CN202186912U - Integral system for generating acidic electrolyzed-oxidizing water - Google Patents
Integral system for generating acidic electrolyzed-oxidizing water Download PDFInfo
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- CN202186912U CN202186912U CN2011202640926U CN201120264092U CN202186912U CN 202186912 U CN202186912 U CN 202186912U CN 2011202640926 U CN2011202640926 U CN 2011202640926U CN 201120264092 U CN201120264092 U CN 201120264092U CN 202186912 U CN202186912 U CN 202186912U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 278
- 230000002378 acidificating effect Effects 0.000 title abstract description 16
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 66
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 47
- 238000002360 preparation method Methods 0.000 claims abstract description 46
- 239000002351 wastewater Substances 0.000 claims abstract description 8
- 238000004891 communication Methods 0.000 claims abstract description 6
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- 239000012528 membrane Substances 0.000 claims description 22
- 238000007789 sealing Methods 0.000 claims description 8
- 239000008213 purified water Substances 0.000 abstract 3
- 210000004027 cell Anatomy 0.000 description 40
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- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 3
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- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
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Abstract
An integral system for generating acidic electrolyzed-oxidizing water comprises a water purifying unit, an RO purified water unit, an electrolytic agent preparation and feed unit, and an electrolysis unit which are connected with one another through pipelines in sequence, wherein each of the units is provided with a sensor; an electromagnetic valve is arranged between each two adjacent units; the integral system further comprises a pollution discharge unit and a control unit; the pollution discharge unit is connected with the water purifying unit, the RO purified water unit, the electrolytic agent preparation and feed unit, and the electrolysis unit through pipelines respectively; and a water draining electromagnetic valve is arranged on each pipeline connected with the pollution discharge unit; the control unit is kept in communication connection with the water purifying unit, the RO purified water unit, the electrolytic agent preparation and feed unit, the electrolysis unit, each electromagnetic valve and each sensor, and controls the opening and the closing of the electromagnetic valve; and when the result detected by the sensors in the units does not meet the requirements, the control unit opens the water draining electromagnetic valves corresponding to the units, so as to discharge waste water into the pollution discharge unit.
Description
Technical field
The utility model relates to a kind of preparation field of acidic oxidized electric potential water, relates to electrolyzed oxidizing water generation system especially.
Background technology
Acidic oxidized electric potential water (Electrolyzed Oxidizing Water; EOW) be that ordinary tap water is added little sodium chloride solution process electrode and special ion exchanges membranous electrolytic tank electrolysis; Produce in positive electrode one side; The increase of H+ concentration is acid in its water, and pH value can be less than 2.7, the redox potential value can be strong oxidizing property, contain O in the water simultaneously greater than+1100mv
3, Cl
2With HClO etc., this glassware for drinking water has the broad-spectrum sterilization effect, is widely used in various disinfections field.Acidic oxidized electric potential water can be reduced to ortho-water after placing for some time, is a kind of cleaning and sterilization water of very environmental protection, and therefore, the application electrolyzed oxidizing water pollutes, reduces the Pollution abatement cost to reducing also have positive effect.
But existing at present acidic oxidized electric potential water draft machine adapts to the water source narrow range, and the electrolyzer part life-span is short, the preparation that has seriously restricted acidic oxidized electric potential water with promote the use of.
The utility model content
Adapt to the water source narrow range in order to overcome existing acidic oxidized electric potential water draft machine, the electrolyzer part life-span is short, and the utility model specially designed has been developed a kind of monobloc(k)type electrolyzed oxidizing water generation system.
The inner integrated water purification of the monobloc(k)type electrolyzed oxidizing water generation system of the utility model unit, pure water unit, electrolytic agent preparation and feed unit, electrolysis cells, control unit; The co-ordination of control unit control water purification unit, pure water unit, electrolytic agent preparation and feed unit, electrolysis cells; Make and produce water efficient height, oxidizing potential water quality stabilizing.Because the monobloc(k)type electrolyzed oxidizing water generation system of the utility model is inner integrated water purification unit and pure water unit makes native system can adapt to water source more widely.
