CN204689685U - A kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance - Google Patents
A kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance Download PDFInfo
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- CN204689685U CN204689685U CN201520116123.1U CN201520116123U CN204689685U CN 204689685 U CN204689685 U CN 204689685U CN 201520116123 U CN201520116123 U CN 201520116123U CN 204689685 U CN204689685 U CN 204689685U
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Abstract
Adopt two groups of electrolysis electrode assemblies to control a new device for brine electrolysis performances, it is characterized in that: comprise container filled with water, be placed in container filled with water without film electrolysis electrode assembly 1 and 2, controllable electrolysis power supply; Former water enters in container, respectively in the anodic-cathodic gap of electrolysis electrode assembly 1,2 by electrolysis; Controllable electrolysis power supply is powered to electrolysis electrode assembly 1,2, electrolysis electrode assembly one can change the acid-basicity of brine electrolysis, its two redox potential that can change brine electrolysis of electrolysis electrode assembly, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly; Electrolysis electrode assembly 1,2 and controllable electrolysis power supply, both mode controllable electrolysis power supply can having been taked to export two groups of voltages power respectively to electrolysis electrode assembly 1,2, or adopt controllable electrolysis power supply to export the mode of one group of electrolysis voltage to electrolysis electrode assembly 1,2 series-fed, realize the Comprehensive Control to brine electrolysis performance, the former controls handiness, and comparatively the latter is high.
Description
Technical field
The present invention relates to a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance, belong to without film brine electrolysis technical field.
Background technology
Brine electrolysis technology can be divided into have film electrolysis with without film electrolysis two greatly classification, film brine electrolysis technology is had to be the mature technology of existing more than 80 years history, brine electrolysis is divided into sour water and alkaline water two regions by barrier film, two kinds of water respectively have purposes, as: meta-alkalescence and redox potential be negative value, be rich in the reductive water of hydrogen (being called for short " negative hydrogen water ") suitablely drinks, help human body anti-oxidant, increase physical efficiency, sharp metabolism, promote human health; And strongly-acid, high normal potential water can disinfections.But, have the apparent shortcoming of film brine electrolysis technology to be: when people only need alkalescence or acid a kind of water, unwanted acidity or alkaline water can be wasted; And be difficult to produce acid negative potential and be rich in the water of hydrogen and be difficult to produce " neutrality " brine electrolysis (refering in particular to the brine electrolysis significantly do not changed with former water acid-basicity herein) etc.What in recent years rise has without film brine electrolysis technology the unique advantage overcoming and have the above-mentioned defect of film brine electrolysis, is the developing direction of brine electrolysis technology.Controlling in the indexs such as the alkalescence of brine electrolysis and redox potential ORP value, barrier film brine electrolysis technology is had to have no good solution so far, it is same high with low natural characteristics with ORP negative value to there is alkalescence in its electrolyzed alkaline water produced, and acidic electrolytic water existence acidity that it produces and ORP are on the occasion of same high with low natural characteristics, be difficult to realize performance index difference regulable control; Also have no good technical scheme without film brine electrolysis technology on the one hand at this to come out.Applicant is through studying for many years, in innovation brine electrolysis principle and method basis, invent a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance, superior performance, simple, what both can produce that alkalescence is rich in hydrogen with neutral negative potential drinks reductive water, can produce again the beauty and skin care reductive water that acid negative potential is rich in hydrogen, etc.
Summary of the invention
The present invention proposes a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performances, is to design in order to people can make the brine electrolysis with different pH values and different redox potential expediently.Applicant finds under study for action: generally can have the technical scheme producing neutral (not changing pH value), alkalescence, acidic electrolytic water three kinds of functions without film brine electrolysis technique device, and the redox potential value of made brine electrolysis is also had nothing in common with each other.Finding through test: generally speaking, combinationally using mainly making sour water without film electrolytic water device with two kinds of mainly making negative potential neutral water, can be produced by Comprehensive Control and substantially not change neutral or the alkaline or acidic electrolytic water of former water ph value.
