the fixing bodies 160 and 170 are disposed to be offset from the protrusions 142, 152, 162 and 172 as mentioned above, The mixing power of oxygen does not drop greatly.
- this embodiment is suitable for use in places that require a large amount of oxygen water and do not require high dissolved oxygen (for example, aquaculture farms or other agricultural plantations).
- the rotating bodies 140 and 150 and the fixing bodies 160 and 170 of the same thickness in order to use the rotating bodies 140 and 150 and the fixing bodies 160 and 170 of the same thickness, the first rotating body 140 and the second rotating body 150 and the first By varying the number of installation of the fixing body 160 and the second fixing body 170, a gap is formed in the interface between the first rotating body 140 and the second rotating body 150.
- FIG. 13 is a cross-sectional view of the oxygen water producing apparatus according to the seventh embodiment of the present invention.
- Oxygen water production apparatus 100 has a difference from the fifth embodiment in that it further comprises a gas finer (190).
- a gas finer 190
- the same components as those of the fifth embodiment have the same reference numerals, and detailed descriptions of these components will be omitted.
- Oxygen water production apparatus 100 further includes a gas micronization means 190 as shown in FIG.
- the gas micronization means 190 serves to help the oxygen gas supplied through the second inlet 124 to be further refined to be easily absorbed by water.
- the gas finer 190 is preferably a high density filter such as a HEPA filter.
- the oxygen water producing apparatus 100 configured as described above can greatly improve the amount of dissolved oxygen through miniaturization of oxygen gas, it can be provided at a place requiring high concentration of dissolved oxygen water (for example, treating oxygen water). Hospitals or other nursing homes that serve as drinking or nursing water).
- the gas microrefining means 190 is described as a means for refining the oxygen gas, but if necessary, bubbles are generated in the water supplied through the first inlet 122 to facilitate the absorption of the oxygen gas. It can be replaced by bubble generating means.
- FIG. 14 is a chart showing the relationship between the oxygen supply and dissolved oxygen in water
- Figure 15 is a chart showing the relationship between the internal pressure and dissolved oxygen
- Figure 16 is a chart showing the change of dissolved oxygen over time
- Figure 17 It is a chart which shows the relationship between the rotation speed and the dissolved oxygen amount of an oxygen water manufacturing apparatus.
- Applicants of the present invention can obtain the relationship between the operating conditions and the dissolved oxygen amount of the oxygen water producing apparatus as shown in the table of Figure 14 to 17 and Table 1 through several experiments with the oxygen water producing apparatus of the present invention there was.
- Applicant changes the amount of oxygen supplied through the second inlet 124 while constantly supplying water through the first inlet 122 (20 L / min) to determine a correlation between the oxygen supply amount and the dissolved oxygen amount. saw.
- the first method is to change the water supply amount
- the second method is to open the opening point of the outlet 114
- the amount of dissolved oxygen was generally proportional to the internal pressure of the oxygen water producing apparatus, but the change slope was not so large. Applicants have therefore found that the pressure increase could be one of the ways to increase dissolved oxygen, but this method is not very effective.
- the applicant has found that the ideal number of series connections of the oxygen water production apparatus does not exceed three, and the increase rate of the number of series connections and the amount of dissolved oxygen according to this experiment is not so large.
- Applicants have left the oxygen water produced by the oxygen water production apparatus of the present invention and the conventional oxygen water production apparatus in the air for several days in order to grasp the correlation between the storage time of the oxygen water and the dissolved oxygen amount.
- the dissolved oxygen content of the oxygen water produced by the conventional oxygen water production apparatus rapidly decreased in about one day (about 60%), and after about five days, the dissolved oxygen content of the conventional water was (About 7 ppm).
- the dissolved oxygen amount of the oxygen water produced by the oxygen water production apparatus of the present invention was reduced by about 20% the next day, about 50% by about 5 days.
- the oxygen water production apparatus of the present invention lasts a longer amount of dissolved oxygen than the conventional oxygen water production apparatus, but it is confirmed again that the storage period of oxygen water (ideally 5 days) is not very long. Was done.
- Applicant tried to change the rotation speed of the rotating shaft 130 through the drive means in order to determine the correlation between the rotation speed and the dissolved oxygen amount of the oxygen water production apparatus of the present invention.
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Abstract
Description
본 발명은 산소수 제조장치에 관한 것으로서, 더욱 상세하게는 고농도의 산소를 수중에 함유시킬 수 있는 산소수 제조장치에 관한 것이다.The present invention relates to an oxygen water production apparatus, and more particularly, to an oxygen water production apparatus capable of containing a high concentration of oxygen in water.
산소수란 산소의 용존량(즉 용존산소량)이 일반적인 평균 용존산소량(대기 중 상온에서 대략 7 ppm이다)보다 큰 물을 말한다. 이러한 산소수는 언급한 바와 같이 물속에 함유된 산소량이 일반적인 물보다 많으므로, 식물이나 동물 또는 사람에게 유익하다.Oxygen water refers to water in which the amount of oxygen dissolved (ie dissolved oxygen) is greater than the average average dissolved oxygen (approximately 7 ppm at room temperature in air). As mentioned above, such oxygen water is beneficial to plants, animals or humans because the amount of oxygen contained in the water is higher than that of ordinary water.
예를 들어, 산소수를 어항이나 양식장에 공급하면, 어항이나 양식장에서 자라는 어류의 성장에 큰 도움을 줄 뿐만 아니라 어류들이 성장하면서 발생하는 배설물이나 기타 부유물이 포함된 물의 정화가 산소수에 함유된 고농도의 산소에 의해 더욱 빠르게 진행될 수 있는 장점이 있다.For example, supplying oxygen water to a fishbowl or aquaculture farms not only contributes to the growth of fish growing in a fishbowl or aquaculture farms, but also purifies water that contains feces or other suspended solids as they grow. There is an advantage that can proceed faster by a high concentration of oxygen.
아울러, 산소수를 식물재배에 사용하면, 식물재배에 따른 농산물의 수확량이 일반적인 농업용수를 공급했을 때 보다 약 10% 이상 증가한다는 농업진흥연구원의 연구결과도 있다.In addition, the use of oxygen water for plant cultivation, the Agricultural Research Institute's research shows that the yield of agricultural products according to plant cultivation increases by more than 10% than when supplying general agricultural water.
또한, 산소수를 식수로 사용하면, 물을 통해서도 산소를 체내에 공급할 수 있으므로, 호흡기를 통한 호흡이 불편한 노약자들에게 작으나마 도움을 줄 수 있다.In addition, when oxygen water is used as drinking water, oxygen can be supplied to the body even through water, so it may be helpful to the elderly, who are uncomfortable breathing through the respiratory system.
따라서 이와 같은 산소수를 널리 저변확대하여 어업(특히 양식업)과 농업 등에 적극적으로 활용할 필요성이 있다.Therefore, it is necessary to actively expand such oxygen water to actively use it for fishing (especially aquaculture) and agriculture.