An aspect according to the utility model; A kind of monobloc(k)type electrolyzed oxidizing water generation system is provided; It is characterized in that comprising: water purification unit, RO pure water unit, electrolytic agent preparation and the feed unit, the electrolysis cells that connect in order through pipeline; In each unit of water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells, be respectively arranged with transmitter, and between water purification unit and RO pure water unit, RO pure water unit and electrolytic agent preparation and feed unit, electrolytic agent preparation and feed unit and electrolysis cells, be respectively arranged with SV; Blowdown unit, blowdown unit are connected through pipeline, and on each connecting pipeline, are respectively arranged with drain solenoid valve with water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells respectively; Control unit; Be connected with keeping communication between water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells, each SV and each transmitter; Control unit detects each unitary working order; Receive the signal of each transmitter, and control the switch of each SV; Said water purification unit is provided with former water inlet end, and has the feed-water end SV, and said electrolysis cells has sour water outlet valve and alkaline water outlet valve.
According to an aspect of the utility model, when the result of the sensor detecting in each unit was undesirable, said control unit was opened the corresponding drain solenoid valve in each unit, and waste water is entered the blowdown unit.
According to an aspect of the utility model, be provided with the water pressure invariableness device at said former water inlet end.
According to an aspect of the utility model, this system also has sour water liquid-storing box and alkaline water liquid-storing box, and said sour water outlet valve and alkaline water outlet valve are separately positioned on sour water liquid-storing box and alkaline water liquid-storing box water outlet place separately.
According to another aspect of the utility model, said electrolysis cells comprises electrolyzer, and this electrolyzer comprises: upper housing and lower housing, upper housing and lower housing combine the back to form the cell vessel of sealing; One or more electrolyzer water inlets and two electrolyzer water outlets; Be arranged alternately at electrolyzer inner battery lead plate and electrode plate assembly; Wherein electrode plate assembly comprises the overlay film framework and is arranged on the intravital battery lead plate of overlay film frame; The tow sides of the overlay film framework of electrode plate assembly have ionic membrane; Overlay film framework inside and outside as different electrode districts; The overlay film framework of electrode plate assembly is provided with framework water inlet and framework water outlet, and the framework water inlet is communicated with the electrolyzer water inlet, and the framework water outlet is communicated with a water outlet of electrolyzer; And wherein every plate electrode plate has electrode contact, is connected with outside electrolysis power through the electrode perforations that is arranged on the electrolyzer.
Another aspect according to the utility model; Said overlay film framework is made up of four frameworks and two ionic membranes; In the middle of two frameworks the front baffle that a slice ionic membrane forms the overlay film framework is set; In the middle of two frameworks the rear frame that a slice ionic membrane forms the overlay film framework is set in addition, in the middle of the framework of front and back battery lead plate is set and is joined together to form electrode plate assembly then.
Determine the life-span that principal element is a battery lead plate of bath life.The front and back framework of the utility model is detachable the installation, therefore is convenient to clean or change the inner battery lead plate of overlay film framework, can prolong the work-ing life of electrolyzer thus.
According to another aspect of the utility model, the spacing of the battery lead plate that the overlay film framework of said electrode plate assembly is inside and outside is made as 2-8mm.This distance can guarantee good electrolysis effectiveness.In addition, the front baffle of said overlay film framework is formed with many parallel separated ribs respectively with the rear frame tow sides, and said spacing at a distance from rib and battery lead plate is set in the 0.6mm.
The utility model has been equivalent to increase the area of battery lead plate through in an electrolyzer, the multi-group electrode plate being set, and can improve the output of brine electrolysis.
Description of drawings
Other feature and advantage according to method and apparatus of the present disclosure will appear in the following accompanying drawing of incorporating this paper into and the detailed description of hereinafter to the utility model or illustrate, accompanying drawing and the detailed description of the utility model is used to explain jointly the certain principles of the utility model.
Fig. 1 is the schematic diagram according to the monobloc(k)type electrolyzed oxidizing water generation system of an embodiment of the utility model;
Fig. 2 is the front view according to the electrolyzer after the assembling of an embodiment of the utility model;
Fig. 3 is the sectional view along the electrolyzer section line A-A among Fig. 2;
Fig. 4 is the diagrammatic cross-section of electrode plate assembly and battery lead plate combination.
Description of reference numerals
Water purification unit 1, RO pure water unit 2, electrolytic agent preparation and feed unit 3, electrolysis cells 4, control unit 5, blowdown unit 6, feed-water end SV 7, SV 8, SV 9, SV 10, water side SV 11, drain solenoid valve 12, drain solenoid valve 13, drain solenoid valve 14, drain solenoid valve 15; Electrolyzer 100; Upper housing 101; Lower housing 102; Battery lead plate 103; Electrode plate assembly 104; Battery lead plate 104 '; Electrolyzer water outlet 105,106; Electrolyzer water inlet 107,108; Electrode contact 109,110; Ionic membrane 123; Framework 124,125,126,127; At a distance from rib 128.
