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    • 专利摘要:
    METHOD OF ELECTROLYZED WATER GENERATION; AND ELECTROLYZED WATER GENERATOR TO PRODUCE ALKALINE METAL CHLORIDE-FREE ACID ELECTROLYZED WATER AND ALKALINE METAL CHLORIDE-FREE ACID ELECTROLYZED WATER THROUGH A TWO-COMPARTMENT CELL. A method of generating electrolyzed water and a generator to produce both alkali metal chloride-free acidic electrolyzed water (19) and alkali metal chloride-free alkaline electrolyzed water (9) by electrolyzing the aqueous solution (7) with dissolved alkali metal chloride (11). Solution: A method of generating electrolyzed water, which comprises the steps of: the anodic electrolyte comprising aqueous solution with dissolved alkali metal chloride is supplied and circulated from an anodic electrolyte storage tank (10) that retains the anodic electrolyte in an anode chamber (2) of a two-compartment cell (1) separated by a cation exchange membrane (4) in two chambers of an anode chamber (2) that accommodates an anode (5) and a chamber of cathode (3) which accommodates a cathode (6), alkali metal chloride-free raw water (7) is supplied to the cathode chamber (3), and electrolysis is carried out, whereby the free alkaline electrolyzed water in (...).
    公开号:BR112015017511B1
    申请号:R112015017511-2
    申请日:2014-01-28
    公开日:2021-07-06
    发明作者:Masaharu Uno；Katsumi Hamaguchi
    申请人:Industrie De Nora S.P.A.；
    IPC主号:
    专利说明:

    TECHNICAL FIELD
    [001] The present invention relates to a method of generating electrolyzed water and a generator, which generates, stably and at a high current efficiency, both acidic electrolyzed water and high quality alkaline electrolyzed water, free of alkali metal chlorides with high corrosivity, such as salt. PRIOR TECHNIQUE
    [002] Recently, the electrolyzed water generator was emphasized through several movements in the industries, such as: JIS certification for the electrolyzed water generator as a domestic appliance in 2005; articles referring to the use of electrolyzed water in the Hygiene Management Standards in School Meals and manuals listed by the Ministry of Education, Culture, Sports, Science and Technology in 2009, and in Teaching Materials by the Japanese Food Hygiene Association, associated with the Ministry of Health in 2009.
    [003] "Electrolyzed water" is a general term for the aqueous solution obtained by electrolysis treatment of tap water or fine brine at a weak DC voltage, and is broadly classified as "acidic electrolyzed water" formed at the anode and "alkaline electrolyzed water" formed at the cathode.
    [004] In general, "acid electrolyzed water" collectively indicates acidic electrolyzed water with a pH value of 6.5 or below. It shows strong sterilizing power broadly to various pathogenic bacteria or drug resistant bacteria from it (such as MRSA) and has a variety of application fields including medical care, dentistry, food or agriculture. The main sterilizing factor is hypochlorous acid water formed by electrolysis.
    [005] Furthermore, "acid electrolyzed water" is classified into strongly acidic electrolyzed water, slightly acidic electrolyzed water and weakly acidic electrolyzed water. Water electrolyzed with hypochlorous acid as a positive ingredient (available chlorine concentration: 20 to 60 ppm) at pH 2.7 or less is called strongly acidic electrolyzed water (strongly acidic hypochlorous acid water). For a strongly acidic electrolyzed water generator, the application is individually authorized based on the Japanese Pharmaceutical Affairs Law, and, until then, the generator is approved as a medical device (with revision of the Pharmaceutical Affairs Law, sale of team production medical) for the purpose of use mentioned below.
    [006] Strongly acidic electrolyzed water (40 ppm available chlorine) shows bactericidal/antiviral activity (in addition, high norovirus inactivation effect) equal to sodium hypochlorite of a high concentration (1000 ppm). This is due to the fact that while the existence rate of hypochlorous acid (HClO) as a sterilization factor is approximately 90% in strongly acidic electrolyzed water, sodium hypochlorite, which is alkaline, remains at less than 5% and 95% or more and exists as a weakly active hypochlorous acid (ClO-) ion. However, hypochlorous acid reacts easily with organic matter and so if there is a lot of organic matter, the sterilizing power of strongly acidic electrolyzed water is considerably reduced. To overcome this, a method is adopted as an effective way for an object to be sterilized to be first treated in strongly alkaline electrolyzed water, where an oil, fat and protein removal effect is found to be high and then treated in strongly acidic electrolyzed water. Several tests have been conducted so far regarding security, from which a high level has been confirmed.
    [007] Slightly acidic electrolyzed water is an aqueous solution of hypochlorous acid with the pH value of 5 to 6.5 and available chlorine at 10 to 30 ppm, and it is characteristic that all the water generated is sterilization water. It shows bactericidal and antiviral activity similar to strongly acidic electrolyzed water. Security test results are the same.
    [008] The weakly acidic electrolyzed water with a pH range between the slightly acidic electrolyzed water and the strongly acidic electrolyzed water was approved by the deliberation of the Food Safety Commission. Weakly acidic electrolyzed water is recognized as having activity and safety that are equal to strongly acidic electrolyzed water or slightly acidic electrolyzed water.
    [009] On the other hand, "alkaline electrolyzed water" is primarily composed of caustic alkali generated on the cathode side simultaneously in electrolysis. "Alkaline electrolyzed water" is roughly classified into two: strongly alkaline electrolyzed water (pH 11 to 11.5) and weakly alkaline electrolyzed water (pH 9 to 10), called alkaline ionized water, formed by electrolyzing tap water with use of a domestic electrolyzed water generator, also called an alkaline ionized water purifier. The electrolyzed household water generator is the name of a household medical equipment classified as "a utility instrument medical supply generator 83" in the Order of Compliance of the Pharmaceutical Affairs Act. The effects, as mentioned below, of alkaline ionized water that have received approval as a medical device have been confirmed as the results of restricted comparative clinical trials. More specifically, it is effective for "chronic diarrhea, indigestion, abnormal fermentation in the stomach and intestines, antacid and hyperacidity". Also, an enhancement effect was accepted for constipation. It has now been revised as having "a gastrointestinal symptom improving effect" with revision (2005) of the Pharmaceutical Affairs Act.
    [010] By electrolyzing the aqueous solution in which alkali metal chlorides containing electrolyte, such as aqueous sodium chloride solution or aqueous potassium chloride solution, the acidic electrolyzed water containing water is dissolved in the electrolyzed water generator of hypochlorous acid is obtained at the anode and alkaline electrolyzed water containing caustic alkali is obtained at the cathode. The electrolytic system for performing electrolysis by applying aqueous sodium chloride solution and aqueous potassium chloride solution as electrolyte forms acidic electrolyzed water, including hypochlorous acid water, which has a sterilizing effect for bacteria, including Escherichia coli on the anode side, while alkaline electrolyzed water which includes caustic alkali which has a strong detergency such as degreasing and protein removal, is formed on the cathode side and is widely used in the fields of food processing, agriculture and medical care and nursing.
