CN213013119U

CN213013119U - Device capable of reducing cost for preparing acid-base water by electrochemical method

Info

Publication number: CN213013119U
Application number: CN202020619058.5U
Authority: CN
Inventors: 李海涛
Original assignee: Individual
Current assignee: Individual
Priority date: 2020-04-22
Filing date: 2020-04-22
Publication date: 2021-04-20
Anticipated expiration: 2030-04-22

Abstract

The device for preparing the alkaline water by the electrochemical method comprises an electrolytic bath body, an electrode and a power supply device; the electrode comprises an anode body and a cathode body, wherein the anode body is composed of a base body and a base body coating layer, the cathode body is only composed of the base body, and a micro-permeation film is arranged between the anode body and the cathode body. The utility model discloses change traditional thinking and be used to the formula, replace the ionic membrane with little infiltration membrane, avoid falling the utmost point, improved the life of electrode, have easy operation, convenience, the abundant advantage of resource saving, utilization has very big innovation. The utility model discloses both can prepare the sour buck, can prepare disinfectant simultaneously again, ingenious utilization electrochemical reaction mechanism, the acid-base water and the disinfectant of simple, the output of process step all have very big practical value.

Description

Device capable of reducing cost for preparing acid-base water by electrochemical method

Technical Field

The utility model relates to an electrochemistry preparation acid-base water technical field, more specifically relates to a but the device of electrochemical method preparation acid-base water of reduce cost, on this basis, still relates to a device of preparation hypochlorous acid sterile water.

Background

With the social development, the living standard of people is improved, and higher requirements are made on the quality of daily domestic water. Generally, as shown in fig. 1, a conventional apparatus for preparing acid-base water includes an electrolytic bath, an anode, a cathode, and an ionic membrane. In order to make the anode active, the structure of the anode is that titanium metal is used as a substrate, and platinum is plated on the surface of the substrate or platinum group metal (ruthenium, iridium and palladium) oxide is coated on the surface of the substrate. Ion exchange is performed to generate an acid-base water by providing an ion membrane that allows only a certain specific ion to pass between an anode and a cathode. The ionic membrane can be blocked due to deposition of hydrated ions during use. In order to avoid the blocking of the ion membrane, a method of exchanging an anode and a cathode, namely, inverting the anode and reversely ionizing to generate alkali and acid water, and generating impact force to conduct deposition ions is adopted. Since it is necessary to invert the anode, which is converted into the cathode, and the cathode is converted into the anode, the conventional apparatus requires not only the anode to be coated with platinum (or platinum group metal) but also the cathode to be coated with platinum (or platinum group metal).

On one hand, China is a country lacking in platinum group metal resources, the yield of China cannot meet the production requirement, and the actual consumption can be met only by importing the platinum group metal resources from abroad; on the other hand, the ionic membrane is used in the device, and because the domestic ionic membrane production technology is different from that of foreign countries, many high-end products also need to use imported ionic membranes, wherein the ionic membrane produced by the U.S. Dupont company has better quality, the price of the ionic membrane is raised by foreign suppliers, and the price of the ionic membrane per square meter is up to more than ten thousand yuan, which both prevent the popularization and the use of the acid-base water preparation device products.

More importantly, even if the problem of high price is overcome, the conventional device still has the problems that the service life of the electrode is damaged, the electrode cannot be fully utilized and the due material value cannot be exerted. As a result of studies on the reversed operation of the anode with titanium-based iridium dioxide and tantalum pentoxide coating, such as Masatsugu Motimitsu, Ryuichi Otogolwa, and Morio Matsunaga (Electrochemica Acta 40(2000)401-406), the working life of the electrode material can reach more than 7000 hours when the electrode material is operated as an anode in a mixed solution of sodium sulfate and sulfuric acid at an ultrahigh current density of 10000 amperes per square meter. And the cathode is operated at 500 amperes per square meter, and the service life of the cathode is less than 200 hours. From this result, it was found that the exchange of the cathode and the anode after the electrode inversion greatly affects the service life of the electrode, and the cost of the apparatus is undoubtedly higher.