Embodiment
Below will be in detail with reference to each embodiment of the utility model, its example is presented in accompanying drawing and the hereinafter description.Although described the utility model, should be appreciated that this specification sheets is not intended to the utility model is limited to these exemplary embodiments in conjunction with exemplary embodiment.On the contrary, the utility model not only is intended to cover these exemplary embodiments, and covers essence and the various surrogates in the scope, modification, Equivalent and other embodiment that is included in the utility model that is limited appended claims.
A kind of embodiment according to the utility model; A kind of monobloc(k)type electrolyzed oxidizing water generation system is provided; Comprise: water purification unit, RO pure water unit, electrolytic agent preparation and the feed unit, the electrolysis cells that connect in order through pipeline; In each unit of water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells, be respectively arranged with transmitter, and between water purification unit and RO pure water unit, RO pure water unit and electrolytic agent preparation and feed unit, electrolytic agent preparation and feed unit and electrolysis cells, be respectively arranged with SV; Blowdown unit, blowdown unit are connected through pipeline, and on each connecting pipeline, are respectively arranged with drain solenoid valve with water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells respectively; Control unit; Be connected with keeping communication between water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells, each SV and each transmitter; Control unit detects each unitary working order; Receive the signal of each transmitter, and control the switch of each SV.Said water purification unit is provided with former water inlet end, and has the feed-water end SV, and said electrolysis cells has sour water outlet valve and alkaline water outlet valve.When the result of the sensor detecting in each unit was undesirable, said control unit was opened the corresponding drain solenoid valve in each unit, and waste water is entered the blowdown unit.
With reference to Fig. 1 the monobloc(k)type electrolyzed oxidizing water generation system according to an embodiment of the utility model is described.
Monobloc(k)type electrolyzed oxidizing water generation system (hereinafter to be referred as system) comprises water purification unit 1, RO (Reverses Osmosis, r-o-) pure water unit 2, electrolytic agent preparation and feed unit 3, electrolysis cells 4, control unit 5, blowdown unit 6.As shown in Figure 1; Water purification unit 1, RO pure water unit 2, electrolytic agent preparation and feed unit 3, electrolysis cells 4 connect successively; And each unit is connected with blowdown unit 6 respectively, and water purification unit 1, RO pure water unit 2, electrolytic agent preparation and feed unit 3, electrolysis cells 4 are provided with drain solenoid valve with each pipeline that blowdown unit 6 is connected respectively.Be respectively arranged with SV between former and later two unit of water purification unit 1, RO pure water unit 2, electrolytic agent preparation and feed unit 3 and electrolysis cells 4.Keep communicating by letter between control unit 5 and water purification unit 1, RO pure water unit 2, electrolytic agent preparation and feed unit 3, electrolysis cells 4 and each SV; Control section 5 detects the state of water purification unit 1, RO pure water unit 2, electrolytic agent preparation and feed unit 3, electrolysis cells 4, and each SV of initialize.
Water purification unit 1 can adopt the cotton filtration of PP, hollow fiber ultrafiltration membrane, the contaminant particles that is used for filtering former water.Alternatively, also can adopt known other water purification unit, basic field.Former water (for example being the municipal tap water) from former water inlet connecting system at first gets into water purification unit 1 and purifies, and after hydraulic pressure and water quality are qualified, is admitted to RO pure water unit 2.
The principle of RO pure water unit 2 is to apply greater than seepage water pressure at former water one end; And the generation counter osmosis; Dissolving this moment can't see through semi-permeable membranes with non-dissolve inorganic salts, heavy metal, organism thalli granule etc.; Make water molecules reach salt infiltrate semi-permeable membranes, flow to water purifying on one side, and pollutant component concentrates in former water than small molecules.Be that condensed water (waste water) is drained when actually operating, continue to infeed former water, to keep constant pressure.The deionized pure water that obtains through RO pure water unit 2 is admitted to electrolytic agent preparation and feed unit 3 after hydraulic pressure and water quality are qualified.
Electrolytic agent preparation and feed unit 3; Through water purification unit 1 and RO pure water unit 2 filter and softening after former water send into electrolytic agent preparation and feed unit 3 through pipeline; Mix the electrolytic agent solution that the back forms desired concn with electrolytic agent, supply with electrolysis cells 4 through pipeline.
