WO2007004709A1 - Electrolytic water and method for production thereof - Google Patents
Electrolytic water and method for production thereof Download PDFInfo
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- WO2007004709A1 WO2007004709A1 PCT/JP2006/313523 JP2006313523W WO2007004709A1 WO 2007004709 A1 WO2007004709 A1 WO 2007004709A1 JP 2006313523 W JP2006313523 W JP 2006313523W WO 2007004709 A1 WO2007004709 A1 WO 2007004709A1
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- Prior art keywords
- water
- electrolyzed
- electrolyzed water
- ascorbic acid
- electrolysis
- Prior art date
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Classifications
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/19—Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/40—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing nitrogen
- A61K8/44—Aminocarboxylic acids or derivatives thereof, e.g. aminocarboxylic acids containing sulfur; Salts; Esters or N-acylated derivatives thereof
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/49—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds
- A61K8/4906—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds with one nitrogen as the only hetero atom
- A61K8/4913—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds with one nitrogen as the only hetero atom having five membered rings, e.g. pyrrolidone carboxylic acid
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/67—Vitamins
- A61K8/676—Ascorbic acid, i.e. vitamin C
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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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K2800/00—Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
- A61K2800/80—Process related aspects concerning the preparation of the cosmetic composition or the storage or application thereof
- A61K2800/83—Electrophoresis; Electrodes; Electrolytic phenomena
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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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/026—Treating water for medical or cosmetic purposes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
- C02F2201/4612—Controlling or monitoring
- C02F2201/46125—Electrical variables
Definitions
- the present invention relates to electrolyzed water and a method for producing the same. More specifically, the present invention relates to electrolyzed water useful for skin care obtained by electrolyzing a L-ascorbic acid aqueous solution to which a predetermined amino acid is added, and a method for producing the same.
- Background art
- L-ascorbic acid is ionized in water by the dissociation of the 2nd and 3rd hydroxyl groups in the chemical structure. Electrolysis by applying a voltage to an aqueous L-ascorbic acid solution is a well-known technique (see, for example, Japanese Patent No. 3 60 2 7 7 3).
- Hydrogen ions and ascorbate ions generated by dissociation of ascorbic acid react with ions generated by electrolysis of water at the respective electrodes to form electrolytic products. That is, ascorbate ion reacts with H + produced by water oxidation on the anode to form ascorbate.
- water is produced by the reaction of hydroxide ions and hydrogen ions produced by the reduction of water. Oxygen generated on the anode surface and hydrogen generated on the cathode surface exist in water as dissolved oxygen or dissolved hydrogen.
- the electrolyte aqueous solution increases the entropy of the solution by electrolysis, and becomes more energetic than the steady state.
- the function as a solvent is activated, and the dissociation degree of water itself tends to increase.
- Electrolyzed water obtained by electrolyzing an aqueous electrolyte solution changes the conformation of water molecules surrounding the solute as the degree of water dissociation increases. For this reason, several reports have revealed that the dissolution rate of solutes increases and the degree of dissociation of low-dissociation substances increases.
- the electrolyzed water of the above ascorbic acid aqueous solution promotes emulsifying action on the skin surface when touched to the skin due to a change in characteristics due to electrolysis and enters the skin. It has been confirmed that the ascorbic acid has improved permeability. Since ascorbic acid permeating the skin itself acts as a strong reducing agent, it has also become clear that when this electrolyzed water is applied to the skin, it exhibits a high whitening effect.
- the electrolyzed water of an ascorbic acid aqueous solution may cause irritation and a feeling of tension when applied to the skin, which may cause a problem in use. Moreover, there is no effect
- the present inventor exhibits various effects on the skin when nonionic substances and ampholytes are added to ascorbic acid electrolyzed water by utilizing changes in physical properties due to electrolysis, particularly improved solubility. I thought that could be expected.
- An object of the present invention is to obtain electrolyzed water having a moisturizing effect in addition to a whitening effect by ascorbic acid by electrolyzing an amino acid substance having high affinity for a living body simultaneously with ascorbic acid in water.
- the present inventors conducted electrolysis of an aqueous solution of ascorbic acid or a derivative thereof to which a predetermined amino acid was added, so that the conventional ascorbic acid electrolyzed water is provided in addition to the whitening effect.
- the inventors have found that electrolyzed water imparted with moisture-retaining properties and skin quality-improving effects that have not been obtained, and have completed the present invention.
- the electrolyzed water of the present invention is obtained by electrolyzing raw electrolyzed water containing a predetermined amino acid using an L-ascorbic acid derivative as an active ingredient and an electrolysis assistant.
- This electrolyzed water has the whitening effect of L-ascorbic acid and can be used as a cosmetic with excellent moisture retention.
- the ascorbic acid and amino acid added to the electrolyzed raw water are safe for the human body, and the safety of the electrolyzed water of the present invention produced by electrolyzing the electrolyzed raw water is extremely high.
- FIG. 1 is a schematic configuration diagram showing an example of an electrolysis apparatus used in the method for producing electrolyzed water of the present invention.
- FIG. 2 is an assembled perspective view showing another example of the electrolysis apparatus used in the method for producing electrolyzed water of the present invention.
- FIG. 3 is an exploded perspective view of the electrolysis apparatus shown in FIG. In FIG. 4, (a) is a perspective view of the liquid supply unit and spray section of the electrolysis apparatus shown in FIG. 2, and (b) is a cross-sectional view thereof.
- 1 0 6 is the raw material raw water tank; 4 is the electrolyte aqueous solution; 6 is the pump; 8 is the electrolyte aqueous solution supply pipe; 1 0 is the diaphragm electrolyzer; 1 2 a, 1 2 b 1 1 9 a and 1 1 9 b are electrodes; 1 6 is an electrolysis power supply; 1 8 and 2 0 is wiring; 2 2 is a mixed electrolyzed water discharge pipe; 1 0 0 is an electrolyzer; 2 is the housing; 1 0 8 is the fluid passage; 1 1 0 is the liquid absorbing medium; 1 1 1 is the electrolyzed raw water; 1 2 0 is the spraying part; 1 2 1 is the vibrator; 1 2 3 Is a perforated spray plate.
- the content of L-ascorbic acid or a derivative thereof in the electrolyzed water of the present invention is:! ⁇ 50 mM, preferably 2 to 20 mM. If the concentration of L-ascorbic acid is less than 1 mM, the whitening effect of electrolyzed water will be insufficient, and the electrolysis will have low conductivity, making electrolysis difficult. When it exceeds 50 mM, a sticky feeling is felt when the obtained electrolyzed water is applied to the skin.
- L-ascorbic acid derivative may include sodium ascorbyl phosphate and magnesium ascorbyl phosphate.
- amino acids blended in electrolyzed water include known amino acids that are usually blended in cosmetics and the like. From the standpoint of preventing skin irritation caused by L-ascorbic acid and imparting high moisture retention to electrolyzed water, It is preferable to use syn (so-called betaine) or L-hydroxyproline.
- the blending amount of these amino acids in the electrolyzed water is 0.05 to 0.8 mass%, preferably 0.08 to 0.3 mass%.
- the blending amount in the electrolyzed water is less than 0.05% by mass, the effect of imparting moisture retention to the electrolyzed water is not sufficient, and when it exceeds 0.8% by mass, a sticky feeling is strongly felt and a feeling of use is felt. descend.
- a mixture of trimethylglycine and L-hydroxyproline may be added to the electrolyzed water.
- the blending amount is 0.05 to 0.8 mass% in total.
- FIG. 1 is a schematic configuration diagram showing an example of an electrolysis apparatus used for producing electrolyzed water of the present invention.
- FIG. 1 is an electrolytic raw water tank in which an electrolytic aqueous solution (electrolytic raw water) 4 is stored.
- the electrolyzed raw water 4 comprises L-ascorbic acid or a derivative thereof in an amount of 1 to 50 mM, preferably 2 to 20 mM, and trimethylglycine or L-hydroxyproline in an amount of 0.05 to 0.8% by mass, preferably 0.08 to 0.3. 3% by mass is contained.
- the raw electrolytic water 4 does not substantially contain an electrolyte such as a water-soluble inorganic salt other than L-ascorbic acid or a derivative thereof.
- the content of the water-soluble inorganic electrolyte is preferably not more than 0.1 mM, particularly preferably not more than 0.02 mM, in total for each water-soluble inorganic electrolyte.
- the flow rate of the aqueous electrolyte solution 4 supplied to the non-diaphragm electrolyzer 10 by the pump 6 is about 5 to 300 m / min, but preferably 50 to L0 00 m 1 in, more preferably Is from 5 0 0 to 1 0 0 0 ml l Zm in.
- the diaphragm electrolyzer 10 has a pair of electrodes 12 a and 12 b facing each other inside.
- the pair of electrodes 1 2 a and 1 2 b are disposed at a predetermined interval, and the interval is 2 to 0.05 mm, preferably 1.5 to 0.1 mm. When the distance between the electrodes exceeds 2 mm, mixing of the positive electrode side electrolyzed water and the negative electrode side electrolyzed water generated by electrolysis becomes insufficient.
