JP5829790B2 - Method for producing biological water containing stabilized ozone nanobubble nuclei and biological water - Google Patents

Description

  The present invention relates to a method for producing biological water containing stabilized ozone nanobubble nuclei and biological water.

  In recent years, attention has been paid to nano-sized bubbles in water, that is, water containing nanobubble nuclei of a desired gas, which has been applied to various fields such as medicine, agriculture, aquaculture and aquaculture. .

  For example, Non-Patent Document 1 describes the basics and engineering applications of microbubbles and nanobubbles. Non-Patent Documents 2 to 4 describe application to the medical field using ozone nanobubble sterilization ability, ozone nanobubble cell activation ability, tissue preservation ability, and the like. Non-Patent Document 5 describes the application to agriculture, and Non-Patent Document 6 describes the application of micro- or nano-bubbles to the aquaculture / culture field. In addition, Non-Patent Document 1 describes a measurement method using a dynamic light scattering photometer and a measurement method using an electron spin resonance method (ESR) that measures free radicals caused by nanobubbles as a nanobubble analysis method. .

  Furthermore, the generation mechanism of microbubbles, the mechanism of stabilization as nanobubbles, and the method of conceptual stabilization are described in Non-Patent Document 1 above, and specific examples of methods for producing ozone nanobubble water are described in Patent Documents. 1.

  That is, in the method for producing ozone nanobubbles described in Patent Document 1, ozone is supplied to water mixed with electrolyte ions of minerals as microbubbles having a diameter of 10 to 50 μm, and shock waves and water accompanying water discharge are generated. By applying physical stimuli such as compression, expansion, and vortex generated during the flow of gas, the microbubbles are reduced. At this time, hydrogen ions, hydroxide ions, and electrolyte ions are concentrated at the gas-liquid interface and reduced. By acting as a shell surrounding the bubble, the reduced microbubbles, that is, the ozone nanobubble nuclei are stabilized and exist in water.

  In the present invention, microbubbles in which hydrogen ions, hydroxide ions, and electrolyte ions surround and stabilize the microbubbles are referred to as “nanobubble nuclei”. In the present invention, water containing nanobubble nuclei of ozone is also referred to as “ozone nanobubble water”. Furthermore, as described above, the operation of applying a physical stimulus to reduce microbubbles is referred to as “crushing” in the present invention.

  As described in item 3 of Non-Patent Document 2, water containing nanobubble nuclei has various potency and bactericidal ability such as repair and regeneration, as well as the ability to preserve tissues. In Non-Patent Document 3, in the application to the treatment of periodontal disease using the strong bactericidal effect of water containing ozone nanobubble nuclei (10-30 times bactericidal effect compared with chlorine-based bactericides) Improvement of periodontal pocket and decrease of BOP have been reported.

Japanese Patent No. 4059506

Takahashi, “Basics and Engineering Applications of Micro Bubbles and Nano Bubbles”, Monthly Material Integration, T.I.C., April 25, 2009, Vol. 22, No. 5, p. 2-19 Kanno, “Application of nanobubbles to the medical field”, Monthly Material Integration, T.I.C., April 25, 2009, Vol. 22, No. 5, p. 30-35 Arakawa, 2 others, “Application of nanobubble water to periodontal disease treatment”, Monthly Material Integration, T.I.C., April 25, 2009, Vol. 22, No. 5, p. 36-43 Hokushin, “Anti-inflammatory and anti-cell proliferation effects of ozone nanobubbles: effects on vascular endothelium and smooth muscle cells”, Monthly Material Integration, T.I.C., April 25, 2009, Volume 22, Volume 5 No., p. 44-48 Tamaki, “Possibility of using microbubbles in the agricultural field-Sterilization of hydroponic culture using ozone microbubbles”, Monthly Material Integration, T.I.C., April 25, 2009, No. Vol. 22, No. 5, p. 20-23 Yamamoto, “Application of microbubbles to aquaculture and aquaculture”, Monthly Material Integration, T.I.C., April 25, 2009, Vol. 22, No. 5, p. 24-29

  As shown in the above-mentioned literature, there are conventional examples of applying to the medical field such as periodontal disease treatment using the powerful bactericidal effect of water containing ozone nanobubble nuclei, but they are used for these There is no example of optimizing the salinity of water containing ozone nanobubble nuclei.