Therefore, in order to reduce the cost of the acid-base water preparation device, save precious metal resources, reduce the import usage of high-end ionic membranes, and improve the service life of the device, it is necessary to improve the existing device and process for preparing the acid-base water.

SUMMERY OF THE UTILITY MODEL

The utility model discloses a first aim at to above-mentioned defect and not enough, provide a device of electrochemical method preparation sour alkaline water with low costs, practice thrift precious metal, that the ionic membrane dependence reduces, life is permanent, need not to fall utmost point.

Another object of the utility model is to provide a device for preparing alkaline-alkaline water by an electrochemical method with high electrolysis efficiency, compact structure and conservation.

In order to achieve the above object, the utility model discloses a specific technical scheme be:

the device for preparing the alkaline water by the electrochemical method comprises an electrolytic bath body, an electrode for electrolysis and a direct current power supply device for supplying electric energy to the electrode; the electrode comprises an anode body and a cathode body, wherein the anode body is composed of a base body and a base body coating layer, the cathode body is only composed of the base body, and a micro-permeation film which can conduct ions and can also permeate solution in a micro-permeation mode is arranged between the anode body and the cathode body.

The working principle involved in the utility model comprises the following reactions:

cathode reaction

2H₂O+2e→2OH^-+H₂↑ (1)

Anodic reaction

2H₂O-4e→4H⁺+O₂↑ (2)

In the apparatus for electrochemically preparing the alkaline solution, the cathode and the anode of the apparatus are activated and coated by using the platinum group noble metal compound, and the purpose is to maintain the conduction of the circuit by using a method of switching the electrodes in order to prevent the ionic membrane from being blocked. This is because many fine particles are not charged by themselves, but water is a polar molecule in an aqueous solution, and the fine particles are charged in the outer layer by hydration under the action of an electric field, and migrate to generate a dynamic potential called zeta potential, which causes the membrane to be clogged, and a reverse process is adopted in order to keep the circuit on. According to the researches of Masatsugu Motimitsu, Ryuichi Otogolwa, Morio Matsunaga and the like, the service life of the electrode is greatly reduced after the electrode is replaced, and the value of the electrode is not fully exerted. The purpose of this patent is to overcome the shortcoming that the fall of the utmost point causes the electrode life-span to descend, and the cost rises.

The utility model discloses well adoption both can switch on the ion, and the little infiltration membrane replacement that can permeate solution a little again only allows the ionic membrane that the ion passes through, for the ionic membrane says, the patency improves, has avoided hydrated ion to pile up the jam that arouses, and then need not adopt the mode of falling the utmost point to guarantee the unblocked working method of circuit, very big improvement the life of electrode. The improvement of the traditional technology is usually trapped in a thinking inertial type based on an ionic membrane, and the research direction of the traditional technology is also how to optimize the pole-reversing process, reduce the damage of the device and prolong the service life. And the technical scheme that the micro-permeable membrane allowing ions and other particles with larger volume to pass through is used for electrolyzing the acid-base water is adopted, the traditional thinking inertial type is broken out, and great innovation is achieved.

The device for preparing the alkaline water by the electrochemical method has high electrolysis efficiency, compact structure and section saving, and the distance between the anode body and the micro-permeation membrane is less than that between the cathode body and the micro-permeation membrane.

In the prior art, because the electrode reversing operation is needed, the distance between the electrode and the ionic membrane needs to be set to be equal, so that the electrolytic path is kept unchanged after the electrode exchanges the cathode and the anode. The utility model can only set the electrolysis path with longer distance on one side of the cathode body according to the requirement without the reverse electrode operation, and the electrolysis path on one side of the anode body is set to be shorter. The structure layout is compact, the electrolytic path on one side of the anode body is shortened, further, the section bar is saved, and the material required by manufacturing is less. Most importantly, because the electrolytic path is shortened, the electrolytic efficiency is improved, and the cost for producing products is further reduced.