    [011] For such an electrolytic system to generate acidic electrolyzed water, including hypochlorous acid water and alkaline electrolyzed water that includes caustic alkali, methods employing the two-compartment cell and the three-compartment cell are known.
    [012] In the present invention, the hypochlorous acid water formed at the anode by electrolysis or the acidic electrolyzed water which includes hypochlorous acid water to be formed by dissolving chlorine gas generated at the anode in the dissolution water after separation and recovery , is simply called "acid electrolyzed water", while alkaline electrolyzed water that includes caustic alkali is simply called "alkaline electrolyzed water".
    [013] As a method that applies a two-compartment cell, Patent Literature 1 describes examples. The two-compartment cell has an anode and cathode separated by a diaphragm, where aqueous sodium chloride solution is supplied to the anode chamber and raw water, such as tap water, or aqueous sodium chloride solution is supplied to the cathode chamber for the electrolysis operation.
    [014] It is indicated that, in acidic electrolyzed water produced in such a way, a relatively high concentration of unreacted sodium chloride remains and that such sodium chloride may be precipitated after service or problems including pipe metal corrosion will occur . In such a two-compartment method electrolyzed water generation system, brine is supplied to the anode chamber to improve the electrolysis efficiency.
    [015] For this reason, the acidic electrolyzed water generated in the anode chamber, which contains not only hypochlorous acid, but also a sodium chloride component, will cause such a phenomenon as chlorine gas evaporation through the equilibrium movement . Since hypochlorous acid will evaporate in a short period of time, it becomes difficult for acidic electrolyzed water to maintain the required sterilizing power for a long period of time, resulting in limited applications. Furthermore, corrosion of the peripheral device by this sodium chloride becomes a serious obstacle to market expansion.
    [016] Thus, a three-compartment cell, which has a configuration consisting of the anode chamber separated by an anion exchange membrane, the cathode chamber separated by a cation exchange membrane and the intermediate chamber separated by the two membranes , can minimize mixing of raw material salt component in formed acid electrolyzed water and alkaline electrolyzed water by supplying raw material brine in the intermediate chamber. Thus, the three-compartment cell can solve the problems encountered so far, including high corrosiveness and unsuitability for agricultural fields, and many companies participate in the development of associated devices and many patent applications have been filed.
    [017] Representative patent literature includes Patent Literature 2 and Patent Literature 3. This method employs a three-compartment cell comprising the anode chamber, the intermediate chamber and the cathode chamber separated by two blades of diaphragm that have ion exchange capability. The electrolysis is conducted in such a way that aqueous sodium chloride solution is supplied to the intermediate chamber, and the alkali metal chloride-free raw water is supplied to the anode chamber and the cathode chamber so as to constitute the acidic electrolyzed water at the anode and alkaline electrolyzed water at the cathode, respectively. In this method, an anion exchange membrane is applied as a diaphragm to separate the anode chamber and the intermediate chamber, and a cation exchange membrane is applied as a diaphragm to separate the cathode chamber and the intermediate chamber. Theoretically, only the chloride ion that is needed for the acidic electrolyzed water composition migrates from the intermediate chamber to the anode chamber, and only the sodium ion that is needed for the alkaline electrolyzed water composition migrates from the intermediate chamber to the chamber of cathode.
    [018] Thus, it is suggested that, compared to the two-compartment cell, this method is advantageous in constituting the electrolyzed water with less residual sodium chloride, improving the problems of salt precipitation after the use or corrosion of metal by salt.
    [019] As mentioned above, the three compartment cell applies two types of ion exchange membrane: anion exchange membrane and cation exchange membrane to constitute acidic electrolyzed water and alkaline electrolyzed water. When the commercially available anion exchange membrane and the cation exchange membrane are compared, it was found that the following problems occur due to the fact that the anion conductivity and ion selectivity of the anion exchange membrane are inferior.
    [020] When, for example, electrolysis is conducted in the three-compartment cell in such a way that the aqueous solution of sodium chloride is supplied to the intermediate chamber and the raw water that does not include alkali metal chloride, such as salt, is supplied to the anode chamber and the cathode chamber, chloride ions migrate from the intermediate chamber to the anode chamber through the anion exchange membrane and, at the same time, sodium ions migrate to the cathode chamber through of the cation exchange membrane. At this point, the chlorine generation reaction, as shown by Equation (1), progresses at the anode and the chlorine formed immediately reacts with water as in Equation (2) to constitute acidic electrolyzed water. However, when the supply of chloride ions is insufficient, oxygen generation competitively progresses through water electrolysis, as shown in Equation (3). On the other hand, at the cathode, the generation of hydrogen progresses through the electrolysis of water, as in Equation (4), and the sodium hydroxide water (alkaline electrolyzed water) is composed of the formed hydroxyl ions and the supplied sodium ions from the middle chamber.
    [021]

    [022]

    [023]

    [024]

    [025] The rate of migration of sodium ions that penetrate a commercial cation exchange membrane is sufficiently fast and even if the current density at the time of electrolysis is changed, for example, from a low level of 3 A/dm2 to a high level of 20 A/dm2, 90% or more of the applied electrical current is used to constitute the alkaline electrolyzed water.
    [026] However, the rate of migration of chloride ions that penetrate a commercial anion exchange membrane is not that high. For example, the electric current used for the composition of acidic electrolyzed water (current efficiency) is about 80%, even through electrolysis at a low current density, and decreases to about 40% at a high current density . Thus, the energy efficiency for composing the hypochlorous acid water at the anode is not high, causing a problem that the higher the current density, the lower the energy efficiency.
    [027] In addition, for example, when electrolysis is continued by the three-compartment cell while circulating and delivering aqueous sodium chloride solution to the intermediate chamber, the pH of the circulating aqueous sodium chloride solution decays (acid) with over time and at the same time chlorine gas which is harmful to the human body is generated as the available chlorine ingredient accumulates in the aqueous sodium chloride solution causing a safety problem of leakage outside the electrolytic system. The cause of the chlorine gas generation is not clear. Hypochlorous acid and hydrochloric acid are composed by Equation (2) and successively by Equation (1), and the hydrogen ion is composed by the side reaction, Equation (3). The commercial anion exchange membrane applied for the separation of the anode chamber and the intermediate chamber is insufficient in ionic selectivity and hypochlorous acid or hydrogen ion is expected to move from the anode chamber to the intermediate chamber through the anion exchange membrane.
    [028] The reason why the ionic selectivity of a commercial anion exchange membrane proves to be insufficient is the fact that even acidic electrolyzed water composed in a three-compartment cell mixes with sodium chloride of a low concentration. The anion exchange membrane does not theoretically penetrate the sodium ion, which is the cation, however, in hypochlorous acid water prepared using a commercial anion exchange membrane, the increase in sodium ion concentration is clearly recognized in comparison to raw water. On the other hand, a commercial cation exchange membrane has a sufficient ionic selectivity and, in alkaline electrolyzed water formed at the cathode, the increase in chloride ion concentration is little admitted compared to raw water.
