CN204987427U - Water storage formula electric water heater of exportable brineelectrolysis - Google Patents
Water storage formula electric water heater of exportable brineelectrolysis Download PDFInfo
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- CN204987427U CN204987427U CN201520116075.6U CN201520116075U CN204987427U CN 204987427 U CN204987427 U CN 204987427U CN 201520116075 U CN201520116075 U CN 201520116075U CN 204987427 U CN204987427 U CN 204987427U
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Abstract
The utility model provides a water storage formula electric water heater of exportable brineelectrolysis, includes water container, electric heat water electrical system, controllable electrolysis power, no membrane electrolysis electrode subassembly, characterized by: water container has water inlet and delivery port, the raw water gets into water container from the water container water inlet, the heating of electric heat water electrical system control water container normal water, controllable electrolysis power provides the electric current for no membrane electrolysis electrode subassembly, the water of no membrane electrolysis electrode subassembly in to water container carries out the electrolysis, the brineelectrolysis is exported from the water container delivery port, no membrane electrolysis electrode subassembly adopts higher efficiency not have membrane brineelectrolysis technique, to effectively electrolysis of the desired temperature scope water storage among the water container, reasonable greatization of area, water electrolysis process water that no membrane electrolysis electrode subassembly design compromise different polarity electrode gap's reasonable lessization of interval, electrode gap have the characteristic in the aspect of three such as suitable circulation at electrode gap to increase aquatic impurity and hydrone by electrolysis probability and quantity, improvement water electrolysis efficiency.
Description
Technical field
The present invention relates to a kind of storage-type electric water heater of exportable brine electrolysis, belong to without film brine electrolysis technical field.
Background technology
Storage-type electric water heater is people's widely used utensils in shower and use hot water etc., and the brine electrolysis that negative potential is rich in hydrogen has anti-oxidant and disinfecting and decontaminating, skin cleaning and beauty effect, apply as shower and washings, have six large benefits at least: one be can less with so that wash clean chemicals without shower cream etc., thus reduce the bad reactions such as allergic skin itching alopecia; Two is treat some pruritus skin diseases effect as beriberi (athlete's foot) etc. in addition; Three is have the health-care efficacies such as face and skin beautifying antioxidant and anti-aging; Four is that scrubber dirt-removing power is strong; Five is that washing fruits and vegetables have the function removed agriculture chemical etc. and pollute; Six is be conducive to environmental protection to reduce chemical contamination.Brine electrolysis technology be combined with water heater as seen, creating a kind of storage-type electric water heater of exportable brine electrolysis, is very with practical value and many-sided meaning.Does so why, the electric heater having no exportable brine electrolysis so far come out? trace it to its cause: one is because popular electrolyzed water machine adopts and inefficient has film brine electrolysis technology, can only electrolysis normal-temperature water, and water temperature will disappear more than brine electrolysis index during 50-60 degree Celsius, the major defect such as simultaneously must export Acidity of Aikalinity two kinds of water in addition, water yield is little, power consumption is large, does not obviously meet and does needed for electrolytic water electric water heater; Although two is present without film brine electrolysis technology the advantage that film brine electrolysis technology do not have, such as: can the former water of electrolysis arbitrary temp and only export the particular advantages such as a kind of brine electrolysis, but defect is electrolytic efficiency or on the low side, was still confined to the electrolysis nature stationary water devices such as glass kettle type that does in the past and supplied drinking water aspect application.Applicant finds: produce the storage-type electric water heater product with practical value, because moisture storage capacity is larger, need configure electrolytic efficiency higher without film brine electrolysis technology, without the technological innovation of film brine electrolysis develop for this type of invention provides feasibility, therefore the present invention arises at the historic moment just.