  For example, in the past, for example, Non-patent Document 3, page 40, left column, lines 4 to 8, “4 patients with moderate periodontitis, subject to ozone nanobubble water stock solution once, 20 ml, 20 seconds As a result, 61.8% of the periodontal pockets of 3 mm or more (139 out of 225 sites improved by 1 mm or more) was given twice a day. Ozone nanobubble water is used as it is, and the salinity of water containing ozone nanobubble nuclei is not optimized. In addition, the salinity of such provided ozone nanobubble water is about 1.8%.

  By the way, the salt contained in water has been used since ancient times for its bactericidal effect due to its osmotic pressure, and the salt contained in ozone nanobubble water plays a part in the bactericidal effect as ozone nanobubble water. However, when used in a living body, if the concentration is too high, the surface of the living body such as skin may be adversely affected due to the osmotic pressure.

  Therefore, when ozone nanobubble water is used for a living body, it is very important to optimize the salt concentration.

  An object of the present invention is to provide a production method for optimizing the salinity concentration in ozone nanobubble water as water to be used for a living body, and biological water containing ozone nanobubble nuclei produced by the production method. It is what.

In order to achieve the above object, the present invention supplies ozone as microbubbles having a size of 50 μm or less to the first raw material water having a salinity concentration of 0.9% or more higher than the value in the vicinity of 0.9%. To produce a first mixing water containing the stabilized ozone nanobubble nuclei in the water,
Ozone is supplied as microbubbles with a size of 50 μm or less to the second raw material water whose salinity is 0.9% or more higher than the value in the vicinity of 0.9%, and collapsed by physical stimulation to stabilize the ozone nanobubble nuclei. After making it contain in water, the reverse osmosis membrane is made to permeate and a desalination process is performed to produce second mixing water,
These first and second mixing waters are mixed to adjust the salt concentration to 0.9% or a value in the vicinity thereof, and then ozone is supplied again as microbubbles having a size of 50 μm or less, and physical stimulation is performed. A method for producing biomedical water containing stabilized ozone nanobubble nuclei, characterized in that the biomedical water is generated by being crushed by the method described above.

In the present invention, the first raw material water having a salinity concentration of 0.9% or more higher than the value in the vicinity thereof is 0.9% or more.
Ozone is supplied as microbubbles with a size of 50 μm or less to the second raw material water whose salinity is 0.9% or more higher than the value in the vicinity of 0.9%, and collapsed by physical stimulation to stabilize the ozone nanobubble nuclei. After containing in water, mix the water for mixing produced by passing through the reverse osmosis membrane and desalting,
The salinity of 0.9% or was adjusted to a value in the vicinity thereof, the ozone is supplied as following microbubble size 50 [mu] m, while crushed by physical stimuli, organism containing the stabilized ozone nanobubbles nuclei in water We propose a method for producing biological water containing stabilized ozone nanobubble nuclei characterized in that it produces irrigation water .

  In addition, the present invention proposes a method for producing biological water containing stabilized ozone nanobubble nuclei in which the first raw material water and the second raw water are the same in the above production method.

  Further, in the present invention, in the above production method, at least one side of the first raw water and the second raw water contains biological ozone water that contains stabilized ozone nanobubble nuclei that are seaside well water having a salinity of about 2%. We propose a manufacturing method.

  Moreover, in this invention, in said manufacturing method, at least one side of the 1st raw material water and the 2nd raw material water contains the stabilized ozone nano bubble nucleus which is the seawater of the clean sea area whose salt concentration is about 3%. A method for producing biological water is proposed.

  As a result of diligent research and experiments, the inventor has determined that the concentration of ozone nanobubble water as biological water used in living organisms is 0.9% or a value in the vicinity thereof, which is equivalent to that of physiological saline. As a result, the adverse effect of the salt on the living tissue was suppressed, and the bactericidal action of the nanobubble nucleus of ozone could be effectively exhibited at the salt concentration.

