CN202265444U - Reactor for continuous generation of water with high redox properties - Google Patents
Reactor for continuous generation of water with high redox properties Download PDFInfo
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- CN202265444U CN202265444U CN2011203126164U CN201120312616U CN202265444U CN 202265444 U CN202265444 U CN 202265444U CN 2011203126164 U CN2011203126164 U CN 2011203126164U CN 201120312616 U CN201120312616 U CN 201120312616U CN 202265444 U CN202265444 U CN 202265444U
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Abstract
A reactor for continuous generation of water with high redox properties comprises a positive electrode (7), a negative electrode (5), a cation exchange membrane, an insulated casing, and an electric cabinet (9); the positive electrode (7) and the negative electrode (5) are disposed at the inner side of the acid and alkali-resistant, high voltage-resistant insulated casing in a length direction; the planes of the positive electrode and the negative electrode are of the same length and are parallel to each other; the positive electrode (7) and the negative electrode (5) are separated by the cation exchange membrane (6); The positive electrode (7) and the negative electrode (5) are connected with a high voltage dc source through the electric cabinet, and the electric cabinet is fixed on the insulated casing. Water is injected into the reactor; water enters from a water inlet end (4), and exits from water outlet ends (1, 2, 3); the high voltage dc source is connected between the positive electrode (7) and the negative electrode (5) to form the reactor for continuous generation of water with high redox properties. The reactor of the utility model can generate and provide a lot of water with high redox potentials in time, is suitable for the requirements for continuous generation of water with high redox properties, and is applicable to civil and industrial water treatment.
Description
Technical field
The utility model relates to a kind of reactor drum of continuous generation high oxidation reductibility water, belongs to the electrolysis tech field.
Background technology
Electrolytic reduction water is a kind of any traditional tap water different from the past, when it is meant tap water is carried out electrolysis, and the water that becomes at negative electrode one adnation, i.e. electrolytic reduction water.At the water that anode one adnation becomes, then be electrolytic oxidation water.The electrolytic reduction water most important character is to have an ionic exchange membrane between negative electrode and the anode, promptly allows ion to see through the property handed over film and produces electric current, and the molecule that stops the electrolysis of negative and positive the two poles of the earth to form simultaneously interpenetrates fusion.Generating the device of this water, is exactly electrolysis water generator.
Electrolytic reduction water contains more hydroxide ion, and [OH-] is higher than [H+], contains abundant active hydrogen, and redox potential is negative value (800 mV), has reductive action.
Electrolytic oxidation water contains more acid ion, and [H+] is higher than [OH-], and a large amount of active oxygen radicals, has oxidisability.On medical science and food technology, be widely used in sterilization.
Electrolytic reduction water has also carried out a series of comparatively complicated electrochemical reactions in generative process.Therefore obvious variation has all taken place in electrolytic reduction water on indexs such as redox potential, potential of hydrogen, water clusters size, ion composition and existence, specific conductivity.Electrolytic reduction water can be eliminated superfluous radical in the human body because of containing abundant active hydrogen.Experimental study shows that electrolytic reduction water can obviously suppress carcinoma of the pancreas, suppresses tumor-blood-vessel growth, treatment mellitus, ephrosis etc.
But there are some problems in existing electrolysis water generator, and little like the electrolyzer capacity of electrolysis water generator, the comparative electrode area is also little, can't generate the high-quality brine electrolysis, also can cause the rapid deterioration of electrode; The electrolyzer of electrolysis water generator (pipe) wall incrustation is difficult for cleaning, and influences the electrolysis water generator life-span.In addition, because present commercially available device for producing electrolytic water, all less than the function of setting and show the brine electrolysis reduction potential; Can only passive regular detection, again because of the employed detecting instrument of user, can be because of impurity in the water or long-pending calcium; Cause transmitter to block; Make detected result produce error, so the human consumer has no way of learning whether conformance with standard of its redox potential at all, even most retail consumer produce query to reductive water on the effectiveness of human body.
Summary of the invention
The purpose of the utility model is that the problem to existing electrolysis water generator exists discloses a kind of reactor drum that can generate high oxidation reductibility water continuously.