    [029] In addition to the problems mentioned above, there is another problem in the commercial anion exchange membrane that refers to the fact that, since deterioration is accelerated by oxidizing agents such as hypochlorous acid, the ionic selectivity and anionic conductivity decrease each time more when electrolysis is continued. Patent Literature 4 and Patent Literature 5 suggest, as a method of restricting the deterioration of the anion exchange membrane, that contact of oxidants, such as hypochlorous acid formed at the anode and an anion exchange membrane, be physically removed by disposing is a porous non-woven tissue or a body with a porous structure between the anode and the anion exchange membrane. However, contact of the oxidant with the anion exchange membrane cannot be completely prevented by these methods, and the cell voltage is increased by inserting an insulating material between the anode and cathode, leading to another problem of increased consumption of electricity energy.
    [030] Thus, the rate of electrical energy utilization (current efficiency) in the production of acidic electrolyzed water by the electrolyzed water generator applying the conventional three-compartment cell is low mainly due to the applied anion exchange membrane, and a small amount of electrolyte mixes with the acid electrolyzed water inevitably produced. In addition, there is a problem that the anodic exchange membrane has deteriorated with an operating time interval of electrolysis by hypochlorous acid generated at the anode. Neither a method nor a device to solve all these problems has been suggested so far. RELATED TECHNICAL LITERATURE
    [031] Patent Literature
    [032] Patent Literature 1: Unexamined Japanese Patent Application Publication Hei07-214063
    [033] Patent Literature 2: Unexamined Japanese Patent Application Publication 2000-212787
    [034] Patent Literature 3: Unexamined Japanese Patent Application Publication 2009-072755
    [035] Patent Literature 4: Unexamined Japanese Patent Application Publication 2006-322053
    [036] Patent Literature 5: Unexamined Japanese Patent Application Publication 2012-110809 SUMMARY OF THE INVENTION Problem of Technique
    [037] The present invention aims to provide a method of generating electrolyzed water and a generator, which can overcome failures and problems of the electrolyzed water generation method and the generator by applying the two-compartment cell and the three conventional compartments, as mentioned above, can produce high quality electrolyzed water comprising both acidic electrolyzed water and alkaline electrolyzed water, free of highly corrosive alkali metal chloride such as salt, at a high current efficiency, can control the pH of acidic electrolyzed water and can operate stably for a long period of time with high durability. Solution to Problem
    [038] As a first solution to the problems mentioned above, the present invention provides a method of generating electrolyzed water, which comprises the steps of:
    [039] the anodic electrolyte comprising aqueous solution with dissolved alkali metal chloride is supplied and circulated from an anodic electrolyte storage tank that retains the anodic electrolyte to an anode chamber of a two-compartment cell separated by a membrane two-chamber cation exchangers of one anode chamber that accommodates one anode and one cathode chamber that accommodates one cathode,
    [040] alkali metal chloride-free raw water is supplied to the cathode chamber, and
    [041] electrolysis is performed, through which
    [042] the alkali metal chloride-free alkaline electrolyzed water in the cathode chamber is produced and simultaneously,
    [043] the chlorine containing gas is produced in the anode chamber,
    [044] after the gas is separated and collected from the anodic electrolyte, it comes into contact with the alkali metal chloride-free dissolving fluid to be dissolved, and
    [045] alkali metal chloride-free acidic electrolyzed water is produced.
    [046] As the second solution to the problems mentioned above, the present invention provides the method of generating electrolyzed water, in which, when the gas separated and collected from the anodic electrolyte comes into contact with the dissolution fluid to be dissolved , the electrolytically produced alkaline electrolyzed water is added to the dissolution fluid at a regulated flow rate to control the pH of the alkali metal chloride-free acidic electrolyzed water.
    [047] As a third solution to the problems mentioned above, the present invention provides the method of generating electrolyzed water, in which, after the chlorine containing gas evolved from the anodic electrolyte storage tank is collected and mixed with chlorine which contains gas evolved in the anode chamber, the mixed chlorine containing gas comes into contact with the dissolving fluid to be dissolved to produce the acidic electrolyzed water free of alkali metal chloride.
    [048] As the fourth solution to the problems mentioned above, the present invention provides the method of generating electrolyzed water, in which a two-compartment cell comprising a cathode which is a porous body and a cation exchange membrane adhered in a manner close to the porous cathode is applied and the cation exchange membrane is pushed to the porous cathode making the back pressure of the anode chamber greater than that of the cathode chamber.
    [049] As the fifth solution to the problems mentioned above, the present invention provides the method of generating electrolyzed water, in which electrolysis is performed by applying the anodic electrolyte in which the alkali metal chloride is dissolved at 10% in weight or more.
    [050] As the sixth solution to the problems mentioned above, the present invention provides the method of generating electrolyzed water, in which the contact and dissolution time of the electrolytically generated chlorine containing gas with the dissolution fluid is 0.05 seconds or more per 1 ml of gas.
    [051] As the seventh solution to the problems mentioned above, the present invention provides an electrolyzed water generator to simultaneously produce the alkali metal chloride-free acidic electrolyzed water and the alkali metal chloride-free alkaline electrolyzed water by the two cell compartments, which comprises:
    [052] a two-compartment cell divided into two chambers of an anode chamber that accommodates an anode and a cathode chamber that accommodates a cathode by a cation exchange membrane,
    [053] an anodic electrolyte storage tank for holding the anodic electrolyte comprising an aqueous solution in which the alkali metal chloride is dissolved,
    [054] a circulator that circulates the anodic electrolyte in the anodic electrolyte storage tank to the anode chamber,
    [055] an anodic electrolyte outlet tube to discharge the chlorine containing gas evolved in the anode chamber and the anodic electrolyte with dissolved gas thereof from the anode chamber,
    [056] a gas-liquid separator that separates chlorine containing gas from the anodic electrolyte and anodic electrolyte outlet tube with the dissolved gas,
    [057] a chlorine gas dissolver to produce the alkali metal chloride-free acidic electrolyzed water, causing the gas, after separated and collected from the anodic electrolyte in the gas-liquid separator, to contact the dissolution fluid free from alkali metal chloride,
    [058] a dissolution fluid inlet tube for supplying the dissolution fluid to the chlorine gas dissolver,
    [059] a raw water inlet pipe to supply the alkali metal chloride-free raw water to the cathode chamber, and
    [060] an alkaline electrolyzed water outlet pipe for discharging the alkaline electrolyzed water generated in the cathode chamber from the cathode chamber.
    [061] As the eighth solution to the problems mentioned above, the present invention provides an electrolyzed water generator, in which the pH of the alkali metal chloride-free acidic electrolyzed water is regulated by adding the electrolytically produced alkaline electrolyzed water to a Controlled flow rate to the chlorine gas dissolver, in which alkali metal chloride-free acidic electrolyzed water is produced with the separated gas and collected from the anodic electrolyte in the gas-liquid separator that is brought into contact with the fluid of dissolution to be dissolved.