In order to improve the electrolysis efficiency and save the manufacturing consumables of the electrolytic bath body, the distance between the anode body and the micro-permeation film is less than the distance between the cathode body and the micro-permeation film. Furthermore, the distance between the anode body and the micro-permeation film is not more than 2mm, and the distance between the anode body and the cathode body is not more than 5 mm.

In order to conveniently lead in and collect the electrolyte, the electrolytic bath body comprises an inner bath body and an outer bath body sleeved on the inner bath body; the inner tank body and the outer tank body are respectively provided with an anode body and a cathode body at the positions corresponding to the micro-permeation film; a micro-permeable membrane is arranged between the inner tank body and the outer tank body. The anode body and the micro-permeable film form an anode area, and the cathode body and the micro-permeable film form a cathode area; the outer tank body is provided with an electrolytic solution inlet and a catholyte outlet which are communicated with the cathode region, and the inner tank body is provided with an anolyte circulation hole and an anolyte outlet. Further, the height of the anolyte flow holes is within the height covered by the micro-permeable membrane.

In order to increase the electrolyte circulation capacity of the anode region, an anolyte inlet is further formed in the inner tank body.

For convenience of processing, the shape of the electrolytic tank body is a cylindrical or prismatic structure, wherein the electrolytic tank body comprises an inner tank body and an outer tank body. Although the shape of the electrolytic cell body of the present invention is explicitly recited in the claims, the actual shape of the electrolytic cell body includes, but is not limited to, the above shape, and the electrolytic cell body may be processed into other shapes, even complicated shapes, as long as the requirements of the actual production can be satisfied.

In order to improve the conduction effect, the micro-permeable membrane comprises a micro-permeable ionic membrane or a ceramic permeable membrane.

In order to ensure that the electrode is protected from corrosion, the substrate is a corrosion-resistant stainless steel, pure titanium, titanium alloy or niobium substrate.

For convenience of processing, the electrode is a column-type, plate-type, or mesh electrode. The electrode in the utility model can be processed into other shapes or even complex shapes according to actual requirements besides the shapes.

In order to save cost, the thickness of the micro-permeable membrane is 0.5-0.8 mm.

The process method for preparing the acid-base water by the electrochemical method comprises the following steps:

s1, injecting an electrolytic solution into an electrolytic cell body;

s2, starting a direct current power supply device to supply power to the electrode;

and S3, leading out the electrolytic solution positioned at the two sides of the micro-permeable membrane.

Because the utility model discloses change traditional thinking and be used to the formula, replaced the ionic membrane with little infiltration membrane, so, avoided falling utmost point process step, improved the life of electrode, it is simpler, convenient to have the operation, and the resource is practiced thrift more, is utilized abundant advantage.

Both can prepare the buck, the technological method that can also produce the sterile water simultaneously establish on above-mentioned technological method, specifically do before step S3, to add NaCl solution on one side of the negative pole body.

The utility model discloses regard as the diaphragm material with little permeable membrane, separate into negative pole district and positive pole district to the electrolysis unit, when leading to the operation of carrying out the brineelectrolysis with appropriate DC voltage, appear oxygen on the positive pole, remaining hydrogen ion, so the water in positive pole district is acidity. Hydrogen is separated out on the cathode, and hydroxide ions are remained, so that the water body in the cathode area is alkaline. Adding NaCl water solution with set concentration into the cathode region to obtain alkaline water solution, and adding chloride ion Cl in the cathode region^-Under the action of the positive electric field, the anode enters the anode area through the micro-permeable membrane, and then competitive reactions of oxygen evolution and chlorine evolution are generated on the anode, such as the reaction formulas (2) and (3).

2Cl^--2e→Cl₂↑ (3)

Because water can dissolve about twice the volume of chlorine, when the saturated solubility is not reached, the chlorine cannot escape from the water body, and the chlorine dissolved in the water can generate secondary reaction of hydrolysis to generate hypochlorous acid HClO, as shown in the reaction formula (4):

Cl₂+H₂O→HCl+HClO (4)

hydrolysis to produce HCl and HClO, which is a perchloric acid-free HClO₄In addition, compounds with the second strongest oxidizing power are known, which have a very strong virucidal power.

