KR20040043149A - Apparatus for purification of air and water using catalytic compound for purification of air and water - Google Patents

Abstract

PURPOSE: Provided is a device for purification of air and water, which removes dusts, harmful gases, microorganisms and organic substances in air or various pollution materials in contaminated water, gives moistening effect, and is used semi-permanently. CONSTITUTION: The device comprises: a catalytic filtering part(1) incorporated with a catalyst mixture(1a) and having an electrode(1b); a high-pressure dust-collecting and ozone-generating part(2) disposed in the downstream of the catalytic filtering part(1) and having an anode(2a) and a cathode(2b) to which a formed body of the catalyst mixture is attached; a gas purifying part(3) disposed in the downstream of the high-pressure dust-collecting and ozone-generating part(2) and comprising straw pieces(3a); a purified air supplying part(4) disposed in the down stream of the gas purifying part(3) to contact the purified air with water in a water tank(5), and having a fan(4a); and a water purifying part(9) disposed in the upstream of the water tank(5) and comprising a catalyst mixture for purifying contaminated water introduced via a water pipe(7).

Description

Air, water purification equipment using catalyst mixture for water purification {APPARATUS FOR PURIFICATION OF AIR AND WATER USING CATALYTIC COMPOUND FOR PURIFICATION OF AIR AND WATER}

The present invention relates to air and water purification apparatus using a catalyst mixture for water purification, and particularly, to remove harmful components in contaminated air, to supply purified air, and to remove harmful components contained in contaminated water. It relates to an air configured to be capable of air, air using a catalyst mixture for water purification, and a water purification device.

In general, air pollution or water pollution is the result of mixing of other substances in clean air or water to the extent that adverse effects on humans, animals and plants and other substances occur.

Air pollution refers to the presence of pollutants in the air for some time that harms human health, health and animal and plant life and adversely affects our daily lives and property. It can be divided into steam, gas, etc., and can be divided into natural and artificial depending on the conditions in which pollutants are generated.

Among the various air pollutants known so far, the most harmful to humans are nitrogen oxides, sulfur oxides, carbon monoxide, hydrocarbon vapors and organic solvent vapors.

On the other hand, water pollution refers to undesirably changing the water quality of natural waters due to the inflow of waste materials. If the liquid wastes that pollute the water are classified in more detail, they are inorganic, microorganisms, radioactive materials, and organic materials. Inorganic substances may cause turbidity in rivers, and some metals may harm ecosystems and humans directly or indirectly through food chains. Microorganisms may be pathogens, and organic substances such as phosphorus, nitrogen, pesticides and synthetic detergents are the most important pollutants.

The air purifier used in the prior art was to deodorize by adsorbing odorous gas or smoke by filling activated carbon therein, but activated carbon had to be used only for a certain time, and there was a problem in that it could not sterilize microorganisms harmful to the human body.

As another example, the air was purified through a nonwoven fabric made of glass fiber or synthetic fiber, but there was a problem in that it could not sterilize harmful bacteria or remove odors.

As another example, an electrostatic precipitator that charges dust and then attaches and cleans a high voltage to the electrode plate has a problem in that it is difficult to sterilize harmful bacteria or remove odors.

On the other hand, the apparatus for purifying water used in the prior art mainly purifies contaminated water by filling activated carbon inside, but activated carbon has to be replaced only because it can only be used for a certain time, and there is a problem in that the activated carbon alone is insufficient to purify the water quality.

Accordingly, the present invention has been made in order to solve the above problems, it is possible to supply a purified air by removing various contaminants of air dust, odorous harmful gas, harmful microorganisms or organic matter or contaminated water quality The purpose of the present invention is to provide air which can purify contaminated water quality in the process of air purification, can continue to use it, can be humidified and can be used semi-permanently, air using catalyst mixture for water purification, and water purification device. .