- the electrodes 1 2 a and 1 2 b are made of an electrochemically inactive metal material.
- As the electrode material platinum, a platinum alloy or the like is preferable.
- the polarities of the power applied to each electrode are switched at predetermined time intervals. By switching the polarity of the applied power at predetermined time intervals, the negative electrode side electrolyzed water and the anode side electrolyzed water are alternately generated in a pair of electrodes, so that the anode side electrolyzed water and the cathode side electrolyzed water are separated from each other. It is mixed efficiently.
- the polarity switching time interval is preferably 2 to 120 times, and more preferably 120 to 600 times. In addition, it is possible to effectively prevent the scale from adhering to the electrode by switching the polarity.
- the electrolyte aqueous solution 4 sent to the diaphragm electrolytic cell 10 through the electrolyte aqueous solution supply pipe 8 is electrolyzed in the diaphragm electrolytic cell 10.
- the amino acid ion that is an ampholyte is not affected by the electric field within a short period of time, and almost no amino acid ion migration is observed. No matter what part of the electrolyzed water is collected, its distribution is almost constant. Electrolytic current density is, 0. 0 0 3 ⁇ 0. 0 8 AZ cm 2 are preferred, 0. 0 1 ⁇ 0. 0 3 AZ cm 2 is particularly preferred. When the electrolysis current density is less than 0.0 3 AZ cm 2 , the dissolved oxygen amount and dissolved hydrogen amount in the electrolyzed water cannot be made higher than the electrolyzed raw water. If it exceeds 0.08 A / cm 2 , the oxidation of L-ascorbic acid accelerates, the amount of dehydroascorbic acid generated increases, and the possibility of becoming oxidized L-ascorbic acid increases. .
- the anode side electrolyzed water and the cathode side electrolyzed water generated during electrolysis in the electrolytic cell are naturally mixed.
- the mixed electrolyzed water in which both electrolyzed waters are mixed is continuously taken out through the mixed electrolyzed water discharge pipe 22.
- an electrolytic cell in which a diaphragm is formed between both electrodes 12 a and 12 b may be used as the electrolytic cell 10.
- a diaphragm what is conventionally used as an electrolytic membrane, such as an ion exchange membrane and an uncharged membrane, can be used as appropriate.
- the electrode is a pair.
- the present invention is not limited to this, and a plurality of electrode pairs may be provided in the electrolytic cell to increase the electrolysis efficiency. Furthermore, it is not necessary to switch the polarity of power.
- the electrolyzer used when producing the electrolyzed water of the present invention is not particularly limited, and any electrolyzed water producing apparatus conventionally used can be used. In other words, any type can be used regardless of the size of the electrolytic device and the presence or absence of a diaphragm in the electrolytic cell.
- FIGS. 2 and 3 are perspective views showing other examples of the electrolyzer used for the production of the electrolyzed water of the present invention.
- Fig. 2 shows the electrolyzer assembled
- Fig. 3 Shows a perspective view of a state in which the electrolytic device is disassembled.
- the electrolyzer 100 shown in FIGS. 2 and 3 includes a housing 1002 that forms the apparatus body, and a liquid supply unit 104 that is detachably attached to the housing 102.
- the liquid supply unit 104 is inserted into the locking holes 14 0 formed in the housing 10 2 and locked at both ends thereof, and is formed at the upper edge thereof.
- the pair of locking claws 1 44 are locked to the locking grooves 1 46 of the housing 10 2 so that they can be attached to the housing 1 0 2.
- FIG. 2 shows a state in which the liquid supply unit 104 is attached to the housing 10
- FIG. 3 shows a state in which the liquid supply unit 10 4 is detached from the housing 10 2.
- FIG. 4 is a perspective view (a) and a cross-sectional view showing the inside of the liquid supply unit 10 4 and the spray section 1 2 0 in a state where the liquid supply unit 10 4 is attached to the housing 10 2. b)
- the liquid supply unit 1 0 4 is an electrolytic raw water tank 1 0 6 for storing electrolytic raw water 1 1 1, a pair of rod-like electrodes 1 1 9 a, 1 1 9 b, and electrodes 1 1 9 a for electrolyzing electrolytic raw water 1 1 9 b
- the supply cross section has a substantially circular liquid passage 10 8.
- the electrolyzed raw water tank 1 0 6 has a liquid absorbing medium 1 1 0 in the mounted state (state shown in FIG. 2) so that the electrolytic raw water 1 1 1 in the tank can be smoothly guided to the liquid absorbing medium 1 1 0. It is arranged above.
- the rod-shaped electrodes 1 1 9 a and 1 1 9 b are arranged in the liquid flow path 1 0 8 immediately upstream of the liquid absorption medium 1 1 0 so that the liquid absorption medium 1 1 0 is sandwiched between the right and left sides. ing. Electrolyzed raw water flows between the electrodes 1 1 9 a and 1 1 9 b through the flow path 1 0 8 By doing so, the electrolyzed raw water is electrolyzed.
- resistance means 1 4 7 composed of a valve, a membrane or the like for adjusting the penetration of the electrolyzed water into the liquid absorbing medium 1 10.
- the electrolyzer 1 100 is provided with a spray section 1 2 0 composed of a piezoelectric vibrator 1 2 1 and a porous spray plate 1 2 3. Electrolyzed raw water (electrolyzed water) electrolyzed by the electrodes 1 1 9 a and 1 1 9 b is sprayed to the outside by the spraying part 1 2 0. One end of the liquid-absorbing medium 110 is in contact with the inner side surface of the porous spray plate 123, and a piezo vibrator 12 21 is fixed to one end side of the outer side surface. By vibrating the piezo vibrator 1 2 1 by applying alternating current or pulse voltage to this piezo vibrator 1 2 1, the porous spray plate 1 2 3 fixed on the piezo vibrator 1 2 1 is vibrated.
- a spray section 1 2 0 composed of a piezoelectric vibrator 1 2 1 and a porous spray plate 1 2 3. Electrolyzed raw water (electrolyzed water) electrolyzed by the electrodes 1 1 9 a and 1 1
- the electrolyzed water absorbed in the liquid absorbing medium 1 1 0 is subjected to a suction action by the vibration of the porous spray plate 1 2 3 and passes through a plurality of through holes formed in the porous spray plate 1 2 3. Thereafter, the spray is diffused and sprayed as fine droplets to the outside from the spray ports 1 2 2 formed in the housing.
- the open / close cover 1 2 6 shown in FIGS. 2 and 3 exposes or hides the spray port 1 2 2 and is slidably attached to the housing 10 2. . Further, the opening / closing cover 1 2 6 and the housing 10 2 have detection means capable of detecting the position of the opening / closing cover 1 2 6 in cooperation. FIG. 2 clearly shows the switch 1 39 on the housing 10 2 side constituting such a detection means.
- a control unit 1 3 6 incorporating a microprocessor is provided in the housing 10 2.
- the control unit 1 3 6 controls the application of voltage to the electrodes 1 1 9 a and 1 1 9 b and the drive of the vibrator 1 2 1, and receives a detection signal from the switch 1 3 9.
- the positive terminal or the negative terminal of the electrolytic power source provided in the control unit 1 3 6 is electrically connected to the electrodes 1 1 9 a and 1 1 9 b through a wiring (not shown).
- Each electrode 1 1 9 a, 1 1 9 b The polarity of the applied power is switched between each other at predetermined time intervals by the control unit 1 36.
- the electrolyzed water formed by mixing the anode-side electrolyzed water and the cathode-side electrolyzed water as described above is continuously sprayed to the outside through the spraying part 120 through the spraying port 1222.
- reference numeral 1 3 2 is a power supply unit for supplying power to the electrodes 1 1 9 a and 1 1 9 b and the vibrator 1 2 1.
- a dry battery 1 3 0 or the like can be used as a power source in the power source section 1 3 2.
- Reference numeral 1 3 4 is a cover of the power supply unit 1 3 2.
- the electrolyzed raw water containing L-ascorbic acid and trimethylglycine was electrolyzed using the electrolyzer shown in FIGS. 2 to 4 to produce electrolyzed water.
- the electrolytic cell was constructed by inserting two cylindrical electrodes with a diameter of 1.6 mm into a liquid passage 10 with an inner diameter of 10 mm at an interval of 0.9 mm. Electrolyzed raw water was supplied to the electrolytic cell at a flow rate of 10 m 1 Zmin and electrolyzed at an electrolysis current density of 0.05 AZ cm 2 to obtain electrolyzed water.
- the electrolyzed raw water was prepared by using 30 mM L-ascorbic acid (As A) and 0.1% by mass trimethylglycine (TMG) dissolved in purified water. Since purified water was used as the solvent, the content of the water-soluble inorganic salt in the electrolytic raw water was extremely small (less than 0. 1 mM).
- the sensory test uses the semantic differential method, with “neither” set to 0. 1 point for “slightly bad”, 1 point for “bad”, 1 point for “very bad”, 3 points for “very bad”, + 1 point for “slightly good”, + 2 points for “good”, “very good” Was rated as +3 points.
- the electrolyzed water of the present invention is not irritating at all, and is more glossy and moist (retained) than the electrolyzed raw water or electrolyzed water containing only L-ascorbic acid. Excellent wetness).