The competing reactions of chlorine evolution and oxygen evolution at the anode depend on the chemical potentials of the different substances and more particularly on the catalytic properties of the electrode material for a certain characteristic reaction. The present invention relates to a method for controlling the concentration of chlorine deposition, and is characterized by that in the research of electrolytic dilute salt water anode material (Lihao, Zhang Sai le, Liwanle, electrolytic low NaCl sea water is used for producing sodium hypochlorite anode material, and its material research and application, 2001,011(001): 41-44), it makes a detailed discussion, and according to Faraday's law, if the DC deposition efficiency of chlorine is used as representative parameter, the sum of chlorine deposition efficiency and oxygen deposition efficiency is one hundred, and the chlorine deposition efficiency can be obtained, and as for chlorine deposition concentration, it can be controlled by regulating two parameters of DC current and solution flow.

The reason why the prior art of the process for producing sterilized water cannot do is that: in order to avoid the blocking of the ion membrane, the anode and the cathode need to be reversed, and the process operation of adding the NaCl aqueous solution into the cathode side (cathode region) after the cathode is reversed is difficult to realize. The utility model discloses both can prepare the sour buck, can prepare disinfectant simultaneously again, ingenious utilization electrochemical reaction mechanism, the acid-base water and the disinfectant of simple, the output of process step all have very big practical value. Meanwhile, acid-base water and disinfectant water are produced simultaneously in one process, so that electric energy is saved, and the production cost is further reduced.

In order to improve the production efficiency, a plurality of apparatuses for preparing an alkaline aqueous solution by an electrochemical method are connected in parallel or in series before the step S1.

Compared with the prior art, the utility model, following beneficial effect has:

the utility model discloses well adoption both can switch on the ion, and the little infiltration membrane replacement that can permeate solution a little again only allows the ionic membrane that the ion passes through, for the ionic membrane, the patency improves, has avoided the ionic membrane to pile up the jam that arouses because of the hydrated ion. The utility model discloses need not adopt the mode of falling the utmost point to guarantee the unblocked working method of circuit, very big improvement the life of electrode. The traditional technology is usually trapped in a thinking inertial type based on an ionic membrane, and the research direction of the traditional technology is also the direction of how to optimize the pole-reversing process, reduce the damage of the device, prolong the service life and the like. And the technical scheme that the micro-permeable membrane allowing ions and other particles with larger volume to pass through is used for electrolyzing the acid-base water is adopted, so that the traditional thinking inertial form of 'pole inversion' is broken out, and great innovation is achieved.

The utility model can only set the electrolysis path with longer distance on one side of the cathode body according to the requirement without the electrode reversing operation, and the electrolysis path on one side of the anode body is shorter. The structure layout is compact, the electrolytic path on one side of the anode body is shortened, further, the section bar is saved, and the material required by manufacturing is less. Most importantly, because the electrolytic path is shortened, the electrolytic efficiency is improved, and the cost for producing products is further reduced.

The utility model discloses change traditional thinking and be used to the formula, replaced the ionic membrane with little infiltration membrane, avoided falling utmost point technology step, improved the life of electrode, it is simpler, convenient to have the operation, and the resource is practiced thrift more, is utilized abundant advantage.

The utility model discloses both can prepare the sour buck, can prepare disinfectant simultaneously again, ingenious utilization electrochemical reaction mechanism, the acid-base water and the disinfectant of simple, the output of process step all have very big practical value. Meanwhile, acid-base water and disinfectant water are produced simultaneously in one process, so that electric energy is saved, and the production cost is further reduced.

The present invention will be further described with reference to the accompanying drawings.

Drawings

Fig. 1 is a schematic structural diagram of a preparation principle of a conventional alkaline water.

Fig. 2 is a schematic structural view of an acid-base water preparation device in a preferred embodiment of the present invention.