In order to achieve the above object, the air of the present invention, the air using the catalyst mixture for water purification, and the water purification apparatus are used as the catalysts such as carbon, iodine, magnesium air, and the catalyst mixture for water purification, included in contaminated air. A catalyst mixture in which the three components of the catalyst are mixed to remove and purify various organic substances, and a high-pressure dust collector installed to generate ozone and high-pressure dust collection, is equipped with a catalyst filter unit equipped with electrodes. And a gas purifying unit having a ozone generating unit, a straw piece into which gaseous iodine penetrates, and water contaminated by contact with the third purified air descended into the water tank by the purge air supply unit. A fish tank; And a water purification unit for purifying the polluted water in the water tank supplied by the pump, and a purifying air receiving unit for purifying the air purified in the fourth order by the water and exhausting the fourth purifying air. It is characterized in that it is configured to supply not only the purified air but also the humidification role by supplying some of the droplets of the droplets that are purified together with the air purified by the car and falling into the water tank to the outside.

1 is a schematic perspective view of air and water purification apparatus using the catalyst mixture of the present invention,

2 is a schematic cross-sectional view taken along the line A-A of FIG.

3 is a schematic cross-sectional view taken along the line B-B of FIG.

4 is a schematic cross-sectional view taken along the line C-C of FIG.

5 is a view showing a reaction in which the protein is decomposed by iodine in the air, water purification device using the catalyst mixture of the present invention,

6 is a view showing a state in which the organic material is continuously oxidized by applying a direct current electric current to the catalytic filter unit.

※ Explanation of code for main part of drawing

1: catalyst filter 1a, 2aa, 2ba, 9c: catalyst mixture

1b, 9d: electrode 2: high pressure dust collection and ozone generating unit

3: gas purifying part 3a: straw piece

4: 3rd purified air supply part 4a: 휀

5: water tank 6: purification air storage

7: water pipe 8: pump chamber

9: water purification part 10: network

11 body 13 power device

15: support plate

Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.

Air and water purification apparatus using the catalyst mixture for air, water purification of the present invention is a catalyst in which activated carbon, iodine and magnesium are mixed as catalysts to remove various organic substances and ozone, as shown in FIGS. A catalyst filter unit 1, in which a mixture 1a is embedded and an electrode 1b is installed so as to be electrolyzed to purify air firstly;

The undesired amount of ozone in the excess ozone generated by the high voltage is removed by removing the organic matter which is not decomposed in the primary purified air while passing under the catalyst filter part 1 while being installed under the catalyst filter part 1. The catalyst mixture (2aa) (2ba), which is a mixture of activated carbon, iodine and magnesium, is formed into coal tar to remove harmful substances in the air polluted by the remaining ozone while collecting high pressure. A high pressure dust collector and an ozone generator 2 for purifying the air by installing the positive electrode 2a and the negative electrode 2b to which the catalyst mixture molded bodies formed by coupling with each other are attached;

It is installed on the lower side of the high pressure dust collecting and ozone generating unit 2 to perform molecular vibration in a physical manner to pass the high pressure dust collecting and ozone generating unit (2) to remove harmful gas in the secondary purified air. A gas purifying part 3 having a straw piece 3a in which gaseous iodine penetrates into the wall so as to be decomposed to purify the air in a third order;

The catalyst filter unit (1) installed in the lower side of the gas purification unit (3) to suck the outside polluted air to purify the air polluted primarily by the suctioned outside polluted air, the second air (4a) to supply the third purified air (hereinafter referred to as the third purified air) while passing through the high pressure dust collecting and ozone generating unit 2 for purifying and the gas purifying unit 3 for purifying the air in third order A tertiary purification air supply unit 4 provided therewith;

The purge air is formed under the tertiary purge air supply unit 4, and the purge air comes into contact with the water 5a to remove ozone or dust remaining in the tertiary purge air. A water tank 5 installed to purify in a fourth order and accommodating polluted water 5a having an open upper side;

The air which is formed between the water tank 5 and the tertiary purified air supply unit 4 and purged in the fourth place while being in contact with the water 5a of the water tank 5 (hereinafter referred to as “fourth purified air”) is A purge air accommodating part 6 formed to be exhausted to the outside;

In order to supply the contaminated water in the water tank 5 by the water pipe 7, the wall 8b and the upper plate 8c on one side of the water tank 5 are separated from the water tank 5, and one wall ( A pump chamber (8) having a communication portion (8b ') formed thereon so that the water (5a) of the water tank (5) flows into 8b), and having a pump (8a) connected to the lower end of the water pipe (7);

