WO2019143039A1 - Système de stérilisation électrolytique - Google Patents

Système de stérilisation électrolytique Download PDF

Info

Publication number
WO2019143039A1
WO2019143039A1 PCT/KR2018/016574 KR2018016574W WO2019143039A1 WO 2019143039 A1 WO2019143039 A1 WO 2019143039A1 KR 2018016574 W KR2018016574 W KR 2018016574W WO 2019143039 A1 WO2019143039 A1 WO 2019143039A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
water
spring
disposed
present
Prior art date
Application number
PCT/KR2018/016574
Other languages
English (en)
Korean (ko)
Inventor
박종하
조정호
Original Assignee
주식회사 케스트
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 주식회사 케스트 filed Critical 주식회사 케스트
Publication of WO2019143039A1 publication Critical patent/WO2019143039A1/fr

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction

Definitions

  • the present invention relates to an electrolytic sterilization system comprising an electrolytic module with an integral automatic and manual safety valve for releasing CO2 gas pressure in the chamber and having stability.
  • Liquid supply pipes which are widely used in industrial facilities such as ship pipelines, piping of sewage sludge treatment facilities, internal piping of construction plant facilities, beverage supply facilities for beer and other food and beverage equipment, and the like, Foreign substances such as scale and bacteria and the like are deposited on the inner wall surface.
  • Corrosion is the reaction of a metal chemically or electrochemically by contact with surrounding liquids or gases. Another definition of corrosion can be described as follows.
  • Oxygen acts on a substance to change it (oxidation)
  • corrosion can be defined as a phenomenon in which material deteriorates due to the environment.
  • a slime called so-called watering is deposited on the inner surface of the conduit.
  • the slime deposited on the inner surface of the conduit not only deteriorates the flavor of the drinking liquid but also becomes a growth site of bacteria and the like, causing the liquid to be contaminated.
  • a slime is formed in the form of a scale deposited by corrosion in a conduit, and a scale is formed in another form of slime in a conduit for food and beverage extraction.
  • the slime removal method according to the prior art has a problem that not only the removal efficiency of the slime is low, but also when the slime removal agent is used, it is harmful to the human body due to the chemical composition of the agent and can cause environmental pollution.
  • It is an object of the present invention to provide an electrolytic sterilization system comprising an electrolytic module with an integral automatic and manual safety valve for releasing CO2 gas pressure in the chamber and having stability.
  • a water electrolytic sterilization system including: a storage unit for storing water; (+) Electrode and (-) electrode disposed adjacent to each other without a diaphragm for exchanging ions of an electrolyte, and electrolysis of the water based on the (+) electrode and (- Decomposition section; A cavitation generating unit into which sterilizing water is introduced; A tube pipe through which the inflowing sterilization water is transferred; A gas exchange unit into which a gas is introduced and in which the introduced gas and the transferred sterilization water are mixed to generate a gas mixture liquid; And an integral type safety valve for discharging at least a part of the gas to the outside in order to lower a pressure inside the storage part by the gas, wherein the integral type safety valve comprises: ; And a second structure that is connected to an end of the first structure and exposes a button for receiving the force of the user to the outside, the lower structure being disposed at the lower end of the region in which the first structure is inserted, wherein a
  • the gas can not be discharged to the outside by a plurality of blocking structures disposed between the lower end of the inserted region and the lower end of the inserted region.
  • a blocking structure disposed between the first structure and the lower end of the inserted region of the plurality of blocking structures can not block the gas, so that at least a part of the gas is discharged to the outside .
  • the first spring when the pressure inside the storage portion by the gas becomes equal to or greater than a predetermined value, the first spring is contracted and the state of the two springs is maintained.
  • the contraction of the first spring As the lower structure rises together, the rising of the first structure and the lower structure prevents the plurality of barrier structures from blocking the gas, so that at least a part of the gas can be discharged to the outside.
  • the electrolysis unit may further include a cap-type cover for protecting the positive and negative electrodes.
  • the present invention can provide a user with a chamber-type electrolytic sterilization module which is a core component of a sterilization water producing system for draft beer supply piping sterilization and cleaning using the developed electrode, securing the manufacturing technology of durability enhanced DSE of more than 300% .
  • the present invention can provide a disinfection membrane electrolysis HOCL (1.0 ppm or higher) sterilization function using a DSE electrode.
  • the present invention can provide a water / CO2 gas mixing function using a shock wave tube to perform a fluid wave shock wave cleaning function.
  • the present invention provides an automatic & manual pressure relief function when a pressure of 5 bar or more is applied in a chamber, provides a departure-preventing function when a KEG coupler is connected to an upper chamber CAP, 4 bar) (pressure standard for German DIN national standard beer containers).