Summary of the invention
The present invention proposes a kind of storage-type electric water heater of exportable brine electrolysis, is to create and design in order to brine electrolysis can be used easily to take a shower for people.Because electric heater moisture storage capacity is comparatively large, for the purpose of practicality, should adopt higher electrolytic efficiency without film brine electrolysis technology, to meet certain brine electrolysis index request.Find and the brine electrolysis new principle of invention and new method according to applicant, higher brine electrolysis efficiency and brine electrolysis index can be obtained, have very large meaning for the practicality improving brine electrolysis shower.Water electrolysis efficiency or title brine electrolysis efficiency, generally can be defined as: under a certain amount of water of electrolysis and electrolysis certain hour situation, the ratio of certain representative index of made brine electrolysis (the ORP negative value of such as electrolytic reduction water or hydrogen content numerical value) and institute's power consumption.In other words, certain electrolytic method or electrolysis unit, it is less that the same water yield of electrolysis reaches same brine electrolysis index institute consuming electric power, and this device brine electrolysis efficiency is higher.
The brine electrolysis new principle that applicant finds and significantly improve the method for brine electrolysis efficiency, root is in deep layer research traditional electrolyte water machine brine electrolysis principle being existed to significant deficiency.Traditional electrolyte water principle is only confined to the ion chemistry molecular balance equation that so-called hydrone electrolysis produces, the impurity ignoring water in electrolytic process completely the electronics that produces by electrolysis and contaminant particles, and to improving the significance of brine electrolysis index and electrolytic efficiency, therefore have no way of explaining that cathodic region alkaline water has comparatively high-reduction water key index and higher oxygen reduction potential (ORP) negative value and higher hydrogeneous (H, H
2, H
-) phenomenon measured, ignore cathodic region water completely and form higher ORP negative value and negative hydrogen (H
-) content needs the key events of a great deal of active electrons, even if therefore cannot solve the difficult problem that existing electrolysis tech efficiency too low increasing Faradaic current does not reach the higher brine electrolysis index of anticipation yet.Applicant studies for a long period of time acquisition six new discoveries:
One of new discovery: brine electrolysis process, in order to improve brine electrolysis efficiency, the impurity that primary is in brine electrolysis.Impurity is produced free electron by electrolysis and is conducive to improving the contaminant particles of brine electrolysis index, be called for short " impurity electrolytic effect " herein, impurity electrolytic effect forms certain Faradaic current, and making hydrone disintegrate becomes hydrogen, oxonium ion or hydroxyl ion root, herein referred to as " hydrone electrolytic effect ".Brine electrolysis efficiency and index are " impurity electrolytic effect " and " hydrone electrolytic effect " coefficient result; New discovery two: disclose active electrons that " impurity electrolytic effect " produce for the double meaning improving electrolytic efficiency, active electrons not only can increase Faradaic current, and reductive water is made for electrolysis also there is another significance, meet ORP (negative oxidation-reduction potential) negative value of certain brine electrolysis index such as electrolytic reduction water and corresponding hydrogen content (negative hydrogen content) thereof exactly to needed for electronics.Therefore for improving electrolytic efficiency, electrolysis process should be strengthened " impurity electrolytic effect " as far as possible, to produce more active electrons; New discovery three: be that opposing electrode small―gap suture (being especially less than the small―gap suture of 1mm) has remarkable result for strengthening " impurity electrolytic effect ", although non-isolating film brine electrolysis technology before this also once mentioned that opposing electrode spacing was less than the design consideration of 3mm, but do not understand closely spaced practical significance, the technique behave matched with it is not more known where to begin, and can not reach the effect significantly improving brine electrolysis efficiency; New discovery four: another significance of electrolysis electrode gap Small Distance design can create active electrons and reactive hydrogen H is combined into the more chance of negative hydrogen and better condition, thus significantly improve the efficiency of electrolysis making reductive water; New discovery five: opposing electrode small―gap suture is little of certain value, electrolytic efficiency does not rise counter falling, does is what reason this? research confirms: need to strengthen " impurity electrolytic effect ", also need in electrolytic process, ensure that water has certain circulation in opposing electrode gap, this can impel more hydrone and impurity more repeatedly by electrolysis, thus strengthening " impurity electrolytic effect ", improve water electrolysis efficiency and brine electrolysis and reduce index; To the further investigation of circulation in brine electrolysis process, explain after why Faradaic current is increased to certain value, brine electrolysis efficiency does not rise counter falling.Major reason is: if the circulation of water is bad in electrode gap, can make electrode gap intermediate ion excessive concentration, thus affect electrolytic efficiency; New discovery six: for the outer power-actuated flowing water such as running water of electrolysis, in certain space shared by electrode assemblie, take the design rationally increasing electrolysis interval area, be conducive to more impurity and hydrone electrolysis more repeatedly in water, water electrolysis efficiency and electrolysis index can be improved.In addition, in the flowing water situation that electrolysis flow velocity is too fast, to the passage installing electrolysis electrode assembly, take the design that exhalant canal (delivery port) is suitably narrower than intake tunnel (water inlet), the flow velocity of water through electrolysis electrode assembly can be reduced, thus increase impurity and hydrone are by the time of electrolysis and chance, improve the index of brine electrolysis.