Be provided with the ion diaphragm of separating anode and cathodic area in electrolysis cells 4 comprises, and the closed electrolysis groove of import and export is arranged.Cell body, anodic-cathodic and ion diaphragm have erosion resistance to electrolysate, and do not have leachable.Electrolytic agent solution by electrolysis, has a high redox potential from what anode electrolytic cell one adnation became in electrolysis cells 4, the acidic aqueous solution of lower concentration available chlorine, the alkaline aqueous solution of the negative redox potential that becomes from electrolyzer inner cathode one adnation.Electrolysis cells 4 has the brine electrolysis outlet, separates to sour water and alkaline water.The monobloc(k)type electrolyzed oxidizing water generation system of the utility model can also be provided with sour water liquid-storing box and alkaline water liquid-storing box respectively, is used to store sour water and the alkaline water that electrolysis generates.
Former water inlet end is provided with feed-water end SV 7; Be provided with SV 8 between water purification unit 1 and the RO pure water unit 2; Be provided with SV 9 between RO pure water unit 2 and electrolytic agent preparation and the feed unit 3; Be provided with SV 10 between electrolytic agent preparation and feed unit 3 and the electrolysis cells 4, electrolysis cells 4 has water side SV 11 (can comprise sour water outlet valve and alkaline water outlet valve).Be provided with drain solenoid valve 12 between water purification unit 1 and the blowdown unit 6; Be provided with drain solenoid valve 13 between RO pure water unit 2 and the blowdown unit 6; Be provided with drain solenoid valve 14 between electrolytic agent preparation and feed unit 3 and the blowdown unit 6, be provided with drain solenoid valve 15 between electrolysis cells 4 and the blowdown unit 6.
Be respectively arranged with the transmitter that is used to detect hydraulic pressure and/or water quality in water purification unit 1, RO pure water unit 2, electrolytic agent preparation and feed unit 3 and the electrolysis cells 4, each transmitter is communicated by letter with control unit 5.The monobloc(k)type electrolyzed oxidizing water generation system of the utility model can also comprise pressure pump or constant pressure arrangement, keeps the constant pressure of former water.For example, at former water water intake end the water pressure invariableness device is set.Those skilled in the art can select and be provided with the above-mentioned detection hydraulic pressure and/or the transmitter of water quality as required, and the water pressure invariableness device.
According to a specific embodiment, behind the system boot, control unit 5 at first detects the state of water purification unit 1, RO pure water unit 2, electrolytic agent preparation and feed unit 3 and electrolysis cells 4, and each SV of initialize and transmitter.After treating that operator press job key; Open feed-water end SV 7, the municipal tap water reaches sterilized water after filtering through water purification unit 1 (PP is cotton to filter hollow fiber ultrafiltration membrane); After control unit 5 detection hydraulic pressure and water quality are qualified; Open the SV 8 of the feed-water end of RO pure water unit 2, if water quality is defective, the drain solenoid valve 12 of opening water purification unit 1 enters blowdown unit 6 with waste water.Obtaining deionized pure water through RO pure water unit 2; After control unit 5 detection hydraulic pressure and water quality are qualified; Open the SV 9 of the feed-water end of electrolytic agent preparation and feed unit 3, if water quality is defective, the drain solenoid valve 13 of opening RO pure water unit 2 enters blowdown unit 6 with waste water.Former water after electrolytic agent preparation and feed unit 3 will filter and soften mixes with saturated aqueous common salt; After control unit 5 mixed electrolytic agent strength of solution of detection and uniformity coefficient are qualified; Open the SV 10 of the feed-water end of electrolysis cells 4; If water quality is defective, open the drain solenoid valve 14 of electrolytic agent preparation and feed unit 3, waste water is entered blowdown unit 6.Electrolytic agent solution forms acidic oxidized electric potential water through electrolysis cells 4 electrolysis, accomplishes the preparation of acidic oxidized electric potential water.
Integrated water purification unit 1 and RO pure water unit 2 in the monobloc(k)type electrolyzed oxidizing water generation system of the utility model, the system that makes can adapt to former comparatively widely water.In addition; Between the water purification unit 1 that is linked in sequence, RO pure water unit 2, electrolytic agent preparation and feed unit 3 and electrolysis cells 4, be respectively arranged with SV; Between each unit and blowdown unit 6, drain solenoid valve is set; And in each unit, be respectively arranged with the transmitter that is used to detect hydraulic pressure and/or water quality; Make it possible to accurately control and have only standard compliant water could get into next unit, underproof water can discharge through blowdown unit 6 automatically, has guaranteed that thus the brine electrolysis of preparation meets the requirements all the time.