In addition, the present invention proposes a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance, adopt applicant to find can obtain higher brine electrolysis efficiency and brine electrolysis index with the brine electrolysis new principle of invention and novel method, have very large meaning for raising acid-basicity brine electrolysis Con trolling index and practicality thereof.From professional angle, water electrolysis efficiency (or claiming 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 current consumption.In other words, certain electrolysis process or electrolyzer, 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.Applicant finds to disclose with the brine electrolysis new principle of invention and novel method the approach improving brine electrolysis efficiency.The brine electrolysis new principle that applicant proposes is as follows: brine electrolysis process, first be the process that the generation of electrolysis impurities in water enlivens that electric energy conversion is the decomposition energy of water molecules by electronics formation electric current, making more water molecules obtain larger electric energy and decomposing is the basis obtaining higher electrolytic efficiency, but the higher electrolytic efficiency of acquisition also needs to possess other essential condition; Because, electrolytic process is simultaneously still: impurity the various ions that discharge by electrolysis especially enliven the process of various hydroxide ions that electronics and water-molecule dissociation produce, ion root generation physical and chemical effect, first, if more impurity is by electrolysis, electronics, the ion of its release are more, the probability that itself and hydroxide ion combine is just higher, and brine electrolysis index may be higher, and electrolytic efficiency is also just higher; The second, if the probability that the objective condition electronic and ionic that makes impurity be discharged by electrolysis and hydroxide ion combine is higher, 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 (applicant is referred to as " negative hydrogen " index), the more electronics that enlivens is needed to participate in, therefore, impurities in water discharged by electrolysis compared with polyelectrons and the probability that combines with hydrogen ion higher, be two essential condition improving negative hydrogen index and electrolytic efficiency.
The brine electrolysis new principle of applicant discloses: improve the processing method that electrolysis making reductive water efficiency will be taked to work along both lines, should strengthen the electrolysis of impurities in water, the electronics of raising impurity electrolysis release again and hydrogen are combined into the probability of negative hydrogen.Applicant studies discovery: one is suitably reduce the distance between anodic-cathodic electrolysis gap, two is the areas suitably expanding anodic-cathodic electrolysis gap, three is the mobility suitably remaining on water turnover in brine electrolysis process anodic-cathodic 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.A kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance of the present invention, what use greater efficiency can obtain more practical performance without film brine electrolysis technology.The brine electrolysis novel method of applicant's invention is adopted to be the better selection improving plant efficiency and performance and cost performance.
A kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performances of the present invention, is characterized in that: comprise container filled with water, be placed in container filled with water without film electrolysis electrode assembly 1 and 2, controllable electrolysis power supply; Former water enters in container, respectively in the anodic-cathodic gap of electrolysis electrode assembly 1,2 by electrolysis; Controllable electrolysis power supply is powered to electrolysis electrode assembly 1,2, electrolysis electrode assembly one can change the acid-basicity of brine electrolysis, its two redox potential that can change brine electrolysis of electrolysis electrode assembly, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
Content two of the present invention: described electrolysis electrode assembly 1,2 and controllable electrolysis power supply, mode controllable electrolysis power supply can being taked to export two groups of voltages power respectively to electrolysis electrode assembly 1,2, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
Content three of the present invention: described electrolysis electrode assembly 1,2 and controllable electrolysis power supply, the anodic-cathodic of two groups of electrolysis electrode assemblies suitably can be connected in series, adopt controllable electrolysis power supply to export the mode of one group of electrolysis voltage to electrolysis electrode assembly 1,2 series-fed, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
Content four of the present invention: described container filled with water, can have water-in and water outlet; Former water enters in container from water-in, through the electrolysis of electrolysis electrode assembly; Brine electrolysis flows out from electrolyzer water outlet.
Content five of the present invention: described 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 water molecules; 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 water molecules by opposing electrode electrolysis more repeatedly, increase impurity and water molecules by the probability of opposing electrode electrolysis and quantity, thus improve the electrolytic efficiency of water.
Content six of the present invention: described 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 unit construction, the electrolysis of strengthening impurities in water and water molecules, improve the efficiency of water electrolysis, and can the effective low conductivity water such as electrolysis pure water and distilled water.