  • the present invention can provide a user with a water electrolytic sterilization system including an integral electrolytic module having an integral automatic and manual safety valve for releasing CO2 gas in the chamber.
  • Figs. 1A and 1B are diagrams for explaining production of acidic ionized water and alkaline ionized water through hydrolysis, in the context of the present invention.
  • FIG. 2A is a view for explaining how acidic ionized water and alkaline ionized water are produced using a whisker membrane electrolytic cell
  • FIG. 2B is a view for explaining that electrolytic efficiency is increased by increasing the number of electrodes.
  • FIG. 3 is a diagram for explaining the production of strong alkali and strongly acidic water by adding NaCl in a whisking membrane electrolytic bath in connection with the present invention.
  • FIG. 4 is a diagram for explaining the production of sterilized water by adding NaCl or HCl in a septum-free electrolytic cell in connection with the present invention.
  • FIG. 5 shows a specific example of a cleaning apparatus using the built-in gas mixture liquid proposed by the present invention.
  • FIG. 6 shows an example of a chamber-type electrolytic sterilizing cleaning vessel to which the DSE electrode proposed by the present invention is applied.
  • Fig. 7 shows experimental results relating to the pressure in relation to the cleaning vessel shown in Fig. 6.
  • Figure 8 shows an example of a KEG Coupler & Impact Wound Tube Fitting chamber type disinfection wash pot top CAP in the context of the present invention.
  • Figure 9 shows another example of a KEG Coupler & Impact Wound Tube Fitting chamber type disinfection wash vessel top CAP, in the context of the present invention.
  • FIG. 10 shows an example of a chamber type sterilization cleaning vessel lower electrolytic sterilization (HOCL hypochlorous acid generation) module, in connection with the present invention.
  • HOCL hypochlorous acid generation electrolytic sterilization
  • Fig. 11 shows an example of a chamber type sterilizing cleaning vessel upper CAP binding type shock wave tube in the context of the present invention.
  • FIG. 12 is a diagram for explaining the principle of impact wave tube washing in the context of the present invention.
  • Fig. 13 shows an example of an improved electrolytic sterilization system proposed by the present invention.
  • FIG. 14 illustrates an example of an integral automatic and manual safety valve for releasing CO 2 gas pressure in a chamber associated with the present invention.
  • Fig. 15 shows a detailed view of the upper lid structure shown in Fig.
  • Fig. 16 shows an example of the internal bonding structure of the improved electrolytic sterilization system proposed by the present invention.
  • FIG 17 shows an example of a water electrolytic sterilization system including the electrolysis module having the stability of the present invention.
  • FIG 18 shows, in the context of the present invention, the standby state of an integral safety valve for release of CO 2 gas pressure in the chamber.
  • Fig. 19 shows the forced pressure release state of the integral safety valve for releasing the CO 2 gas pressure in the chamber, in the context of the present invention.
  • Fig. 20 shows an automatic pressure release state of the integral safety valve for releasing the CO 2 gas pressure in the chamber, in the context of the present invention.
  • a watering module structure of a cleaning device using a liquid mixed with sterilized water and gas generated by electrolysis of water is provided to a user.
  • an ionizer is called an ionized water generator or a reduced water, and an ionizer has a water purifier and an electrolytic cell, and acidic ionized water and alkaline ionized water are produced by electrolysis.
  • the alkaline ionized water thus generated is mainly used for beverage, and the acidic ionized water is used for skin cosmetic or disinfecting water and washing water.
  • the acidic water produced in a general ionizer is low in sterilizing power and the acidic water generated in a general alkaline ionizer is electrolyzed in a general water, Lt; / RTI >
  • the strong acidic ionized water is produced in the general alkaline ionized water, but when the diluted salt solution (0.2% or less) is supplied through the metering pump and subjected to the electrolysis process, strongly acidic hypochlorous acid water having strong sterilizing power is generated.
  • FIG. 1A is a diagram for explaining the production of acidic ionized water and alkaline ionized water through hydrolysis, in the context of the present invention.
  • FIG. 1A is a diagram for explaining the production of acidic ionized water and alkaline ionized water through hydrolysis, in the context of the present invention.
  • a positive electrode and a negative electrode are present on the basis of a diaphragm, and an anion in an electrolyte moves to a (+) pole and a cation moves to a (-) pole.
  • FIG. 1B there is shown a process in which tap water is used as an electrolyte to move the elements classified as anions to the (+) pole and the elements classified as positive to the (-) pole.
  • acidic ionized water can be generated and output at the (+) electrode, and alkaline ionized water can be generated at the (-) electrode and output.
  • Electrolysis without diaphragm is called no-septation electrolysis.
  • the non-diaphragm electrolysis means electrolysis that does not use a diaphragm between the (+) electrode and the (-) electrode, and since the electrolysis is performed with a small force, the electric resistance is small, .
  • the channeling membrane uses a diaphragm to pass only ions between the (+) electrode and the (-) electrode and to prevent water from passing through the membrane.