According to the another kind of embodiment of the utility model, the electrolyzer of electrolysis cells comprises: upper housing and lower housing; One or more electrolyzer water inlets; Two electrolyzer water outlets are respectively as sour water water outlet and alkaline water water outlet; Be arranged alternately at electrolyzer inner battery lead plate and electrode plate assembly; Wherein electrode plate assembly comprises the overlay film framework and is arranged on the intravital battery lead plate of overlay film frame; The tow sides of the overlay film framework of electrode plate assembly have ionic membrane; Can be used as different electrode districts inside and outside the overlay film framework; The overlay film framework of electrode plate assembly is provided with framework water inlet and framework water outlet, and the framework water inlet is communicated with the electrolyzer water inlet, and the framework water outlet is communicated with a water outlet of electrolyzer; Wherein every plate electrode plate has electrode contact, is connected with outside electrolysis power through the electrode perforations that is arranged on the electrolyzer.Said upper housing and lower housing can be respectively U type grooves, and the shape and size of the opening portion of U type groove are identical, in conjunction with the time can form the cell vessel of sealing.
Alternatively; The overlay film framework can be made up of four frameworks and two ionic membranes; In the middle of two frameworks the front baffle that a slice ionic membrane forms the overlay film framework is set; In the middle of two frameworks the rear frame that a slice ionic membrane forms the overlay film framework is set in addition, in the middle of the framework of front and back battery lead plate is set and is joined together to form electrode plate assembly then.The front and back framework is detachable the installation, therefore is convenient to clean or change the inner battery lead plate of overlay film framework, can prolong the work-ing life of electrolyzer thus.
Alternatively, the spacing of the battery lead plate that the overlay film framework of said electrode plate assembly is inside and outside is made as 2-8mm, can guarantee good electrolysis effectiveness.
Fig. 2 is the front view according to the electrolyzer after the assembling of an embodiment of the utility model; Fig. 3 is the sectional view along the electrolyzer section line A-A among Fig. 2.Further describe the embodiment of the electrolyzer of the utility model with reference to the accompanying drawings.
The electrolyzer 100 of electrolysis cells 4 comprises: upper housing 101 and lower housing 102; Upper housing 101 is respectively the U type groove structure with lower housing 102; The shape and size of the opening portion of U type groove are identical, make upper housing 101 and lower housing 102 when opening portion docks, can form the electrolyzer 100 of sealing.Electrolyzer 100 can be at set inside multi-disc battery lead plate 103 and electrode plate assembly 104, and the sealing of electrolyzer 100 is accomplished by the housing of electrolyzer, and is irrelevant with the structure of battery lead plate 103 and electrode plate assembly 104.
Periphery at electrolyzer upper housing 101 and lower housing 102 butted parts forms a plurality of perforation, uses coupling device to pass fastening upper housing 101 of perforation and lower housing 102.According to an embodiment,, can between upper housing 101 and lower housing 102, sealring be set for better sealed electrolytic cell.Preferably, can form the sealing groove of circumference type, sealing-ring is set in groove at the butted part of upper housing 101 or lower housing 102 (present embodiment is at lower housing 102).
The internal space of the electrolyzer 100 of present embodiment is roughly rectangular shape; But the interior shape of electrolyzer 100 and space are not limited to the shape shown in the figure in the practical application, and depend primarily on shape, size and the quantity of inner set battery lead plate 103 and electrode plate assembly 104.For example; Shape is roughly rectangular parallelepiped owing to multi-disc battery lead plate in the present embodiment 103 and electrode plate assembly 104 are arranged alternately in together; Therefore the internal space of the electrolyzer 100 of hold electrodes plate 103 and electrode plate assembly 104 also is roughly rectangular shape; And the overall volume after the internal capacity of electrolyzer 100 and battery lead plate 103 are provided with electrode plate assembly 104 is roughly the same, therefore can the most effectively utilize the volume of electrolyzer.
According to present embodiment, as shown in Figure 2, electrolyzer 100 end in the vertical has two shell nozzles as electrolyzer water outlet 105 and 106, the other end in the vertical have two shell nozzles as electrolyzer water inlet 107 and 108. Electrolyzer water outlet 105 and 106 is respectively sour water water outlet and alkaline water water outlet, and the water outlet that is communicated with the anode electrode plate electrolyte space is as the sour water water outlet, and the water outlet that is communicated with the cathode electrode plate electrolyte space is as the alkaline water water outlet.