Fig. 3 is a schematic structural view of a cross section of an electrode according to a preferred embodiment of the present invention.

FIG. 4 is a schematic view showing the structure of the shape of the electrolytic cell body in the preferred embodiment of the present invention.

Fig. 5 is a schematic structural diagram of the shape of the electrode in the preferred embodiment of the present invention.

FIG. 6 is a flow chart of the process of the preferred embodiment of the present invention.

FIG. 7 is a graph showing the experimental results of the verification of the hypochlorous acid produced in the present invention.

Description of reference numerals:

the electrolytic cell comprises an electrolytic cell body 1, an electrolytic solution inlet 11, an electrolytic solution inlet 12, an inner cell body 13, an external cell body 121, an anolyte inlet 2, an electrode 21, an anolyte 22, a catholyte 211, a matrix 212 coating layer, an anolyte 213 circulation hole, a direct current power supply 3, a micro-permeable membrane 4, an anolyte 5 area, an anolyte 51 outlet, a catholyte 6 area and a catholyte 61 outlet.

Detailed Description

The present invention is further explained and illustrated by the following embodiments, it should be understood that the following embodiments are for the purpose of making the technical solution of the present invention clearer and easier to understand, and do not limit the scope of the claims.

As shown in fig. 2, the device for preparing an alkaline water by an electrochemical method according to the present invention comprises an electrolytic cell body 1, an electrode 2 for electrolysis, and a dc power supply device 3 for supplying electric energy to the electrode 2; the electrode 2 includes an anode body 21 and a cathode body 22, the anode body 21 is composed of a substrate 211 and a substrate coating layer 212, the cathode body 22 is composed of the substrate 211 only, and a micro-permeable film 4 capable of conducting ions and micro-permeating a solution is provided between the anode body 21 and the cathode body 22. In order to enhance the conduction effect, the micro-permeable membrane 4 includes a micro-permeable ion membrane, or a ceramic permeable membrane. To ensure that the electrodes are protected from corrosion, the substrate 211 is a corrosion-resistant stainless steel, pure titanium, titanium alloy, or niobium substrate.

In a preferred embodiment, the thickness of the micro-osmotic membrane 4 may be 0.5 to 0.8mm, preferably 0.5 to 0.6 mm.

In a preferred embodiment, the distance between the anode body 21 and the micro-permeable membrane 4 is smaller than the distance between the cathode body 22 and the micro-permeable membrane 4 in order to improve the electrolysis efficiency and save the manufacturing consumables of the electrolytic cell body. Furthermore, the distance between the anode body 21 and the micro-permeable membrane 4 is not more than 2mm, and the distance between the anode body 21 and the cathode body 22 is not more than 5 mm.

In a preferred embodiment, in order to facilitate introduction and collection of the solution, the electrolytic bath body 1 includes an inner bath body 12, and an outer bath body 13 fitted over the inner bath body 12; a micro-permeable membrane 4 is arranged between the inner tank body 12 and the outer tank body 13. The corresponding positions of the inner tank body 12 and the outer tank body 13 on the micro-permeable membrane 4 are an anode body 21 and a cathode body 22 respectively; the inner tank body 12 and the micro-permeable membrane 4 form an anode region 5, and the outer tank body 13 and the micro-permeable membrane 4 form a cathode region 6; the outer tank 13 is provided with an electrolytic solution inlet 11 and a catholyte outlet 61 communicating with the cathode region 6, and the inner tank 12 is provided with an anolyte flow hole 213 and an anolyte outlet 51. The height of the anolyte outlet 51 is within the height covered by the micro-osmotic membrane 4. In order to increase the electrolyte circulation capacity of the anode region, the inner tank 12 is further provided with an anolyte inlet 121.

In a preferred embodiment, as shown in fig. 3, the electrolytic bath body 1 has a circular or polygonal column structure for easy processing. Although the shape of the electrolytic cell body of the present invention is explicitly recited in the claims, the actual shape of the electrolytic cell body includes, but is not limited to, the above shape, and the electrolytic cell body may be processed into other shapes, even complicated shapes, as long as the requirements of the actual production can be satisfied.