  At this time, the ozone nanobubble water uses water whose salt concentration is 0.9% or more higher than the value in the vicinity thereof as raw water, and reduces the salinity concentration of biological water to the above-mentioned 0.9% or a value in the vicinity thereof. As dilution water to be mixed, ozone was supplied as microbubbles with a size of 50 μm or less to water with a salinity of 0.9% or more higher than the value in the vicinity of 0.9%, and stabilized by crushing by physical stimulation. Since water containing ozone nanobubble nuclei in water and then desalted by permeation through a reverse osmosis membrane is used, the nanobubble nuclei of ozone are effectively present in the water, and the bactericidal action due to salt is reduced. The bactericidal effect of ozone nanobubble nuclei could be demonstrated even at the salt concentration.

  The above-described process of decreasing the salt concentration by mixing may be performed before or after the crushing process. Moreover, you may go back and forth.

  By using natural water containing various salinity, such as seaside well water with a salinity of about 2% or clean seawater with a salinity of about 3%, the raw water mentioned above can be destroyed. , It is possible to generate ozone nanobubble nuclei satisfactorily.

FIG. 1 is a schematic system diagram showing the flow of a first reference example for explaining the first embodiment of the manufacturing method of the present invention. FIG. 2 is a schematic system diagram showing the flow of the second reference example for explaining the second embodiment of the manufacturing method of the present invention. FIG. 3 is a schematic system diagram showing the flow of the third embodiment of the manufacturing method of the present invention. FIG. 4 is a schematic system diagram showing the flow of the fourth embodiment of the manufacturing method of the present invention.

  Embodiments of the manufacturing method of the present invention will be described below with reference to the accompanying drawings.

First, in FIG. 1 showing a first reference example for explaining the first embodiment of the production method of the present invention, reference numeral 1 is a salt concentration of 0.9% or more than twice the value in the vicinity thereof. The first raw material water (or its tank) to be contained is shown, and the first raw water 1 is supplied to the crushing container 2. The crushing container 2 is supplied with gas, in this case, ozone, as microbubbles having a size of 50 μm or less from the gas cylinder 3, and in this state, physical crushing is applied to perform crushing. Needless to say, the mixing of the first raw material water and the ozone microbubbles can be performed in another mixing tank or the like.

  The ozone supplied to the crushing container 2 as microbubbles having a size of 50 μm or less is shrunk by physical stimulation. At this time, hydrogen ions, hydroxide ions and electrolyte ions in water are concentrated at the gas-liquid interface, It acts as a shell surrounding the reduced microbubbles, and is stabilized and present in water as reduced microbubbles, that is, ozone nanobubble nuclei.

  Thus, in the crushing container 2, the first mixing water in which ozone is crushed is introduced into the mixing tank 4.

  Next, reference numeral 5 indicates a second raw material water (or a tank thereof) containing a salinity of 0.9% or more than twice the value in the vicinity thereof, and this second raw water 5 It is supplied to the crushing container 6. The crushing container 6 is supplied with ozone from the gas cylinder 7 as microbubbles having a size of 50 μm or less, and in this state, physical stimulation is applied to perform crushing. Of course, the mixing of the second raw material water and the ozone microbubbles can also be performed in another mixing tank or the like as described above.

  The ozone supplied to the crushing container 6 as microbubbles having a size of 50 μm or less is reduced by physical stimulation. At this time, hydrogen ions, hydroxide ions and electrolyte ions in water are concentrated at the gas-liquid interface, It acts as a shell surrounding the reduced microbubbles, and is stabilized and present in water as reduced microbubbles, that is, ozone nanobubble nuclei.

  In this manner, the second raw material water in which ozone is crushed in the crushing container 6 passes through the reverse osmosis membrane 8 to remove salt and impurities such as bacteria, Mn, and Mg, and is generated as the second mixing water. The second mixing water is introduced into the mixing tank 4. The removal of salt and the like by the reverse osmosis membrane 8 may be performed in only one stage, or may be performed in a plurality of stages, for example, two stages.

  In the mixing tank 4, the first mixing water and the second mixing water are mixed at a predetermined mixing ratio by a well-known mixing means, whereby the salt concentration is 0.9%, which is equivalent to physiological saline, or a value in the vicinity thereof. To be produced as biological water.