Applicant passes through for above-mentioned six newfound comprehensive analyses, following brine electrolysis new principle is proposed: brine electrolysis process, first, be that the generation of electrolysis impurities in water enlivens electronics, forming electric current, is the process of the decomposition energy of hydrone by electric energy conversion, therefore more hydrone is made to obtain larger electric energy and decompose, be the basis obtaining higher electrolytic efficiency, but obtain higher electrolytic efficiency, also need to possess other essential condition.This is because electrolytic process is simultaneously still: impurity the various ions (especially enlivening electronics) that discharge by electrolysis produce with water-molecule dissociation various hydroxyl ions, ion root generation physical and chemical effect process, in the process, for the electrolytic efficiency improving water has two essential condition, first, if more impurity is by electrolysis, electronics, the ion of its release are more, and the probability that itself and hydroxyl ion combine is just higher, brine electrolysis index may be higher, and electrolytic efficiency is also just higher; The second, if can create conditions, the probability that the electronic and ionic that impurity is discharged by electrolysis and hydroxyl ion combine is higher, and brine electrolysis index may be higher, and electrolytic efficiency is also just higher.The higher ORP negative value of such as electrolytic reduction water and hydrogen content (two indexes is briefly collectively referred to as by applicant " negative hydrogen " index), the more electronics that enlivens is needed to participate in, therefore, impurities in water is discharged by electrolysis that to be combined as the probability of negative hydrogen compared with polyelectron and electronics and hydrogen ion higher, just can improve negative hydrogen index and electrolytic efficiency.
The brine electrolysis new principle of applicant discloses: improve electrolysis making reductive water efficiency and will take three-pronged process, the electrolysis of impurities in water should be strengthened, improve the electronics of impurity electrolysis release again, also will increase the probability that electronics that electrolysis discharges and hydrogen are combined into negative hydrogen.Applicant studies and has found to realize this three-pronged concrete electrolysis process method: one is suitably reduce the distance between opposing electrode electrolysis gap, two is the areas suitably expanding opposing electrode electrolysis gap, three is the mobility suitably remaining on water turnover in brine electrolysis process opposing electrode gap, the coordination of these three technology conditions realizes, strengthening impurity electrolysis can be taken into account preferably and effect of raising reduction index, thus significantly improve brine electrolysis efficiency.The storage-type electric water heater of a kind of exportable brine electrolysis of the present invention, because certain requirement of moisture storage capacity and brine electrolysis time, what use greater efficiency has higher practicality without film brine electrolysis technology.The brine electrolysis new method of applicant's invention is adopted to be the better selection improving unit efficiency and performance and cost performance.
The storage-type electric water heater of a kind of exportable brine electrolysis of the present invention, comprises tank, electric hot water electric-control system, controllable electrolysis power supply, without film electrolysis electrode assembly, it is characterized in that: tank has water inlet and delivery port; Former water enters tank from tank water inlet; The heating of water in electric hot water electric control system controls tank; Controllable electrolysis power supply is provided electric current without film electrolysis electrode assembly; Without film electrolysis electrode assembly, electrolysis is carried out to the water in tank; Brine electrolysis exports from tank delivery port; Adopt greater efficiency without film brine electrolysis technology without film electrolysis electrode assembly, the water storage for scope temperature required in tank can effectively electrolysis.