    [062] As the ninth solution to the problems mentioned above, the present invention provides an electrolyzed water generator, in which alkali metal chloride-free acidic electrolyzed water is produced by collecting the chlorine that contains evolved gas in the storage tank of the anodic electrolyte, mixing it with the chlorine containing gas evolved in the anode chamber and bringing these into contact with the dissolution fluid to be dissolved.
    [063] As the tenth solution to the problems mentioned above, the present invention provides an electrolyzed water generator, in which a portion of raw water in the inlet tube to provide raw water free of alkali metal chloride to the cathode chamber is branched and connected to the inlet tube to supply dissolution fluid to the chlorine gas dissolver, and the branched raw water is used as the dissolution fluid.
    [064] As the eleventh solution to the problems mentioned above, the present invention provides an electrolyzed water generator, in which a two-compartment cell comprising a cathode which is a porous body and a closely adhered cation exchange membrane to the porous cathode is applied and the cation exchange membrane is pushed to the porous cathode making the back pressure of the anode chamber greater than that of the cathode chamber. Advantageous Effects of the Invention
    [065] According to the electrolyzed water generation method and the generator that the present invention suggests, the electrolysis is performed with the alkali metal chloride-free raw water that is supplied to the cathode chamber of the two-compartment cell divided by the cation exchange membrane. Then, alkaline electrolyzed water almost free of alkali metal chloride can be produced on the cathode side at a high current efficiency. Meanwhile, on the anode side, the anodic electrolyte comprising the aqueous solution with the dissolved alkali metal chloride is circulated from the anodic electrolyte storage tank which holds the anodic electrolyte, producing the chlorine containing high concentration gas a a high current efficiency. Chlorine containing high concentration gas is collected in the gas-liquid separator, separated from the anodic electrolyte which comprises an aqueous solution with dissolved alkali metal chloride and placed in contact with dissolving fluid which does not dissolve the alkali metal chloride, the be dissolved in the chlorine gas dissolver. In such a way, acidic electrolyzed water practically free of alkali metal chloride can be efficiently produced. Furthermore, the present invention can improve durability due to the fact that the two-compartment cell comprising the anode, cathode and cation exchange membrane only with a high durability is used, without the use of an anion exchange membrane with many problems, including durability.
    [066] In addition, the present invention can produce any arbitrarily desired force of strongly acidic electrolyzed water, weakly acidic electrolyzed water or slightly acidic electrolyzed water by regulating the pH value of the alkali metal chloride-free acidic electrolyzed water with addition of electrolytically produced alkaline electrolyzed water under flow rate control when the gas separated and collected from the anodic electrolyte comes in contact with the dissolution fluid to be dissolved.
    [067] In addition, when chlorine is released from the anodic electrolyte retained in the anodic electrolyte storage tank and gradually permeates the anodic electrolyte storage tank if electrolysis is continued, the present invention can prevent chlorine from leaking and can promote an effective utilization of chlorine gas by allowing the chlorine containing gas in the anodic electrolyte storage tank to join the chlorine containing gas that has been evolved at the anode and sending it to the chlorine gas dissolver.
    [068] In addition, in the electrolytic cell of the present invention, the applied cathode is the porous body and is disposed in close contact with the cation exchange membrane. The anode chamber is configured to have a higher back pressure than the cathode chamber so that the cation exchange membrane is pushed to the porous cathode, which can maintain a low cell voltage and considerably reduce energy consumption per effect. synergy with improved current efficiency compared to conventional three-compartment cell.
    [069] In addition, according to the present invention, the generation of chlorine by Equation (1) is effectively promoted by electrolysis, applying the anodic electrolyte with alkali metal chloride dissolved at 10% by weight or more. The chlorine generated first reacts with the anodic electrolyte, as shown in Equation (2), and accumulates as hypochlorous acid and hydrochloric acid. When the chlorine dissolved in the anodic electrolyte reaches saturation, the chlorine occurs as a gas.
    [070] In addition, according to the present invention, chlorine can be prevented from being released to the outside of the present generator by controlling the contact and dissolution time of the chlorine containing gas and the dissolution fluid by 0.05 seconds or more per 1 ml of gas.
    [071] Furthermore, according to the present invention, the portion of raw water in the raw water inlet pipe to supply the alkali metal chloride-free raw water to the cathode chamber can be branched and connected to the inlet pipe of dissolution fluid to supply the dissolution fluid to the chlorine gas dissolver. In this way, branched raw water can be used as a dissolution fluid, leading to an efficient utilization of the facilities. However, since the purpose of raw water is different from the dissolution fluid, as will be mentioned, the individual aqueous solution may be better used in some cases. BRIEF DESCRIPTION OF THE DRAWINGS
    [072] Fig.1 A flowchart showing an example of electrolyzed water generator of the present invention;
    [073] Fig.2 A flowchart showing an example of a conventional electrolyzed water generator. MODE DESCRIPTION
    [074] The embodiment of the present invention is described below with reference to the figures.
    [075] Fig. 1 shows an example of the electrolyzed water generator of the present invention comprising the two-compartment cell 1, the anode chamber 2, the cathode chamber 3, the cation exchange membrane 4, the anode 5, cathode 6, raw water inlet pipe 7, alkaline electrolyzed water storage tank 8, alkaline electrolyzed water outlet pipe 9, anodic electrolyte storage tank 10, circulator 11, gas separator -liquid 12, anodic gas tube 13, chlorine gas tube 14, dissolution fluid inlet tube 15, alkaline electrolyzed water pump 16, flow control valve 17, liquid gas dissolver. chlorine 18, the acid electrolyzed water outlet tube 19 and the anodic electrolyte outlet tube 20.
    [076] In the present invention, the anodic electrolyte comprising the aqueous solution in which the alkali metal chloride, as salt, is dissolved is supplied to the anode chamber 2 of the two-compartment cell 1 separated into two compartments: the anode 2 which accommodates anode 5 and the cathode chamber 3 which accommodates cathode 6 by the cation exchange membrane 4 from the anodic electrolyte storage tank 10 which stores the anodic electrolyte using the circulator 11, and electrolysis is performed while the alkali metal chloride-free raw water, such as salt, is being supplied from the raw water inlet pipe 7 to the cathode chamber 3. Through the electrolysis operation, the metal chloride-free alkaline electrolyzed water Alkaline is produced in the cathode chamber 3. The produced alkaline electrolyzed water is discharged from the alkaline electrolyzed water outlet tube 9 through the alkaline electrolyzed water storage tank 8.
    [077] Chlorine containing gas is generated in anode chamber 2 and is separated from the anodic electrolyte in gas-liquid separator 12 and then the collected gas is sent to chlorine gas dissolver 18 through the gas tube anodic 13. The alkali metal chloride-free dissolving fluid, as salt, is supplied to the chlorine gas dissolver 18 from the dissolving fluid inlet tube 15 and the alkali metal chloride-free acidic electrolyzed water, as salt, it is generated in chlorine gas dissolver 18. The generated acid electrolyzed water is discharged through the acid electrolyzed water outlet pipe 19.