In a preferred embodiment, the electrodes 2 are solid cylindrical, tubular, plate-type, or mesh-type electrodes for ease of machining, as shown in fig. 4. The electrode in the utility model can be processed into other shapes or even complex shapes according to actual requirements besides the shapes.

As shown in fig. 5, the process for preparing acid-base water by electrochemical method of the present invention comprises the following steps:

s1, injecting an electrolytic solution into the electrolytic cell body 1;

s2, starting the direct current power supply device 3 to supply power to the electrode 2;

and S3, leading out the electrolytic solution positioned at the two sides of the micro-permeable membrane 4.

Both can prepare the buck, the technological method that can also produce the sterile water simultaneously establish on above-mentioned technological method, it is specific before step S3, to add NaCl solution on one side of the negative pole body 22.

The present invention will be further described with reference to the following specific examples.

Example 1

In this example 1, the matrix of the anode body is made of titanium, and the coating layer is a platinum-plating layer of 1 μm; the matrix of the cathode body is made of titanium. The spacing between the anode regions is 1.5mm and the spacing between the cathode regions is 2.5 mm. Experiments prove that when the micro-permeable membrane of the embodiment 1 is applied to electrolytic water, acidic water with pH not more than 4.5 can be obtained in an anode region and alkaline water with pH more than 8 can be obtained in a cathode region by adjusting parameters such as current and water flow.

When dilute brine is electrolyzed to prepare hypochlorous acid water by using the device in the embodiment 1, a slightly permeable diaphragm material is used, which is more beneficial, for example, when dilute brine with concentration of about three thousandth is electrolyzed, NaCl solution entering a cathode area is separated out hydrogen on a cathode, and generated hydroxide radicals and sodium act to generate dilute alkaline solution. Under the action of the positive electric field, chloride ions migrate to the anode region, and a competitive reaction of oxygen evolution and chlorine evolution occurs on the anode. The research of the utility model 'electrolyzing the anode material of dilute brine' proves that the electric effect of chlorine evolution is about 60 percent when electrolyzing a NaCl solution with six thousandths of a thousand.

Based on this, when a dc voltage of 5V was applied to the apparatus to generate a dc voltage of 3A, the amount of chlorine generated per hour at the anode was 3Ah/53.6Ah (faradaic electricity) × 22.4 liters × 60% electric efficiency ═ 0.752 liters of chlorine gas per hour of anode chlorine evolution at the time of electrolysis.

The water can dissolve about twice the volume of chlorine and the flow rate of water in the anode region can be adjusted to practically 10 liters per hour or more. At this point, the solubility of chlorine does not reach saturation, and no chlorine gas can escape from the system.

When chlorine is dissolved in water, the chlorine undergoes secondary hydrolysis reaction to generate hydrochloric acid and hypochlorous acid

Cl₂+H₂O→HCl+HClO

I.e. half of the chlorine is converted into hypochlorous acid, the concentration of which is

0.752 l/22.4 l × 71g chlorine ═ 2.38g chlorine

Wherein 1.19g of chlorine is hydrolyzed to produce a hypochlorous acid aqueous solution with a concentration of about 120ppm, 1.19 g/10L × 1000 g-120 ppm

The concentration of hypochlorous acid in water was adjusted by adjusting the amount of electricity and the flow rate of water, and as shown in FIG. 7, the experiment in which hypochlorous acid was substituted for iodine in KI to produce free iodine showed that the solution changed from colorless to yellow, confirming that hypochlorous acid was electrolytically generated.

The reaction mechanism is as follows:

KI+CH₃COOH (acetic acid) ═ CH₃COOH+HI

2HI+HClO＝HClO+H₂O+I₂

Further, in order to confirm whether hypochlorous acid prepared by the utility model has the effect of disinfection and sterilization, in 2020, 04/02/s, the microbial analysis and detection center in Guangdong province is processed to make a detection report, the report number is 2020FM08376R01, and the sample name is "hypochlorous acid decomposer-self-made hypochlorous acid disinfectant".