Content two of the present invention: described without film electrolysis electrode assembly, between its opposing electrode stay the spacing in gap by rationally littleization principle design, clearance distance is being less than 5mm, is being greater than between 0mm, is beneficial to the electrolysis strengthening impurities in water and hydrone; In certain space shared by electrolysis electrode assembly, between opposing electrode, the area in gap is by rationally largeizationr principle design, to make in water more impurity and water molecule energy in electrode gap more repeatedly by electrolysis; The feature of electrolysis electrode assembly and mounting process condition thereof is: in brine electrolysis process, water can comparatively smooth flow in opposing electrode gap, make to be changed by the water of electrolysis in opposing electrode gap, and make more impurity and hydrone by opposing electrode electrolysis more repeatedly, increase impurity and hydrone by the probability of opposing electrode electrolysis and quantity, thus improve the electrolytic efficiency of water.
Content three of the present invention: described without film electrolysis electrode assembly, if desired, spacing between electrolysis electrode assembly opposing electrode can be as small as 1mm or less, to be comparatively beneficial under certain electrolysis power and certain electrolysis electrode modular construction, the electrolysis of strengthening impurities in water and hydrone, improves the efficiency of water electrolysis.
Content four of the present invention: described without film electrolysis electrode assembly, by daily drinking-water and can be made into water the electrolytic reduction water that oxidation-reduction potential is negative value, hydrogen content is greater than zero.
Content five of the present invention: described without film electrolysis electrode assembly, opposing electrode structural design makes: when water in electrode gap is produced mobility by electrolysis, in electrode gap, water and ion can be taken advantage of a situation and be flowed, so that more water flows through opposing electrode gap, change in gap by the water of electrolysis, make more impurities in water and water molecule energy by the electrolysis more repeatedly of electric current between opposing electrode, increase impurity and hydrone, by the probability of opposing electrode electrolysis and quantity, improve the efficiency of water electrolysis.
Content six of the present invention: described without film electrolysis electrode assembly, certain space is left in outside, electrode gap two-port position, when making water produce flowing in by the process of electrolysis, water can in opposing electrode gap comparatively smooth flow, improve the efficiency of water electrolysis.
Content seven of the present invention: described without film electrolysis electrode assembly, in certain space shared by electrolysis electrode assembly, by rationally increasing the area of electrode gap, flowing water can be extended in electrode gap by the time of electrolysis, make more impurity and hydrone by opposing electrode electrolysis more repeatedly, increase impurity and hydrone, by the probability of opposing electrode electrolysis and quantity, improve the efficiency of water electrolysis.
Content eight of the present invention: described without film electrolysis electrode assembly, when the cell wall material and shape of wrapping up electrolysis electrode assembly fit cooperating electrode, it suitably can be connected as electrolysis electrode, increase electrolysis electrode interval area, improve the electrolytic efficiency of water.
Content nine of the present invention: to be describedly made up of the electrode of two opposed polarities without film electrolysis electrode assembly, one of electrode is bore shape, tubular electrode number is N number of, N is equal to or greater than 1, and barrel can non-notch or jagged, and the position of each bore electrode is fixed and is electrically connected to each other for machinery; Two of electrode is column, and each post position is fixed for mechanical and be electrically connected to each other, and the post number of columnar electrode is M, and M is equal to or greater than 1; Post be hollow or solid, can non-notch or jagged; The height of tubular electrode and columnar electrode is not limit, according to required selection; Tubular electrode grafting corresponding to columnar electrode, namely each post of columnar electrode inserts in each corresponding bore, leaves between the post electrode surface inserted and bore electrode apparent surface gap water being done to electrolysis; In the electrolysis course of work, the water in electrode gap can flow; Certain space is left in the outside of electrode gap two port position, so that water is by the process of electrolysis, can flow in electrode gap.