  • the capillary membrane depolarization achieves maximum efficiency per unit time compared to the non-septic electrolysis, and the reason for the diaphragm is to map the pH to the desired value.
  • the impulsive membrane has no water flow on both electrodes, so it requires a lot of electric power, which means that heat is generated and the electric resistance is large.
  • FIG. 2A is a view for explaining how acidic ionized water and alkaline ionized water are produced using a whisker membrane electrolytic cell
  • FIG. 2B is a view for explaining that electrolytic efficiency is increased by increasing the number of electrodes.
  • FIG. 2A shows a whitening membrane electrolytic cell of the most commonly used type.
  • the degree of saturation of the dissolved hydrogen in the alkaline water side can be increased according to the selection of the ion diaphragm, and the water having the increased dissolved amount of the hydrogen molecule compared to the conventional ionizer can be referred to as hydrogen water.
  • FIG. 2B there is shown an example in which the number of electrodes is increased to increase the amount of water or to obtain more strong physical properties.
  • the strength of the acidic ionized water and the alkaline ionized water can be adjusted.
  • FIG. 3 is a diagram for explaining the production of strong alkali and strongly acidic water by adding NaCl in a whisking membrane electrolytic bath in connection with the present invention.
  • NaCl is added to the galvanic cell to produce strong alkaline and strongly acidic water, and two physical properties are suitably mixed according to the application.
  • sterilized water such as hypochlorous acid water can be produced in addition to the above-mentioned acidic ionized water and alkaline ionized water.
  • FIG. 4 is a diagram for explaining the production of sterilized water by adding NaCl or HCl in a septum-free electrolytic cell in connection with the present invention.
  • FIG. 4 there is shown a specific example of a method of generating hypochlorous acid water by adding NaCl or HCl to the seawater electrolytic cell and using it as sterilized water.
  • acidic water, alkaline water, and sterilized water can be prepared through the diaphragm or diaphragm, and acidic water, alkaline water, and pH of sterilized water can be adjusted depending on the number of electrodes and the presence or absence of additives.
  • alkaline ionized water is small in water particles and absorbs quickly in the body, and has an antioxidant function for removing active oxygen.
  • It can be used when cooking rice, coffee, tea, green tea, boiling tea, drinking water, hanging out, washing vegetables and fruits, cooking, drinking or making cocktails.
  • acidic ionized water has sterilization and bleaching action. You can use it when you bathe, wash your face, and when you wash a chopping board, tableware, cloth, etc., and it is wounded by insect bites or skin.
  • Table 5 is data on the sterilizing force data which can be obtained through the acidic ionized water as the oxidation potential number.
  • the characteristics of the sterilized water produced by the non-septic electrolysis may be neutral or alkaline with a pH of 7 to 8.5, and an ORP of +100 to -300 mV.
  • sterilized water is harmless and non-toxic to the human body and is reduced to ordinary water when exposed to sunlight or air for a long period of time.
  • NaOCl sodium chloride
  • the electrolytic water produced by electrolysis differs in function according to the electrolysis method, and sterilizing, cleaning, promoting the growth of plants and plants, promoting the health of the human body according to the presence or absence of the added oil, And so on.
  • Harmless and non-toxic electrolytic water is used as a substitute for chemicals such as disinfectant, detergent, detergent, detergent, wax, pesticide, etc. It can be used in various industrial fields to reduce pollutants and prevent water pollution and air pollution. It is possible to alleviate the health environmental hazards.
  • an object of the present invention is to provide a user with an outrigger module structure of a cleaning apparatus using a liquid in which a sterilized water and a gas are mixed by electrolysis of water.
  • the present invention relates to a method for producing sterilized water by using a plurality of electrodes of a diaphragm, using the generated sterilized water to effectively remove slime such as scale and bacteria deposited in various conduits,
  • the present invention relates to an apparatus and a method for controlling the sterilization and cleaning of a draft beer extraction device and a draft beer extraction device, I would like to propose.
  • the cleaning device using the gaseous mixture sterilizing water liquid proposed by the present invention can be divided into a built-in type and an external type.
  • FIG. 5 shows a specific example of a cleaning apparatus using the built-in gas mixture liquid proposed by the present invention.
  • the cleaning apparatus shown in Fig. 5 can be used for sterilizing and cleaning the draft beer extraction apparatus and draft beer extraction apparatus.
  • the object of the present invention is not limited thereto.
  • the cleaning apparatus using the gas mixture liquid proposed by the present invention includes an outflow module structure 10 for discharging sterilized water out of the sterilized water reservoir 600, an upper cover structure 500, A sterilization water reservoir 600 in which sterilizing water is contained, and a gas inlet 610 through which gas such as carbon dioxide is supplied from above the sterilizing water reservoir 600.
  • a plurality of electrodes 410 and 420 are disposed in the sterilized water reservoir 600 in the form of a septum membrane and the water is electrolyzed using the positive electrode 420 and the negative electrode 410 arranged in a septum membrane, Sterilized water is produced.