  Here, the second mixing water is stable because it supplies and crushes ozone as microbubbles in the second raw material water containing a salt concentration of 0.9% or more higher than the value close to 0.9%. Ozone nanobubble nuclei are efficiently generated, and therefore, when passing through the reverse osmosis membrane 8, nanobubble nuclei are not a little removed, but there are not a few smaller nanobubble nuclei. May remain.

  Therefore, after crushing, the amount of ozone nanobubble nuclei is larger than that in the case of producing biological water by diluting the first mixing water that does not pass through the reverse osmosis membrane with simple fresh water or pure water. It is possible to produce biomedical water that is contained in good quality and quality.

  Here, as the first raw material water and the second raw water containing a salinity of 0.9% or more than the value in the vicinity thereof, the seaside well water having a salinity of about 2% or the salinity Clean sea water with a concentration of about 3% can be used. One of these well water and seawater is used as the first (or second) raw water, the other is used as the second (or first) raw water, and only one of these well water and seawater. Can also be used as the first and second raw water. That is, in the latter, the first raw material water and the second raw water are the same.

FIG. 2 shows a second reference example for explaining the second embodiment of the production method of the present invention. In this second reference example , the raw water is only one of well water and seawater. Is used.
Reference numeral 11 indicates raw water (or a tank thereof) containing a salinity higher than 0.9% or a value close to twice the value in the vicinity thereof, and this raw water 11 is supplied to the crushing container 12. The crushing container 12 is supplied with ozone from the gas cylinder 13 as microbubbles having a size of 50 μm or less, and in this state, physical stimulation is applied to perform crushing. Needless to say, mixing of raw water and ozone microbubbles can be performed in another mixing tank or the like.

  The ozone supplied to the crushing container 12 as microbubbles having a size of 50 μm or less is reduced by physical stimulation. At this time, hydrogen ions, hydroxide ions and electrolyte ions in water are concentrated at the gas-liquid interface, It acts as a shell surrounding the reduced microbubbles, and is stabilized and present in water as reduced microbubbles, that is, ozone nanobubble nuclei.

  Thus, the first mixing water in which ozone is crushed in the crushing container 12 is introduced into the mixing tank 4.

  A part of the first water for mixing is introduced into the reverse osmosis membrane 15 and permeated therethrough to remove salt and impurities such as germs, Mn, Mg and the like, and is generated as the second water for mixing. The mixing water is introduced into the mixing tank 14. The removal of salt and the like by the reverse osmosis membrane 15 may be performed in only one stage, or may be performed in a plurality of stages, for example, two stages.

  In the mixing tank 14, the first mixing water and the second mixing water are mixed at a predetermined mixing ratio by a well-known mixing means in the same manner as described above, whereby the salinity is 0.9%, which is equal to that of physiological saline or It is adjusted to a value in the vicinity thereof and generated as biological water.

  As described above, also in the second embodiment, the first and second mixing waters contain ozone in raw water containing a salinity that is 0.9% or more higher than the value in the vicinity thereof. As a result, the stabilized ozone nanobubble nuclei are efficiently generated as the microbubbles are crushed. Therefore, when the second mixing water is permeated through the reverse osmosis membrane, there are few nanobubble nuclei. Even if it is removed, the nanobubble nuclei with a smaller diameter still remain, and therefore, as in the first embodiment, after the collapse, the first non-permeating membrane does not pass through the reverse osmosis membrane. To produce biological water containing ozone nanobubble nuclei quantitatively and qualitatively better than the case of producing biological water by mixing and diluting mixing water with simple fresh water or pure water Can do.

Next, FIG. 3 shows a third embodiment of the manufacturing method of the present invention.
In FIG. 3, reference numeral 21 indicates a first raw water (or a tank thereof) containing a salinity having a salinity concentration of 0.9% or more than twice the value in the vicinity thereof. And introduced into the mixing tank 22.

  The code | symbol 23 shows the 2nd raw material water (or its tank) containing the salinity whose salt concentration is 0.9% or more 2 times or more of the value of the vicinity, This 2nd raw material water 23 is a container for crushing 24. The crushing container 24 is supplied with ozone from a gas cylinder 25 as microbubbles having a size of 50 μm or less, and in this state, physical stimulation is applied to perform crushing. Of course, the mixing of the second raw material water and the ozone microbubbles can also be performed in another mixing tank or the like as described above.