The upper and lower sides of the catalyst filter unit 1, the high pressure dust collecting and ozone generating unit 2, the gas purifying unit 3, and the tertiary purifying air supply unit 4 and the wall are opened to the other side of the upper side and the lower side. The cylindrical body 9a in which the annular recess 9aa and the annular protrusion 9ab are formed in the lower part of the outer side and the inner surface of a part is provided, and it is inserted and fixed in the annular recess 9a of the upper end of the said body 9a. A cover 9b having an annular protrusion 9ba is formed inside the edge of the bottom surface, and a circular net 10 is fixed on the upper surface of the annular protrusion 9ab of the body 9a. And a catalyst mixture 9c in which activated carbon, iodine and magnesium are mixed to remove ozone and various organic substances in the body 9a, and an electrode 9d is installed so as to be electrolyzed. In the upper side of the inside containing the mixture (9c) Ultraviolet lamp 16 is installed in the part, and the upper end of the water pipe 7 is connected through the cover 9b so that the contaminated water passed through the water pipe 7 by the pump 8a is the body ( 9a) consists of a water purification unit (9) which is installed to be purified to be introduced into the contaminated water quality.

The catalyst filter unit 1, the high pressure dust collecting and ozone generating unit 2, the gas purifying unit 3, and the tertiary purifying air supply unit 4 are partitioned into four layers by a rectangular mesh 10. The support protrusions 11a are formed on the inner surface of the box body 11 so as to be mounted and fixed, and the upper and lower sides thereof are respectively formed in the box-shaped body 11 opened.

A support protrusion 12aa is formed at the lower end of the inner surface, and the lower side is open while the upper portion of the body 11, the power supply device 13, and the water purification unit 9 are built in, and an intake hole 12ab is formed on one side of the upper surface. ) Is formed in the hexahedral upper body (12a), the purifying air accommodating part (6), the lower part of the water purification unit (9), the water tank (5) and the pump chamber (8), the exhaust hole in the three-sided side 12ba are formed at regular intervals, and the support body 12bb is formed on the inner surface so that the water purification part 9 is fixed, and the upper body is formed of a hexahedral lower body 12b having an open side, and the upper body 12a. The inner body 12 is formed by inserting and fixing the inner dolce 12bc formed along the rim of the lower body 12b in the outer dolce 12ac formed along the rim of the lower end.

The power supply device 13 is installed in the space portion partitioned by the partition 14 and the wall of the body 11 on one side of the upper body 12a except for the body 11 and the water purification unit 9, A fixing hole 15b is formed at one side so that the body 9a of the water purification unit 9 can be penetrated and fixed on the support plate 15 having a plurality of exhaust holes 15a formed at regular intervals. The body 11 and the power supply 13 are mounted and fixed.

The cover 9b of the water purifying part 9 is fixed by inserting an upper end of the ultraviolet lamp 16 into a fixing hole 9bb formed at the center thereof, and formed on both sides of the fixing hole 9bb. The upper end of the electrode 9d is inserted into and fixed to the fixing hole 9bc, and the end of the upper bent portion of the water pipe 7 penetrating the upper body 12a is inserted into the fixing hole 9bd formed on one side. It's fixed,

The lower end of the water pipe 7 is connected through the wall of the pump chamber 8 while penetrating the lower body 12b.

The electrode for generating the high pressure dust and ozone is composed of a positive electrode (2a) and a negative electrode (2b), each of which is fixed to the catalyst mixture molding, the positive electrode (2a) and the negative electrode (2b) is provided with the catalyst mixture molding The catalyst mixture formed by mixing coal tar in the catalyst mixture (2aa) (2ba) in which the carbon, iodine, and magnesium are mixed and heated to a high temperature is attached to the conductors of the anode (2a) and the cathode (2b). In addition, the catalyst mixture molded body uses a high-voltage current, so that the organic matter decomposition effect as in the catalyst filter unit 1 can be obtained, and in particular, the organic material is removed by the remaining ozone while removing unnecessary ozone from the ozone generated by the high voltage. It is possible to decompose and obtain the dust collecting effect by high pressure at the same time.