한편, 이와 같이 유익한 산소수 제조장치는 크게 2가지 방식으로 산소수를 제조한다. 하나는 전기분해방식을 이용하여 산소수를 제조하는 것이고, 다른 하나는 미세한 구멍이 형성된 다수의 칸막이에 물과 산소를 동시에 가압하여 산소수를 제조하는 방식이다.On the other hand, this advantageous oxygen water production apparatus produces oxygen water in two ways. One is to produce oxygen water by using an electrolysis method, and the other is to produce oxygen water by simultaneously pressurizing water and oxygen to a plurality of partitions in which fine pores are formed.
그러나, 전자의 방식을 취하는 산소수 제조장치는 제조 및 설치비용이 고가이고, 발생된 산소가 물속에 용존하기 보다는 기포형태로 발생하여 대기 중으로 사라지는 문제점이 있다.However, the oxygen water production apparatus using the former method is expensive to manufacture and install, there is a problem that the generated oxygen is generated in the form of bubbles rather than dissolved in the water disappears into the atmosphere.
그리고, 후자의 방식을 취하는 산소수 제조장치는 비교적 높은 농도의 용존산소량을 얻을 수 있는 장점이 있으나, 산소의 농도를 높이기 위해 상당히 높은 압력을 요구한다. 아울러, 후자의 산소수 제조장치는 생산된 산소수의 용존산소량이 대기 중에서 급격히 떨어지는 문제점이 있으므로(도 9 참조), 대량의 산소수를 필요로 하는 양식장이나 농산물 재배농가에서 활용되기 어렵다.In addition, the oxygen water producing apparatus using the latter method has an advantage of obtaining a relatively high concentration of dissolved oxygen, but requires a considerably high pressure to increase the concentration of oxygen. In addition, the latter oxygen water production apparatus has a problem that the amount of dissolved oxygen of the produced oxygen water drops sharply in the atmosphere (see FIG. 9), so it is difficult to be utilized in farms or agricultural products cultivators that require a large amount of oxygen water.
본 발명은 위와 같은 문제점을 해소하기 위한 것으로서, 고 농도의 용존산소량을 함유하면서 시간에 따른 용존산소량의 변화가 비교적 적은 산소수를 생산할 수 있는 산소수 제조장치를 제공하는데 그 목적이 있다.The present invention is to solve the above problems, an object of the present invention is to provide an oxygen water production apparatus capable of producing oxygen water containing a relatively small amount of dissolved oxygen changes with time while containing a high concentration of dissolved oxygen.
상기 목적을 달성하기 위한 본 발명의 한 실시예에 따르면, 물을 포함한 액체와 산소를 포함한 기체를 혼합하는 산소수 제조장치로서, 윗면이 개방되고, 배출구가 형성된 원통형상의 케이스; 상기 케이스의 윗면에 결합되고, 물과 산소 또는 기체가 각각 유입되는 제1유입구와 제2유입구가 각각 형성된 덮개; 상기 케이스의 내부에 회전 가능하게 설치되는 회전축; 상기 회전축에 일정간격으로 설치되고, 외측 면에 톱니모양의 돌기가 일정하게 형성된 원판형상의 제1회전체; 상기 회전축에 일정간격으로 설치되고, 외측 면에 톱니모양의 돌기가 일정하게 형성되며, 상기 제1회전체 보다 큰 지름을 갖는 원판형상의 제2회전체; 상기 케이스의 내측 면에 일정간격으로 설치되고, 내측 면에 톱니모양의 돌기가 일정하게 형성되며, 내측 지름이 상기 제1회전체의 외측 지름보다 큰, 링 형상의 제1고정체; 상기 케이스의 내측 면에 일정간격으로 설치되고, 내측 면에 톱니모양의 돌기가 일정하게 형성되며, 내측 지름이 상기 제2회전체의 외측 지름보다 큰, 링 형상의 제2고정체; 및 상기 회전축을 회전시키는 구동수단을 포함하는 산소수 제조장치가 제공된다.According to an embodiment of the present invention for achieving the above object, an oxygen water production apparatus for mixing a liquid containing water and a gas containing oxygen, the upper surface is open, the cylindrical case formed with an outlet; A cover coupled to an upper surface of the case and having a first inlet and a second inlet through which water, oxygen, or gas are respectively introduced; A rotating shaft rotatably installed in the case; A disk-shaped first rotating body installed at a predetermined interval on the rotating shaft and having a tooth-shaped protrusion formed on an outer surface thereof; A disc-shaped second rotating body provided at a predetermined interval on the rotating shaft, and having a tooth-shaped protrusion formed on an outer surface thereof and having a larger diameter than the first rotating body; A ring-shaped first fixing body installed at a predetermined interval on the inner side of the case, having a serrated protrusion formed on the inner side thereof, and having an inner diameter larger than an outer diameter of the first rotating body; A ring-shaped second stationary body installed at a predetermined interval on the inner side of the case, having a serrated protrusion formed on the inner side, and having an inner diameter larger than an outer diameter of the second rotating body; And a driving means for rotating the rotating shaft.
바람직하게는, 상기 제1회전체와 상기 제2회전체는 각각 2장 이상씩 연속하여 설치되고, 상기 제1고정체와 상기 제2고정체는 각각 상기 제1회전체와 상기 제2회전체의 설치위치에 대응되도록 상기 케이스에 설치되는 것이 좋다.Preferably, the first rotating body and the second rotating body are respectively installed in succession of two or more sheets, and the first fixing body and the second fixing body are respectively the first rotating body and the second rotating body. It is preferable to be installed in the case so as to correspond to the installation position of the.
또한, 상기 제1회전체, 상기 제2회전체, 상기 제1고정체, 상기 제2고정체는 인접한 부재의 돌기가 서로 어긋나도록 배치되는 것이 좋다.The first rotating body, the second rotating body, the first fixing body, and the second fixing body may be disposed so that protrusions of adjacent members are shifted from each other.
또한, 상기 덮개에는 상기 제1유입구를 통해 유입되는 액체와 상기 제2유입구를 통해 유입되는 기체의 혼합 시 기포가 발생하도록, 기체미세화수단이 더 설치되는 것이 좋다.In addition, the cover may be further provided with a gas micronization means to generate bubbles when mixing the liquid flowing through the first inlet and the gas flowing through the second inlet.
또한, 상기 기체미세화수단은 상기 제2유입구에 설치되는 필터부재인 것이 좋다.In addition, the gas atomization means is preferably a filter member provided in the second inlet.
본 발명의 산소수 제조장치는 비교적 간단한 구조를 통해 고 농도의 산소수를 생산할 수 있는 장점이 있다.Oxygen water production apparatus of the present invention has the advantage that can produce a high concentration of oxygen water through a relatively simple structure.
또한, 본 발명의 산소수 제조장치는 산소수의 연속적인 생산이 가능함은 물론이고 내부의 회전체와 고정체의 배치구조 및 배치 수의 변경을 통해 산소수의 용존산소량의 변경도 가능하므로, 대량의 산소수와 고 농도의 산소수를 필요로 하는 대형 양식장이나 대형 농산물 재배지에 활용이 가능하다.In addition, the oxygen water production apparatus of the present invention can not only continuously produce oxygen water, but also change the dissolved oxygen amount of oxygen water by changing the arrangement and arrangement number of the rotating body and the fixed body inside, It can be used in large farms or large agricultural fields that require high oxygen and high concentrations of oxygen.