    [078] On the other hand, the anodic electrolyte separated by the gas-liquid separator 12 is circulated to the anodic electrolyte storage tank 10.
    [079] The alkali metal chloride contained in the anodic electrolyte in the anodic electrolyte storage tank 10 is partially decomposed to evolve the chlorine gas. In order to eliminate the negative effect of gas leakage occurring from the chlorine gas and to use it effectively, the chlorine gas evolved in the anodic electrolyte storage tank 10 is sent to the chlorine gas dissolver 18 through the chlorine gas tube 14 to be used to produce the acidic electrolyzed water.
    [080] The raw water portion can be used as the dissolution fluid to be supplied to the chlorine gas dissolver 18 by means of a pipe (not shown) branched from the raw water inlet pipe 7.
    [081] The electrolytically produced alkaline electrolyzed water in the cathode chamber 3 can be added to the dissolving fluid in the chlorine gas dissolver 18 under the flow rate control through the flow control valve 17 through the water storage tank alkaline electrolysed water 8 by alkaline electrolyzed water pump 16. In this way, the pH value of the acidic electrolyzed water produced in chlorine gas dissolver 18 can be controlled to a desired value.
    [082] For the alkali metal chloride to be used for the anodic electrolyte, LiCl, NaCl and KCl are exemplified, among which NaCl and KCl can be preferentially applied. As raw water, well water and public mains water are available. Soft water prepared by removing the Ca ion and Mg ion contained in tap water and tap water, ion exchange water prepared by additionally removing another cation and another anion, and pure water prepared by removing are more appropriately available. up even organic components.
    [083] When electrolysis is conducted while anodic electrolyte containing one or more types of these alkali metal chlorides is being supplied to anode chamber 2, the chlorine generation reaction shown in Equation (1) and the generation reaction of oxygen in Equation (3) progress competitively at anode 5. The present invention allows the generation of chlorine in Equation (1) to progress effectively by controlling the concentration of alkali metal chloride in the aqueous solution supplied to the chamber. of anode by 2 to 10% by weight or more. Evolved chlorine first reacts with the anodic electrolyte, as shown in Equation (2), and accumulates as hypochlorous acid and hydrochloric acid, and when the dissolved amount of chlorine in the anodic electrolyte reaches saturation, the chlorine evolves as gas. In order to generate chlorine gas effectively, it is effective to allow the anodic electrolyte to circulate until the dissolved amount of chlorine reaches saturation or decreases the saturation concentration of the chlorine dissolution by lowering the pH value with HCl added to anodic electrolyte.
    [084] When electrolysis is conducted while the raw water exemplified above is being supplied to cathode chamber 3, the hydroxyl ion is generated from the electrolytic reaction of water shown in Equation (4) at cathode 6 and electrolyzed water alkaline in which the cation from anode chamber 2 penetrated through the cation exchange membrane 4 is the counterion produced and discharged from the alkaline electrolyzed water outlet tube 9 through the alkaline electrolyzed water storage tank 8. The pH of water alkaline electrolyte is 8 or more, although it varies with raw water flow rate or current density at the time of electrolysis. When hardness ingredients such as Ca ion and Mg ion are contained in raw water, scale develops on the surface of cathode 6, inside cathode chamber 3 and inside the alkaline electrolyzed water outlet tube 9. Such problems are easy to occur, in a long time of electrolysis, where the cathode reaction is inhibited or the alkaline electrolyzed water flow volume decreases. To suppress such malfunction, it is particularly preferable to use soft water, ion exchange water or pure water so that raw water is supplied to the cathode chamber 3.
    [085] Since raw water that has a low conductivity is supplied to the cathode chamber 3, the cell voltage at the time of electrolysis becomes considerably high if a cavity exists between the cation exchange membrane 4 and the cathode 6, resulting in a high power consumption problem. So, to deal with this situation, the cathode 6 is produced with porous materials such as mesh, perforated plate and foamed body and is arranged so that it is fixed closely to the cation exchange membrane 4, and the back pressure of the chamber. anode 2 is made larger than that of cathode chamber 3, so that the electrolyte voltage at the time of electrolysis is kept low by the configuration where the cation exchange membrane 4 is driven to porous cathode 6. To anode chamber 2 , the increase in cell voltage at the time of electrolysis is small even if a cavity exists between the cation exchange membrane 4 and the anode 5, since the anodic electrolyte of high conductivity is provided. Thus, it is not always necessary for the cation exchange membrane 4 to be attached closely to anode 5. It is exemplified as a method to keep the back pressure of anode chamber 2 greater than that of cathode chamber 3, where the height of the gas-liquid separator 12 located above the anode chamber 2 is kept greater than the height of the alkaline electrolyzed water storage tank 8 and the alkaline electrolyzed water outlet tube 9 located downstream of the cathode chamber 3.
    [086] The chlorine containing gas evolved in anode 5 is supplied to the gas-liquid separator 12 with the anodic electrolyte and the collected gas only moves to the anode gas tube 13 and the anodic electrolyte is returned to the storage tank of anodic electrolyte 10. As mentioned above, chlorine dissolves in the anodic electrolyte almost to the saturation concentration. When electrolysis is continued, chlorine can be released from the anodic electrolyte accumulated in the anodic electrolyte storage tank 10 and gradually the tank becomes filled with chlorine and finally a safety issue occurs as the chlorine leaks out. of the tank. Such a chlorine leakage problem can be avoided in such a way that the chlorine containing gas in the anodic electrolyte storage tank 10 is led to the chlorine gas tube 14 and joined to the chlorine containing gas evolved in anode 5 and transferred to the anode gas tube 13.
    [087] The chlorine in the gas comes in contact with the dissolution fluid in the chlorine gas dissolver 18 and dissolves to become acidic electrolyzed water through the reaction shown in Equation (2). Whereas, when the entire amount of chlorine supplied to the chlorine gas dissolver 18 does not come into contact with the dissolving fluid and is not dissolved, the undissolved chlorine is released out of the system, causing a safety problem. To prevent this problem from occurring, it is necessary to provide the dissolution fluid in an amount sufficient to dissolve the chlorine supplied to the chlorine gas dissolver 18. In addition, it is preferred that the chlorine gas dissolver 18 has a means to promote contact and dissolving chlorine as a sprinkler, a gas diffuser, an external stirrer, a static stirrer and a scrubber. Furthermore, the release of chlorine out of the system can be prevented by controlling the contact time for the dissolution of chlorine containing gas evolved from electrolysis with the dissolution fluid for 0.05 seconds or more per 1 ml of gas.