  The ozone supplied to the crushing container 24 as microbubbles having a size of 50 μm or less is reduced by physical stimulation. At this time, hydrogen ions, hydroxide ions, and electrolyte ions in water are concentrated at the gas-liquid interface, It acts as a shell surrounding the reduced microbubbles, and is stabilized and present in water as reduced microbubbles, that is, ozone nanobubble nuclei.

  In this way, in the crushing container 24, the second raw material water in which ozone is crushed passes through the reverse osmosis membrane 26, and salt and impurities such as germs, Mn, and Mg are removed to generate water for mixing. The mixing water is introduced into the mixing tank 22. The removal of salt and the like by the reverse osmosis membrane 26 may be performed in only one stage, or may be performed in a plurality of stages, for example, two stages.

  In the mixing tank 22, the first raw water and the mixing water are mixed at a predetermined mixing ratio by a well-known mixing means in the same manner as described above, whereby the salinity is 0.9%, which is equivalent to that of physiological saline, or the vicinity thereof. Adjusted to the value and then introduced into the crush container 27.

  The crushing container 27 is supplied with ozone from the gas cylinder 28 as microbubbles having a size of 50 μm or less, and in this state, physical stimulation is applied to perform crushing. Of course, the mixing of the mixed first raw material water and mixing water and the microbubbles of ozone can be performed in another mixing tank or the like.

  The ozone supplied to the crushing container 27 as microbubbles having a size of 50 μm or less is reduced by physical stimulation. At this time, hydrogen ions, hydroxide ions and electrolyte ions in water are concentrated at the gas-liquid interface, It acts as a shell surrounding the reduced microbubbles, and is stabilized and present in water as reduced microbubbles, that is, ozone nanobubble nuclei.

  In this way, in the crushing container 27, the ozone is crushed, thereby generating biological water 29 in which the salt concentration is adjusted to 0.9% or a value in the vicinity thereof.

  In the crushing container 27, the concentration of water in which ozone is crushed is adjusted to 0.9% or a value in the vicinity thereof. From the viewpoint of the salinity concentration, the first raw material water is crushed at the same concentration. Compared to the case, the generation efficiency of ozone nanobubble nuclei is poor. However, the water used as the dilution water in order to reduce the concentration in this way is the mixing water in which the second raw material water is crushed and then permeated through the reverse osmosis membrane 26. This mixing water is as described above. In addition, when the nanobubble nuclei are removed in the permeation through the reverse osmosis membrane, the nanobubble nuclei having a smaller diameter remain, so that they are mixed with the first raw material water 21. By crushing in the crushing container 27, it is possible to produce biomedical water containing ozone nanobubble nuclei quantitatively and qualitatively even if the crushing is in a state where the salinity is low.

  Also in this embodiment, the first raw material water and the second raw water containing a salinity of 0.9% or higher than the value in the vicinity of 0.9% or more are the seaside with a salinity of about 2%. Well water and clean seawater with a salinity of about 3% can be used. One of these well water and seawater is used as the first (or second) raw water, the other is used as the second (or first) raw water, and only one of these well water and seawater. Can be used as the first and second raw water. That is, in the latter, the first raw material water and the second raw water are the same.

FIG. 4 shows a fourth embodiment of the production method of the present invention. In the fourth embodiment, the raw water is only one of well water and seawater.
In FIG. 4, reference numeral 31 indicates raw water (or a tank thereof) containing a salinity of 0.9% or more than the value in the vicinity thereof, or the raw water 31 is introduced into the mixing tank 32. Is done.

  In the mixing tank 32, it is mixed with water for mixing, which will be described later, by a well-known mixing means in the same manner as described above, whereby the salinity concentration is adjusted to 0.9% or a value close to that of physiological saline, and then for crushing. It is introduced into the container 33.

  The crushing container 33 is supplied with ozone from the gas cylinder 34 as microbubbles having a size of 50 μm or less, and in this state, physical stimulation is applied to perform crushing. Of course, the mixing of the mixed raw material water 31 and the mixing water with the microbubbles of ozone can be performed in another mixing tank or the like.