The technical scheme of the utility model is that the positive and negative electrode that will discharge places the pipeline of insulation acid and alkali-resistance inboard; Two electrodes are parallel equidistantly; Make the pipeline series connection reach several meters, to desired length, that is positive and negative electrode reaches several meters; The electrode area that this ducted electrode area is used much larger than traditional electrolyzer has greatly increased discharge electrode length and machining area.
The utility model generates the reactor drum of high oxidation reductibility water continuously and is made up of positive electrode 7, negative potential 5, cationic exchange membrane 6, insulated shell 8 and electric control box 9; Said positive electrode 7, negative potential 5 place acid and alkali-resistance, high voltage bearing insulated shell 8 length directions inboard; Positive electrode and negative potential plane are isometric and be parallel to each other, and separate with cationic exchange membrane 6 in the middle of positive electrode 7 and the negative potential 5; Positive electrode 7 and negative potential 8 connect high-voltage DC power supply through electric control box, and electric control box is fixed on the insulated shell.
The making method of said reactor drum is following:
Select the certain-length sectional area be rectangle, can acid and alkali-resistance and high voltage bearing plastic casing 8, positive electrode 7, negative potential 5 are placed equidistant position that is parallel to each other along its length, shell inboard, and between positive electrode 7 and negative potential 5, cationic exchange membrane 6 are set; Both sides connect inlet tube and outlet tube respectively; Between positive electrode 7 and the negative potential 5 at a distance of 2mm-80mm; Cationic exchange membrane 6 be positioned at parallel with positive electrode 7, negative potential 5 and respectively with two equidistant positions of electrode surface; Draw positive electrode 7 and negative pole 5 terminal studs from the pipeline edge, constitute reactor drum.
Shell of reactor is provided with water-in and water outlet, and water outlet can be one or more, selects as required.The water-in 4 of reactor drum connects tap water, closes water outlet 1,2,3, and tap water is filled with in the reactor drum; Impose the 5V-5000V volts DS between reactor drum positive electrode 7 and the negative potential 5, between positive electrode 7 in the reactor drum and the negative potential 5 to the water generates exoelectrical reaction; After for some time is carried out in discharge, open shell water outlet 1,2,3, high oxidation reductibility water flows out from water outlet 1,2,3; Constantly water inlet and water outlet of current forms and dynamically makes water continuously in the reactor drum.After positive and negative electrode 7 energisings, can produce the water of high oxidation potential near the positive electrode 7, redox potential reaches 800mV to 1500mV, and it is acid that its pH value is; Can produce the water of high reduction potential near the negative potential 5 after the energising, redox potential reaches-and 800mV arrives-1200mV, and it is alkaline that its pH value is.
In order to increase the water treatment capacity of reactor drum; The reactor drum of positive and negative electrode and cationic exchange membrane can several be equipped with; Adopt the bend pipe polyphone to be tightly connected together, until our required length, the positive and negative electrode with all processing units is together in parallel then; Be connected to direct supply, constitute a compound reactor.
The pipeline of the utility model reactor drum can be as required, and being together in series is several meters or longer, so the electrode area used much larger than traditional electrolysis water generator electrolyzer system water of the electrode total area, also just increases discharge electrode length and machining area widely.Because machining area is big, and electrolysis power foot, this makes oxidation, reduction potential and the conductance of the interior water of reactor drum change rapidly, can generate high oxidation, reduction potential water continuously.
Separate with cationic exchange membrane in the middle of the utility model reactor drum positive and negative electrode; This film allows positively charged ion to pass; Keeping film both sides high redox potential water, whether the visual demand decision of this film is provided with, if want to obtain sour water and the alkaline water of high redox potential then film need be set.
The material of the utility model positive electrode can select for use materials such as graphite cake, platinum plating plate, ruthenium iridium coating layer titanium plate, titanium plate to manufacture.
Also can in water, add compositions such as Repone K, sodium-chlor, hydrochloric acid in the utility model reactor assembly, the energising back produces the hypochlorite that electrochemical reaction obtains having more sterilization effect, to improve the sterilizing ability of water.