  • the sterilizing water storage box 600 is provided therein with an outflow module structure 10 for transferring sterilized water to the upper part and a gas supplied into the sterilization water storage box 600 through the gas inlet 610 is sterilized
  • the sterilized water flows through the inlet provided at the lower end portion of the water module structure 10 and the sterilized water introduced through the inlet port flows through the outgoing module structure 10 to the outside of the sterilized water storage container 600 .
  • an outflow module structure 10 for discharging sterilized water to the outside is formed at the central portion of the upper cover structure 500, and a gas inlet 610 is connected to the upper cover It may be desirable to form the structure 500 in a circular shape along the periphery of the outflow module structure 10. [ However, the shape of the gas inlet 610 is not limited thereto.
  • cavitation phenomenon and pulsation phenomenon through the outflow module structure (10) effectively remove slime such as scale generated in various industrial conduits in which a liquid flows and bacteria contained in various conduits, and sterilization And a device capable of facilitating cleaning management.
  • the cavitation phenomenon refers to a phenomenon in which, when a liquid is flowing, the pressure at a certain point is lower than the vapor pressure of the liquid at that point, so that the air and water vapor in the liquid are separated to generate bubbles and make cavities.
  • Such a cavitation phenomenon may occur through the cavitation generating part 100 of the water outlet module structure 10, and details thereof will be described later.
  • the pulsation phenomenon in the present invention is a phenomenon in which the pressure of the liquid and the discharge amount periodically fluctuate in the flow of the liquid without free water surface in the pipe, which causes periodic vibration in the pipe.
  • the pulsation phenomenon is a factor that hinders the smooth flow of the fluid in the tube.
  • a method for preventing the pulsation phenomenon such as removing the air in the pipe, adjusting the cross-sectional area, flow rate and flow rate of the pipe has been studied.
  • the present invention proposes a method of cleaning and cleaning the inside of the pipe through the vibration generated by the pulsation phenomenon and the amount of the impact applied to the pipe wall.
  • the present invention which effectively removes slime such as scale generated in various industrial conduits in which liquid flows through cavitation phenomenon and pulsation phenomenon, bacteria which have been deposited in various conduits, and facilitates sterilization and cleaning management in conduits
  • the outgoing module structure 10 will be described in detail.
  • FIG. 6 shows an example of a chamber-type electrolytic sterilizing cleaning vessel to which the DSE electrode proposed by the present invention is applied.
  • FIG. 6 a chamber-type electrolytic sterilization cleaning vessel, a chamber-type electrolysis vessel exploded view, an impact wave tube & electrolysis module is shown.
  • Fig. 7 also shows experimental results relating to the pressure in relation to the cleaning vessel shown in Fig. 6.
  • Fig. 7 also shows experimental results relating to the pressure in relation to the cleaning vessel shown in Fig. 6.
  • stress distribution analysis was performed under a pressure load of 9 atmospheres in a pressure vessel after applying a closed boundary condition in pressure analysis.
  • Figure 8 shows an example of a KEG Coupler & Impact Wound Tube Fitting chamber type disinfection wash pot top CAP in the context of the present invention.
  • Figure 9 shows another example of a KEG Coupler & Impact Wound Tube Fitting chamber type disinfection wash vessel top CAP, in the context of the present invention.
  • Fig. 10 also shows an example of a chamber type sterilization cleaning vessel lower electrolytic sterilization (HOCL hypochlorous acid generation) module, in connection with the present invention.
  • HOCL hypochlorous acid generation electrolytic sterilization
  • Fig. 11 shows an example of a chamber type sterilizing cleaning vessel upper CAP binding type shock wave tube in the context of the present invention.
  • FIG. 12 is a diagram for explaining the principle of impact wave tube washing in the context of the present invention.
  • Water + CO2 gas mixing is a cleaning technique using microbubble impact waves of a fluid, and the principle of generating a pulse is applied to the principle of Bernoulli.
  • Bernoulli's definition is that the pressure decreases as the velocity of the fluid such as air or water decreases and the pressure increases as the velocity decreases.
  • the flow is slow and the pressure is high, the flow of fluid is fast and the pressure is low where the cross section is small.
  • a kind of momentary energy conversion of the fluid flowing through the pipe is a phenomenon in which the fluid flowing through the pipe at a constant flow rate is converted into the pressure energy by the sudden opening and closing of the flow control device such as a valve .
  • Figs. 12 (b) and 12 (c) are shown as the structure of the pulse and surge generating module and the principle of generating the shock wave.
  • the present invention can provide a user with a chamber-type electrolytic sterilization module which is a core component of a sterilization water producing system for draft beer supply piping sterilization and cleaning using the developed electrode, securing the manufacturing technology of durability enhanced DSE of more than 300% .
  • the present invention can provide a disinfection membrane electrolysis HOCL (1.0 ppm or higher) sterilization function using a DSE electrode.