    [088] In the present generator, the dissolution fluid to be used to produce the acidic electrolyzed water may or may not be equal to the raw water to be used to manufacture the alkaline electrolyzed water. In the water and chlorine reaction shown in Equation (2), hydrochloric acid is underproduced in addition to hypochlorous acid, and so the acidic electrolyzed water by the present generator tends to become acidic. As mentioned above, as the raw water supplied to the cathode chamber 23, the use of soft water, ion-exchanged water or pure water is preferred to control Ca ion and Mg ion fouling. While, for the dissolution fluid to be used to make the hypochlorous acid water, waters that contain Ca ion and Mg ion, such as well water or tap water, can be used without problems.
    [089] In the present generator, the concentration of hypochlorous acid in acidic electrolyzed water can be regulated by the supply volume of dissolution fluid and that of chlorine containing gas evolved from anode 5. However, the pH value decreases with the concentration of hypochlorous acid, since hydrochloric acid is underproduced, as shown in Equation (2). As mentioned above, the hypochlorous acid water in acidic electrolyzed water has a great oxidizing power, and is used for sterilization use of Escherichia coli and bacteria. Sterilizing power, however, varies with pH value and a pH of around 6 is known to be strong. When at low pH, hypochlorous acid becomes balanced with chlorine, creating a risk that chlorine gas will be released from the hypochlorous acid water into the acidic electrolyzed water. Thus, in the present generator, the produced alkaline electrolyzed water is held once in the alkaline electrolyzed water storage tank 8, as shown in Fig. 1 , and the pH value of the generated acidic electrolyzed water can be regulated by mixing a adequate amount of alkaline electrolyzed water with the dissolution fluid using the alkaline electrolyzed water pump 16 and the flow control valve 17. EXAMPLE
    [090] The following are explained examples of the production of hypochlorous acid water and alkaline electrolyzed water with the use of the electrolyzed water generator by the present invention, however, the present invention is not limited to these modalities. Example 1
    [091] In the electrolytic system, as shown in Fig. 1, the two-compartment cell 1 comprises the electrodes (JL-510 manufactured by Permelec Electrode Ltd.) of anode 5 and cathode 6 prepared in such a way that the platinum catalyst was coated onto the network-shaped titanium substrate by the thermal decomposition method with 60 cm2 of projected area and the cation exchange membrane 4 (Nafion (trademark) N-115 manufactured by Du Pont) which separates the anode chamber 2 and the cathode chamber 3. The cation exchange membrane 4 was arranged so that the respective electrode came into contact with the membrane on each side. The gas-liquid separator 12 was placed 5 cm above the anode chamber 2 and was adjusted so that a back pressure of 50 mmH2O was applied to the anode chamber 2, and the alkaline electrolyzed water outlet tube 9 was also placed 5 cm above cathode chamber 3 and was set so that back pressure of 50 mmH2O was applied to cathode chamber 3.
    [092] In Example 1, the chlorine gas tube 14 above the anode electrolyte storage tank 10 in Fig. 1 was not installed and the anode gas tube 13 was directly connected to the chlorine gas dissolver 18. chlorine gas dissolver 18, the dissolution fluid from the dissolution fluid inlet tube 15 and the alkaline electrolyzed water from the alkaline electrolyzed water storage tank 8 were mixed and sprayed from the top of the chlorine gas 18.
    [093] The anodic electrolyte which was an aqueous solution of sodium chloride of about 8% by weight was circulated between the anodic electrolyte storage tank 10 and the anode chamber 2 by the circulator 11. While the soft water was being supplied as raw water for cathode chamber 3 at a flow rate of 1 l/min, electrolysis was carried out using electrical current applied at 6A for anode 5 and cathode 6. For chlorine gas dissolver 18 , tap water was supplied at the flow rate of 1 l/min as the dissolution fluid, which was brought into contact with the chlorine containing gas supplied through the anode gas tube 13 for dissolution so as to compose the water acid electrolysed. The capacity of the chlorine gas dissolver 18 is designed so that the contact and dissolution time of the dissolving fluid and chlorine containing gas is controlled within one second.
    [094] After one hour from the start of electrolysis, the cell voltage measurement was 28 V, the available chlorine concentration in the hypochlorous acid water sampled from the acidic electrolyzed water outlet tube 19 was 108 mg /l as chlorine, and the pH was 2.7 and the increase in density of sodium chloride was 4 mg/l. The pH value of the alkaline electrolyzed water sampled from the alkaline electrolyzed water outlet tube 9 was 11.6, and the increase in density of sodium chloride was 1 mg/l. Around the outlet of the acidic electrolyzed water outlet tube 19 and the anodic electrolyte storage tank 10, the chlorine odor was felt slightly, but not to a problematic level. The amount of chlorine generation that was calculated from the amount of electricity applied was about 40 Nml/min and the contact and dissolution time of the dissolution fluid with the chlorine containing gas in the chlorine gas dissolver 18 was estimated as being 0.025 seconds per 1 ml of gas. Example 2
    [095] Under the same conditions as in Example 1, electrolysis was carried out using the electrolytic system mentioned in Example 1, adding an arbitrary amount of alkaline electrolyzed water formed by electrolysis to the dissolution fluid supplied to the chlorine gas dissolver 18. After one hour from the start of electrolysis, the cell voltage measurement was 28 V and, when the amount of alkaline electrolyzed water added to the dissolution fluid was changed, the amount of acidic electrolyzed water generated, the concentration of available chlorine and the pH value, the amount of generated alkaline electrolyzed water and the pH value were as shown in Table 1. Adjustment of the pH value was possible by controlling the addition of alkaline electrolyzed water to the dissolution fluid.
    Example 3
    [096] With the same electrolytic system described in Example 1, the electrolysis operation was performed by the same method as in Example 1, using the same electrolyzed water generator as in Example 1, except that the chlorine gas 14 was connected to the top of anodic electrolyte storage tank 10 and connected to chlorine gas dissolver 18 after chlorine gas tube 14 and anode gas tube 13 were joined in Example 3.
    [097] After one hour from the start of electrolysis, the cell voltage measurement was 28 V, the available chlorine concentration in the acid electrolyzed water sampled from the acid electrolyzed water outlet tube 19 was 108 mg/ l as chlorine, and the pH was 2.7 and the increase in density of sodium chloride was 4 mg/l. the pH value of the alkaline electrolyzed water sampled from the alkaline electrolyzed water outlet tube 9 was 11.6, and the increase in density of sodium chloride was 1 mg/l. chlorine odor was felt slightly around the outlet of the acid electrolyzed water outlet tube 19, however, no chlorine odor was felt around the anodic electrolyte storage tank 10. Example 4
    [098] Electrolysis was started using the same electrolytic system and the same method as in Example 3, except that the alkaline electrolyzed water outlet tube 9 is disposed 5 cm above the cathode chamber 3 as in Example 1 , and the back pressure in the cathode chamber 3 was being set at 50 mmH2O, the gas-liquid separator 12 was disposed 30 cm above the anode chamber 2 and the back pressure in the anode chamber 2 was being set at 300 mmH2O in Example 4 Then, in Example 4, the cation exchange membrane was pushed into the porous cathode by increasing the back pressure of the anode chamber to be greater than that of the cathode chamber.