Carbon, iodine, and magnesium used in the catalyst filter unit 1, the high pressure dust collecting and ozone generating unit 2, and the water purification unit 9 are installed to supply DC electricity from the air and the water purification unit. By supplying direct current electricity to the catalyst mixture in which the three components of the catalyst are mixed, the catalytic reaction occurs continuously so that the catalyst mixture can be used for a long time.

The mixing ratio of each catalyst of the catalyst mixture (1a) (2aa) (2ba) (9c) is preferably 80 to 90% by weight of carbon, 5 to 10% by weight of iodine, and 5 to 10% by weight of magnesium. The mixing ratio of the catalyst mixture (2aa) and coal tar of 2a), and the mixing ratio of the catalyst mixture (2ba) and coal tar were respectively formed by mixing 70% by weight of the catalyst mixture and 30% by weight of coal tar and then heating them at 70 ° C to 90 ° C. It is preferable to make it.

Catalytic reaction occurs when DC electricity is applied in a state in which carbon, iodine and magnesium are mixed at the above mixing ratios.

In the catalyst mixture, carbon uses activated carbon, and if carbon is contained in the ratio above, the current flows a lot and the power supply is broken.

If iodine is contained in a large amount above the above-mentioned ratio, the iodine evaporates with water by the moisture generated by supplying the direct current electricity and becomes a gas and smells a lot. There is a lot of problems, on the contrary, if the three catalyst components are less than the above ratio, respectively, the air or water purification function is reduced.

The catalytic reaction decomposes the polymer organic matter, removes and cleans various kinds of pollutants including ozone, and the catalytic reaction is continuously performed when DC electricity is supplied to the catalyst mixture as compared to conventional activated carbon which can be used only for a certain time. Because of this, there is an advantage that the catalyst mixture can be used for a long time. Specific catalytic reaction will be described later.

In the figure, reference numeral 17 denotes a cock for draining the water in the water tank 5 when installed through the walls of the lower body 12b and the water tank 5, and 18 is a wall of the lower body 12b and the water tank 5; It is installed through the water supply valve for replenishing the water in the tank (5).

The process and action of the air of the present invention configured as described above, the air using the catalyst mixture for water purification, and the water purification apparatus until the contaminated air is purified together with the reaction of the catalyst mixture will be described.

In the air and water purification process using the catalyst mixture of the present invention, the catalyst mixture 1a of the catalyst filter unit 1 is electrolyzed by the electrode 1b, and the outside polluted air is introduced into the air by the water 4a. Purifies air first by removing various organics and ozone

As the primary purified air passes through the high-pressure dust collector and the ozone generator 2, a high voltage is applied, and as the generation of ozone is reduced by the catalyst mixture of the catalyst mixture formed on the anode 2a and the cathode 2b, By applying a high voltage to the cathode and the anode, the catalyst mixture (2aa) (2ba) of the catalyst mixture molded body is electrolyzed to decompose and remove undecomposed organic matter in the primary purified air with high organic decomposition and dust collection ability. At the same time, various fine dusts are collected in the air to purify the air secondaryly.

The secondary purified air passes through the gas purifying part 3, and the secondary purged air is removed by the straw fragment 3a in which iodine penetrates into the wall, thereby purifying the air in the third time.

The third purifying air supplied by the water tank (4a) removes dust and ozone while contacting the water (5a) of the water tank (5) to purify the air in the fourth and discharge it to the outside,

Purifying the air by the fourth step, the contaminated water 5a in the water tank 5 is pumped through the water pipe 7 by the pump 8a, and the water mixture of the catalyst mixture 9c and the electrode 9d is built in. Inlet (9),

The contaminated water introduced into the water purification unit 9 flows down from the upper side to the lower side of the water purification unit 9, and purifies the water contaminated by the built-in catalyst mixture 9c to purify the water. It is a water purification process which falls to (5), and contaminated air and water quality are purified by repeating each said process continuously.