  • the present invention can provide a water / CO2 gas mixing function using a shock wave tube to perform a fluid wave shock wave cleaning function.
  • the present invention provides an automatic & manual pressure relief function when a pressure of 5 bar or more is applied in a chamber, provides a departure-preventing function when a KEG coupler is connected to an upper chamber CAP, 4 bar) (pressure standard for German DIN national standard beer containers).
  • Fig. 13 shows an example of an improved electrolytic sterilization system proposed by the present invention.
  • the cleaning device using the gas mixture liquid proposed by the present invention includes an outflow module structure 10 for discharging sterilized water to the outside of the disinfection water reservoir 600, A structure 500, an electrolysis unit 400 for generating sterilized water, a sterilization water reservoir 600 in which sterilization water is contained, and the like.
  • Fig. 14 shows an example of an integral automatic and manual safety valve for releasing CO 2 gas pressure in the chamber according to the present invention.
  • the upper cover structure 500 may include a pressure hole 510, a sealing surface 520, and a pressure release button 700.
  • the pressure release button 700 means an integral safety valve for releasing the CO 2 gas pressure in the chamber.
  • the pressure release button 700 is referred to as an integral safety valve 700.
  • Fig. 15 shows a detailed view of the upper lid structure shown in Fig.
  • an integral safety valve 700 is inserted into a part of the upper cover structure 500 according to the present invention.
  • the integral safety valve 700 is implemented by combining the first structure 710 inserted into the upper cover structure 500 and the second structure 720 exposing the button to the outside.
  • a double bottom CAP for pressure safety and leakage prevention is applied in order to change the optimum pressure vessel resistance (capacity) and use voltage.
  • the capacity of the chamber for user convenience was changed from 4L to 3L, and the internal pressure performance was maintained above 9 bar.
  • the DC 12V to DC 24V can be applied.
  • a manual pressure release (open) button for releasing the CO 2 gas pressure within 5 bar in the chamber for user safety Respectively.
  • an automatic pressure release (open) structure for automatic pressure release is applied when CO2 gas overpressure occurs around the user's part.
  • FIG. 18 The specific operation of the integral safety valve 700 will be described later with reference to FIGS. 18 to 20.
  • FIG. 18 The specific operation of the integral safety valve 700 will be described later with reference to FIGS. 18 to 20.
  • 16 (a) to 16 (c) illustrate an example of the internal bonding structure of the improved electrolytic sterilization system proposed by the present invention.
  • FIG 17 shows an example of the electrolytic sterilization system including the electrolysis module having the stability of the present invention.
  • a chamber inner electrode holder titanium stick
  • a separator protection ring for DSE electrode cut surface was applied.
  • a lower CAP coated with an electrode protective cover (DSE Cover) was applied, and a chamber bottom type electrolytic sterilizing cleaning device for internal safety and leakage prevention was used.
  • DSE Cover electrode protective cover
  • FIG. 18 shows, in the context of the present invention, the standby state of the integral safety valve for releasing the CO 2 gas pressure in the chamber.
  • the integral safety valve 700 is realized by a combination of a first structure 710 inserted into the upper cover structure 500 and a second structure 720 exposing the button to the outside .
  • the second structure 720 for exposing the button to the outside may be screwed and fixed to the integral safety valve 700, though not shown, and the first structure 710 may be fixed inside the upper cover structure 500 Respectively.
  • the state shown in FIG. 18 is a standby state, and the generated CO2 gas 800 pressurizes the inner vessel 600.
  • the head portion of the first structure 710 and the lower structure 760 are disposed in the region where the CO 2 gas is input, so that the CO 2 gas can not be discharged to the outside.
  • a first spring 730 which is a large spring structure is inserted between the upper structure 770 and the lower structure 760 to maintain the tension between the upper structure 770 and the lower structure 760.
  • a second spring 740 which is a spring structure smaller than the first spring 730, is inserted between the upper structure 770 and the first structure 710 to reduce the tension between the upper structure 770 and the first structure 710 .
  • Two O-ring structures 751 and 754 are inserted into the lower end of the lower structure 760 and two O-ring structures 752 and 753 are inserted into the lower end of the first structure 710.
  • Fig. 19 shows the forced pressure release state of the integral safety valve for releasing the CO 2 gas pressure in the chamber, in the context of the present invention.
  • the manual pressure release method described in FIG. 19 is for the user to push a button on the external second structure 720.
  • Fig. 20 shows an automatic pressure release state of the integral safety valve for releasing the CO 2 gas pressure in the chamber, in the context of the present invention.
  • the first spring 730 is contracted by this pressure.
  • the present invention can provide a user with a water electrolytic sterilization system including an integral electrolytic module having an integrated automatic and manual safety valve for releasing CO2 gas in the chamber.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