Detection of available chlorine content

Detection basis and method: the content of available chlorine is determined according to the Disinfection technical Specification 2002 edition 2.2.1.2.1.

The instrument name: acid-base burette GWC-B4782.

And (4) detection conclusion: the available chlorine content (25 ℃ C.) was 101.0mg/L (101 ppm).

Detection of pH value

Instrument name and number: a pH meter (number: CRHJ-8048).

The detection basis is as follows: disinfection Specification (2002 edition of Ministry of health) 2.2.1.4.

Detection conditions are as follows: ambient temperature 15.7 ℃ and relative humidity 67%.

And (4) detection conclusion: the pH (25 ℃) was 4.5.

Quantitative identification test of neutralizer carrier and quantitative sterilization test of carrier soaking

And (4) detection conclusion: the utility model discloses the sample former state of preparation, the action time is 0.5 minute, 1.5 minutes, 3 minutes respectively, and the experiment is repeated 3 times, and is greater than or equal to 3.00 to the log value of killing of pseudomonas aeruginosa (ATCC15442), accords with the standard value of "disinfection technical specification" (2002 edition) 2.1.1.7 regulation, and is qualified to the disinfection of this bacterial strain.

Sterilization effect detection

And (4) detection conclusion: the disinfectant prepared by the utility model has the function of killing staphylococcus aureus, colon bacillus and candida albicans.

Disinfection effect detection

Detecting a sample: the utility model discloses self-control hypochlorous acid antiseptic solution

Test strains: H1N1A/PR8/34, provided by Guangdong province microbial strain protection management center.

Neutralizer components and concentrations: 0.5% sodium thiosulfate.

Media name and lot number: nutrient agar medium containing 0.5% sodium thiosulfate (batch No. 202000323).

A laboratory: 15m³A chamber.

A sampler: a biochemical incubator (model: GWC-6056), a water bath (model: GWC-23015), and JWL-8 sieve mesh impact type six-grade air microorganism samplers (model: GWC-3-5019C).

The method comprises the following steps:

the detection basis is as follows: disinfection Specification 2015 edition-3.3.2.5 simulates field testing.

Detecting the environment: temperature: 25 ℃, humidity: 51 percent.

Spraying for 5min, stirring for 5min, and standing for 5 min.

The method comprises the following steps: during the test, 300mL of sample stock solution is atomized into the air by using an air humidifier, a culture medium plate containing 0.5% of sodium thiosulfate neutralizer is filled into a six-stage sampler after 0.5min/3min of action, and the air in the space is sampled at the same position. When in sampling, the JWL-6 sieve mesh impact type six-level air microorganism sampler is placed at the 1.5m high position in the center of the cabinet, one point is arranged for sampling, and the sampling is carried out with the air draft of 16.7 liters for 1 minute. The sampling time of the control group is 1min, the sampling time of the test group is 1min, and the test is repeated for 3 times.

After sampling, the plates were incubated at 36 ℃ for 24 h.

And (4) detection conclusion: the detection result of the disinfection solution prepared by the utility model on the H1N1 influenza A virus killing rate in the air is more than 99 percent, which accords with the standard requirement of the disinfection technical specification 2015 edition-3.3.2.5, and the disinfection is qualified.

Comparative example 1

As shown in FIG. 1, in comparative example 1, the anode body was made of titanium, and the coating layer was a platinum plating layer of 1 μm; the cathode body adopts a titanium base, and the coating layer is a platinum coating layer with the thickness of 1 mu m; the distance between the cathode area and the anode area is 2.5mm, and the total distance is 5 mm.