- Table 2 shows the results of measuring the pH, redox potential (ORP), dissolved oxygen content (DO), and electrical conductivity (E C) of the electrolyzed water obtained.
- the electrolyzed water of the present invention has no irritation and has improved pores and texture as compared with electrolyzed water containing only electrolyzed raw water or L-ascorbic acid, and has a smooth and moist feeling (moisturizing property). It was.
- Table 4 shows the results of measuring the pH, redox potential (OR P), dissolved oxygen content (D0), and electrical conductivity (EC) of the electrolyzed water obtained.
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Abstract
Description
明細書 電解水及びその製造方法 技術分野 Description Electrolyzed water and method for producing the same Technical Field
本発明は、 電解水及びその製造方法に関する。 更に詳述すれば所定の アミノ酸を添加した L—ァスコルビン酸水溶液を電気分解して得られる スキンケアに有用な電解水、 及びその製造方法に関する。 背景技術 The present invention relates to electrolyzed water and a method for producing the same. More specifically, the present invention relates to electrolyzed water useful for skin care obtained by electrolyzing a L-ascorbic acid aqueous solution to which a predetermined amino acid is added, and a method for producing the same. Background art
L —ァスコルビン酸は水中で化学構造式における 2位と 3位の水酸基 が解離することによりイオン化する。 L—ァスコルビン酸水溶液に電圧 を印加して電気分解を行うことは既によく知られた技術である (例えば、 特許第 3 6 0 2 7 7 3号公報参照)。 L-ascorbic acid is ionized in water by the dissociation of the 2nd and 3rd hydroxyl groups in the chemical structure. Electrolysis by applying a voltage to an aqueous L-ascorbic acid solution is a well-known technique (see, for example, Japanese Patent No. 3 60 2 7 7 3).
Lーァスコルピン酸水溶液を電気分解すると、 水中でァスコルビン酸 の解離により生成している水素イオンとァスコルビン酸イオンが互いに 反対の電極に向かって移動する。 同時に、 溶媒である水が電気分解され、 陽極表面では酸化反応により酸素及び水素イオンが、 陰極表面では還元 反応により水素及び水酸化イオンが発生する。 When the L-ascorbic acid aqueous solution is electrolyzed, hydrogen ions and ascorbate ions generated by dissociation of ascorbic acid in water move toward the opposite electrodes. At the same time, water as a solvent is electrolyzed, and oxygen and hydrogen ions are generated by an oxidation reaction on the anode surface, and hydrogen and hydroxide ions are generated by a reduction reaction on the cathode surface.
ァスコルビン酸の解離により生成している水素イオンとァスコルビン 酸イオンは、 それぞれの電極で水の電気分解により発生しているイオン と反応し、 電解生成物を形成する。 即ち、 ァスコルビン酸イオンは陽極 上で水の酸化によって生成した H +と反応してァスコルビン酸となる。 陰極表面では、 水の還元により生成した水酸化イオンと水素イオンとが 反応して水が生成する。 陽極表面に生成する酸素と陰極表面に生成する 水素とは、 溶存酸素又は溶存水素として水中に存在する。 Hydrogen ions and ascorbate ions generated by dissociation of ascorbic acid react with ions generated by electrolysis of water at the respective electrodes to form electrolytic products. That is, ascorbate ion reacts with H + produced by water oxidation on the anode to form ascorbate. On the cathode surface, water is produced by the reaction of hydroxide ions and hydrogen ions produced by the reduction of water. Oxygen generated on the anode surface and hydrogen generated on the cathode surface exist in water as dissolved oxygen or dissolved hydrogen.
一般に、 水溶性物質が水に溶解するに際しては、 溶媒の状態によりそ の溶解特性が変化することが知られている。 同じ水を溶媒として用いた 場合でも温度や圧力あるいは外力などの条件により水溶性物質と水との 相互作用は変化し、 その結果水溶性物質の溶解特性も変化する。 In general, when a water-soluble substance dissolves in water, it depends on the state of the solvent. It is known that the solubility characteristics of Even when the same water is used as a solvent, the interaction between the water-soluble substance and water changes depending on conditions such as temperature, pressure, and external force. As a result, the solubility characteristics of the water-soluble substance also change.
電解質水溶液は、 一定条件の下では電気分解により溶液のェントロピ 一が増大し、 定常状態よりもエネルギー的に活性化された状態となる。 その結果、 溶媒としての機能が活性化され、 水自体の解離度が増加する 傾向を示す。 電解質水溶液を電気分解して得られる電解水は、 水の解離 度が増加することにより溶質を取り囲む水分子のコンホメーションが変 化する。 そのため、 溶質の溶解速度が速くなつたり低解離物質の解離度 が増加したりすることがいくつかの報告により明らかとなっている。 Under certain conditions, the electrolyte aqueous solution increases the entropy of the solution by electrolysis, and becomes more energetic than the steady state. As a result, the function as a solvent is activated, and the dissociation degree of water itself tends to increase. Electrolyzed water obtained by electrolyzing an aqueous electrolyte solution changes the conformation of water molecules surrounding the solute as the degree of water dissociation increases. For this reason, several reports have revealed that the dissolution rate of solutes increases and the degree of dissociation of low-dissociation substances increases.
ァスコルピン酸水溶液の電気分解においては、 溶媒である水が電気分 解の影響を受けて活性化される。 水の構造的特性変化によりァスコルビ ン酸の解離度が増加して溶解性を促進する効果が生じている。 また、 水 と溶質であるァスコルビン酸との相互作用に変化が生じている。 即ち、 ァスコルビン酸自身の反応性を高める特性変化がもたらされていると考 えられる。 In the electrolysis of ascorbic acid aqueous solution, the solvent water is activated under the influence of electrolysis. Changes in the structural characteristics of water increase the degree of dissociation of ascorbic acid, which has the effect of promoting solubility. There is also a change in the interaction between water and the solute ascorbic acid. That is, it is considered that a characteristic change that increases the reactivity of ascorbic acid itself is brought about.
本発明者等はァスコルビン酸水溶液の電気分解におけるこれらの作用 に着目し、 この能力を保持した電解水を得るため種々検討した。 その結 果、 水溶性金属塩等の無機電解質を電解助剤として用いることなく、 比 較的低濃度のァスコルビン酸の単独水溶液を電気分解すると、 スーパ一 ォキシラジカルを不均化する能力を保持した陽極側電解水が得られるこ とを発見し、 既に特許を取得した (特許第 3 6 0 2 7 7 3号公報 (請求 項 1 ) )。 発明の開示 The present inventors paid attention to these actions in the electrolysis of ascorbic acid aqueous solution, and conducted various studies to obtain electrolyzed water retaining this ability. As a result, when an aqueous solution of relatively low concentration of ascorbic acid alone is electrolyzed without using an inorganic electrolyte such as a water-soluble metal salt as an electrolysis aid, an anode that retains the ability to disproportionate super radicals. It was discovered that side electrolyzed water can be obtained, and a patent has already been obtained (Patent No. 3 60 27 7 3 (Claim 1)). Disclosure of the invention
上述したァスコルビン酸水溶液の電解生成水は、 電気分解による特性 変化により、 皮膚に触れた際の皮膚表面の乳化作用の促進や皮膚内部へ のァスコルビン酸の浸透性の向上が見られることが確認されている。 皮 膚に浸透したァスコルビン酸自体が強力な還元剤として作用するので、 この電解生成水を皮膚に塗布した場合には高い美白効果を示すことも明 らかとなつている。 The electrolyzed water of the above ascorbic acid aqueous solution promotes emulsifying action on the skin surface when touched to the skin due to a change in characteristics due to electrolysis and enters the skin. It has been confirmed that the ascorbic acid has improved permeability. Since ascorbic acid permeating the skin itself acts as a strong reducing agent, it has also become clear that when this electrolyzed water is applied to the skin, it exhibits a high whitening effect.
しかしながら、 ァスコルビン酸水溶液の電解生成水は皮膚に対して塗 布した場合に刺激やつっぱり感を感じるため使用感が問題になることが ある。 また皮膚の保湿性を向上させる作用はない。 However, the electrolyzed water of an ascorbic acid aqueous solution may cause irritation and a feeling of tension when applied to the skin, which may cause a problem in use. Moreover, there is no effect | action which improves the moisture retention of skin.
本発明者は、 電気分解による物性変化、 特に溶解性の向上を利用して ァスコルビン酸電解生成水に非イオン性物質や両性電解質を配合した場 合には、 皮膚に対する種々の効果を発現することが期待できるのではな いかと考えた。 The present inventor exhibits various effects on the skin when nonionic substances and ampholytes are added to ascorbic acid electrolyzed water by utilizing changes in physical properties due to electrolysis, particularly improved solubility. I thought that could be expected.