Shown in Figure 2 only is a kind of embodiment, also one or more electrolyzer water inlet can only be set.For example, a water inlet can only be set, the runner hole entering electrolyzer inside of water through being communicated with in the runner that is communicated with water inlet and runner and the electrolyzer.In addition, get into the electrolyzer inner even laminar flow of current, pressure-stabilisation, also two or more water inlets can be set, make water evenly get into electrolyzer inside in order to make.
Two ends on electrolyzer water inlet in the present embodiment and water outlet are separately positioned on vertically can make the length direction of the battery lead plate that water flows through therefore can make that electrolysis time is longer in electrolyzer.
With reference to Fig. 3 and 4, shown the inner case after electrolyzer 100 assemblings are accomplished.Fig. 3 has shown that multi-disc battery lead plate 103 and multi-disc electrode plate assembly 104 replace the synoptic diagram of arranging setting in electrolyzer 100 housings, and Fig. 4 is the diagrammatic cross-section (drawing according to the electrode plate assembly and the battery lead plate number of reality) of electrode plate assembly and battery lead plate combination.
In the present embodiment, 5 plate electrode plates 103 and 4 plate electrode board components 104 in electrolyzer 100, have alternately been arranged.Being respectively battery lead plate 103, electrode plate assembly 104 from left to right, by that analogy, is battery lead plate 103 at last.In the present embodiment, the battery lead plate 104 ' in the electrode plate assembly 104 is used as negative electrode, is used for electrolysis and generates alkaline reduction current potential water, and battery lead plate 103 is used as anode, is used for electrolysis and generates acidic oxidized electric potential water.Because therefore the quantity of anode electrode plate increased the area of anode electrode plate more than the quantity of cathode electrode plate in the present embodiment, improved the electrolytic efficiency of acidic oxidized electric potential water.The utility model is not limited to be provided with the situation of 5 plate electrode plates 103 and 4 plate electrode board components 104; The battery lead plate 103 and electrode plate assembly 104 of other quantity also can be set; And the quantity of battery lead plate 103 and electrode plate assembly 104 also can be the quantity of the quantity of electrode plate assembly 104 more than battery lead plate 103; Also can be that quantity is identical, depend on actual applicable cases.On the other hand, battery lead plate 104 ' also can be used as anode, and battery lead plate 103 is used as negative electrode accordingly, and this need can realize the electrode reversal connection of power supply, so can realize the water outlet conversion of acidic oxidized electric potential water and alkaline reduction current potential water.
In the present embodiment, electrode contact 109 is connected with battery lead plate 103 conductions, and electrode contact 110 is connected with battery lead plate 104 ' conduction.Through conducting strip all electrode contacts 109 are connected to positive source, all electrode contacts 110 are connected to power cathode through conducting strip.
Because the alkaline reduction current potential moisture that need the acidic oxidized electric potential water and the catholyte of anode electrolysis generation be generated separates, and therefore need in electrolyzer 100, with ionic membrane positive column and cathodic area be separated.Through electrode plate assembly 104 positive column and cathodic area are separated in the present embodiment.Electrode plate assembly 104 comprises the overlay film framework and is arranged on the inner battery lead plate 104 ' of overlay film framework, and the tow sides of overlay film framework have ionic membrane 123, and battery lead plate 104 ' is arranged in the overlay film framework.The separation of overlay film framework makes that acidic oxidized electric potential water and alkaline reduction current potential water are to separate mobile in electrolyzer 100.
Alternatively; The overlay film framework of electrode plate assembly 104 also can have the framework runner (not shown) that is communicated with the framework water inlet; The framework runner is through the internal communication of hole and overlay film framework, so water gets into the framework runner from the framework water inlet, the entering framework inside, hole that is provided with from the longshore current road then; The overlay film framework of electrode plate assembly 104 is flowed out afterwards by electrolysis in the surface of flowing through battery lead plate 104 ' from the framework water outlet.In addition alternatively; The overlay film framework of electrode plate assembly 104 also can have the framework runner (not shown) that is communicated with the framework water outlet; This framework runner is provided with a plurality of and hole overlay film framework internal communication, even this framework runner can be the runner that does not seal, and in the face of the inner position of framework an opening is set at it; Be used to compile the liquid that produces after the electrolysis, make things convenient for the inner liquid of overlay film framework to flow out.