Content seven of the present invention: described 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 eight of the present invention: described electrolysis electrode assembly, the water exit of its place container designs narrower than water entry, suitably to slow down the flow velocity of the water flowing to electrolysis electrode gap, make more impurity and water molecules by the electrolysis more repeatedly of electric current between opposing electrode, increase impurity and water molecules, by the probability of opposing electrode electrolysis and quantity, improve the efficiency of water electrolysis.
Content nine of the present invention: described electrolysis electrode assembly, when the cell wall material and shape of wrapping up electrolysis electrode assembly fit cooperating electrode, suitably can connect it as electrolysis electrode, increase electrolysis electrode interval area, improve the electrolytic efficiency of water.
Content ten of the present invention: described electrolysis electrode assembly, is made up of the electrode of two opposed polarities, 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 electrolysis working process, 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: a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performances of the present invention, is characterized in that: comprise container filled with water, be placed in container filled with water without film electrolysis electrode assembly 1 and 2, controllable electrolysis power supply; Former water enters in container, respectively in the anodic-cathodic gap of electrolysis electrode assembly 1,2 by electrolysis; Controllable electrolysis power supply is powered to electrolysis electrode assembly 1,2, electrolysis electrode assembly one can change the acid-basicity of brine electrolysis, its two redox potential that can change brine electrolysis of electrolysis electrode assembly, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
One of concrete technical scheme: described electrolysis electrode assembly 1,2 and controllable electrolysis power supply, mode controllable electrolysis power supply can being taked to export two groups of voltages power respectively to electrolysis electrode assembly 1,2, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
Concrete technical scheme two: described electrolysis electrode assembly 1,2 and controllable electrolysis power supply, the anodic-cathodic of two groups of electrolysis electrode assemblies suitably can be connected in series, adopt controllable electrolysis power supply to export the mode of one group of electrolysis voltage to electrolysis electrode assembly 1,2 series-fed, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
Concrete technical scheme three: described container filled with water, can have water-in and water outlet; Former water enters in container from water-in, through the electrolysis of electrolysis electrode assembly; Brine electrolysis flows out from electrolyzer water outlet.
Concrete technical scheme four: described 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 water molecules; 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 water molecules by opposing electrode electrolysis more repeatedly, increase impurity and water molecules by the probability of opposing electrode electrolysis and quantity, thus improve the electrolytic efficiency of water.
Concrete technical scheme five: described 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 unit construction, the electrolysis of strengthening impurities in water and water molecules, improve the efficiency of water electrolysis, and can the effective low conductivity water such as electrolysis pure water and distilled water.
Concrete technical scheme six: described 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 seven: described electrolysis electrode assembly, the water exit of its place container designs narrower than water entry, suitably to slow down the flow velocity of the water flowing to electrolysis electrode gap, make more impurity and water molecules by the electrolysis more repeatedly of electric current between opposing electrode, increase impurity and water molecules, by the probability of opposing electrode electrolysis and quantity, improve the efficiency of water electrolysis.
Concrete technical scheme eight: described electrolysis electrode assembly, when the cell wall material and shape of wrapping up electrolysis electrode assembly fit cooperating electrode, suitably can connect it as electrolysis electrode, increase electrolysis electrode interval area, improve the electrolytic efficiency of water.
Concrete technical scheme nine: described electrolysis electrode assembly, is made up of the electrode of two opposed polarities, 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 electrolysis working process, 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.
Fig. 1 is that the embodiment of the present invention 1 one kinds adopts two groups of electrolysis electrode assemblies to control the new device of brine electrolysis performance
Fig. 2 is that the embodiment of the present invention 2 one kinds adopts two groups of electrolysis electrode assemblies to control the new device of brine electrolysis performance
Fig. 3 is that the embodiment of the present invention 3 one kinds adopts two groups of electrolysis electrode assemblies to control the new device of brine electrolysis performance
Fig. 4 is that the embodiment of the present invention 4 one kinds adopts two groups of electrolysis electrode assemblies to control the new device of brine electrolysis performance
Embodiment
Below in conjunction with embodiment 1 accompanying drawing 1 illustrated embodiments basic structure and basic functional principle.