本発明は、 生体に対する親和性の高いアミノ酸系の物質を水中でァス コルビン酸と同時に電気分解することにより、 ァスコルビン酸による美 白効果に加えて保湿効果を有する電解生成水を得ることを目的とする。 本発明者等は、 検討を行った結果、 所定のアミノ酸を添加したァスコ ルビン酸又はその誘導体水溶液の電気分解を行うことにより、 美白効果 に加えて、 従来のァスコルビン酸電解生成水には具備されていない保湿 性や肌質改善効果を付与した電解生成水が得られることを見出し、 本発 明を完成するに到った。 An object of the present invention is to obtain electrolyzed water having a moisturizing effect in addition to a whitening effect by ascorbic acid by electrolyzing an amino acid substance having high affinity for a living body simultaneously with ascorbic acid in water. And As a result of the study, the present inventors conducted electrolysis of an aqueous solution of ascorbic acid or a derivative thereof to which a predetermined amino acid was added, so that the conventional ascorbic acid electrolyzed water is provided in addition to the whitening effect. The inventors have found that electrolyzed water imparted with moisture-retaining properties and skin quality-improving effects that have not been obtained, and have completed the present invention.
本発明は、 以下に記載するものである。 The present invention is described below.
〔 1〕 水溶性無機塩を 0 . I m M未満、 トリメチルグリシン又は L ーヒドロキシプロリンを 0 . 0 5〜 0 . 8質量%、 Lーァスコルビン酸 又はその誘導体を 1〜 5 0 m M含有する電解水。 [1] Electrolysis containing a water-soluble inorganic salt of less than 0.1 mM, trimethylglycine or L-hydroxyproline in an amount of 0.5 to 0.8% by mass, and L-corsorbic acid or a derivative thereof in an amount of 1 to 50 mM. water.
〔 2〕 L —ァスコルビン酸誘導体が、 リン酸ァスコルビルナトリウ ム又はリン酸ァスコルビルマグネシウムである 〔 1〕 に記載の電解水。 [2] The electrolyzed water according to [1], wherein the L-ascorbic acid derivative is sodium ascorbyl phosphate or magnesium ascorbyl phosphate.
〔 3〕 水溶性無機塩を 0 . I m M未満、 トリメチルグリシン又は L ーヒドロキシプロリンを 0 . 0 5〜 0 . 8質量%、 Lーァスコルビン酸 又はその誘導体を 1〜 5 0 ηιΜ含有する電解原水を電気分解して電解水 を取り出すことを特徴とする電解水の製造方法。 [3] Water-soluble inorganic salt less than 0.1 mM, trimethylglycine or L-hydroxyproline from 0.05 to 0.8% by mass, L-ascorbic acid Alternatively, a method for producing electrolyzed water, characterized in that electrolyzed raw water containing 1 to 50 ηιΜ of a derivative thereof is electrolyzed to take out electrolyzed water.
〔4〕 Lーァスコルビン酸誘導体が、 リン酸ァスコルビルナトリウ ム又はリン酸ァスコルビルマグネシウムである 〔3〕 に記載の電解水の 製造方法。 [4] The method for producing electrolyzed water according to [3], wherein the L-ascorbic acid derivative is sodium ascorbyl phosphate or magnesium ascorbyl phosphate.
〔 5〕 電解原水を電気分解する電解槽が無隔膜電解槽である 〔3〕 に記載の電解水の製造方法。 [5] The method for producing electrolyzed water according to [3], wherein the electrolytic cell for electrolyzing the raw electrolytic water is a non-diaphragm electrolytic cell.
〔 6〕 電気分解する際の電流密度が 0. 0 0 3〜 0. O S AZc m 2である 〔 3〕 に記載の電解水の製造方法。 [6] The method for producing electrolyzed water according to [3], wherein the current density during electrolysis is 0.0 3 to 0. OS AZcm 2 .
〔 7〕 水溶性無機塩を 0. I mM未満、 トリメチルグリシン又は L ーヒドロキシプロリンを 0. 0 5〜 0. 8質量%、 L—ァスコルビン酸 又はその誘導体を 1〜 5 0 mM含有する電解原水を流量 5〜 3 0 0 0 m 1 /m i nで連続流通型無隔膜電解槽に供給し、 電解電流密度 0. 0 0 3〜 0. 0 8 A/ c m2で連続的に電気分解する 〔 3〕 に記載の電解水 の製造方法。 本発明の電解水は、 Lーァスコルビン酸誘導体を有効成分とすると共 に電解助剤とし、 所定のアミノ酸を含有する電解原水を電気分解して得 られるものである。 この電解水は、 Lーァスコルビン酸の美白効果を有 し、 保湿性に優れた化粧料として利用できる。 電解原水に添加するァス コルピン酸及びアミノ酸は人体に対して安全であり、 電解原水を電気分 解して製造する本発明の電解水の安全性も極めて高いものである。 [7] Electrolyzed raw water containing water-soluble inorganic salt in an amount of less than 0.1 mM, trimethylglycine or L-hydroxyproline in an amount of 0.05 to 0.8 mass%, and L-ascorbic acid or a derivative thereof in an amount of 1 to 50 mM. It was fed into the continuous circulation type non-membrane electrolysis cell at a flow rate 5~ 3 0 0 0 m 1 / min, continuously degrades electricity electrolytic current density 0. 0 0 3~ 0. 0 8 a / cm 2 [3 ] The manufacturing method of the electrolyzed water of description. The electrolyzed water of the present invention is obtained by electrolyzing raw electrolyzed water containing a predetermined amino acid using an L-ascorbic acid derivative as an active ingredient and an electrolysis assistant. This electrolyzed water has the whitening effect of L-ascorbic acid and can be used as a cosmetic with excellent moisture retention. The ascorbic acid and amino acid added to the electrolyzed raw water are safe for the human body, and the safety of the electrolyzed water of the present invention produced by electrolyzing the electrolyzed raw water is extremely high.
アミノ酸自身はほとんど電気分解には関与しないが、 電解原水の電解 プロセスで生じた溶媒と溶質の相互作用の変化によるァミノ酸の溶解性 向上効果が生じている。 この効果と、 電解水中に存在する溶存酸素等の 要因により、 本発明の電解水を皮膚に塗布した場合には高い保湿性効果 が得られる。 図面の簡単な説明 Amino acids themselves are hardly involved in electrolysis, but the effect of improving the solubility of amino acids is caused by changes in the interaction between the solvent and the solute generated in the electrolysis process of the raw water. Due to this effect and factors such as dissolved oxygen present in the electrolyzed water, a high moisturizing effect can be obtained when the electrolyzed water of the present invention is applied to the skin. Brief Description of Drawings
第 1図は、 本発明の電解水の製造方法に使用する電解装置の一例を示 す概略構成図である。 第 2図は、 本発明の電解水の製造方法に使用する 電解装置の他の例を示す組立斜視図である。 第 3図は、 第 2図に示す電 解装置の分解斜視図である。 第 4図中、 ( a) は第 2図に示す電解装置 の給液ユニッ トおよび噴霧部の斜視図であり、 (b) はその断面図であ る。 FIG. 1 is a schematic configuration diagram showing an example of an electrolysis apparatus used in the method for producing electrolyzed water of the present invention. FIG. 2 is an assembled perspective view showing another example of the electrolysis apparatus used in the method for producing electrolyzed water of the present invention. FIG. 3 is an exploded perspective view of the electrolysis apparatus shown in FIG. In FIG. 4, (a) is a perspective view of the liquid supply unit and spray section of the electrolysis apparatus shown in FIG. 2, and (b) is a cross-sectional view thereof.
図中、 2、 1 0 6は、 輋解原水タンク ; 4は、 電解質水溶液; 6は、 ポンプ; 8は、 電解質水溶液供給管; 1 0は、 無隔膜電解槽; 1 2 a、 1 2 b、 1 1 9 a、 1 1 9 bは、 電極; 1 6は、 電解電源; 1 8、 2 0 は、 配線; 2 2は、 混合電解水取出し管; 1 0 0は、 電解装置; 1 0 2 は、 ハウジング; 1 0 8は、 通液路; 1 1 0は、 吸液媒体; 1 1 1は、 電解原水; 1 2 0は、 噴霧部; 1 2 1は、 振動子; 1 2 3は、 多孔噴霧 プレートである。 発明を実施するための最良の形態 In the figure, 2, 1 0 6 is the raw material raw water tank; 4 is the electrolyte aqueous solution; 6 is the pump; 8 is the electrolyte aqueous solution supply pipe; 1 0 is the diaphragm electrolyzer; 1 2 a, 1 2 b 1 1 9 a and 1 1 9 b are electrodes; 1 6 is an electrolysis power supply; 1 8 and 2 0 is wiring; 2 2 is a mixed electrolyzed water discharge pipe; 1 0 0 is an electrolyzer; 2 is the housing; 1 0 8 is the fluid passage; 1 1 0 is the liquid absorbing medium; 1 1 1 is the electrolyzed raw water; 1 2 0 is the spraying part; 1 2 1 is the vibrator; 1 2 3 Is a perforated spray plate. BEST MODE FOR CARRYING OUT THE INVENTION
本発明の電解水における Lーァスコルビン酸又はその誘導体の含有量 は、 :!〜 5 0mM、 好ましくは 2〜 2 0 mMである。 Lーァスコルビン 酸の濃度が 1 mM未満の場合は、 電解水の美白効果が不十分となり、 電 気分解に際しては導電率が低く、 電解が困難となる。 5 0mMを超える 場合は得られる電解水を皮膚等に適用する際にべたつき感が感じられる。 The content of L-ascorbic acid or a derivative thereof in the electrolyzed water of the present invention is:! ˜50 mM, preferably 2 to 20 mM. If the concentration of L-ascorbic acid is less than 1 mM, the whitening effect of electrolyzed water will be insufficient, and the electrolysis will have low conductivity, making electrolysis difficult. When it exceeds 50 mM, a sticky feeling is felt when the obtained electrolyzed water is applied to the skin.