Le système de stérilisation électrolytique selon un mode de réalisation de la présente invention comprend : une partie de stockage pour stocker de l'eau; un partie électrolyse qui comprend une électrode positive et une électrode négative agencées à proximité l'une de l'autre sans séparateur pour l'échange d'ions d'électrolytes, et qui génère de l'eau stérilisée par électrolyse de l'eau à partir de l'électrode positive et de l'électrode négative; une partie de génération de cavitation vers laquelle est envoyée l'eau stérilisée; une conduite tubulaire par laquelle l'eau stérilisée introduite est transportée; une partie d'échange gazeux vers laquelle du gaz est envoyée et dans laquelle le gaz introduit et l'eau stérilisée transportée sont mélangés pour produire un liquide mélangé à du gaz; et une soupape de sécurité de type intégrée pour l'évacuation, vers l'extérieur, d'au moins une partie du gaz afin d'abaisser la pression à l'intérieur de la partie de stockage en raison de la présence du gaz. La soupape de sécurité de type intégrée comprend : une première structure dont une extrémité est insérée dans la partie de stockage; et une seconde structure reliée à une pointe de la première structure et laissant exposé à l'extérieur un bouton destiné à recevoir l'action d'une force utilisateur, un premier ressort se trouvant entre la structure inférieure agencée au niveau de l'extrémité inférieure de la zone dans laquelle la première structure est insérée, et une structure supérieure agencée au niveau de l'extrémité supérieure de la zone d'insertion, un second ressort se trouvant entre la structure supérieure et une extrémité de la première structure, et une pluralité de structures barrières se trouvant entre la structure inférieure et l'extrémité inférieure de la zone d'insertion et entre la première structure et l'extrémité inférieure de la zone d'insertion. En fonction d'une force d'appui appliquée par l'utilisateur au moyen du bouton et/ou de la pression à l'intérieur de la partie de stockage en raison de la présence du gaz, le premier ressort ou le second ressort peut être comprimé afin d'expulser au moins une partie du gaz vers l'extérieur.
PCT/KR2018/016574 2018-01-18 2018-12-24 Système de stérilisation électrolytique WO2019143039A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR20180006745 2018-01-18
KR10-2018-0006745 2018-01-18