  In this way, in the crushing container 33, ozone is crushed, thereby generating biological water 35 having a salt concentration adjusted to 0.9% or a value in the vicinity thereof, and a part thereof is introduced into the reverse osmosis membrane 36. And it permeate | transmits this reverse osmosis membrane 36, a desalination process is carried out, the water for mixing is produced | generated, this water for mixing is introduce | transduced into the mixing tank 32 mentioned above, and the mixing mentioned above is made.

  Since the concentration of water in which the ozone crushing is performed in the crushing container 33 is adjusted to 0.9% or a value in the vicinity thereof, from the viewpoint of the salinity concentration, it is compared with the case where the raw material water is crushed at the same concentration. The generation efficiency of ozone nanobubble nuclei is poor. However, the water used as dilution water in order to reduce the concentration in this way is the water for mixing that has passed through the reverse osmosis membrane 36 after crushing the raw material water, and for reducing the concentration after crushing. Since it does not have a dilution process, it is possible to produce biomedical water containing ozone nanobubble nuclei in a quantitatively and qualitatively good manner even when the salt concentration is low.

A test was conducted to clarify whether biological water containing an ozone nanobubble nucleus with a salinity of 0.9% produced by the method shown as the fourth embodiment of the present invention is effective in improving periodontitis. .
[Examination contents]
Periodontitis patients were given 2 days a day with biomedical water produced according to the present invention and, as a control, 1.8% saline colored red 106 to make the color of the biomedical water according to the present invention the same. (Morning / Evening) for 2 weeks, the following items were examined.
・ Changes in clinical parameters ・ Changes in the amount of GCF ・ Presence or absence of periodontopathic bacteria in plaque samples and increase / decrease in the number of bacteria (ratio to the total number of bacteria)
[Test conditions]
・ Target 30 volunteers.
・ Double blind randomized control trial
・ Impregnated with the above-described biological water and control water according to the present invention (20 ml once, 30 seconds, twice in the morning and evening)
・ Clinical and bacteriological analyzes are performed after gagging

[Test results]
Number of final subjects Biomedical water group according to the present invention: 17 people Control water group: 18 people Amount of change at the start of the test and after 2 weeks Difference in pocket depth (average) of sampling site Biomedical water group according to the present invention: 0.5 mm decrease (p <0.05: significant difference)
Control water group: 0.5 mm decrease (p <0.05: significant difference)
2. Difference in the number of pockets of 4 mm or more Biomedical water group according to the present invention: 3.167 decrease (p <0.05: significant difference)
Control water group: 3.938 places decreased (p <0.05: significant difference)
3. Change in pocket average depth of 4 mm or more Biomedical water group according to the present invention: 0.714 mm decrease (p <0.05: significant difference)
Control water group: 0.886mm decrease (p <0.05: significant difference)
4). Periotron value: Biomedical water group according to the present invention: 26.111 decrease (p <0.05: significant difference)
Change after 1 and 2 weeks: decrease of 11.556 Control water group: decrease of 24.938 (p <0.05: no significant difference)
4. Change after 1 week and 2 weeks: increase 7.867 Bacteria test
As a result of examining the change in the ratio of the number of each bacterium to the total number of bacteria in the Red complex, there was no statistically significant difference between the two groups in the rate of change at the start of the test and after 2 weeks.

[Analysis of results]
-As a result of analyzing the improvement rate for each item, items 1, 2, and 3 were statistically significantly improved in both groups by 2 weeks of gargle. In addition, there was no statistically significant difference between the two groups in each value.
-Regarding the bacterial test, as a result of examining the change in the ratio of the number of each bacteria to the total number of bacteria in the Red complex, there was a statistically significant difference between the two groups in the rate of change at the start of the test and after 2 weeks. There wasn't.
-Regarding the periotron value, when the average value was compared at the start of the test and 2 weeks later, the value decreased statistically only in the biological water group according to the present invention. Further, in comparison between every week and after 2 weeks, it decreased in the biological water group according to the present invention, but increased in the control water group.