아울러, 본 발명의 산소수 제조장치는 기체미세화수단을 통해 수중의 산소를 미세기포 형태로 용존시킬 수 있으므로, 산소수에 의해 효과를 증대시킬 수 있다.In addition, the oxygen water production apparatus of the present invention can dissolve the oxygen in the water in the form of micro bubbles through the gas micronization means, it is possible to increase the effect by the oxygen water.
도 1 은 본 발명에 따른 산소수 제조장치의 구성도이다.1 is a block diagram of an oxygen water production apparatus according to the present invention.
도 2 는 본 발명의 제1실시 예에 따른 산소수 제조장치의 분해 사시도다.2 is an exploded perspective view of the oxygen water production apparatus according to the first embodiment of the present invention.
도 3 은 본 발명의 제1실시 예에 따른 산소수 제조장치의 종단면도이다.3 is a longitudinal sectional view of the oxygen water production apparatus according to the first embodiment of the present invention.
도 4 는 도 3 의 선 A-A 에 따른 단면도이다.4 is a cross-sectional view taken along the line A-A of FIG. 3.
도 5 는 의 제2실시 예에 따른 산소수 제조장치의 분해 사시도이다.5 is an exploded perspective view of the oxygen water production apparatus according to the second embodiment of the present invention.
도 6 은 의 제3실시 예에 따른 산소수 제조장치의 분해 사시도이다.6 is an exploded perspective view of the oxygen water production apparatus according to the third embodiment of the present invention.
도 7 은 의 제4실시 예에 따른 산소수 제조장치의 분해 사시도이다.7 is an exploded perspective view of an oxygen water producing apparatus according to a fourth embodiment of the present invention.
도 8은 본 발명의 제5실시 예에 따른 산소수 제조장치의 분리 사시도이고,8 is an exploded perspective view of the oxygen water production apparatus according to the fifth embodiment of the present invention,
도 9는 도 8에 도시된 산소수 제조장치의 결합 단면도이고,9 is a cross-sectional view of the oxygen water producing apparatus shown in FIG.
도 10은 도 9에 도시된 산소수 제조장치의 사용상태를 나타낸 단면도이고,10 is a cross-sectional view showing a state of use of the oxygen water production apparatus shown in FIG.
도 11은 본 발명의 제6실시 예에 따른 산소수 제조장치의 분리 사시도이고,11 is an exploded perspective view of the oxygen water production apparatus according to the sixth embodiment of the present invention,
도 12는 도 11에 도시된 산소수 제조장치의 결합 단면도이고,12 is a cross-sectional view of the oxygen water producing apparatus shown in FIG.
도 13은 본 발명의 제7실시 예에 따른 산소수 제조장치의 결합 단면도이고,13 is a cross-sectional view of the oxygen water producing apparatus according to the seventh embodiment of the present invention,
도 14는 산소공급량과 수중 용존산소량 간의 관계를 나타낸 도표이고,14 is a chart showing the relationship between the oxygen supply amount and dissolved oxygen amount in water,
도 15는 내부압력과 용존산소량의 관계를 나타낸 도표이고,15 is a chart showing the relationship between the internal pressure and the dissolved oxygen amount,
도 16은 시간경과에 따른 용존산소량의 변화를 나타낸 도표이고,16 is a chart showing the change in dissolved oxygen amount over time,
도 17은 산소수 제조장치의 회전수와 용존산소량의 관계를 나타낸 도표이다.17 is a chart showing the relationship between the rotational speed and the dissolved oxygen amount of the oxygen water production apparatus.
< 도면의 주요부분에 대한 부호의 설명 ><Description of Symbols for Major Parts of Drawings>
1, 100: 산소수 제조장치 2, 180 : 구동수단1, 100: oxygen
3 : 제어부 4, 122: 제2유입구3:
5, 124: 제2유입구 6 : 기타장치5, 124: second inlet 6: other equipment
7, 114: 배출구 11, 100: 케이스7, 114:
12, 130: 회전축 13, 15, 23, 33, 140, 150: 회전체12, 130: rotating
14, 16, 24, 34, 160, 170: 고정체14, 16, 24, 34, 160, 170: stationary
16a : 중간판 49 : 오목부16a: intermediate plate 49: recess
19, 20, 144, 154, 164, 174: 키홈19, 20, 144, 154, 164, 174: keyway
21, 22, 132: 키 112: 윗면21, 22, 132: key 112: top
120: 덮개 190: 기체미세화수단(또는 필터)120: cover 190: gas micronization means (or filter)
17, 18, 27, 28, 37, 38, 49, 142, 152, 162, 172: 돌기 17, 18, 27, 28, 37, 38, 49, 142, 152, 162, 172: projection
이하, 본 발명의 바람직한 실시예를 첨부된 예시도면에 의거하여 상세히 설명한다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.
아래에서 본 발명을 설명함에 있어서, 본 발명의 구성요소를 지칭하는 용어들은 각각의 구성요소들의 기능을 고려하여 명명된 것이므로, 본 발명의 기술적 구성요소를 한정하는 의미로 이해되어서는 안 될 것이다.In the following description of the present invention, terms that refer to the components of the present invention are named in consideration of the function of each component, it should not be understood as a meaning limiting the technical components of the present invention.
(제1실시 예)(First embodiment)
도 1 은 본 발명에 따른 산소수 제조장치의 구성도이며, 도 2 내지 도 4 는 본 발명의 제1실시 예에 대한 도면이다.1 is a configuration diagram of an oxygen water production apparatus according to the present invention, Figures 2 to 4 is a view of a first embodiment of the present invention.