Embodiment 1
As Fig. 1, a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance of the present invention, for the example of electrolysis nature stationary water, two groups that comprise brine electrolysis container, have the controllable electrolysis power supply 9 of two groups of power supplys outputs, can power respectively without film electrolysis electrode assembly 8 and 28,8 is similar to 28 structural shapes as can be seen from Fig. 1, therefore be all applicable to 28 about the description of electrolysis electrode assembly 8 internal structure and principle, brine electrolysis container has water-in 5, installing electrodes assembly 8 and 28 in 10, former water puts into brine electrolysis container from water-in 5; Two groups of out-put supplies of controllable electrolysis power supply 9 power to electrode assemblie 8,28 respectively by wire 6 and 7,26 and 27, wherein one group of electrolysis electrode assembly (8 or 28) can change the acid-basicity of brine electrolysis, another group electrolysis electrode assembly (28 or 8) can change the redox potential of brine electrolysis, thus realization is to the control of the brine electrolysis indexs such as the acid-basicity of brine electrolysis and redox potential.
The feature of the present embodiment 1 electrolysis electrode assembly 8 is: assembly is made up of two opposing electrodes 1,2, electrode 1 is bore shape (hereinafter referred is poroid), in figure, signal draws 3 holes, electrolysis power 9, for machinery is fixing, hole wall is electrically connected to each other and forms electrode 1, is connected by wire 7 in each hole site; Electrode 2 is column, and in figure, signal draws 3 posts, and each post position is fixed for machinery and is electrically connected to each other and forms electrode 2, connects electrolysis power 9 by wire 6; 1 and 2 may correspond to grafting, namely the post of columnar electrode 2 can insert in the corresponding aperture of poroid electrode 1, electrolysis gap 3 is left between post surface and hole surface, this gap in a tubular form, schematically depict 3 gaps 3 that 3 columnar electrodes and 3 poroid electrodes are formed in Fig. 1, gap clearance can optionally be selected within the specific limits, such as, be less than 5mm to the scope being greater than 0mm; If desired, the desirable smaller value of spacing in gap 3 i.e. reasonable littleization, as being less than 1mm to the scope being greater than 0mm, can the electrolysis effectiveness of fortified water and wherein impurity, during the former water such as this pure water needing electrolytic conductivity low at device, distilled water, higher brine electrolysis efficiency and index can be obtained; Under electrode gap distance one stable condition, impurity is directly proportional to interval area by the probability of electrolysis and quantity to water molecules, because reasonable largeizationr of this gap 3 area can improve electrolytic efficiency; In Fig. 1, assembly 8 cell wall is the material being applicable to doing electrolysis electrode use, is connected to the part that electrolysis power becomes electrode 2, forms electrolysis gap 4 with electrode 1, stiffening device electrolysis effectiveness via wire 7; Roughly the same, electrolysis gap 24 and 4 acts on also roughly the same electrolysis electrode assembly 28 and 8, not superfluous words.
In Fig. 1, 11 and 12, 25 and 29 bottoms being respectively electrode assemblie 8 or 28, upper space, have and make the effect that in each electrode gap, water can smoothly flow, in brine electrolysis process, water molecules in gap is by after electrolytic decomposition, hydrogen can be produced, oxygen bubbles is upwards elegant along gap, thus drive water in gap 3 (or 23) upwards to flow, flow out from gap 3 (or 23) upper port, water is caused to flow in a steady stream electrode gap 3 (or 23) from gap 3 (or 23) lower opening and space 11 (or 24), in container the water in other spaces can flow to 11 supplement, in the process that water flows in gap 3 (or 23), water impurity and water molecules can by Faradaic current electrolysis repeatedly in gap 3 (or 23), obviously, if 11,12 or 25,29 is too narrow, the mobility of water in electrode gap 3 (or 23) may be affected, the electrolytic efficiency of water can be reduced.