[Summary of examination]
Laboratory test results: Improvement was observed in both groups for pockets larger than 4 mm. In the control water group, it was clear that periodontal pathogenic bacteria were strongly affected together with other oral bacteria for a high salinity of 1.8%, resulting in a bactericidal effect and a periodontal disease countermeasure. became. At the same time, in the biomedical water according to the present invention, although the salinity is about half lower than the salinity of the control water and is about the same as the physiological saline, a bactericidal effect can be obtained and it can be a countermeasure for periodontal disease. It became clear.
The periotron value is a numerical value obtained by indirectly measuring the amount of gingival crevicular fluid, and it is possible to indirectly detect the degree of inflammation in the periodontal pocket. Therefore, when the average value is compared for the numerical value at the start of the test and two weeks later, the meaning that the value is statistically significantly reduced only in the biological water group according to the present invention is the biological water according to the present invention. Because of its high penetrability, the bactericidal and restorative effects of ozone nanobubble nuclei work synergistically on periodontal tissues with periodontitis of 4 mm or more, which is impossible with high-salt solution alone It is considered that the recovery of the damaged periodontal tissue is promoted.
For this reason, if it is mild periodontal disease (gingivitis), a high salinity solution of 1.8% can be used as a sufficient countermeasure against periodontal disease, but teeth with a pocket depth of 4 mm or more that require treatment It can be seen that it cannot be used as a sufficient periodontal disease countermeasure for peritonitis. On the other hand, the biological water according to the present invention can sterilize periodontopathic bacteria without adversely affecting periodontal tissues due to the salt concentration equivalent to that of physiological saline. It can be seen that it can be used effectively as a countermeasure.

  Since the present invention is as described above, the produced biological water can be used as a countermeasure against periodontal disease, etc. without adversely affecting the normal tissue of the living body due to its bactericidal and restorative effects. It can be used in various ways as functional water for living organisms, such as prevention of acute food poisoning by drinking.

1,5,11,21,23,31 Raw water (or its tank)
2, 6, 12, 22, 24, 33 Crushing containers 3, 7, 13, 25, 28, 34 Ozone tanks 4, 14, 22, 32 Mixing tanks 8, 15, 26, 36 Reverse osmosis membranes 9, 16, 29, 35 Water for biological use

Claims (5)

Ozone is supplied as microbubbles with a size of 50 μm or less to the first raw water whose salinity is 0.9% or more higher than the value in the vicinity of 0.9%, and collapsed by physical stimulation. Producing the first mixing water contained in the water;
Ozone is supplied as microbubbles with a size of 50 μm or less to the second raw material water whose salinity is 0.9% or more higher than the value in the vicinity of 0.9%, and collapsed by physical stimulation to stabilize the ozone nanobubble nuclei. After making it contain in water, the reverse osmosis membrane is made to permeate and a desalination process is performed to produce second mixing water,
These first and second mixing waters are mixed to adjust the salt concentration to 0.9% or a value in the vicinity thereof, and then ozone is supplied again as microbubbles having a size of 50 μm or less, and physical stimulation is performed. A method for producing biomedical water containing stabilized ozone nanobubble nuclei, characterized in that the biomedical water is produced by crushing with water. To the first raw material water whose salinity is 0.9% or more higher than the value in the vicinity of 0.9%,
Ozone is supplied as microbubbles with a size of 50 μm or less to the second raw material water whose salinity is 0.9% or more higher than the value in the vicinity of 0.9%, and collapsed by physical stimulation to stabilize the ozone nanobubble nuclei. After containing in water, mix the water for mixing produced by passing through the reverse osmosis membrane and desalting,
The salinity of 0.9% or was adjusted to a value in the vicinity thereof, the ozone is supplied as following microbubble size 50 [mu] m, while crushed by physical stimuli, organism containing the stabilized ozone nanobubbles nuclei in water A method for producing biomedical water containing stabilized ozone nanobubble nuclei, characterized by producing irrigation water. The method for producing biological water containing stabilized ozone nanobubble nuclei according to claim 1 or 2 , wherein the first raw water and the second raw water are the same. 3. The stabilized ozone nanobubble nucleus according to claim 1 , wherein at least one side of the first raw water and the second raw water is seaside well water having a salinity of about 2%. A method for producing biological water. The biological water containing the stabilized ozone nanobubble nucleus according to claim 1 or 2 , wherein at least one side of the first raw water and the second raw water is seawater in a clean sea area having a salinity of about 3%. Production method.

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