산소수 제조장치(1)는 원통형의 케이스(11)를 포함하며, 케이스(11)의 상단면(도면에서 위쪽)에는 물이 공급되는 제1유입구(4)와 산소기체가 공급되는 제2유입구(5)가 형성되며, 케이스(11)의 하단면(도면에서 아래쪽)에는 구동수단(2)이 결합된다. 구동수단(2)의 작동은 제어부(3)에 의해서 제어된다. 케이스(11)내로 공급된 물과 산소기체는 산소수 제조장치(1)에 의해 혼합되며, 배출구(7)를 통해 배출되어 필요한 장치(6)에 공급된다.Oxygen
구동수단(2)은 케이스(11)의 중심축에 위치하는 회전축(12)에 연결되어, 회전축(12)이 회전할 수 있도록 구동한다.The driving means 2 is connected to the
회전축(12)의 주위에는 회전체(13)가 고정되어, 구동수단(2)에 의해 회전축(12)이 회전할 때, 회전체(13)도 함께 회전한다. 회전체(13)에는 그 직경방향 바깥쪽으로 연장되는 복수의 돌기(17)가 형성된다.The rotating
도 2, 도 3, 도 4 에 도시된 본 발명의 제1실시 예에서, 회전체(13)는 회전축(12)의 축방향으로 포개지는 복수의 고리형 회전체(15)로 이루어지며, 각각의 회전체(15)에는 그 직경방향 바깥쪽으로 연장되는 육면체형의 돌기(17)가 형성된다. 따라서, 회전체(15)는 육면체형의 톱니를 가지는 기어 모양으로 형성된다.In the first embodiment of the present invention shown in Figs. 2, 3 and 4, the
또한, 본 발명의 제1실시 예에서 각각의 회전체(15)는 돌기(17)가 회전축(12)의 축방향으로 인접한 회전체(15)의 돌기(17)사이에 위치하도록, 즉 인접한 회전체(15)의 돌기(17)가 서로 어긋나도록 배치된다.Further, in the first embodiment of the present invention, each of the
도 2 에서 볼 수 있듯이, 상기와 같이 인접한 회전체(15)를 어긋나게 배치하기 위해서, 각각의 회전체(15)의 소정 위치에 키홈(19)을 형성하여, 회전축(12)의 일측에 형성된 키(21)와 맞춰지게 할 수 있다.As shown in FIG. 2, in order to displace the adjacent
케이스(11)의 내부면에는 고정체(14)가 고정된다.The fixed
본 발명의 제1실시 예에서 고정체(14)는 회전축(12)의 축방향으로 포개지는 복수의 고리형 고정체(16)로 이루어지며, 각각의 고정체(16)에는 직경방향 안쪽으로 연장되는 육면체형의 돌기(18)가 형성된다.In the first embodiment of the present invention, the
또한, 본 발명의 제1실시 예에서 각각의 고정체(16)는 돌기(18)가 회전축(12)의 축방향으로 인접한 고정체(16)의 돌기(18)사이에 위치하도록, 즉 인접한 고정체(16)의 돌기(18)가 서로 어긋나도록 배치된다.Further, in the first embodiment of the present invention, each
도 2 에서 볼 수 있듯이, 상기와 같이 인접한 고정체(16)를 어긋나게 배치하기 위해서, 각각의 고정체(16)의 소정 위치에 키홈(20)을 형성하여, 케이스(11)의 일측에 형성된 키(22)와 맞춰지게 할 수 있다.As can be seen in Figure 2, in order to displace the
상기와 같은 구성에 의해서, 구동수단(2)에 의해 회전축(12)과 회전체(13)가 함께 회전하면, 회전체(15)의 돌기(17)와 고정체(16)의 돌기(18)의 형상과 배치로 인해서 케이스(11)내의 물과 산소기체의 혼합액이 와류를 일으키게 되고, 그로 인해 혼합액의 입자가 미세화되고 균질하게 분포하게 되어 더욱 안정적인 산소수를 얻을 수 있게 된다.By the above structure, when the rotating
그리고, 도 2 에서 볼 수 있듯이, 고정체(16) 중 하나인 중간판(16a)에는 돌기(18)가 형성되지 않을 수 있다. 돌출부가 형성되지 않은 중간판(16a)에 의해서, 중간판(16a)상하의 흡입측과 토출측의 압력에 차이가 생기도록 할 수 있어, 흡입측에서 물과 산소기체가 충분히 혼합되게 할 수 있다. 중간판(16a)은 고정체(16) 중 어느 것이든 될 수 있지만, 중간 부근의 고정체(16)인 것이 바람직하다. 또한, 중간판(16a)은 하나인 것으로 도시되었지만, 필요에 따라 2개 이상을 형성할 수도 있다.As shown in FIG. 2, the
본 발명의 제1실시 예에서, 회전체(13)및 고정체(14)가 복수의 판으로 이루어지며, 돌기(17, 18)가 육면체형인 것으로 형성되지만, 이에 한정되는 것은 아니며 회전체(13)및 고정체(14)가 각각 일체의 원통형상으로 형성될 수도 있고, 돌기(17, 18)가 다른 형상을 가질 수도 있다.In the first embodiment of the present invention, the
(제2실시 예)Second Embodiment
본 발명의 제2실시 예는 도 5 에 도시된 바와 같이, 회전체(23)및 고정체(24)가 각각 중심을 관통하는 구멍을 가지는 일체의 원통형상으로 형성되며, 회전체(23)에는 그 직경방향 바깥쪽으로 연장되는 복수의 육면체형 돌기(27)가 원주방향 및 축방향으로 배열되도록 형성된다. 또한, 고정체(24)에는 그 직경방향 안쪽으로 연장되는 복수의 육면체형 돌기(28)가 원주방향 및 축방향으로 배치되도록 형성된다.As shown in FIG. 5, the second embodiment of the present invention is formed in an integral cylindrical shape having a hole penetrating the center of the
(제3실시 예)(Third Embodiment)
본 발명의 제3실시 예는 도 6 에 도시된 바와 같이, 회전체(33)및 고정체(34)가 중심을 관통하는 구멍을 가지는 원통형상을 가지며, 회전체(33)에는 그 직경방향 바깥쪽으로 연장되는 복수의 반구형 돌기(37)가 원주방향 및 축방향으로 배열되도록 형성된다. 고정체(34)에는 제 2 실시 예와 동일한 형상의 돌기(38)가 원주방향 및 축방향으로 배치되도록 형성된다.As shown in FIG. 6, the third embodiment of the present invention has a cylindrical shape in which the
(제4실시 예)(Example 4)
본 발명의 제4실시 예는 도 7 에 도시된 것과 같이, 회전체(43)에 돌출부 대신에 오목부(49)를 형성할 수 있다. 즉, 회전체(43)상에 직경방향 안쪽으로 연장되는 복수의 오목부(49)를 형성하여 오목부(49)를 제외한 부분이 상대적으로 직경방향 바깥쪽으로 돌출되도록 함으로써, 돌출된 부분이 돌기(47)로 형성되게 할 수 있다. 결과적으로 회전체(43)의 오목부(49)에 의해 형성되는 돌기(47)와, 고정체(44)의 돌출부(48)에 의해 와류를 발생시킬 수 있어 안정적인 산소수를 제조할 수 있다.In the fourth embodiment of the present invention, as shown in FIG. 7, the
(제5실시 예)(Example 5)
도 8은 본 발명의 제5실시 예에 따른 산소수 제조장치의 분리 사시도이고, 도 9는 도 8에 도시된 산소수 제조장치의 결합 단면도이고, 도 10은 도 9에 도시된 산소수 제조장치의 사용상태를 나타낸 단면도이다.8 is an exploded perspective view of the oxygen water production apparatus according to the fifth embodiment of the present invention, Figure 9 is a cross-sectional view of the oxygen water production apparatus shown in Figure 8, Figure 10 is the oxygen water production apparatus shown in FIG. Is a cross-sectional view showing the state of use.