Lーァスコルビン酸誘導体としては、 例えばリン酸ァスコルビルナト リウム又はリン酸ァスコルビルマグネシウムを挙げることができる。 電解水に配合するアミノ酸には、 通常化粧料等に配合される公知のァ ミノ酸を挙げることができる。 Lーァスコルビン酸に起因する肌への刺 激を防止して電解水に高い保湿性を付与する観点から、 トリメチルダリ シン (いわゆるべタイン) 又は Lーヒドロキシプロリンを使用すること が好ましい。 Examples of the L-ascorbic acid derivative may include sodium ascorbyl phosphate and magnesium ascorbyl phosphate. Examples of amino acids blended in electrolyzed water include known amino acids that are usually blended in cosmetics and the like. From the standpoint of preventing skin irritation caused by L-ascorbic acid and imparting high moisture retention to electrolyzed water, It is preferable to use syn (so-called betaine) or L-hydroxyproline.
電解水におけるこれらのアミノ酸の配合量は、 0. 0 5〜 0. 8質 量%、 好ましくは 0. 0 8〜 0. 3質量%とする。 電解水における配合 量が 0. 0 5質量%より少ないと電解水に保湿性を付与する効果が充分 でなく、 0. 8質量%を超えるとべとつき感が強く感じられるようにな り使用感が低下する。 The blending amount of these amino acids in the electrolyzed water is 0.05 to 0.8 mass%, preferably 0.08 to 0.3 mass%. When the blending amount in the electrolyzed water is less than 0.05% by mass, the effect of imparting moisture retention to the electrolyzed water is not sufficient, and when it exceeds 0.8% by mass, a sticky feeling is strongly felt and a feeling of use is felt. descend.
アミノ酸としてはトリメチルグリシンと Lーヒドロキシプロリンの混 合物を電解水に配合してもよい。 その場合、 配合量はこれらの合計で 0. 0 5〜 0. 8質量%とする。 As an amino acid, a mixture of trimethylglycine and L-hydroxyproline may be added to the electrolyzed water. In that case, the blending amount is 0.05 to 0.8 mass% in total.
以下、 本発明の電解水の製造方法につき第 1図を用いて説明する。 第 1図は、 本発明の電解水の製造に使用する電解装置の一例を示す概 略構成図である。 Hereinafter, the method for producing electrolyzed water of the present invention will be described with reference to FIG. FIG. 1 is a schematic configuration diagram showing an example of an electrolysis apparatus used for producing electrolyzed water of the present invention.
第 1図中、 2は電解原水タンクで、 その内部には電解質水溶液 (電解 原水) 4が貯留されている。 In FIG. 1, 2 is an electrolytic raw water tank in which an electrolytic aqueous solution (electrolytic raw water) 4 is stored.
前記電解原水 4は、 L—ァスコルビン酸又はその誘導体を 1〜 5 0 m M、 好ましくは 2〜 2 0 mMと、 トリメチルグリシン又は Lーヒドロキ シプロリンを 0. 0 5〜 0. 8質量%、 好ましくは 0. 0 8〜 0. 3質 量%含有している。 The electrolyzed raw water 4 comprises L-ascorbic acid or a derivative thereof in an amount of 1 to 50 mM, preferably 2 to 20 mM, and trimethylglycine or L-hydroxyproline in an amount of 0.05 to 0.8% by mass, preferably 0.08 to 0.3. 3% by mass is contained.
上記電解原水 4には、 L—ァスコルビン酸又はその誘導体以外の水溶 性無機塩等の電解質を実質的に含有していないことが望ましい。 水溶性 無機電解質の含有量は、 各水溶性無機電解質の合計で 0. I mM以下で あることが好ましく、 特に 0. 0 2 mM以下であることが望ましい。 It is desirable that the raw electrolytic water 4 does not substantially contain an electrolyte such as a water-soluble inorganic salt other than L-ascorbic acid or a derivative thereof. The content of the water-soluble inorganic electrolyte is preferably not more than 0.1 mM, particularly preferably not more than 0.02 mM, in total for each water-soluble inorganic electrolyte.
このような電解原水 4の調製方法としては、 蒸留水や、 脱イオン水等 の精製水 (純水) に、 Lーァスコルビン酸又はその誘導体とトリメチル ダリシン又は L一ヒドロキシプロリンとを上記濃度範囲に溶解する方法 が例示される。 第 1図中、 6は電解質水溶液供給管 8に介装されたポンプである。 こ のポンプ 6を作動させることにより、 電解質水溶液 4は供給管 8を通つ て連続流通型無隔膜電解槽 1 0に送られる。 ポンプ 6により無隔膜電解 槽 1 0に供給される電解質水溶液 4の流量は 5〜 3 0 0 0 m 1 /m i n 程度とするが、 好ましくは 5 0〜: L 0 0 0 m 1 i n、 より好ましく は 5 0 0〜; 1 0 0 0m l Zm i nである。 As a method for preparing such electrolyzed raw water 4, L-ascorbic acid or a derivative thereof and trimethyldaricin or L monohydroxyproline are dissolved in distilled water or purified water (pure water) such as deionized water within the above concentration range. The method of doing is illustrated. In FIG. 1, 6 is a pump interposed in the electrolyte aqueous solution supply pipe 8. By operating the pump 6, the aqueous electrolyte solution 4 is sent to the continuous flow type diaphragm electrolyzer 10 through the supply pipe 8. The flow rate of the aqueous electrolyte solution 4 supplied to the non-diaphragm electrolyzer 10 by the pump 6 is about 5 to 300 m / min, but preferably 50 to L0 00 m 1 in, more preferably Is from 5 0 0 to 1 0 0 0 ml l Zm in.
無隔膜電解槽 1 0は、 互いに対向する一対の電極 1 2 a、 1 2 bを内 部に有している。 前記一対の電極 1 2 a、 1 2 bは所定間隔離間されて 配設され、 その間隔は 2〜 0. 0 5mm、 好ましくは 1. 5〜 0. l m mである。 電極間距離が 2 mmを超える場合は、 電解により生成する陽 極側電解水と陰極側電解水との混合が不十分になる。 The diaphragm electrolyzer 10 has a pair of electrodes 12 a and 12 b facing each other inside. The pair of electrodes 1 2 a and 1 2 b are disposed at a predetermined interval, and the interval is 2 to 0.05 mm, preferably 1.5 to 0.1 mm. When the distance between the electrodes exceeds 2 mm, mixing of the positive electrode side electrolyzed water and the negative electrode side electrolyzed water generated by electrolysis becomes insufficient.
電極 1 2 a、 1 2 bは電気化学的に不活性な金属材料で形成されてい る。 電極材料としては、 白金、 白金合金等が好ましい。 The electrodes 1 2 a and 1 2 b are made of an electrochemically inactive metal material. As the electrode material, platinum, a platinum alloy or the like is preferable.
1 6は電解電源で、 そのプラス端子及びマイナス端子と、 前記両電極 1 2 a、 1 2 bとはそれぞれ配線 1 8、 2 0により接続されている。 上 記各電極に印加する電力の極性は所定時間間隔で互いに切り換わるもの である。 印加する電力の極性を所定時間毎に切り換えることにより、 陰 極側電解水と陽極側電解水とが 1対の電極において交互に生成されるの で、 陽極側電解水と陰極側電解水とが効率よく混合される。 極性の切替 え時間間隔は、 2〜 1 2 0 0回 分が好ましく、 1 2 0〜 6 0 0回 分 がより好ましい。 また極性を切替えることにより電極にスケールが付着 することを有効に防止する。 16 is an electrolytic power source, and its positive terminal and negative terminal are connected to both electrodes 1 2 a and 1 2 b by wirings 18 and 20, respectively. The polarities of the power applied to each electrode are switched at predetermined time intervals. By switching the polarity of the applied power at predetermined time intervals, the negative electrode side electrolyzed water and the anode side electrolyzed water are alternately generated in a pair of electrodes, so that the anode side electrolyzed water and the cathode side electrolyzed water are separated from each other. It is mixed efficiently. The polarity switching time interval is preferably 2 to 120 times, and more preferably 120 to 600 times. In addition, it is possible to effectively prevent the scale from adhering to the electrode by switching the polarity.
前記電解質水溶液供給管 8を通って無隔膜電解槽 1 0に送られる電解 質水溶液 4は、 無隔膜電解槽 1 0内で電気分解される。 The electrolyte aqueous solution 4 sent to the diaphragm electrolytic cell 10 through the electrolyte aqueous solution supply pipe 8 is electrolyzed in the diaphragm electrolytic cell 10.