Example 1 comparison with the consumable price of comparative example 1, the weight of one micron per square meter of platinum is 21.35 grams, the price per gram is about two hundred dollars, plus the preparation costs of the compound and bath, making it practical to make a platinized layer that can be electrolyzed at a cost that is roughly twice the price of the metal itself, about ten thousand dollars per square meter. The price of the micro-permeable membrane with one micron and one square meter is lower than one thousand yuan, and the price of the ionic membrane with one micron and one square meter is about ten thousand yuan. Example 1 compared to comparative example 1, the anode body was the same and the cathode body was left out of a 1 μm thick platinum coating and the film was different. In a single unit with a cathode body electrode area of 3.5 square decimeters and a permeate membrane area of 3.5 square decimeters, example 1 saves 735 yuan compared to comparative example 1.

In addition, in this embodiment 1, the reverse operation is not required, and the service life of the anode and cathode bodies is increased. The life of example 1 was improved by at least 35-fold, as predicted by the results of Masatsugu Motimitsu et al.

Furthermore, in this example 1, a NaCl solution was added to the cathode region to prepare HClO disinfectant water.

In addition, the distance between the anode regions is shortened and the electrolytic efficiency is improved in the embodiment 1 and the comparative example 1.

The present invention has been described in terms of embodiments, but not limitations, and other variations of the disclosed embodiments, as would be readily apparent to one skilled in the art, are intended to be included within the scope of the present invention as defined in the following claims, in view of the description of the present invention.

Claims

1. The device for preparing acid-base water by an electrochemical method is characterized in that: comprises an electrolytic bath body (1), an electrode (2) for electrolysis and a direct current power supply device (3) for providing electric energy for the electrode (2); the electrode (2) comprises an anode body (21) and a cathode body (22), wherein the anode body (21) is composed of a base body (211) and a base body coating layer (212), the cathode body (22) is only composed of the base body (211), and a micro-permeation film (4) which can conduct ions and can be used for micro-permeation of solution is arranged between the anode body (21) and the cathode body (22).

2. The apparatus for electrochemically preparing acid-base water according to claim 1, characterized in that: the distance between the anode body (21) and the micro-permeable membrane (4) is less than the distance between the cathode body (22) and the micro-permeable membrane (4).

3. The apparatus for electrochemically preparing acid-base water according to claim 2, characterized in that: the distance between the anode body (21) and the micro-permeable membrane (4) is not more than 2mm, and the distance between the anode body (21) and the cathode body (22) is not more than 5 mm.

4. The apparatus for electrochemically preparing acid-base water according to claim 1, characterized in that: the electrolytic tank body (1) comprises an inner tank body (12) and an outer tank body (13) sleeved on the inner tank body (12); the positions of the inner tank body (12) and the outer tank body (13) corresponding to the micro-permeable membrane (4) are an anode body (21) and a cathode body (22) respectively; a micro-permeable membrane (4) is arranged between the inner tank body (12) and the outer tank body (13).

5. The apparatus for electrochemically preparing acid-base water according to claim 4, wherein: the anode body (21) and the micro-permeable film (4) form an anode region (5), and the cathode body (22) and the micro-permeable film (4) form a cathode region (6); the outer tank body (13) is provided with an electrolytic solution inlet (11) communicated with the cathode region (6) and a catholyte outlet (61), and the inner tank body (12) is provided with an anolyte circulation hole (213) and an anolyte outlet (51).

6. The apparatus for electrochemically preparing acid-base water according to claim 5, wherein: the height of the anolyte flow hole (213) is within the height covered by the micro-permeable membrane (4).

7. The apparatus for electrochemically preparing acid-base water according to claim 5, wherein: an anolyte inlet (121) is also arranged on the inner tank body (12).

8. The apparatus for electrochemically preparing acid-base water according to claim 1, characterized in that: the micro-permeable membrane (4) comprises a micro-permeable ionic membrane or a ceramic permeable membrane.

9. The apparatus for electrochemically preparing acid-base water according to claim 1, characterized in that: the electrode (2) is a column-shaped, plate-shaped or mesh-shaped electrode.

10. The apparatus for electrochemically preparing acid-base water according to claim 1, characterized in that: the substrate (211) is a corrosion-resistant stainless steel, pure titanium, titanium alloy or niobium substrate.