Basic technical scheme: the storage-type electric water heater of a kind of exportable brine electrolysis of the present invention, comprises tank, electric hot water electric-control system, controllable electrolysis power supply, without film electrolysis electrode assembly, it is characterized in that: tank has water inlet and delivery port; Former water enters tank from tank water inlet; The heating of water in electric hot water electric control system controls tank; Controllable electrolysis power supply is provided electric current without film electrolysis electrode assembly; Without film electrolysis electrode assembly, electrolysis is carried out to the water in tank; Brine electrolysis exports from tank delivery port; Adopt greater efficiency without film brine electrolysis technology without film electrolysis electrode assembly, the water storage for scope temperature required in tank can effectively electrolysis.
One of concrete technical scheme: described without film electrolysis electrode assembly, between its opposing electrode stay the spacing in gap by rationally littleization principle design, clearance distance is being less than 5mm, is being greater than between 0mm, is beneficial to the electrolysis strengthening impurities in water and hydrone; In certain space shared by electrolysis electrode assembly, between opposing electrode, the area in gap is by rationally largeizationr principle design, to make in water more impurity and water molecule energy in electrode gap more repeatedly by electrolysis; The feature of electrolysis electrode assembly and mounting process condition thereof is: in brine electrolysis process, water can comparatively smooth flow in opposing electrode gap, make to be changed by the water of electrolysis in opposing electrode gap, and make more impurity and hydrone by opposing electrode electrolysis more repeatedly, increase impurity and hydrone by the probability of opposing electrode electrolysis and quantity, thus improve the electrolytic efficiency of water.
Concrete technical scheme two: described without film electrolysis electrode assembly, if desired, spacing between electrolysis electrode assembly opposing electrode can be as small as 1mm or less, to be comparatively beneficial under certain electrolysis power and certain electrolysis electrode modular construction, the electrolysis of strengthening impurities in water and hydrone, improves the efficiency of water electrolysis.
Concrete technical scheme three: described without film electrolysis electrode assembly, by daily drinking-water and can be made into water the electrolytic reduction water that oxidation-reduction potential is negative value, hydrogen content is greater than zero.
Concrete technical scheme four: described without film electrolysis electrode assembly, opposing electrode structural design makes: when water in electrode gap is produced mobility by electrolysis, in electrode gap, water and ion can be taken advantage of a situation and be flowed, so that more water flows through opposing electrode gap, change in gap by the water of electrolysis, make more impurities in water and water molecule energy by the electrolysis more repeatedly of electric current between opposing electrode, increase impurity and hydrone, by the probability of opposing electrode electrolysis and quantity, improve the efficiency of water electrolysis.
Concrete technical scheme five: described without film electrolysis electrode assembly, certain space is left in outside, electrode gap two-port position, when making water produce flowing in by the process of electrolysis, water can in opposing electrode gap comparatively smooth flow, improve the efficiency of water electrolysis.
Concrete technical scheme six: described without film electrolysis electrode assembly, in certain space shared by electrolysis electrode assembly, by rationally increasing the area of electrode gap, flowing water can be extended in electrode gap by the time of electrolysis, make more impurity and hydrone by opposing electrode electrolysis more repeatedly, increase impurity and hydrone, by the probability of opposing electrode electrolysis and quantity, improve the efficiency of water electrolysis.
Concrete technical scheme seven: described without film electrolysis electrode assembly, when the cell wall material and shape of wrapping up electrolysis electrode assembly fit cooperating electrode, it suitably can be connected as electrolysis electrode, increase electrolysis electrode interval area, improve the electrolytic efficiency of water.