The beneficial effect of the utility model and prior art comparison is because the utility model structure of reactor electrode area can be done very greatly as required, when carrying out the electrolysis treatment of water, can generate superelevation oxidation or reduction potential water continuously in large quantities; The current density of the utility model reactor drum unit electrode area is far below traditional water electrolysis machine, so the positive electrode material corrosion is less; The utility model can carry out sterilization, deodorizing, decomposition TVOCs to the water that is processed simultaneously, makes water cleaner.Because current constantly flow in the reactor drum, outer casing inner wall does not scale, and reactor drum can exempt to clean, and has prolonged the life-span of reactor drum.The utility model reactor drum can generate and provide in real time the water of high oxidation, reduction potential in a large number, give drunk, places such as washing, sterilization, irrigation and process water, can solve present device for producing electrolytic water high price on the market, problem that aquifer yield is little.
The utility model is suitable for the requirement that generates high oxidation reductibility water continuously, can be used for civilian and Treatment of Industrial Water.
Description of drawings
Fig. 1 generates the structure of reactor figure of high oxidation reductibility water continuously for the utility model;
Fig. 2 generates the structure of reactor sectional view of high oxidation reductibility water continuously for the utility model;
Fig. 3 is the reactor drum outside view of the continuous generation high oxidation reductibility water of band electric control box;
Fig. 4 is the reactor drum outside view of compound continuous generation high oxidation reductibility water;
Fig. 5 generates the reactor drum outside view of high oxidation reductibility water continuously for laminated devices;
Fig. 6 moves towards figure for the reactor fluid that laminated devices generates high oxidation reductibility water continuously;
Picture in picture number expression: the 1st, water outlet A; The 2nd, water outlet B; The 3rd, water outlet C; The 4th, water-in; The 5th, negative potential; The 6th, cationic exchange membrane; The 7th, positive electrode; The 8th, insulated shell; The 9th, electric control box; The 10th, the fluid tendency.
Embodiment
The embodiment of the utility model such as Fig. 1, Fig. 2 and shown in Figure 3.
Present embodiment generates the reactor drum of high oxidation reductibility water continuously and is made up of positive electrode 7, negative potential 5, cationic exchange membrane 6, insulated shell 8,9 of electric control boxs.Insulated shell 8 is that one section xsect is rectangular body structure, is processed by acid and alkali-resistance, high voltage bearing engineering plastics, and water-in 4 and water outlet 1,2,3 are left in insulated shell 8 both sides; The conduit upper cover plate is detachable, but strict seal when using.Positive electrode 7, negative potential 5 are placed shell inside length direction equidistant position that is parallel to each other; Positive electrode 7 and negative potential 5 are respectively apart from duct wall 5 ㎜; Distance is 50 ㎜ between positive electrode 7 and the negative potential 5; In the middle of positive electrode 7 and negative potential 5, cationic exchange membrane 6 is set, cationic exchange membrane 6 leaves with positive electrode 7, negative potential 5 parallel equidistant respectively.
Reactor drum when operation, sealing water outlet 1,2,3 earlier, through water-in 4 to the reactor drum fills with water; Between positive electrode 7 and negative potential 5, apply 3000 volts of volts DSs then, after for some time, water outlet 1,2,3 discharges water, and keeps flooding quantity and aquifer yield balance, and the control flooding velocity can continuously obtain high oxidation reductibility water.
Fig. 4 is the structure of reactor figure of compound continuous generation high oxidation reductibility water, and it is formed by three reactors in series, and positive electrode 7 inserts electric control box 9 with negative potential 5; Water gets into reactor drum from water-in 4, flows out high oxidation reductibility water by water outlet 1,2,3 respectively.
Present embodiment is the reactor drum that laminated devices generates high oxidation reductibility water continuously, and Fig. 5 is its outside view, and Fig. 6 moves towards figure for its reactor fluid.