In sum, visible: the spacing that gap 3 (or 23) choose reasonable is less and larger area and in meeting gap 3 (or 23) water have certain circulation, the process technology scheme that these three aspects are coordinated to take into account can significantly improve electrolytic efficiency.
Table 1: embodiment 1 adopts two groups of electrolysis electrode assemblies to control the measured data of the made brine electrolysis of novel method of brine electrolysis performance
As seen from Table 1, acid-basicity pH value is 7.2, redox potential ORP is+378mv without the former water of hydrogen, through the inventive method embodiment 1 electrolysis 1 minute, making became weakly acidic, the brine electrolysis of high negative potential, high hydrogen richness, was the high-quality water that can use as beauty and skin care shower.
Table 2 is the measured data of made brine electrolysis after embodiment 1 device change table 1 liang group electrolysis electrode electrical component intensity of flow.
Table 2: embodiment 1 adopts two groups of electrolysis electrode assemblies to control the made brine electrolysis measured data of novel method of brine electrolysis performance
Visible: the Faradaic current (or electrolysis voltage, electrolysis power) changing two electrode assemblies, remarkable change can be there is in the acid-basicity of made brine electrolysis, pH value changes into 8.1 weakly alkalines of brine electrolysis from 7.0 neutrality of former water, also there is remarkable change in ORP and hydrogen richness, become weakly acidic, negative potential and all higher brine electrolysis of hydrogen richness, can be used as the high-quality tap water of antioxidant and anti-aging.Obviously, by the functional performance of change two electrode assemblie, the control to brine electrolysis acid-basicity and other brine electrolysis indexs can also be realized.
Embodiment 2
As Fig. 2, a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance of the present invention, for the example of the outer power-actuated flowing water of electrolysis, two groups that comprise electrolyzer 10, have the controllable electrolysis power supply 9 of two groups of power supplys outputs, can power respectively without film electrolysis electrode assembly 8 and 28,8 is similar to 28 structural shapes as seen from the figure, therefore be all applicable to 28 about the description of electrolysis electrode assembly 8 internal structure and principle, electrolyzer 10 has water-in 13 and water outlet 5,10 to be provided with electrolysis electrode assembly 8 and 28; Former water enters space 11 in electrolyzer 10 from water-in 13, and former water first passes through the electrode gap 3 of electrolysis electrode assembly 8 by electrolysis, then enters the electrode gap 23 of electrode assemblie 28 by electrolysis; Two groups of out-put supplies of controllable electrolysis power supply 9 power to electrode assemblie 8,28 respectively by wire 6 and 7,26 and 27, wherein one group of electrolysis electrode assembly (8 or 28) can change the acid-basicity of brine electrolysis, another group electrolysis electrode assembly (28 or 8) can change the redox potential of brine electrolysis, thus realizes the control to brine electrolysis indexs such as brine electrolysis acid-basicity and redox potentials; Brine electrolysis flows out from the water outlet 5 of electrolyzer.
The feature of the present embodiment 2 electrolysis electrode assembly 8 and 28 and embodiment 1 roughly the same, not superfluous words.Embodiment 1 difference of the present embodiment 2 device and electrolysis nature stationary water, be applied to electrolysis to flow into from container water-in 13, from the flowing water that water outlet 5 flows out, generally speaking, if the space 11 outside the port of gap 3, 12 or 25, 29 is enough open, just easily meet the circulation of water in gap, the noticeable another aspect problem that brine electrolysis efficiency on the contrary may be caused to reduce: if the flowing water flow velocity flowing into electrolyzer is too fast, water flows through the flow velocity of electrode gap also can be too fast, electrolytic efficiency may be reduced, therefore, when application of installation is in the flowing water that electrolysis flow velocity is too fast, can meet on device traffic demand basis, take the design suitably slowing down flow rate of water flow in electrolyzer, simpler scheme designs suitably narrower than water-in 13 by the water outlet 5 of electrolyzer 10, water is slowed down to some extent by the flow velocity of electrolyzer, the flow rate of water flow entering electrode gap like this can suitably slow down naturally thereupon, water time of electrolysis in gap is extended to some extent, thus strengthen the electrolysis effectiveness of water.