両性電解質であるアミノ酸イオンは短時間内では電場の影響を受けず、 アミノ酸イオンの移動は殆ど見られない。 電解生成水のどの部分を採取 してもその分布はほぼ一定である。 電解電流密度は、 0 . 0 0 3〜 0 . 0 8 A Z c m 2が好ましく、 0 . 0 1〜 0 . 0 3 A Z c m 2が特に好ましい。 電解電流密度が 0 . 0 0 3 A Z c m 2未満の場合は、 電解水中の溶存酸素量及び溶存水素量を電解 原水よりも高くすることができない。 0 . 0 8 A / c m 2を超える場合 は、 L —ァスコルビン酸の酸化が加速度的に進み、 デヒドロアスコルビ ン酸の生成量が多くなり、 酸化型の Lーァスコルビン酸になる可能性が 高くなる。 The amino acid ion that is an ampholyte is not affected by the electric field within a short period of time, and almost no amino acid ion migration is observed. No matter what part of the electrolyzed water is collected, its distribution is almost constant. Electrolytic current density is, 0. 0 0 3~ 0. 0 8 AZ cm 2 are preferred, 0. 0 1~ 0. 0 3 AZ cm 2 is particularly preferred. When the electrolysis current density is less than 0.0 3 AZ cm 2 , the dissolved oxygen amount and dissolved hydrogen amount in the electrolyzed water cannot be made higher than the electrolyzed raw water. If it exceeds 0.08 A / cm 2 , the oxidation of L-ascorbic acid accelerates, the amount of dehydroascorbic acid generated increases, and the possibility of becoming oxidized L-ascorbic acid increases. .
上記のようにして電気分解することにより、 電解槽内で電解中に生成 する陽極側電解水と陰極側電解水とが自然に混合にされる。 両電解水が 混合した混合電解水が混合電解水取出し管 2 2を通って連続的に外部に 取出される。 By electrolysis as described above, the anode side electrolyzed water and the cathode side electrolyzed water generated during electrolysis in the electrolytic cell are naturally mixed. The mixed electrolyzed water in which both electrolyzed waters are mixed is continuously taken out through the mixed electrolyzed water discharge pipe 22.
なお、 電解槽 1 0には両電極 1 2 a、 1 2 b間に隔膜を形成した電解 槽を使用してもよい。 隔膜としては、 イオン交換膜や、 無電荷膜等、 電 解隔膜として従来使用されているものが適宜使用できる。 Note that an electrolytic cell in which a diaphragm is formed between both electrodes 12 a and 12 b may be used as the electrolytic cell 10. As a diaphragm, what is conventionally used as an electrolytic membrane, such as an ion exchange membrane and an uncharged membrane, can be used as appropriate.
上記説明においては、 電極は一対としたが、 これに限られず複数の電 極対を電解槽に配備し、 電解効率を高めるようにしても良い。 また更に、 電力の極性を切り換えなくてもよい。 In the above description, the electrode is a pair. However, the present invention is not limited to this, and a plurality of electrode pairs may be provided in the electrolytic cell to increase the electrolysis efficiency. Furthermore, it is not necessary to switch the polarity of power.
本発明の電解水を製造する際に用いる電解装置は特に制限が無く、 従 来用いられている電解水製造装置の何れもが使用できる。 即ち、 電解装 置の大きさ、 電解槽中に隔膜の有無等に関係なく何れの形式のものでも 利用できる。 The electrolyzer used when producing the electrolyzed water of the present invention is not particularly limited, and any electrolyzed water producing apparatus conventionally used can be used. In other words, any type can be used regardless of the size of the electrolytic device and the presence or absence of a diaphragm in the electrolytic cell.
更に、 上記説明においては陽極側電解水と陰極側電解水とを混合した 混合電解水として取り出したが、 これに限られず、 陽極側電解水と陰極 側電解水とを別々に取り出して別々に使用しても良い。 この場合は電極 に印加する電力の極性を切り換えない方式が合理的である。 Furthermore, in the above description, it was taken out as mixed electrolyzed water in which anode side electrolyzed water and cathode side electrolyzed water were mixed. However, the present invention is not limited thereto, and anode side electrolyzed water and cathode side electrolyzed water are taken out separately and used separately. You may do it. In this case, it is reasonable to switch the polarity of the power applied to the electrode.
第 2図及び第 3図は、 本発明の電解水の製造に使用する電解装置の他 の例を示す斜視図である。 第 2図は電解装置を組み立てた状態、 第 3図 は電解装置を分解した状態の斜視図を示している。 2 and 3 are perspective views showing other examples of the electrolyzer used for the production of the electrolyzed water of the present invention. Fig. 2 shows the electrolyzer assembled, Fig. 3 Shows a perspective view of a state in which the electrolytic device is disassembled.
第 2図及び第 3図に示す電解装置 1 0 0は、 装置本体を形成するハウ ジング 1 0 2と、 ハウジング 1 0 2に対して着脱自在に取り付けられる 給液ュニッ ト 1 04とから成る。 給液ュニッ ト 1 04は、 その両側に突 設された係止片 1 4 2をハウジング 1 0 2に形成された係止孔 1 4 0に 挿入して係止させるとともに、 その上端縁に形成された一対の係止爪 1 44をハウジング 1 0 2の係止溝 1 4 6に係止させることにより、 ハウ ジング 1 0 2に取り付けられるようになつている。 第 2図は給液ュニッ ト 1 04がハウジング 1 0 2に取り付けられた状態、 第 3図は、 給液ュ ニッ ト 1 0 4がハウジング 1 0 2から取り外された状態である。 The electrolyzer 100 shown in FIGS. 2 and 3 includes a housing 1002 that forms the apparatus body, and a liquid supply unit 104 that is detachably attached to the housing 102. The liquid supply unit 104 is inserted into the locking holes 14 0 formed in the housing 10 2 and locked at both ends thereof, and is formed at the upper edge thereof. The pair of locking claws 1 44 are locked to the locking grooves 1 46 of the housing 10 2 so that they can be attached to the housing 1 0 2. FIG. 2 shows a state in which the liquid supply unit 104 is attached to the housing 10 2, and FIG. 3 shows a state in which the liquid supply unit 10 4 is detached from the housing 10 2.
第 4図は、 給液ュニッ ト 1 0 4がハウジング 1 0 2に対して取り付け られた状態における給液ュニッ ト 1 0 4内部と噴霧部 1 2 0を示す斜視 図 ( a) 及び断面図 (b) である。 FIG. 4 is a perspective view (a) and a cross-sectional view showing the inside of the liquid supply unit 10 4 and the spray section 1 2 0 in a state where the liquid supply unit 10 4 is attached to the housing 10 2. b)
給液ュニット 1 0 4は、 電解原水 1 1 1を蓄える電解原水タンク 1 0 6と、 電解原水を電気分解する一対の棒状電極 1 1 9 a、 1 1 9 bと、 電極 1 1 9 a、 1 1 9 bによって電気分解された電解水を吸収する吸液 媒体 (例えば、 吸収力の高いスポンジ) 1 1 0と、 電解原水タンク 1 0 6内の電解原水を吸液媒体 1 1 0へと供給する断面が略円形の通液路 1 0 8とを有している。 The liquid supply unit 1 0 4 is an electrolytic raw water tank 1 0 6 for storing electrolytic raw water 1 1 1, a pair of rod-like electrodes 1 1 9 a, 1 1 9 b, and electrodes 1 1 9 a for electrolyzing electrolytic raw water 1 1 9 b Absorbing medium that absorbs electrolyzed water electrolyzed by b (for example, sponge with high absorbency) 1 1 0 and electrolyzed raw water in electrolytic raw water tank 1 0 6 into liquid absorbing medium 1 1 0 The supply cross section has a substantially circular liquid passage 10 8.
電解原水タンク 1 0 6は、 タンク内の電解原水 1 1 1を吸液媒体 1 1 0へとスムーズに導くことができるように、 取付状態 (第 2図の状態) において吸液媒体 1 1 0よりも上方に配置されている。 電解原水タンク 1 0 6の底面には、 電解原水タンク 1 0 6の内部と通液路 1 0 8とを連 通する通液口 1 0 6 aが設けられている。 The electrolyzed raw water tank 1 0 6 has a liquid absorbing medium 1 1 0 in the mounted state (state shown in FIG. 2) so that the electrolytic raw water 1 1 1 in the tank can be smoothly guided to the liquid absorbing medium 1 1 0. It is arranged above. On the bottom surface of the electrolyzed raw water tank 10 6, there is provided a liquid flow port 10 6 a that connects the inside of the electrolyzed raw water tank 10 6 and the liquid flow path 10 8.