Concrete technical scheme eight: to be describedly made up of the electrode of two opposed polarities without film electrolysis electrode assembly, one of electrode is bore shape, tubular electrode number is N number of, N is equal to or greater than 1, and barrel can non-notch or jagged, and the position of each bore electrode is fixed and is electrically connected to each other for machinery; Two of electrode is column, and each post position is fixed for mechanical and be electrically connected to each other, and the post number of columnar electrode is M, and M is equal to or greater than 1; Post be hollow or solid, can non-notch or jagged; The height of tubular electrode and columnar electrode is not limit, according to required selection; Tubular electrode grafting corresponding to columnar electrode, namely each post of columnar electrode inserts in each corresponding bore, leaves between the post electrode surface inserted and bore electrode apparent surface gap water being done to electrolysis; In the electrolysis course of work, the water in electrode gap can flow; Certain space is left in the outside of electrode gap two port position, so that water is by the process of electrolysis, can flow in electrode gap.
Accompanying drawing explanation
Below by accompanying drawing, the present invention is further explained.
Appended Fig. 1 is the storage-type electric water heater of the embodiment of the present invention 1 one kinds of exportable brine electrolysis
Detailed description of the invention
Below in conjunction with embodiment 1 accompanying drawing 1 illustrated embodiments basic structure and basic functional principle.
Embodiment 1
As Fig. 1, the storage-type electric water heater of a kind of exportable brine electrolysis of the present invention, comprise tank 14, electric hot water electric-control system 5, controllable electrolysis power supply 9, be immersed in water without film electrolysis electrode assembly 10, its course of work is: tank 14 has water inlet 18 and delivery port 13; Former water enters tank 14 from tank 14 water inlet 18; In figure, dotted line 15 is the waterline of water in tank 14; Electric hot water electric-control system 5 controls the heating of water in tank 14; Controllable electrolysis power supply 9 is provided electric current without film electrolysis electrode assembly 10; Water in electrolysis electrode assembly 10 pairs of tanks carries out electrolysis; Brine electrolysis exports from tank delivery port; Electrolysis electrode assembly adopts greater efficiency without film brine electrolysis technology, and the water storage for scope temperature required in tank can effectively electrolysis; The feature of electrolysis electrode assembly 8 is: two opposing electrodes are respectively bore shape electrode 1 (the poroid electrode of hereinafter referred) and may correspond to it the pole 2 of grafting, the tooth of pole 2 inserts in the corresponding aperture of poroid electrode, electrolysis gap 3 is left between tooth surface and hole surface, schematically depict 3 gaps 3 in Fig. 1, the spacing-visible in gap needs the scope being greater than 0 to 5mm to select; To meet in the electrolysis course of work in certain circulation situation of water in gap 3, the desirable smaller value of spacing (as equal and even be less than 2mm) in gap 3, with the electrolysis effectiveness of fortified water and wherein impurity, this is especially favourable for the water that the electrical conductivity such as electrolysis pure water distilled water are low; Under clearance distance one stable condition, obvious impurity is directly proportional to interval area by the probability of electrolysis and quantity to hydrone, because this gap 3 area largeizationr (i.e. pore diameter with highly get higher value) can improve electrolytic efficiency; 11,12 bottom, the upper spaces being respectively electrolysis electrode assembly 8, design to make water in electrode gap smoothly to flow, in brine electrolysis process, hydrone in gap is by after electrolytic decomposition, hydrogen, oxygen bubbles can be produced upwards elegant along gap, thus drive water in gap 3 upwards to flow, flow out gap 3 upper port, water is caused to flow into continually electrode gap from gap 3 lower opening and space 11, water is in the process of Clearance Flow, and water impurity and hydrone can by Faradaic current electrolysis repeatedly in gap; Obviously, the spacing that gap 3 choose reasonable is less and larger area also meet glassware for drinking water in gap 3 and have good circulation, the process technology scheme that these three aspects are coordinated to take into account is conducive to intensified electrolysis effect, improves water storage in container 4 by the index (ORP negative value and hydrogen content as electrolytic reduction water) of the efficiency of electrolysis and brine electrolysis.If not spacing 11 or 11 is too narrow bottom gap 3, the water in gap 3 can not smoothly flow, and electrolytic efficiency can significantly reduce, and in like manner, gap 3 top not spacing 12 or 12 is too narrow, and electrolytic efficiency also can significantly reduce; But also have the situation of another possibility, namely in electrode gap, flow rate of water flow is too fast, treating method is that the free air space 12 of water side, gap saliva can be suitably narrower than the free air space 11 of water inlet end saliva, suitably to slow down the flow velocity of water by gap, thus in increase gap water by the time of electrolysis, intensified electrolysis effect.Table 1 detects data and contributes to understanding above description.