Table 3: embodiment 2 adopts two groups of electrolysis electrode assemblies to control the made brine electrolysis measured data of novel method of brine electrolysis performance
Note: 8,28 liang of group electrolysis electrode assembly Faradaic currents are 0.8A.
As seen from Table 3, acid-basicity pH value is 7.5, redox potential ORP is+421mv without the former water of hydrogen, make through the inventive method embodiment 1 device become weakly acidic, negative potential and all higher brine electrolysis of hydrogen richness, can be used as the high-quality water that beauty and skin care is had a bath.
Table 4 is the measured data of embodiment 1 device made brine electrolysis after changing in table 1 intensity that two groups of electrolysis electrode assemblies are energized respectively.
Table 4: embodiment 1 one kinds adopts two groups of electrolysis electrode assemblies to control the new device brine electrolysis measured data of brine electrolysis performance
Visible: the Faradaic current (or electrolysis voltage, electrolysis power) changing two electrode assemblies, remarkable change can be there is in the acid-basicity of made brine electrolysis, pH value changes into 7.8 weakly alkalines of brine electrolysis from 7.2 of former water, also there is remarkable change in ORP and hydrogen richness, become the brine electrolysis of weakly alkaline, high negative potential and high hydrogen content, can be used as the high-quality tap water of antioxidant and anti-aging.Obviously, by the functional performance of change two electrode assemblie, the control to brine electrolysis acid-basicity and other brine electrolysis indexs can also be realized.
Embodiment 1,2 experimental installation detected result sufficient proof: the present invention is a kind of control brine electrolysis acid-basicity without film brine electrolysis new process, there is feasibility and practicality, to the innovation without film brine electrolysis technology, for significant without film brine electrolysis technology popularization application.
Embodiment 3
As Fig. 3, a kind of one adopting two groups of electrolysis electrode assemblies to control the new device of brine electrolysis performance of the present invention simplifies control techniques scheme, distinguish from embodiment 1 and be only: the mode of connection without film electrolysis electrode assembly 8 and 28 and electrolysis power 9 is different, as seen from the figure 8 with 28 opposing electrodes be connected in series after be connected with two ports of electrolysis power 9 one groups of output voltages, specifically describe as follows: one of voltage output end mouth of 9 is connected to the poroid electrode 1 of 8 by wire 6, columnar electrode 2 is led to through 1 and the water (the electrolysis loads of 8) in the gap 3 of columnar electrode 2, the columnar electrode 22 of electrolysis electrode assembly 28 is connected to again via the wire 7 and 26 be connected with columnar electrode 2, poroid electrode 21 is connected to by 22 and the water (the electrolysis loads of 28) in the gap 23 of poroid electrode 21, the voltage output end mouth two of 9 is connected to again by wire 27 and 6.Visible, be not both with embodiment 1,2: 9 only export one group of electrolysis voltage, power to series connection electrolysis electrode load 8 and 28; Therefore the present embodiment controls brine electrolysis performance and embodiment 1,2 different, is under the control under same current, and by control brine electrolysis performances such as the characteristic of electrolysis electrode assembly 1,2 and voltages, control device and handiness are than embodiment 1,2 few.
Table 5: embodiment 3 adopts two groups of electrolysis electrode assemblies to control the made brine electrolysis measured data of novel method of brine electrolysis performance
As seen from Table 1, acid-basicity pH value is 7.2, redox potential ORP is+378mv without the former water of hydrogen, make through the inventive method embodiment 1 electrolysis 1 minute become weakly acidic, the brine electrolysis of high negative potential, high hydrogen richness, be can to take a shower the high-quality water used as beauty and skin care.
Embodiment 4
As Fig. 4, a kind of experimental installation adopting two groups of electrolysis electrode assemblies to control the new device of brine electrolysis performance of the present invention, with the difference with natural stationary water in embodiment 3 electrolytic vessel, that container 10 adds water-in 13,5 is water outlet, device can be used for electrolyte flow water, and former water from container water-in 13 flows into, brine electrolysis flows out from water outlet 5.The present embodiment, for the too fast problem that may reduce electrolytic efficiency of flowing water flow velocity flowing into container, can be taked and the flow rate of water flow design slowed down described in embodiment 2 by electrolysis electrode assembly, strengthens the electrolysis effectiveness of water.