본 발명의 제5실시 예에 따른 산소수 제조장치(100)는 도 8에 도시된 바와 같이, 케이스(110), 덮개(120), 다수의 제1회전체(140), 다수의 제2회전체(150), 다수의 제1고정체(160), 다수의 제2고정체(170), 구동수단(180)을 포함한다.Oxygen
케이스(110)는 대체로 원통형상의 부재로서, 다수의 회전체들(140, 150)과 다수의 고정체들(160, 170)을 수용한다. 케이스(110)의 윗면(112)은 이들 부재들이 쉽게 설치 및 분리될 수 있도록 개방되며, 케이스(110)의 측면, 더욱 상세하게는 측면 하부에는 케이스(110)의 내부에 물질이 외부로 배출될 수 있는 배출구(114)가 형성된다. 아울러, 케이스(110)의 내부에는 다수의 고정체들(160, 170)이 움직이지 않고 단단히 고정될 수 있도록 케이스(110)의 반경 중심을 향해 돌출된 키(116)가 형성된다. 한편, 배출구(114)에는 도시되지 않았으나 케이스(110)로부터 배출되는 산소수의 유량과 배출시점을 조절하기 위한 밸브가 설치될 수 있다.The
덮개(120)는 케이스(110)의 개방된 윗면(112)을 밀폐시키는 부재로서, 볼트와 너트 등의 체결수단에 의해 케이스(110)의 위쪽에 결합된다. 덮개(120)에는 액체(특히 물)와 기체(특히 산소)를 케이스(110)의 내부로 공급하기 위한 제1유입구(122)와 제2유입구(124)가 형성된다. 즉, 제1유입구(122)는 액체를 저장한 탱크(도시되지 않음)와 연결되고, 제2유입구(124)는 기체를 저장한 탱크(도시되지 않음)와 연결된다. 한편, 각각의 유입구(122, 124)에는 도시되지 않았으나 공급유량을 조절하기 위한 밸브가 설치될 수 있다. 아울러 덮개(120)의 가장자리 또는 덮개(120)와 케이스(110)의 밀착면에는 두 부재 간의 기밀을 위한 기밀부재(예를 들어 고무패킹)가 더 설치될 수 있다.The
회전축(130)은 케이스(110)의 중앙에 케이스(110)의 길이방향을 따라 길게 설치된다. 회전축(130)의 일 단은 케이스(110)의 바닥을 뚫고 돌출되며, 타 단은 케이스(110)의 내부에서 케이스(110)의 윗면을 벗어나지 않는 범위까지 연장된다. 회전축(130)에는 키(132)가 회전축(130)의 길이방향을 따라 길게 형성된다. 이 키(132)는 회전축(130)에 설치되는 다수의 회전체들(140, 150)이 회전축(130)과 일체로 회전될 수 있도록, 이들 회전체들(140, 150)을 회전축(130)에 고정시키는 구실을 한다. 한편, 도 8에는 도시되어 있지 않으나, 회전축(130)과 케이스(110)의 결합부위(즉 회전축(130)이 케이스(110)를 관통하는 케이스(110)의 바닥면)에는 회전축(130)의 회전을 허용하면서, 회전축(130)과 케이스(110)의 경계면으로 케이스(110)에 수용된 물질이 새어나가지 않도록 하는 베어링과 기밀부재가 설치된다. 이러한 구성은 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자에게 있어서 공지된 기술이므로, 이에 대한 상세한 설명은 생략한다.The
제1회전체(140)는 대체로 얇은 원판형태의 부재로서, 둘레에 원주방향을 따라 일정간격으로 돌출된 다수의 돌기(142)를 갖는다. 제1회전체(140)의 중심에는 회전축(130)이 끼워지는 구멍(143)과 회전축(130)의 키(132)가 끼워지는 키홈(144)이 각각 형성된다. 이와 같이 형성된 제1회전체(140)는 전체적으로 중앙에 구멍(143)이 뚫린 톱니바퀴의 형태를 이루며, 회전축(130)의 길이방향을 따라 일정간격으로 설치된다.The first
제2회전체(150)는 제1회전체(140)보다 얇으나 제1회전체(140)의 지름(d1)보다 큰 지름(d2)을 갖는 원판형태의 부재로서, 둘레에 원주방향을 따라 일정간격으로 돌출된 다수의 돌기(152)를 갖는다. 제2회전체(150)의 중심에는 제1회전체(140)와 마찬가지로 회전축(130)이 끼워지는 구멍(153)과 회전축(130)의 키(132)가 끼워지는 키홈(154)이 각각 형성된다. 이와 같이 형성된 제2회전체(150)는 제1회전체(140)보다 크고 얇은 톱니바퀴의 형태를 이루며, 회전축(130)의 길이방향을 따라 일정간격으로 설치된다(본 실시 예에서는 도 9에 도시된 바와 같이 제1회전체(140)의 사이사이에 설치된다). 바람직하게는 제2회전체(150)는 제2회전체(150)의 돌기들(152)이 상하 인접한 제1회전체(140)의 돌기들(142)과 서로 어긋나도록 배치되는 것이 좋다.The second
제1고정체(160)는 대체로 얇은 링 형태의 부재로서, 안쪽 면을 따라 일정간격으로 돌출된 다수의 돌기(162)를 갖는다. 제1고정체(160)의 안쪽 면에는 케이스(110)의 키(116)가 끼워지는 키홈(164)이 형성된다. 이와 같이 형성된 제1고정체(160)는 전체적으로 안쪽 면에 톱니가 형성된 링 형태를 이루며, 케이스(110)의 길이방향을 따라 일정간격으로 설치된다. 한편, 제1고정체(160)의 안쪽 지름(다수의 돌기(162)가 이루는 가상 원의 지름; D1)은 제1회전체(140)가 삽입될 수 있도록, 제1회전체(140)의 바깥 지름(다수의 돌기(142)가 이루는 가상 원의 지름; d1)보다 크다. 바람직하게는 제1고정체(160)의 안쪽 지름(D1)과 제1회전체(140)의 바깥 지름(d1)의 편차는 3 ~ 7 ㎜인 것이 좋다. 아울러, 제1고정체(160)의 안쪽 지름(D1)은 회전체들(140, 150)과 고정체들(160, 170)이 형성하는 간극이 최적화될 수 있도록, 제2회전체(150)의 바깥 지름(d2)과 같거나 또는 더 큰 것이 좋다(도 9 참조).The
제2고정체(170)는 제1고정체(160)보다 두꺼운 링 형태의 부재로서, 안쪽 면을 따라 일정간격으로 돌출된 다수의 돌기(162)를 갖는다. 제2고정체(170)의 안쪽 면에는 케이스(110)의 키(116)가 끼워지는 키홈(174)이 형성된다. 이와 같이 형성된 제2고정체(170)는 전체적으로 안쪽 면에 톱니가 형성된 링 형태를 이루며, 케이스(110)의 길이방향을 따라 일정간격으로 설치된다(본 실시 예에서는 도 9에 도시된 바와 같이 제1고정체(160)의 사이사이에 설치된다). 바람직하게는 제2고정체(170)는 제2고정체(170)의 돌기들(172)이 상하 인접한 제1고정체(160)의 돌기들(162)과 서로 어긋나도록 배치되는 것이 좋다. 한편, 제2고정체(170)의 안쪽 지름(다수의 돌기(172)가 이루는 가상 원의 지름; D2)은 제2회전체(150)가 삽입될 수 있도록, 제2회전체(150)의 바깥 지름(다수의 돌기(152)가 이루는 가상 원의 지름;d2)보다 크다. 바람직하게는 제2고정체(170)의 안쪽 지름(D2)과 제2회전체(150)의 바깥 지름(d2)의 편차는 3 ~ 7 ㎜인 것이 좋다.The