    [099] After one hour from the start of electrolysis, the cell voltage measurement was 2.8 V, the available chlorine concentration in the acid electrolyzed water sampled from the acid electrolyzed water outlet tube 19 was 108 mg/l as chlorine, and the pH was 2.7 and the increase in density of sodium chloride was 4 mg/l. the pH value of the alkaline electrolyzed water sampled from the alkaline electrolyzed water outlet tube 9 was 11.6, and the increase in density of sodium chloride was 1 mg/l. Example 5
    [0100] The electrolysis operation was carried out by the same electrolytic system and by the same method as that described in Example 4, except that the anodic electrolyte was a 30% by weight aqueous solution of sodium chloride in Example 5.
    [0101] After one hour from the start of electrolysis, the cell voltage measurement was 2.6 V, the available chlorine concentration in the acid electrolyzed water sampled from the acid electrolyzed water outlet tube 19 was 113 mg/l as chlorine, the pH was 2.8 and the increase in density of sodium chloride was 4 mg/l. The pH value of the alkaline electrolyzed water sampled from the alkaline electrolyzed water outlet tube 9 was 11.7, and the increase in density of sodium chloride was 1 mg/l. Example 6
    [0102] The electrolysis operation was performed by the same electrolytic system and the same method as that described in Example 5, except that the contact and dissolution time of the dissolution fluid with the chlorine containing gas in the gas dissolver chlorine 18 was two seconds in Example 6.
    [0103] After one hour from the start of electrolysis, the cell voltage measurement was 2.6 V, the available chlorine concentration in the acid electrolyzed water sampled from the acid electrolyzed water outlet tube 19 was 120 mg/l as chlorine, the pH was 2.7 and the increase in density of sodium chloride was 4 mg/l. The pH value of the alkaline electrolyzed water sampled from the alkaline electrolyzed water outlet tube 9 was 11.7, and the increase in density of sodium chloride was 1 mg/l. No chlorine odor was felt around the anodic electrolyte storage tank 10 and the acid electrolyzed water outlet tube outlet 19.
    [0104] The contact and dissolution time of the dissolution fluid with chlorine containing gas was estimated to be 0.05 seconds per 1 ml of gas. Comparative Example 1
    [0105] Fig. 2 is a conventional type of electrolyzed water generator with the use of a three-compartment cell, which comprises the three-compartment cell 21, the anode chamber 22, the cathode chamber 23, the chamber intermediate 24, anion exchange membrane 25, cation exchange membrane 26, anode 27, cathode 28, intermediate chamber electrolyte storage tank 29 and circulator 30. In the electrolyzed water generator shown in Fig. 2 , the three-compartment cell 21 is separated by anion exchange membrane 25 (Neosepta (trademark) AHA manufactured by Tokuyama Corporation) in anode chamber 22 and intermediate chamber 24 and further separated by cation exchange membrane 26 (Nafion (trademark) registered) N-115 manufactured by Du Pont) in the cathode chamber 23 and the intermediate chamber 24. The electrodes (JL-510 manufactured by Permelec Electrode) of anode 27 and cathode 28, each produced from substrate titanium in format the mesh with a projected area of 60 cm2 coated with platinum catalyst by the thermal decomposition method, were placed in the anode chamber 22 and in the cathode chamber 23, respectively.
    [0106] The intermediate chamber solution which was about 30% by weight aqueous sodium chloride solution was circulated through the circulator 30 between the intermediate chamber electrolyte storage tank 29 and the intermediate chamber 24. The soft water, as raw water, it was supplied to the cathode chamber 23 at a flow rate of 1 l/min and tap water, as raw water, was supplied to the anode chamber 22, and the electrolysis was performed by applied electric current to 6A to anode 27 and cathode 28.
    [0107] One hour after the start of electrolysis, the cell voltage measurement was 6.2 V, the available chlorine concentration in the acidic electrolyzed water produced at anode 27 was 71 mg/l as chlorine, and the pH was 2.6 and the increase in density of sodium chloride was 47 mg/l. the pH value of the alkaline electrolyzed water produced at cathode 28 was 11.7, and the increase in density of sodium chloride was 1 mg/l. INDUSTRIAL APPLICABILITY
    [0108] The electrolyzed water generation method and the generator, according to the present invention, can minimize the mixing of raw material salt ingredients in the generated acid electrolyzed water and alkaline electrolyzed water and thus can be applied widely in industry associated with high corrosivity and in agricultural fields. LIST OF NUMERICAL REFERENCES
    [0109] 1 Two-compartment cell
    [0110] 2 Anode Chamber
    [0111] 3 Cathode Chamber
    [0112] 4 Cation Exchange Membrane
    [0113] 5 Anode
    [0114] 6 Cathode
    [0115] 7 Raw water inlet pipe
    [0116] 8 Alkaline electrolyzed water storage tank
    [0117] 9 Alkaline electrolyzed water outlet tube
    [0118] 10 Anodic electrolyte storage tank
    [0119] 11 Circulator
    [0120] 12 Gas-liquid separator
    [0121] 13 Anodic gas tube
    [0122] 14 Chlorine gas tube
    [0123] 15 Dissolving fluid inlet tube
    [0124] 16 Alkaline Electrolyzed Water Pump
    [0125] 17 Flow control valve
    [0126] 18 Chlorine gas dissolver
    [0127] 19 Acid electrolyzed water outlet tube
    [0128] 20 Anodic electrolyte outlet tube
    [0129] 21 Three-compartment cell
    [0130] 22 Anode chamber
    [0131] 23 Cathode Chamber
    [0132] 24 Intermediate Chamber
    [0133] 25 Anion exchange membrane
    [0134] 26 Cation Exchange Membrane
    [0135] 27 Anode
    [0136] 28 Cathode
    [0137] 29 Intermediate chamber electrolyte storage tank
    [0138] 30 Circulator
    权利要求:
    Claims (9)
    [0001]
    1. METHOD OF ELECTROLYSED WATER GENERATION, characterized in that it comprises the steps of: the anodic electrolyte comprising an aqueous solution with dissolved alkali metal chloride is supplied and circulated from an anodic electrolyte storage tank (10) that retains the anodic electrolyte in an anode chamber (2) of a two-compartment cell (1) separated by a cation exchange membrane (4) in two chambers of an anode chamber (2) that accommodates an anode (5) and a chamber of cathode (3) which accommodates a cathode (6), wherein said cathode (6) is produced with porous materials and is arranged so that it is attached closely to the cation exchange membrane (4), and wherein the back pressure of said anode chamber (2) is greater than that of the cathode chamber (3), alkali metal chloride free raw water is supplied to the cathode chamber (3), wherein said free raw water of alkali metal chloride consists of electrolyzed water prepared by removal. ion of Ca ions and Mg ions contained in well water or mains water or ion exchange water prepared by additionally removing another cation and another anion, and pure water prepared by removing even organic components, the electrolysis be carried out, through of which: the alkali metal chloride-free electrolyzed alkaline water in the cathode chamber (3) is produced and simultaneously, the chlorine containing gas is produced in the anode chamber (2), after the gas has been separated and collected from of the anodic electrolyte, said gas is allowed to come into contact with the alkali metal chloride-free dissolving fluid to be dissolved, and alkali metal chloride-free acidic electrolyzed water to be produced.