As can beappreciated from fig. 4, each electrode plate assembly 104 comprises the overlay film framework that is made up of four frameworks 124,125,126,127 and ionic membrane 123 and is arranged on the intravital battery lead plate 104 ' of overlay film frame.At framework 124 and the framework 125 middle ionic membranes 123 that are provided with, then framework 124 and framework 125 are joined together to form the front baffle of electrode plate assembly 104.At framework 126 and the framework 127 middle ionic membranes 123 that are provided with, then framework 126 and framework 127 are joined together to form the rear frame of electrode plate assembly 104.Then battery lead plate 104 ' is arranged in the middle of the front and back framework of electrode plate assembly 104, the front and back framework of electrode plate assembly 104 is docking together forms electrode plate assembly 104.Being connected of the front baffle of electrode plate assembly 104 and rear frame can be fixed, can link together through modes such as bonding, welding, welding, adopts the mode of ultrasonic welding to weld together in the present embodiment.
Alternatively, the front baffle of electrode plate assembly 104 connects together with rear frame removably, has made things convenient for thus to clean internal electrical pole plate 104 ' in the future.For the ease of connecting, can form projection and groove respectively at the front baffle of electrode plate assembly 104 and the butted part of rear frame, the mode through projection and groove clamping links together.And the mode of projection and groove clamping also can improve sealing effectiveness, makes the inside of electrode plate assembly 104 form enclosed space.Alternatively, in order to strengthen sealing effectiveness, sealring can be set in groove.Other connection means known in the art that can satisfy basic seal request also can be used for being connected of front baffle and rear frame.
5 plate electrode plates 103 and 4 plate electrode board components 104 are arranged alternately in together, adjacent setting between battery lead plate 103 and the electrode plate assembly 104.In the present embodiment, the spacing of battery lead plate 103 and battery lead plate 104 ' is made as 2-8mm, is preferably 3-5mm.The overlay film framework of electrode plate assembly 104 and the spacing of battery lead plate 103 are set to be preferably 0.1mm-0.3mm in the 0.6mm.Spacing between the overlay film framework of electrode plate assembly 104 and the intravital battery lead plate 104 ' of frame is set to be preferably 0.1mm-0.3mm in the 0.6mm.If it is too tight that battery lead plate 103 or 104 ' contacts with framework, then influence heat radiation, but hypertelorism then can not well play the effect of water conservancy diversion, can not make the good presentation layer stream mode of the current that flow through electrode plate surface.
Framework 124,125,126,127 has a plurality of at a distance from rib 128 respectively; A plurality of separated rib 128 on each framework laterally arranges; The position of the separated rib 128 of each framework is corresponding, so the front baffle of electrode plate assembly 104 and rear frame all have separated rib 128 at tow sides.Separated rib 128 and battery lead plate 104 ' adjacent setting that the overlay film framework of electrode plate assembly 104 is inner, the spacing in the present embodiment between rib 128 and battery lead plate 104 ' is set to be preferably 0.1mm-0.3mm in the 0.6mm.The separated rib 128 and the battery lead plate 103 adjacent settings of the overlay film framework outside surface of electrode plate assembly 104, the separated rib 128 of overlay film framework is set to be preferably 0.1mm-0.3mm in the 0.6mm with the spacing of battery lead plate 103 in the present embodiment.Through make the current presentation layer stream mode that flows through battery lead plate 103 and 104 ' surface at a distance from rib 128.At a distance from the effect of rib 128 mainly is guiding water the flowing of battery lead plate 103 and 104 ' surface, and makes the basic presentation layer stream mode of current that electrolyzer 100 is interior, and whole electrolytic process is more even.
Preceding text have presented the certain exemplary embodiments of the utility model in order to describe and purpose of description.These exemplary embodiments and non exhaustive, or the utility model is restricted to disclosed precise forms, significantly, according to many modifications of above-mentioned teaching with to change all be feasible.Selecting and describing these exemplary embodiments is certain principles and practical application thereof in order to explain the utility model, thereby those skilled in the art are made and uses each exemplary embodiment of the utility model, and various surrogate and modification.In fact the scope of the utility model is limited appending claims and Equivalent thereof.
Claims (8)
1. monobloc(k)type electrolyzed oxidizing water generation system is characterized in that comprising:
Water purification unit, RO pure water unit, electrolytic agent preparation and the feed unit, the electrolysis cells that connect in order through pipeline; In each unit of water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells, be respectively arranged with transmitter, and between water purification unit and RO pure water unit, RO pure water unit and electrolytic agent preparation and feed unit, electrolytic agent preparation and feed unit and electrolysis cells, be respectively arranged with SV;
Blowdown unit, blowdown unit are connected through pipeline, and on each connecting pipeline, are respectively arranged with drain solenoid valve with water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells respectively;
Control unit; Be connected with keeping communication between water purification unit, RO pure water unit, electrolytic agent preparation and feed unit, electrolysis cells, each SV and each transmitter; Control unit detects each unitary working order; Receive the signal of each transmitter, and control the switch of each SV;
Said water purification unit is provided with former water inlet end, and has the feed-water end SV, and said electrolysis cells has sour water outlet valve and alkaline water outlet valve.