구동수단(180)은 회전축(130)을 회전시키는 부재로서, 케이스(110)의 아래쪽에 설치된다. 구동수단(180)은 바람직하게는 회전축(130)의 고속회전을 가능케 하고 아울러 회전축(130)의 회전속도 변경을 가능케 하는 변속장치를 구비한 모터인 것이 좋다. 참고로, 회전축(130)은 구동수단(180)의 구동축일 수도 있다.The driving means 180 is a member for rotating the
참고로, 미 설명된 도면부호 148은 회전축(130)의 끝에 결합하여 회전체들(140, 150)의 이탈을 방지하는 수단이다. 한편, 본 실시 예에서 도면부호 148은 물과 산소의 혼합이 더욱더 원활하게 이루어질 수 있도록 왕관형태의 부재와 너트로 구성되었으나, 경우에 따라 단순한 너트만으로 구성될 수 있다.For reference,
이와 같이 이루어진 산소수 제조장치(100)는 도 9에 도시된 바와 같이 제1회전체(140)와 제2회전체(150)가 회전축(130)에 교대로 설치되고, 제1고정체(160)와 제2고정체(170)가 각각의 내부에 제1회전체(140)와 제2회전체(150)를 수용할 수 있도록 케이스(110)에 교대로 설치되는 구조를 갖는다. 특히, 제1회전체(140)와 제2회전체(150)그리고 제1고정체(160)와 제2고정체(170)의 두께가 서로 상이하므로, 제1고정체(160)의 안쪽 지름이 제2회전체(150)의 바깥 지름보다 크거나 같음에도 불구하고 유체가 유동할 수 있는 유로가 형성된다.In the oxygen
다음에서는 본 실시 예에 따른 산소수 제조장치(100)의 사용상태를 도 10을 참조하여 설명하겠다.Next, a state of use of the oxygen
산소수 제조장치(100)가 작동하면, 물과 산소(기체상태 임)가 각각 제1유입구(122)와 제2유입구(124)를 통해 케이스(110)의 내부로 공급되고, 구동수단(180)에 의해 회전축(130)이 고속으로 회전된다(바람직하게는 4000rpm).When the oxygen
그러면, 케이스(110)의 내부로 공급된 물과 산소는 고속으로 회전하는 회전체들(140, 150)과 정지된 고정체들(160, 170)의 사이(특히 돌기들 사이)를 지나면서 서로 혼합된다(실질적으로 산소기체가 물 속에 용존된다). 그리고 이와 같이 물과 산소가 혼합된 유체(즉, 산소수)는 케이스(110)의 하부에 형성된 배출구(114)를 통해 외부로 배출된다. 여기서 산소수는 고속으로 회전하는 다수의 회전체들(140, 150)과 정지된 고정체들(160, 170)사이를 통과하는 물과 산소의 지속적인 충돌에 의해 계속적으로 생산된다. 따라서 본 발명에 따르면 비교적 고 농도의 산소수를 지속적으로 생산할 수 있다.Then, water and oxygen supplied to the inside of the
(제6실시 예)(Sixth Embodiment)
도 11은 본 발명의 제6실시 예에 따른 산소수 제조장치의 분리 사시도이고, 도 12는 도 11에 도시된 산소수 제조장치의 결합 단면도이다.11 is an exploded perspective view of the oxygen water production apparatus according to the sixth embodiment of the present invention, Figure 12 is a cross-sectional view of the combined oxygen water production apparatus shown in FIG.
본 실시 예에 따른 산소수 제조장치(100)는 회전체들(140, 150)과 고정체들(160, 170)의 배치구조에 있어서 제5실시 예와 차이점을 갖는다. 참고로, 제5실시 예와 동일한 구성요소는 동일한 도면부호를 사용하고, 이들 구성요소에 대한 상세한 설명은 생략한다.Oxygen
본 실시 예의 산소수 제조장치(100)는 도 11 및 도 12에 도시된 바와 같이 동일한 크기의 제1회전체(140)와 동일 크기의 제2회전체(150)가 연속적으로 각각 배치된 구조를 갖는다. 여기서 연속 설치된 회전체들(140, 150)은 자신들의 돌기들(142, 152)이(상하)인접한 회전체들(140, 150)의 돌기들(142, 152)과 어긋나게 위치되도록 배치된다. 이러한 배치형태는 연속 설치된 고정체들(160, 170)도 마찬가지로 적용된다.The oxygen
이와 같이 이루어진 본 실시 예는 동일 크기의 회전체들(140, 150)과 동일 크기의 고정체들(160, 170)이 연속적으로 배치된 구조이므로, 케이스(110)의 내부로 유입된 유체(특히, 물)의 순환이 제1실시 예에 비해 원활하다. 그러나, 본 실시 예는 연속된 회전체들(140, 150)과 고정체들(160, 170)이 앞서 언급한 바와 같이 돌기들(142, 152, 162, 172)서로 어긋나게 배치되어 있으므로, 물과 산소의 혼합력이 크게 떨어지지 않는다.The present embodiment made as described above has a structure in which the
따라서 본 실시 예는 대량의 산소수를 필요로 하면서 높은 용존산소량을 요구하지 않는 장소(예를 들어, 양식장이나 기타 농산물 재배지)에 활용하는데 적합하다. 참고로, 본 실시 예는 동일한 두께의 회전체들(140, 150)와 고정체들(160, 170)를 사용하기 위해, 제1회전체(140)와 제2회전체(150)그리고 제1고정체(160)와 제2고정체(170)의 설치 수를 달리하여, 제1회전체(140)와 제2회전체(150)가 이루는 경계면에 틈새가 생기도록 하였다.Therefore, this embodiment is suitable for use in places that require a large amount of oxygen water and do not require high dissolved oxygen (for example, aquaculture farms or other agricultural plantations). For reference, in the present embodiment, in order to use the
(제7실시 예)(Example 7)
도 13은 본 발명의 제7실시 예에 따른 산소수 제조장치의 결합 단면도이다.13 is a cross-sectional view of the oxygen water producing apparatus according to the seventh embodiment of the present invention.