Table 6: embodiment 2 adopts two groups of electrolysis electrode assemblies to control the measured data of the made brine electrolysis of novel method of brine electrolysis performance
As seen from Table 6, acid-basicity pH value is 7.5, redox potential ORP is+421mv without the former water of hydrogen, make through the inventive method embodiment 1 device become weakly acidic, negative potential and all higher brine electrolysis of hydrogen richness, can be used as the high-quality water that beauty and skin care is had a bath.
A kind of electrolysis electrode assembly adopting two groups of electrolysis electrode assemblies to control the new device of brine electrolysis performances of the present invention is not limited to the concrete apparatus structure using embodiment 1-4 to adopt, can use in principle any kind realize basic skills of the present invention without film electrolytic water device structure.
Claims (10)
1. adopt two groups of electrolysis electrode assemblies to control a new device for brine electrolysis performances, it is characterized in that: comprise container filled with water, be placed in container filled with water without film electrolysis electrode assembly 1 and 2, controllable electrolysis power supply; Former water enters in container, respectively in the anodic-cathodic gap of electrolysis electrode assembly 1,2 by electrolysis; Controllable electrolysis power supply is powered to electrolysis electrode assembly 1,2, electrolysis electrode assembly one can change the acid-basicity of brine electrolysis, its two redox potential that can change brine electrolysis of electrolysis electrode assembly, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
2. a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance according to claim 1, it is characterized in that: described electrolysis electrode assembly 1,2 and controllable electrolysis power supply, mode controllable electrolysis power supply can being taked to export two groups of voltages power respectively to electrolysis electrode assembly 1,2, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
3. a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance according to claim 1, it is characterized in that: described electrolysis electrode assembly 1,2 and controllable electrolysis power supply, the anodic-cathodic of two groups of electrolysis electrode assemblies suitably can be connected in series, adopt controllable electrolysis power supply to export the mode of one group of electrolysis voltage to electrolysis electrode assembly 1,2 series-fed, two groups of electrolysis electrode assemblies realize the Comprehensive Control to brine electrolysis performance jointly.
4. a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance according to claim 1, is characterized in that: described container filled with water, can have water-in and water outlet; Former water enters in container from water-in, through the electrolysis of electrolysis electrode assembly; Brine electrolysis flows out from electrolyzer water outlet.
5. a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance according to claim 1, it is characterized in that: described 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 water molecules; 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 water molecules by opposing electrode electrolysis more repeatedly, increase impurity and water molecules by the probability of opposing electrode electrolysis and quantity, thus improve the electrolytic efficiency of water.
6. a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance according to claim 1, it is characterized in that: described electrolysis electrode assembly, spacing between electrolysis electrode assembly opposing electrode is little of 1mm or less, to be comparatively beneficial under certain electrolysis power and certain electrolysis electrode unit construction, the electrolysis of strengthening impurities in water and water molecules, improve the efficiency of water electrolysis, and can effectively electrolysis pure water and distilled water low conductivity water.
7. a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance according to claim 1, it is characterized in that: described 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.
8. a kind of adopt two groups of electrolysis electrode assemblies to control the new device of brine electrolysis performance according to claim 1 with according to claim 4, it is characterized in that: described electrolysis electrode assembly, the water exit of its place container designs narrower than water entry, suitably to slow down the flow velocity of the water flowing to electrolysis electrode gap, make more impurity and water molecules by the electrolysis more repeatedly of electric current between opposing electrode, increase impurity and water molecules, by the probability of opposing electrode electrolysis and quantity, improve the efficiency of water electrolysis.
9. a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance according to claim 1, it is characterized in that: described 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.
10. a kind of new device adopting two groups of electrolysis electrode assemblies to control brine electrolysis performance according to claim 1, it is characterized in that: described electrolysis electrode assembly, be made up of the electrode of two opposed polarities, 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 electrolysis working process, 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.
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