Accordingly, the anode 2a provided with the catalyst mixture body of the electrode 1b, the high pressure dust collector, and the ozone generator 2 of the catalyst filter unit 1 by turning on the power switch of the power supply unit 13 (on). When the direct current is supplied to the electrode 9d of the electrode and the water purifying part 9 composed of the negative electrode 2b, and the fan 4a, the ultraviolet lamp 16 and the pump 8a are operated, the tertiary purifying air supply part The air purified through the catalyst filter unit 1, the high pressure dust collecting and ozone generating unit 2, and the gas purifying unit 3 through the filter 4a of (4) is the third purified air supply unit ( 4) the air is purged in the fourth step while being in contact with the water from the water surface of the water tank 5 downwardly, and the fourth purification air is separated from the water purifying part 9 by the part of the purified water drops falling into the water tank 5. Fourth purification hole is discharged to the outside through the exhaust hole (12ba) formed on the side of the lower body (12b) forming the purification air receiving portion (6) together It is possible to discharge as well as to act as a humidification, and part of the purified water flows down to the lower side of the water purification unit (9) is received by falling into the water tank (5) and then contaminated again while continuing to contact with the tertiary purification air. The contaminated water 5a is continuously introduced into the water purification unit 9 through the water pipe 7 by the pump 8a, thereby purifying the water and discharging the purified air to the outside. .

Next, the process of purifying the outside polluted air will be described in more detail.

The outside contaminated air flows into the catalyst filter unit 1, and then the catalytic reaction in the catalyst filter unit 1 will be described.

Without applying any liquid components such as any solvent, the catalyst is applied to the catalyst mixture 1a in which each of the catalysts of the three components, which are 80 to 90% by weight, 5 to 10% by weight of iodine, and 5 to 10% by weight of magnesium, is mixed. Since the reaction occurs continuously, the air and the water purification device using the catalyst mixture 1a can be used for a long time,

The reaction generated by applying electricity consisting of a positive electrode and a negative electrode of a direct current electric current to a catalyst filter part 1 including a catalyst mixture 1a mixed with carbon, iodine and magnesium is mediated electrochemical oxidation (MEO). And can be explained by semiconductor theory. Instead of the electrolytic solution, the above-described solid catalyst activated carbon (carbon) or magnesium and a direct current can be considered as a modified MEO process method.

An anode and a cathode are formed on each particle of the catalyst and distributed by using the activated carbon and iodine adhered to the activated carbon as a catalyst.

The oxidant produced at the anode of each particle reacts with the organic matter adsorbed in the numerous micropores in the porous activated carbon itself to oxidatively decompose the organic matter, and at the same time, it is reduced again and oxidized at the anode, thereby continuously producing As a water-soluble process using the principle of oxidization, organic matter is almost completely destroyed, and carbon and hydrogen in the organic matter are converted into carbon dioxide and water, and most of them are mineralized. The process also has the ability to dissolve radioactive material in mixed wastes that are chemically harmful and contain radioactive material.

When electricity is applied to the installed electrode 1b, a catalytic reaction occurs, and the polymer organic matter in the air introduced by the catalytic reaction is decomposed and various kinds of pollutants are removed and purified.

Next, the catalytic reaction with respect to each component of the catalyst mixture 1a embedded in the catalyst filter 1 will be described.

When water is removed from the water-producing reaction, the reaction is accelerated and water contained in the air is easily removed, so the reaction is promoted by magnesium, which is a metal that lacks oxygen.

Mg _x-1 + H ₂ O → Mg _x O + H ₂

Therefore, the effect of the enhancer increases the reaction rate by removing the moisture in the air by magnesium.

Ozone easily reduces the smell of mold, soil, fish, and sludge, but produces fruity odors (aldehydes, ketones) after treatment. Plastics, chemicals, and astringents are odors that are difficult to reduce with ozone.

In addition, irritant gas ozone is harmful to health when light of less than 200nm wavelength is emitted into the air.

In order to remove such odors and irritating gases such as ozone, when the catalyst mixture 1a is used in the catalyst filter unit 1 at normal temperature and pressure, ozone is decomposed.

Ozone is decomposed using the catalyst mixture 1a mixed with 80 to 90% by weight of activated carbon, 5 to 10% by weight of magnesium, and 5 to 10% by weight of iodine.

2O ₃ + metal oxides → catalyst + 3O ₂

Since the oxygen present on the surface of magnesium can attract protons, the oxygen can act as a base and the second ionization potential is greater than its primary ionization potential because the removal of electrons from cations is more difficult than the ionization of neutral atoms.