본 실시 예에 따른 산소수 제조장치(100)는 기체미세화수단(190)을 더 구비한 점에 있어서 제5실시 예와 차이점을 갖는다. 참고로, 제5실시 예와 동일한 구성요소는 동일한 도면부호를 사용하고, 이들 구성요소에 대한 상세한 설명은 생략한다.Oxygen
제7실시 예에 따른 산소수 제조장치(100)는 도 13에 도시된 바와 같이 기체미세화수단(190)을 더 구비한다. 기체미세화수단(190)는 제2유입구(124)를 통해 공급되는 산소기체를 더욱 미세화하여 물에 용이하게 흡수되도록 도와주는 구실을 한다. 기체미세화수단(190)으로는 HEPA 필터와 같이 고밀도의 필터가 좋다.Oxygen
이와 같이 구성된 산소수 제조장치(100)는 산소기체의 미세화를 통해 용존산소량을 크게 향상시킬 수 있으므로, 고농도 용존산소량의 산소수를 필요로 하는 장소에 제공될 수 있다(예를 들어 산소수를 치료용 또는 건강보조용 식수로 사용하는 병원이나 기타 요양소).Since the oxygen
한편, 본 실시 예에서는 기체미세화수단(190)을 산소기체를 미세화하는 수단으로 설명하였으나, 필요에 따라 제1유입구(122)를 통해 공급되는 물에 기포를 발생시켜 산소기체의 흡수를 원활하게 하는 기포발생수단으로 대체될 수 있다. On the other hand, in the present embodiment, the gas microrefining means 190 is described as a means for refining the oxygen gas, but if necessary, bubbles are generated in the water supplied through the
(실험 예)(Experimental example)
다음에서는 위와 같이 이루어진 본 발명의 여러 실시 예를 통해 실험한 결과를 도표와 표를 참조하여 설명하겠다. 도 14은 산소공급량과 수중 용존산소량 간의 관계를 나타낸 도표이고, 도 15은 내부압력과 용존산소량의 관계를 나타낸 도표이고, 도 16은 시간경과에 따른 용존산소량의 변화를 나타낸 도표이고, 도 17은 산소수 제조장치의 회전수와 용존산소량의 관계를 나타낸 도표이다.Next will be described with reference to the table and the results of the experiment through the various embodiments of the present invention made as described above. 14 is a chart showing the relationship between the oxygen supply and dissolved oxygen in water, Figure 15 is a chart showing the relationship between the internal pressure and dissolved oxygen, Figure 16 is a chart showing the change of dissolved oxygen over time, Figure 17 It is a chart which shows the relationship between the rotation speed and the dissolved oxygen amount of an oxygen water manufacturing apparatus.
본 발명의 출원인은 본 발명의 산소수 제조장치를 통한 수차례의 실험을 통해 도 14 ~ 도 17의 도표와 표 1에 도시된 바와 같이 산소수 제조장치의 작동조건과 용존산소량 간의 관계를 얻을 수 있었다.Applicants of the present invention can obtain the relationship between the operating conditions and the dissolved oxygen amount of the oxygen water producing apparatus as shown in the table of Figure 14 to 17 and Table 1 through several experiments with the oxygen water producing apparatus of the present invention there was.
1. 산소(기체)공급량과 용존산소량의 관계1. Relationship between oxygen (gas) supply and dissolved oxygen
출원인은 산소공급량과 용존산소량 간의 상관관계를 파악하기 위해, 제1유입구(122)를 통해 일정하게 물을 공급하면서(20ℓ/min)제2유입구(124)를 통해 공급되는 산소의 양을 변화시켜 보았다.Applicant changes the amount of oxygen supplied through the
실험결과, 도 14에 도시된 바와 같이, 산소의 공급량을 대략 200㏄/min까지 증가시킨 경우에는 용존산소량이 대략 31ppm까지 비교적 급격하게 증가였으나, 산소의 공급량을 300㏄/min 이상으로 증가시킨 경우에는 용존산소량이 그리 큰 폭으로 증가되지 않았다.As a result, as shown in FIG. 14, when the oxygen supply amount was increased to about 200 kPa / min, the dissolved oxygen amount increased relatively rapidly to about 31 ppm, but when the oxygen supply amount was increased to 300 kPa / min or more. There was no significant increase in dissolved oxygen.
출원인은 이 실험을 통해 물 20ℓ/min에 대한 바람직한 산소공급량이 300㏄/min임을 파악하게 되었다.Applicants have found that the desired oxygen supply for 20 L / min of water is 300 kW / min through this experiment.
2.(산소수 제조장치의)내부압력과 용존산소량의 관계2. Relationship between Internal Pressure and Dissolved Oxygen Amount (in Oxygen Water Production Equipment)
출원인은 본 발명의 산소수 제조장치의 내부압력과 용존산소량 간의 상관관계를 파악하기 위해, 2가지 방법(첫 번째 방법은 물 공급량을 변화시키는 것이고, 두 번째 방법은 배출구(114)의 개방시점을 조절하는 것이다)을 이용하여 산소 제조장치의 내부압력을 변경시켜보았다.Applicants, in order to determine the correlation between the internal pressure and the dissolved oxygen amount of the oxygen water production apparatus of the present invention, two methods (the first method is to change the water supply amount, the second method is to open the opening point of the outlet 114) To adjust the internal pressure of the oxygen production apparatus.
실험결과, 도 15에 도시된 바와 같이, 용존산소량은 산소수 제조장치의 내부압력 크기와 대체로 비례하였으나, 그 변화기울기가 그리 크지 않았다. 따라서 출원인은 용존산소량을 증가시키는 방안 중 하나로 압력증가를 선택할 수 있으나, 이 방안이 그리 효과적인 방법이 아님을 파악하였다.As a result, as shown in FIG. 15, the amount of dissolved oxygen was generally proportional to the internal pressure of the oxygen water producing apparatus, but the change slope was not so large. Applicants have therefore found that the pressure increase could be one of the ways to increase dissolved oxygen, but this method is not very effective.
3. 산소수 제조장치 연결 수와 용존산소량의 관계3. Relationship between the number of oxygen water generators and the amount of dissolved oxygen
출원인은 산소수 제조장치의 직렬연결 대수와 용존산소량 간의 상관관계를 파악하기 위해, 동일한 운행조건의 산소수 제조장치를 직렬로 연결하여 보았다. 표 1은 그 실험결과이다.Applicants have tried to connect the oxygen water production equipment under the same operating conditions in series in order to find out the correlation between the number of oxygen in the oxygen production apparatus and the dissolved oxygen amount in series. Table 1 shows the experimental results.
실험결과, 산소수 제조장치의 직렬연결 수를 1대에서 3대까지 증가시킨 경우에는 용존산소량의 크기가 그리 큰 폭은 아니지만 대체로 비례하여 증가하였으나, 4대 이상에서는 용존산소량의 증가크기가 즐어듬을 알 수 있었다.As a result, when the number of series connections of oxygen water production equipment was increased from 1 to 3 units, the amount of dissolved oxygen was generally increased proportionally, although the size of dissolved oxygen was largely increased, but the increase in dissolved oxygen amount was enjoyed more than 4 units. Could know.