    [0002]
    2. METHOD according to claim 1, characterized in that when the gas separated and collected from the anodic electrolyte comes into contact with the dissolution fluid to be dissolved, the electrolytically produced alkaline electrolyzed water is added to the dissolution fluid to a regulated flow rate to control the pH of acidic electrolyzed water free from alkali metal chloride.
    [0003]
    3. METHOD according to any one of claims 1 or 2, characterized in that, after the chlorine containing evolved gas from the anodic electrolyte storage tank has been collected and mixed with the chlorine containing evolved gas in the anode chamber , the chlorine containing mixed gas is brought into contact with the dissolution fluid to be dissolved to produce the alkali metal chloride-free acidic electrolyzed water.
    [0004]
    4. METHOD, according to any one of claims 1 to 3, characterized in that the electrolysis is performed by applying the anodic electrolyte, in which the alkali metal chloride is dissolved at 10% by weight or more.
    [0005]
    5. METHOD, according to any one of claims 1 to 4, characterized in that the contact and dissolution time of the electrolytically generated chlorine containing gas with the dissolution fluid is 0.05 seconds or more per 1 ml of gas.
    [0006]
    6. ELECTROLYZED WATER GENERATOR FOR SIMULTANEOUSLY PRODUCING ACID ELECTROLYZED WATER ALKALINE METAL CHLORIDE AND ALKALINE METAL CHLORIDE FREE ALKALINE ELECTROLYZED WATER THROUGH A TWO-COMPARTMENT CELL (1-compartment one (1) cell: ) divided into two compartments of an anode chamber (2) that accommodates an anode (5) and a cathode chamber (3) that accommodates a cathode (6) through a cation exchange membrane (4), wherein said cathode (6) is made of a porous material and is arranged in close contact with the cation exchange membrane (4), and wherein, in operation, the back pressure of said anode chamber (2) is greater than that of said cathode chamber (3), an anodic electrolyte storage tank (10) for holding the anodic electrolyte comprising an aqueous solution in which the alkali metal chloride is dissolved, a circulator (11) which circulates the anodic electrolyte in the storage (10) of electrolyte anode to the anode chamber (2), an outlet tube (20) of the anode electrolyte to discharge the chlorine containing evolved gas in the anode chamber (2) and the anodic electrolyte with dissolved gas thereof from the anode chamber (2), a gas-liquid separator (12) which separates the chlorine containing gas from the outlet tube (20) of the anodic electrolyte and the anodic electrolyte with the dissolved gas, a chlorine gas dissolver (18) to produce the alkali metal chloride-free acidic electrolyzed water causing the gas, after separated and collected from the anodic electrolyte in the gas-liquid separator (12), to contact the alkali metal chloride-free dissolving fluid, a dissolution fluid inlet tube (15) for supplying dissolution fluid to the chlorine gas dissolver, a raw water inlet tube (7) for supplying alkali metal chloride free raw water to the cathode chamber ( 3), and an outlet tube (9) of alkaline electrolyzed water for to discharge the alkaline electrolyzed water generated in the cathode chamber from the cathode chamber (3), where the height of the gas-liquid separator (12) located above the anode chamber (2) is kept greater than the height the alkaline electrolyzed water storage tank (8) and the alkaline electrolyzed water outlet tube (9) located downstream of the cathode chamber (3).
    [0007]
    7. GENERATOR according to claim 6, characterized in that the pH of the alkali metal chloride-free acidic electrolyzed water is regulated by adding electrolytically produced alkaline electrolyzed water at a controlled flow rate to the chlorine gas dissolver, where the water Alkali metal chloride-free acidic electrolysate is produced with the gas separated and collected from the anodic electrolyte in the gas-liquid separator, whereby said gas is allowed to come into contact with the dissolution fluid to be dissolved.
    [0008]
    8. GENERATOR according to any one of claims 6 or 7, characterized in that the alkali metal chloride-free acidic electrolyzed water is produced by collecting the chlorine that contains evolved gas in the anodic electrolyte storage tank, mixing it with the chlorine containing gas evolved in the anode chamber and placing the mixed gases in contact with the dissolution fluid to be dissolved.
    [0009]
    A GENERATOR according to any one of claims 6 to 8, characterized by the portion of raw water in the inlet tube to supply raw water free of alkali metal chloride to the cathode chamber to be branched and connected to the inlet tube to supply the dissolution fluid for the chlorine gas dissolver, and branched raw water is used as the dissolution fluid.
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    同族专利:
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    AU2014209803A1|2015-07-09|
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    JP5688103B2|2015-03-25|
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    AR094542A1|2015-08-12|
    BR112015017511A2|2020-02-04|
    TR201802932T4|2018-03-21|
    WO2014114806A1|2014-07-31|
    EP2948413B1|2017-12-27|
    KR20150110782A|2015-10-02|
    IL238923A|2018-11-29|
    ZA201504556B|2016-11-30|
    TW201430174A|2014-08-01|
    MX2015009411A|2015-09-24|
    KR102218817B1|2021-02-25|
    CA2892547A1|2014-07-31|
    JP2014145102A|2014-08-14|
    EA201591400A1|2015-12-30|
    EA030556B1|2018-08-31|
    CA2892547C|2021-02-16|
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    法律状态:
    2018-02-27| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2019-10-22| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|
    2019-11-12| B06I| Publication of requirement cancelled [chapter 6.9 patent gazette]|Free format text: ANULADA A PUBLICACAO CODIGO 6.21 NA RPI NO 2546 DE 22/10/2019 POR TER SIDO INDEVIDA.O PRESENTE PEDIDO TEVE UM PARECER DE EXIGENCIA PRELIMINAR (6.21) NOTIFICADO NA RPI NO 2546 DE 22/10/2019, TENDO SIDO CONSTATADO QUE ESTE FOI INADEQUADO/INDEVIDO, VISTO QUE A NOTIFICACAO DE ENTRADA NA FASE NACIONAL (1.3) FOI ANULADA POR DESPACHO 1.3.4, PUBLICADO NA RPI 2547, DE 29/102019. |
    2020-03-24| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|
    2021-06-15| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|
    2021-07-06| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 28/01/2014, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    JP2013013760A|JP5688103B2|2013-01-28|2013-01-28|Electrolyzed water production method and apparatus|
    JP2013-013760|2013-01-28|
    PCT/EP2014/051567|WO2014114806A1|2013-01-28|2014-01-28|An electrolyzed water generating method and a generator|
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