Publications (1)

Publication Number Publication Date
WO2019143039A1 true WO2019143039A1 (fr) 2019-07-25

Family

ID=67302376

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR2018/016574 WO2019143039A1 (fr) 2018-01-18 2018-12-24 Système de stérilisation électrolytique

Country Status (1)

Country Link
WO (1) WO2019143039A1 (fr)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07171442A (ja) * 1993-12-16 1995-07-11 Keihin Seiki Mfg Co Ltd キャビテーション洗浄装置における噴射ノズル
US20070063072A1 (en) * 2004-09-30 2007-03-22 Ganan Calvo Alfonso M Device and procedure for the pneumatic atomization of liquids through an implosive gas flow
JP2009005747A (ja) * 2007-06-26 2009-01-15 Sanyo Electric Co Ltd 洗浄装置
JP2011217785A (ja) * 2010-04-05 2011-11-04 Koken Ltd 殺菌洗浄処理装置およびその方法
KR20160021535A (ko) * 2014-08-18 2016-02-26 박종하 기체 혼합 액체를 이용한 세정 장치
KR20160055110A (ko) * 2016-03-31 2016-05-17 박종하 살균수 세척수기
KR20170022616A (ko) * 2015-08-21 2017-03-02 조정호 기체 혼합 액체를 이용한 세정 장치