따라서, 출원인은 이 실험을 통해 산소수 제조장치의 이상적인 직렬연결 수가 3대를 넘지 못하고, 실질적으로 직렬연결 대수와 이에 따른 용존산소량의 증가비가 그리 크지 않음을 알게 되었다.Therefore, the applicant has found that the ideal number of series connections of the oxygen water production apparatus does not exceed three, and the increase rate of the number of series connections and the amount of dissolved oxygen according to this experiment is not so large.
표 1
4. 산소수 저장기간과 용존산소량의 관계4. Relationship between oxygen water storage period and dissolved oxygen content
출원인은 산소수의 저장시간과 용존산소량 간의 상관관계를 파악하기 위해, 본 발명의 산소수 제조장치와 종래의 산소수 제조장치에 의해 생산된 산소수를 수일 동안 대기 중에 방치해 두었다.Applicants have left the oxygen water produced by the oxygen water production apparatus of the present invention and the conventional oxygen water production apparatus in the air for several days in order to grasp the correlation between the storage time of the oxygen water and the dissolved oxygen amount.
실험결과, 도 16에 도시된 바와 같이, 종래의 산소수 제조장치에 의해 생산된 산소수의 용존산소량은 하루만에 급격하게 감소되었고(약 60%), 약 5일 이후부터는 통상적인 물의 용존산소량(약 7 ppm)과 같아졌다. 반면, 본 발명의 산소수 제조장치에 의해 생산된 산소수의 용존산소량은 다음날 약 20% 감소되었고, 약 5일째에는 약 50% 감소되었다.As a result, as shown in FIG. 16, the dissolved oxygen content of the oxygen water produced by the conventional oxygen water production apparatus rapidly decreased in about one day (about 60%), and after about five days, the dissolved oxygen content of the conventional water was (About 7 ppm). On the other hand, the dissolved oxygen amount of the oxygen water produced by the oxygen water production apparatus of the present invention was reduced by about 20% the next day, about 50% by about 5 days.
본 실험을 통해, 본 발명의 산소수 제조장치가 종래의 산소수 제조장치에 비해 용존산소량이 오랫동안 지속됨을 알 수 있었으나, 산소수의 저장기간(이상적으로는 5일)이 그리 길지 않음을 재차 확인하게 되었다.Through this experiment, it was found that the oxygen water production apparatus of the present invention lasts a longer amount of dissolved oxygen than the conventional oxygen water production apparatus, but it is confirmed again that the storage period of oxygen water (ideally 5 days) is not very long. Was done.
5.(산소수 제조장치의)회전수와 용존산소량의 관계5.Relationship between Rotation Speed and Dissolved Oxygen (Oxygen Water Production Equipment)
출원인은 본 발명의 산소수 제조장치의 회전수와 용존산소량 간의 상관관계를 파악하기 위해, 구동수단을 통한 회전축(130)의 회전수를 변화시켜 보았다.Applicant tried to change the rotation speed of the
실험결과, 도 17에 도시된 바와 같이, 물속의 용존산소량은 2500rpm에서 현저하게 증가하기 시작하여, 3500rpm 부근에서 급격하게 증가함을 알게 되었다. 다만, 회전축(130)을 지나치게 고속으로 회전시키면 물과 회전체의 마찰에 의해 수증기가 발생하므로, 3000 ~ 4000rpm 범위로 회전시키는 것이 바람직하다.As a result, as shown in FIG. 17, it was found that the amount of dissolved oxygen in the water began to increase significantly at 2500 rpm and increased rapidly around 3500 rpm. However, when the
위에서 언급한 실험결과들은 모두 본 발명의 산소수 제조장치를 최적화하기 위한 운행조건들로서, 본 발명의 특징을 특별히 한정하는 것은 아니지만, 본 발명의 산소수 제조장치와 종래의 산소수 제조장치를 명확하게 구별하는 인자로서 활용될 수 있다.The above-mentioned experimental results are all operating conditions for optimizing the oxygen water producing apparatus of the present invention, but do not specifically limit the features of the present invention, the oxygen water producing apparatus of the present invention and the conventional oxygen water producing apparatus clearly It can be used as a distinguishing factor.
이상에서는 본 발명을 특정의 바람직한 실시예에 대해서 도시하고 설명하였지만, 본 발명은 상술한 실시예에만 한정되는 것은 아니며, 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자라면 이하의 실용신안등록청구범위에 기재된 본 발명의 기술적 사상의 요지를 벗어나지 않는 범위에서 얼마든지 다양하게 변경하여 실시할 수 있을 것이다.Although the present invention has been illustrated and described with respect to specific preferred embodiments, the present invention is not limited to the above-described embodiments, and those skilled in the art to which the present invention pertains may claim the following utility model registrations. Various modifications can be made without departing from the spirit of the technical idea of the present invention described in the scope.
Claims (5)
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| Application Number | Priority Date | Filing Date | Title |
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| KR20-2008-0008669 | 2008-06-30 | ||
| KR2020080008669U KR200450992Y1 (en) | 2008-06-30 | 2008-06-30 | Emulsifying Oil Manufacturing Equipment |
| KR20-2009-0008124 | 2009-06-24 | ||
| KR2020090008124U KR200458752Y1 (en) | 2009-06-24 | 2009-06-24 | An Apparatus for Producing Water having High Density of Oxygen |
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| WO2010002164A2 true WO2010002164A2 (en) | 2010-01-07 |
| WO2010002164A3 WO2010002164A3 (en) | 2010-03-25 |
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| Application Number | Title | Priority Date | Filing Date |
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| PCT/KR2009/003525 Ceased WO2010002164A2 (en) | 2008-06-30 | 2009-06-30 | Oxygenated water production device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| EP3281919A4 (en) * | 2015-04-06 | 2018-10-24 | NABAS Group, Inc. | Nanobubble-and-hydroxyl-radical generator and system for processing polluted water without chemicals using same |
| EP4043096A4 (en) * | 2019-10-11 | 2023-11-08 | Fawoo Nanotech Co., Ltd | NANOBUBLE GENERATION SYSTEM USING FRICTION |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2004074131A (en) * | 2002-08-16 | 2004-03-11 | Takeshi Nakajima | Liquid containing micro-bubbles and its production method |
| FR2871711B1 (en) * | 2004-06-18 | 2006-09-22 | Pcm Pompes Sa | DYNAMIC MIXING DEVICE ONLINE |
| KR200418831Y1 (en) * | 2006-03-14 | 2006-06-14 | (주)퓨쳐솔루션 | Oil-in-water emulsion fuel manufacturing device |
| JP4335888B2 (en) * | 2006-05-23 | 2009-09-30 | 幸夫 中島 | Liquid purification treatment equipment |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| EP3281919A4 (en) * | 2015-04-06 | 2018-10-24 | NABAS Group, Inc. | Nanobubble-and-hydroxyl-radical generator and system for processing polluted water without chemicals using same |
| EP4043096A4 (en) * | 2019-10-11 | 2023-11-08 | Fawoo Nanotech Co., Ltd | NANOBUBLE GENERATION SYSTEM USING FRICTION |
| US12042771B2 (en) | 2019-10-11 | 2024-07-23 | Fawoo Nanotech Co., Ltd. | Nanobubble generation system using friction |
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