棒状の電極 1 1 9 a、 1 1 9 bは、 吸液媒体 1 1 0の直ぐ上流側の通 液路 1 0 8内に、 吸液媒体 1 1 0の左右にこれを挟むように配置されて いる。 通液路 1 0 8を通じて電極 1 1 9 a、 1 1 9 b間に電解原水を流 すことにより、 電解原水が電気分解される。 通液路 1 0 8内には、 吸液 媒体 1 1 0中への電解水の浸透を調整する弁や膜等から成る抵抗手段 1 4 7が設けられている。 The rod-shaped electrodes 1 1 9 a and 1 1 9 b are arranged in the liquid flow path 1 0 8 immediately upstream of the liquid absorption medium 1 1 0 so that the liquid absorption medium 1 1 0 is sandwiched between the right and left sides. ing. Electrolyzed raw water flows between the electrodes 1 1 9 a and 1 1 9 b through the flow path 1 0 8 By doing so, the electrolyzed raw water is electrolyzed. In the liquid flow path 10 8, there is provided resistance means 1 4 7 composed of a valve, a membrane or the like for adjusting the penetration of the electrolyzed water into the liquid absorbing medium 1 10.
電解装置 1 0 0にはピエゾ振動子 1 2 1、 多孔噴霧プレート 1 2 3か らなる噴霧部 1 2 0が設けられている。 電極 1 1 9 a、 1 1 9 bにより 電気分解された電解原水 (電解生成水) は、 噴霧部 1 2 0により外部へ 噴霧される。 多孔噴霧プレ一ト 1 2 3の内側面には吸液媒体 1 1 0の一 端が接触しており、 外側面の一端側にはピエゾ振動子 1 2 1が固定され ている。 このピエゾ振動子 1 2 1に交流やパルス電圧を印加してピエゾ 振動子 1 2 1を振動させることにより、 ピエゾ振動子 1 2 1に固定され た多孔噴霧プレ一ト 1 2 3を振動させることができる。 吸液媒体 1 1 0 に吸収された電解水は、 多孔噴霧プレート 1 2 3の振動による吸引作用 を受け、 多孔噴霧プレート 1 2 3に形成された多数の貫通孔を通過する。 その後、 ハウジングに形成された噴霧口 1 2 2から外部に微細液滴とし て拡散噴霧される。 The electrolyzer 1 100 is provided with a spray section 1 2 0 composed of a piezoelectric vibrator 1 2 1 and a porous spray plate 1 2 3. Electrolyzed raw water (electrolyzed water) electrolyzed by the electrodes 1 1 9 a and 1 1 9 b is sprayed to the outside by the spraying part 1 2 0. One end of the liquid-absorbing medium 110 is in contact with the inner side surface of the porous spray plate 123, and a piezo vibrator 12 21 is fixed to one end side of the outer side surface. By vibrating the piezo vibrator 1 2 1 by applying alternating current or pulse voltage to this piezo vibrator 1 2 1, the porous spray plate 1 2 3 fixed on the piezo vibrator 1 2 1 is vibrated. Can do. The electrolyzed water absorbed in the liquid absorbing medium 1 1 0 is subjected to a suction action by the vibration of the porous spray plate 1 2 3 and passes through a plurality of through holes formed in the porous spray plate 1 2 3. Thereafter, the spray is diffused and sprayed as fine droplets to the outside from the spray ports 1 2 2 formed in the housing.
第 2図及び第 3図に示す開閉カバ一 1 2 6は、 噴霧口 1 2 2を露出さ せたり隠したりするもので、 ハウジング 1 0 2に対して上下に摺動可能 に取り付けられている。 また、 開閉カバー 1 2 6およびハウジング 1 0 2は、 協働して開閉カバー 1 2 6の位置を検出できる検出手段を有して いる。 第 2図には、 そのような検出手段を構成するハウジング 1 0 2側 のスィッチ 1 3 9が明確に示されている。 The open / close cover 1 2 6 shown in FIGS. 2 and 3 exposes or hides the spray port 1 2 2 and is slidably attached to the housing 10 2. . Further, the opening / closing cover 1 2 6 and the housing 10 2 have detection means capable of detecting the position of the opening / closing cover 1 2 6 in cooperation. FIG. 2 clearly shows the switch 1 39 on the housing 10 2 side constituting such a detection means.
ハウジング 1 0 2内には、 マイクロプロセッサを組込んだ制御部 1 3 6が設けられている。 この制御部 1 3 6は、 電極 1 1 9 a、 1 1 9 bへ の電圧の印加と振動子 1 2 1の駆動を制御するとともに、 前記スィッチ 1 3 9からの検知信号を受信する。 制御部 1 3 6に設けられた電解電源 のプラス端子またはマイナス端子は、 不図示の配線を介して電極 1 1 9 a、 1 1 9 bと電気的に接続されている。 各電極 1 1 9 a、 1 1 9 bに 印加される電力の極性は、 制御部 1 3 6により所定の時間間隔で互いに 切り換えられる。 以上のようにして陽極側電解水と陰極側電解水とが混 合してなる電解生成水は、 噴霧部 1 2 0を通じて噴霧口 1 2 2から連続 的に外部へ噴霧される。 A control unit 1 3 6 incorporating a microprocessor is provided in the housing 10 2. The control unit 1 3 6 controls the application of voltage to the electrodes 1 1 9 a and 1 1 9 b and the drive of the vibrator 1 2 1, and receives a detection signal from the switch 1 3 9. The positive terminal or the negative terminal of the electrolytic power source provided in the control unit 1 3 6 is electrically connected to the electrodes 1 1 9 a and 1 1 9 b through a wiring (not shown). Each electrode 1 1 9 a, 1 1 9 b The polarity of the applied power is switched between each other at predetermined time intervals by the control unit 1 36. The electrolyzed water formed by mixing the anode-side electrolyzed water and the cathode-side electrolyzed water as described above is continuously sprayed to the outside through the spraying part 120 through the spraying port 1222.
第 2図及び第 3図中、 参照符号 1 3 2は、 電極 1 1 9 a、 1 1 9 bお よび振動子 1 2 1に電力を供給するための電源部である。 電源部 1 3 2 における電源としては、 乾電池 1 3 0等を使用することができる。 また、 参照符号 1 3 4は、 電源部 1 3 2の蓋である。 2 and 3, reference numeral 1 3 2 is a power supply unit for supplying power to the electrodes 1 1 9 a and 1 1 9 b and the vibrator 1 2 1. As a power source in the power source section 1 3 2, a dry battery 1 3 0 or the like can be used. Reference numeral 1 3 4 is a cover of the power supply unit 1 3 2.
なお、 第 2図及び第 3図に示す電解装置の電極間距離、 電解電流密度、 電極に印加する電圧の極性の切替え時間間隔、 電解原水の流量等の値は、 第 1図に示す電解装置の値と同様である。 実施例 The values of the distance between electrodes of the electrolyzer shown in FIGS. 2 and 3, the electrolysis current density, the switching time interval of the polarity of the voltage applied to the electrode, the flow rate of the electrolyzed raw water, etc. It is the same as the value of. Example
実施例 1 Example 1
第 2〜第 4図に示す電解装置を用いて Lーァスコルビン酸とトリメチ ルグリシンを含有する電解原水を電解し、 電解水を製造した。 電解槽は、 内径 1 0 mmの通液路 1 0 8内に直径 1. 6 mmの円柱状の電極 2本を 間隔 0. 9 mmに挿入して構成した。 この電解槽に電解原水を 1 0m 1 Zm i nの流量で供給し、 電解電流密度 0. 0 5 AZ c m2で電解し電 解水を得た。 The electrolyzed raw water containing L-ascorbic acid and trimethylglycine was electrolyzed using the electrolyzer shown in FIGS. 2 to 4 to produce electrolyzed water. The electrolytic cell was constructed by inserting two cylindrical electrodes with a diameter of 1.6 mm into a liquid passage 10 with an inner diameter of 10 mm at an interval of 0.9 mm. Electrolyzed raw water was supplied to the electrolytic cell at a flow rate of 10 m 1 Zmin and electrolyzed at an electrolysis current density of 0.05 AZ cm 2 to obtain electrolyzed water.
電解原水には Lーァスコルピン酸 (A s A) 3 0 mMと 0. 1質量% トリメチルグリシン (TMG) を精製水に溶解したものを調製して使用 した。 なお、 溶媒に精製水を用いたので、 電解原水中の水溶性無機塩の 含有量は極めて微量 ( 0. O l mM未満) であった。 The electrolyzed raw water was prepared by using 30 mM L-ascorbic acid (As A) and 0.1% by mass trimethylglycine (TMG) dissolved in purified water. Since purified water was used as the solvent, the content of the water-soluble inorganic salt in the electrolytic raw water was extremely small (less than 0. 1 mM).
得られた電解水を用いて 2 0〜 5 0歳代の女性 1 0人による官能試験 を行った。 塗布回数は顔前面に朝夕一日 2回とし、 2週間行った。 Using the resulting electrolyzed water, a sensory test was conducted with 10 women in their 20s to 50s. The application was performed twice a day in the morning and evening on the front of the face for 2 weeks.
官能試験の方法は意味微分法を用い、 「どちらでもない」 を 0点とし て 「やや悪い」 を一 1点、 「悪い」 を一 2点、 「非常に悪い」 を一 3点、 一方 「やや良い」 を + 1点、 「良い」 を + 2点、 「非常に良い」 を + 3点 として評価した。 The sensory test uses the semantic differential method, with “neither” set to 0. 1 point for “slightly bad”, 1 point for “bad”, 1 point for “very bad”, 3 points for “very bad”, + 1 point for “slightly good”, + 2 points for “good”, “very good” Was rated as +3 points.