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07171442A (ja) * 1993-12-16 1995-07-11 Keihin Seiki Mfg Co Ltd キャビテーション洗浄装置における噴射ノズル
US20070063072A1 (en) * 2004-09-30 2007-03-22 Ganan Calvo Alfonso M Device and procedure for the pneumatic atomization of liquids through an implosive gas flow
JP2009005747A (ja) * 2007-06-26 2009-01-15 Sanyo Electric Co Ltd 洗浄装置
JP2011217785A (ja) * 2010-04-05 2011-11-04 Koken Ltd 殺菌洗浄処理装置およびその方法
KR20160021535A (ko) * 2014-08-18 2016-02-26 박종하 기체 혼합 액체를 이용한 세정 장치
KR20170022616A (ko) * 2015-08-21 2017-03-02 조정호 기체 혼합 액체를 이용한 세정 장치
KR20160055110A (ko) * 2016-03-31 2016-05-17 박종하 살균수 세척수기

Similar Documents

Publication Publication Date Title
Hart et al. The fate of both intra- and extracellular toxins during drinking water treatment
JP3910095B2 (ja) オゾン発生用の電解槽
AU696309B2 (en) Synergistic biocidal combinations
KR101256896B1 (ko) 마이크로 전류를 이용하여 조류를 전기분해 멸균 제거하는 장치 및 방법
US20030049163A1 (en) Chemical modification of electrochemically activated solutions for improved performance
AP0102197A0 (en) Electrolytic apparatus, methods for purification of aqueous solutions and synthesis of chemicals.
BG105679A (en) Electrolysys apparatus, methods for purification of aqueous solutions and synthesis of chemicals
CN101198551A (zh) 含有氨态氮的废水的电解处理方法及装置
WO2013077496A1 (fr) Procédé et dispositif pour traiter l'eau de ballast de navires
WO2019143039A1 (fr) Système de stérilisation électrolytique
ES2125633T3 (es) Composicion limpiadora y procedimiento modificador del ph para separar aguas residuales utilizando un carboxilato anfotero y una composicion desestabilizadora cationica.
AU2004299043B2 (en) Composition and method for cleaning contained bodies of water
ES2078580T3 (es) Procedimiento para separar poli(tereftalato de etileno) de poli(cloruro de vinilo).
WO2018097636A1 (fr) Structure d'un module d'évacuation d'eau d'un dispositif de nettoyage utilisant un liquide mélangé à un gaz
KR100794732B1 (ko) 살균제 농도조절부가 구비된 전해살균 시스템
US20070000790A1 (en) Method and device for electrochemical disinfection of water
WO2013039291A1 (fr) Appareil de fabrication d'eau hydrogénée et d'eau ozonée ayant une fonctionnalité
WO2022119407A1 (fr) Appareil d'électrolyse de l'eau de mer et système de liaison de pile à combustible à électrolyse de l'eau de mer le comprenant
CN103896372A (zh) 利用辉光放电协同处理含有As(III)、Cr(VI)废水的方法及其装置
EP2089326B1 (fr) Système de traitement de l'eau de ballast des navires, des plates-formes pétrolières en mer et de contenants, en général, à l'aide d'un procédé dans un réacteur électrochimique
KR100587400B1 (ko) 용수처리장치
WO2022260187A1 (fr) Appareil de traitement d'eau stérilisée et son procédé de régulation
CN202415217U (zh) 一种紫外光反应器
CN102198981B (zh) 一种用于海水或淡水***的协同防污方法及装置
KR101063572B1 (ko) 음전극판 보호부재를 설치한 전기분해장치

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 18901196

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 18901196

Country of ref document: EP

Kind code of ref document: A1

122 Ep: pct application non-entry in european phase

Ref document number: 18901196

Country of ref document: EP

Kind code of ref document: A1