Table 1: the measured data of the storage-type electric water heater embodiment 1 of a kind of exportable brine electrolysis of the present invention
Note: decomposition voltage 12V, former water: ORP=+365-402mv, hydrogen content=0, normal temperature
Data are detected relatively: electrolysis electrode gap 3 area difference half from A, B hurdle or A, C hurdle, or water flow sex differernce in electrode gap, brine electrolysis index is all significantly different, confirms the brine electrolysis new principle that applicant proposes and new method. related detection digital proof: the storage-type electric water heater of the exportable brine electrolysis of the present invention has feasibility, novelty, practicality.
The storage-type electric water heater of a kind of exportable brine electrolysis of the present invention; its electrolysis electrode assembly is not limited to the concrete structure using embodiment 1 to take; in actual product selection of technical scheme; use any one of required (low middle height) the brine electrolysis index of the storage-type electric water heater product reaching the exportable brine electrolysis of the present invention without film electrolysis electrode structure, all belong to scope.
Claims (6)
1. a storage-type electric water heater for exportable brine electrolysis, comprises tank, electric hot water electric-control system, controllable electrolysis power supply, without film electrolysis electrode assembly, it is characterized in that: tank has water inlet and delivery port; Former water enters tank from tank water inlet; The heating of water in electric hot water electric control system controls tank; Controllable electrolysis power supply is provided electric current without film electrolysis electrode assembly; Without film electrolysis electrode assembly, electrolysis is carried out to the water in tank; Brine electrolysis exports from tank delivery port.
2. the storage-type electric water heater of a kind of exportable brine electrolysis according to claim 1, is characterized in that: described without film electrolysis electrode assembly, electrode gap distance is being less than 5mm, is being greater than between 0mm.
3. the storage-type electric water heater of a kind of exportable brine electrolysis according to claim 1, is characterized in that: described without film electrolysis electrode assembly, the spacing between electrolysis electrode assembly opposing electrode can be as small as 1mm or less.
4. the storage-type electric water heater of a kind of exportable brine electrolysis according to claim 1, is characterized in that: described without film electrolysis electrode assembly, certain space is left in outside, electrode gap two-port position.
5. the storage-type electric water heater of a kind of exportable brine electrolysis according to claim 1, is characterized in that: described without film electrolysis electrode assembly, and the cell wall of parcel electrolysis electrode assembly connects as electrolysis electrode.
6. the storage-type electric water heater of a kind of exportable brine electrolysis according to claim 1, it is characterized in that: described without film electrolysis electrode assembly, be made up of the electrode of two opposed polarities, one of electrode is bore shape, bore shape electrode number is N number of, N is equal to or greater than 1, barrel non-notch or jagged, and the position of each bore shape electrode is fixed for mechanical and be electrically connected to each other; Two of electrode is column, and each post position is fixed for mechanical and be electrically connected to each other, and the post number of columnar electrode is N number of, and N is equal to or greater than 1; Post is hollow or solid, non-notch or jagged; The height of bore shape electrode and columnar electrode is not limit, according to required selection; The grafting corresponding to columnar electrode of bore shape electrode, namely each post of columnar electrode inserts in each corresponding bore, leaves between the columnar electrode surface of inserting and bore shape electrode apparent surface gap water being done to electrolysis; In the electrolysis course of work, the water in electrode gap can flow; Certain space is left in the outside of electrode gap two port position.
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| CN104633912A (en) * | 2015-02-26 | 2015-05-20 | 罗民雄 | Water storage type electric water heater capable of draining electrolyzed water |
| WO2016134621A1 (en) * | 2015-02-26 | 2016-09-01 | 罗民雄 | New membraneless water electrolysis method for significantly improving electrolysis efficiency |
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