2. monobloc(k)type electrolyzed oxidizing water generation system as claimed in claim 1; It is characterized in that; When the result of the sensor detecting in each unit was undesirable, said control unit was opened the corresponding drain solenoid valve in each unit, and waste water is entered the blowdown unit.
3. according to claim 1 or claim 2 monobloc(k)type electrolyzed oxidizing water generation system is characterized in that, is provided with the water pressure invariableness device at said former water inlet end.
4. according to claim 1 or claim 2 monobloc(k)type electrolyzed oxidizing water generation system; It is characterized in that; Also have sour water liquid-storing box and alkaline water liquid-storing box, said sour water outlet valve and alkaline water outlet valve are separately positioned on sour water liquid-storing box and alkaline water liquid-storing box water outlet place separately.
5. according to claim 1 or claim 2 monobloc(k)type electrolyzed oxidizing water generation system is characterized in that said electrolysis cells comprises electrolyzer, and this electrolyzer comprises:
Upper housing and lower housing, upper housing and lower housing combine the back to form the cell vessel of sealing;
One or more electrolyzer water inlets and two electrolyzer water outlets;
Be arranged alternately at electrolyzer inner battery lead plate and electrode plate assembly;
Wherein electrode plate assembly comprises the overlay film framework and is arranged on the intravital battery lead plate of overlay film frame; The tow sides of the overlay film framework of electrode plate assembly have ionic membrane; Overlay film framework inside and outside as different electrode districts; The overlay film framework of electrode plate assembly is provided with framework water inlet and framework water outlet, and the framework water inlet is communicated with the electrolyzer water inlet, and the framework water outlet is communicated with a water outlet of electrolyzer; And
Wherein every plate electrode plate has electrode contact, is connected with outside electrolysis power through the electrode perforations that is arranged on the electrolyzer.
6. monobloc(k)type electrolyzed oxidizing water generation system as claimed in claim 5; It is characterized in that; Said overlay film framework is made up of four frameworks and two ionic membranes; In the middle of two frameworks the front baffle that a slice ionic membrane forms the overlay film framework is set, in the middle of two frameworks the rear frame that a slice ionic membrane forms the overlay film framework is set in addition, in the middle of the framework of front and back battery lead plate is set and is joined together to form electrode plate assembly then.
7. monobloc(k)type electrolyzed oxidizing water generation system as claimed in claim 5 is characterized in that, the spacing of the battery lead plate that the overlay film framework of said electrode plate assembly is inside and outside is made as 2-8mm.
8. monobloc(k)type electrolyzed oxidizing water generation system as claimed in claim 5 is characterized in that, the front baffle of overlay film framework is formed with many parallel separated ribs respectively with the rear frame tow sides, and said spacing at a distance from rib and battery lead plate is set in the 0.6mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202640926U CN202186912U (en) | 2011-07-25 | 2011-07-25 | Integral system for generating acidic electrolyzed-oxidizing water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202640926U CN202186912U (en) | 2011-07-25 | 2011-07-25 | Integral system for generating acidic electrolyzed-oxidizing water |
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| Publication Number | Publication Date |
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| CN202186912U true CN202186912U (en) | 2012-04-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011202640926U Expired - Fee Related CN202186912U (en) | 2011-07-25 | 2011-07-25 | Integral system for generating acidic electrolyzed-oxidizing water |
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| CN (1) | CN202186912U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107857402A (en) * | 2017-11-28 | 2018-03-30 | 夏秦 | A kind of acidic oxidized electric potential water production technology |
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2011
- 2011-07-25 CN CN2011202640926U patent/CN202186912U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107857402A (en) * | 2017-11-28 | 2018-03-30 | 夏秦 | A kind of acidic oxidized electric potential water production technology |
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Effective date of registration: 20131224 Address after: 100176, Beijing economic and Technological Development Zone, Beijing No. two road, No. 27, No. 2 hospital building Patentee after: Beijing Zhouji Resource Environmental Protection Technology Co.,Ltd. Address before: 100176, No. 2 building, No. 27, No. two, Hai Lu, Beijing economic and Technological Development Zone, Beijing, Daxing District Patentee before: Zhang Dunjie |
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