Present embodiment is divided into multilayer with reactor drum plastic casing inside with electrode, and electrode is followed successively by positive pole-negative pole-positive pole-negative pole and arranges, and promptly relative two of each sheaf space is a positive and negative electrode, and fluidic moves towards as shown in Figure 6 in the reactor drum.Between this reactor drum positive and negative electrode cationic exchange membrane is not set.
Claims (4)
1. reactor drum that generates continuously high oxidation reductibility water; Form by positive electrode (7), negative potential (5), cationic exchange membrane (6), insulated shell (8) and electric control box (9); It is characterized in that; Said positive electrode (7), negative potential (5) place acid and alkali-resistance, high voltage bearing insulated shell (8) length direction inboard, and positive electrode and negative potential plane are isometric and be parallel to each other, and positive electrode (7) separates with cationic exchange membrane (6) with negative potential (5) centre; Positive electrode (7) and negative potential (8) connect high-voltage DC power supply through electric control box, and electric control box is fixed on the insulated shell.
2. the reactor drum of a kind of continuous generation high oxidation reductibility water according to claim 1 is characterized in that, between said positive electrode (7) and the negative potential (5) at a distance of 2mm-80mm; Said cationic exchange membrane (6) be positioned at positive electrode (7), negative potential (5) is parallel and respectively with two equidistant positions of electrode surface.
3. the reactor drum of a kind of continuous generation high oxidation reductibility water according to claim 1 is characterized in that, is provided with water-in (4) and water outlet (1,2,3) on the said insulated shell, and water outlet can be one or more.
4. the reactor drum of a kind of continuous generation high oxidation reductibility water according to claim 1; It is characterized in that; Can several be equipped with the reactor drum of positive and negative electrode and cationic exchange membrane, adopt the bend pipe polyphone to be tightly connected together, the positive and negative electrode with all processing units is together in parallel then; Be connected to direct supply, constitute a compound reactor.
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CN2011203126164U CN202265444U (en) | 2011-08-25 | 2011-08-25 | Reactor for continuous generation of water with high redox properties |
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CN2011203126164U CN202265444U (en) | 2011-08-25 | 2011-08-25 | Reactor for continuous generation of water with high redox properties |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104098162A (en) * | 2013-04-15 | 2014-10-15 | 刘华鑫 | Electromagnetic water treatment apparatus |
CN106311729A (en) * | 2015-07-07 | 2017-01-11 | 刘颖姝 | Application of electro-catalysis water equipment to soil pollution treatment and soil pollution treatment method |
JP2018001152A (en) * | 2016-07-06 | 2018-01-11 | 崑喨 洪 | Processing method of converter stone waste |
US11332887B2 (en) | 2019-06-26 | 2022-05-17 | Kun-Liang Hong | Tailings-reclaimed green stone paper processing method |
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2011
- 2011-08-25 CN CN2011203126164U patent/CN202265444U/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104098162A (en) * | 2013-04-15 | 2014-10-15 | 刘华鑫 | Electromagnetic water treatment apparatus |
CN106311729A (en) * | 2015-07-07 | 2017-01-11 | 刘颖姝 | Application of electro-catalysis water equipment to soil pollution treatment and soil pollution treatment method |
CN106311729B (en) * | 2015-07-07 | 2020-07-31 | 苏州鼎德电环保科技有限公司 | Application of electrocatalytic water equipment in soil pollution treatment and soil pollution treatment method |
JP2018001152A (en) * | 2016-07-06 | 2018-01-11 | 崑喨 洪 | Processing method of converter stone waste |
US20180009709A1 (en) * | 2016-07-06 | 2018-01-11 | Kun-Liang Hong | Basic oxygen furnace slag treatment method |
DE102017006293A1 (en) | 2016-07-06 | 2018-01-11 | Kun-Liang Hong | Basic method for treating the slag of oxygen-inflating converters |
US10604415B2 (en) * | 2016-07-06 | 2020-03-31 | Kun-Liang Hong | Basic oxygen furnace slag treatment method |
US11332887B2 (en) | 2019-06-26 | 2022-05-17 | Kun-Liang Hong | Tailings-reclaimed green stone paper processing method |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120606 Termination date: 20180825 |