更に、 比較のため、 上記電解原水と、 上述した電解装置を用いて L一 ァスコルビン酸 3 0 m Mのみを精製水に溶解した電解原水を同様の条件 で電気分解した電解水とについて官能試験を行った。 結果を表 1に示す。 表 1 Furthermore, for comparison, a sensory test was conducted on the electrolyzed raw water and electrolyzed water obtained by electrolyzing the electrolyzed raw water obtained by dissolving only 30 mM L-ascorbic acid in purified water using the above-described electrolysis apparatus under the same conditions. went. The results are shown in Table 1. table 1
本発明の電解水は、 刺激性が全くなく、 電解原水や Lーァスコルビン 酸のみを含有する電解水に比較してはり、 つやが増し、 しっとり感 (保 湿性) に優れていた。 The electrolyzed water of the present invention is not irritating at all, and is more glossy and moist (retained) than the electrolyzed raw water or electrolyzed water containing only L-ascorbic acid. Excellent wetness).
得られた電解水の p H、 酸化還元電位 (ORP)、 溶存酸素量 (DO)、 電気伝導度 (E C) を測定した結果を表 2に示す。 表 2 Table 2 shows the results of measuring the pH, redox potential (ORP), dissolved oxygen content (DO), and electrical conductivity (E C) of the electrolyzed water obtained. Table 2
実施例 2 Example 2
実施例 1 と同じ条件、 同じ電解装置を用いて L—ァスコルビン酸 3 0 mMと 0. 3 5質量%の ーヒドロキシプロリン (HY P) を精製水に 溶解した電解原水を電解し、 電解水を製造した。 Using the same electrolysis apparatus as in Example 1, electrolyzed raw electrolyzed water in which 30 mM L-ascorbic acid and 0.35% by mass of hydroxyproline (HYP) were dissolved in purified water was used. Manufactured.
得られた電解水と、 比較のため電解原水とを用いて実施例 1 と同様に 女性 1 0人による官能試験を行った。 表 3に官能試験の結果を示す。 Using the obtained electrolyzed water and the electrolyzed raw water for comparison, a sensory test was conducted by 10 women in the same manner as in Example 1. Table 3 shows the results of the sensory test.
表 3 Table 3
本発明の電解水は、 刺激性が全くなく、 電解原水や Lーァスコルビン 酸のみを含有する電解水に比較して毛穴やきめが改善され、 なめらかさ やしつとり感 (保湿性) に優れていた。 The electrolyzed water of the present invention has no irritation and has improved pores and texture as compared with electrolyzed water containing only electrolyzed raw water or L-ascorbic acid, and has a smooth and moist feeling (moisturizing property). It was.
得られた電解水の p H、 酸化還元電位 (OR P)、 溶存酸素量 (D〇)、 電気伝導度 (E C) を測定した結果を表 4に示す。 表 4 Table 4 shows the results of measuring the pH, redox potential (OR P), dissolved oxygen content (D0), and electrical conductivity (EC) of the electrolyzed water obtained. Table 4
p H OR P DO E C p H OR P DO E C
(mV) (m g/L) (mSZm) 電解原水 3. 1 0 1 2 3 5. 2 3 6. 3 電解水 3. 1 7 一 7 3. 3 4. 5 3 6. 1 (mV) (mg / L) (mSZm) Electrolyzed raw water 3. 1 0 1 2 3 5. 2 3 6. 3 Electrolyzed water 3. 1 7 1 7 3. 3 4. 5 3 6. 1
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| US7928111B2 (en) | 2007-06-08 | 2011-04-19 | Senomyx, Inc. | Compounds including substituted thienopyrimidinone derivatives as ligands for modulating chemosensory receptors |
| US8609173B2 (en) | 2008-07-31 | 2013-12-17 | Senomyx Inc. | Compositions comprising sweetness enhancers and methods of making them |
| US8633186B2 (en) | 2007-06-08 | 2014-01-21 | Senomyx Inc. | Modulation of chemosensory receptors and ligands associated therewith |
| US8877922B2 (en) | 2012-08-06 | 2014-11-04 | Senomyx, Inc. | Sweet flavor modifier |
| US9000054B2 (en) | 2010-08-12 | 2015-04-07 | Senomyx, Inc. | Method of improving stability of sweet enhancer and composition containing stabilized sweet enhancer |
| US9000151B2 (en) | 2013-02-19 | 2015-04-07 | Senomyx, Inc. | Sweet flavor modifier |
| US9382196B2 (en) | 2008-07-31 | 2016-07-05 | Senomyx, Inc. | Processes and intermediates for making sweet taste enhancers |
| US9603848B2 (en) | 2007-06-08 | 2017-03-28 | Senomyx, Inc. | Modulation of chemosensory receptors and ligands associated therewith |
| US11945813B2 (en) | 2018-08-07 | 2024-04-02 | Firmenich Incorporated | 5-substituted 4-amino-1H-benzo[c][1,2,6]thiadiazine 2,2-dioxides and formulations and uses thereof |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6085625B2 (en) * | 2014-11-27 | 2017-02-22 | 株式会社バイオレドックス研究所 | Cosmetic liquid and method for producing the same |
| WO2018073910A1 (en) * | 2016-10-19 | 2018-04-26 | 株式会社プライマリーステップ | Cosmetic and cosmetic spraying device |
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| US7928111B2 (en) | 2007-06-08 | 2011-04-19 | Senomyx, Inc. | Compounds including substituted thienopyrimidinone derivatives as ligands for modulating chemosensory receptors |
| US8541421B2 (en) | 2007-06-08 | 2013-09-24 | Senomyx Inc. | Methods of enhancing sweet taste of compositions using substituted thieno{2,3-D}pyrimidines |
| US9603848B2 (en) | 2007-06-08 | 2017-03-28 | Senomyx, Inc. | Modulation of chemosensory receptors and ligands associated therewith |
| US8633186B2 (en) | 2007-06-08 | 2014-01-21 | Senomyx Inc. | Modulation of chemosensory receptors and ligands associated therewith |
| US9181276B2 (en) | 2007-06-08 | 2015-11-10 | Senomyx, Inc. | Modulation of chemosensory receptors and ligands associated therewith |
| US10570105B2 (en) | 2008-07-31 | 2020-02-25 | Firmenich Incorporated | Processes and intermediates for making sweet taste enhancers |
| US8609173B2 (en) | 2008-07-31 | 2013-12-17 | Senomyx Inc. | Compositions comprising sweetness enhancers and methods of making them |
| US10087154B2 (en) | 2008-07-31 | 2018-10-02 | Senomyx, Inc. | Processes and intermediates for making sweet taste enhancers |
| US9732052B2 (en) | 2008-07-31 | 2017-08-15 | Senomyx, Inc. | Processes and intermediates for making sweet taste enhancers |
| US10308621B2 (en) | 2008-07-31 | 2019-06-04 | Senomyx, Inc. | Processes and intermediates for making sweet taste enhancers |
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| US11129397B2 (en) | 2010-08-12 | 2021-09-28 | Firemenich Incorporated | Method of improving stability of sweet enhancer and composition containing stabilized sweet enhancer |
| US10244779B2 (en) | 2010-08-12 | 2019-04-02 | Senomyx, Inc. | Method of improving stability of sweet enhancer and composition containing stabilized sweet enhancer |
| US9000054B2 (en) | 2010-08-12 | 2015-04-07 | Senomyx, Inc. | Method of improving stability of sweet enhancer and composition containing stabilized sweet enhancer |
| US9420814B2 (en) | 2012-08-06 | 2016-08-23 | Senomyx, Inc. | Sweet flavor modifier |
| US9687015B2 (en) | 2012-08-06 | 2017-06-27 | Senomyx, Inc. | Sweet flavor modifier |
| US8877922B2 (en) | 2012-08-06 | 2014-11-04 | Senomyx, Inc. | Sweet flavor modifier |
| US9745293B2 (en) | 2012-08-06 | 2017-08-29 | Senomyx, Inc. | Sweet flavor modifier |
| US9138013B2 (en) | 2012-08-06 | 2015-09-22 | Senomyx, Inc. | Sweet flavor modifier |
| US9000151B2 (en) | 2013-02-19 | 2015-04-07 | Senomyx, Inc. | Sweet flavor modifier |
| US9695162B2 (en) | 2013-02-19 | 2017-07-04 | Senomyx, Inc. | Sweet flavor modifier |
| US9475803B2 (en) | 2013-02-19 | 2016-10-25 | Senomyx, Inc. | Sweet flavor modifier |
| US9371317B2 (en) | 2013-02-19 | 2016-06-21 | Senomyx, Inc. | Sweet flavor modifier |
| US11945813B2 (en) | 2018-08-07 | 2024-04-02 | Firmenich Incorporated | 5-substituted 4-amino-1H-benzo[c][1,2,6]thiadiazine 2,2-dioxides and formulations and uses thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2007007591A (en) | 2007-01-18 |
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