Mg ⁺ (g) → Mg ⁺² + e-

Thus, metal oxide catalysts such as magnesium are used to remove polymer organics and ozone.

When protein reacts with iodine, the protein is broken down by water in iodine and air. Recently, studies have been reported in which allylglycine is introduced at a specific site using an inhibitory t-RNA, and the protein is degraded using iodine (J. Am. Chem. Soc. 2000, 122). , 7402)

That is, as shown in Fig. 5, when allylglycine is introduced to a specific position and reacted with iodine, a ring intermediate formed by iodine is formed, which is divided into two peptides having a lactone and an amine by reacting with water.

This decomposition depends largely on the location of allylglycine introduced, which is determined by how well the water in the air is accessible. This reaction converts trypsinogen, a precursor protein, to trypsin, an active protein.

Next, the action of activated carbon will be described.

In the desorption reaction, oxygen in the acid gas combines with carbon of activated carbon to cause oxidation reaction, and desorption reaction proceeds in the capillary of activated carbon. This reaction increases the specific surface area of capillary tube and causes adsorption by adsorption. The adsorption performance is improved while repeating the desorption. The loss of adsorbent caused by the reaction of oxygen in the adsorbed acid gas with carbon of activated carbon to produce carbon dioxide (CO ₂ ) is compensated.

Activated carbon is mostly carbonaceous charcoal with strong adsorption, and adsorption is an interfacial phenomenon in which powdery substances such as activated carbon or silica gel absorb contaminants from the surface. In order for this phenomenon to occur on the surface, the surface area of the powdery material must be large. Activated carbon has a very large number of fine holes, and the total area of the fine hole wall, or surface area, is usually 500 to 150 m 2 per gram. Activated carbon adsorbs so many chemicals that it can be used as a deodorant in refrigerators. Its adsorption characteristics are greatly influenced not only by the structure of the fine pores, but also by the chemical properties of the activated carbon surface. When activated carbon is added to the waste water and stirred, the concentration of organic matter in the water is remarkably decreased. This is because activated carbon adsorbs them. Since activated carbon is made of wood or coal, the original main component is organic matter.

Next, the electrolysis in the catalyst filter unit 1 will be described.

An oxidant produced on the surface of the anode reacts with the organic material to oxidatively decompose the organic material, and at the same time, it is reduced again and oxidized on the surface of the electrode 1b to reproduce the organic material continuously (Fig. 6). Through this, organic matter is almost completely destroyed, and ultimately, carbon and hydrogen in organic matter are converted into carbon dioxide and water, and most of them are mineralized.

In the reaction of positive electrode ^{_{H 2 O → H + + OH}} - OH in the reaction scheme of ^- the pH is lowered to a reduction in the increase in the ion H ⁺ ions, electrons (Electron: e-) is increased oxidative I got lost.

In the reaction of the negative electrode ^{_{H 2 O → H + + OH}} - in the reaction scheme of the H ⁺ ion and the reduction of the OH ^- and the pH is raised to increase the ion, the reducing power is increased with increase of the electron.

When electricity is applied to the installed electrode 1b, Joule heat is generated and dried and regenerated by Joule heat.The Joule heat causes the temperature of the conductor to increase when current flows, and when the temperature is kept constant, heat flows out of the conductor. This amount of heat is called Joule heat, and Joule's law states that the Joule's law is established and the amount of Joule heat that flows out within a certain time in a conductor that is maintained at a constant temperature by the steady current flowing in the conductor is proportional to the square of the current intensity and the lead resistance {Q = I ² R (I: current strength, R: resistance, Q: calories)} Heat flows out of the conductor to dry and regenerate. At this time, activated carbon serves as electrode 1b and catalyst simultaneously. Done.

The air passing through the catalyst filter part 1 passes through the high pressure dust collecting and ozone generating part 2, and a catalyst mixture of the catalyst mixture molded body attached to the ozone generated by the high voltage and the anode 2a and the cathode 2b ( 2aa) (2ba) is removed from the catalytic filter unit 1, the harmful gas introduced in the state is not decomposed and various dusts and dust in the air is collected and removed, high pressure dust and ozone generating unit (2) Esau's main role is to collect dust in the air, and in order to collect more dust, more voltage can be collected. However, the higher the voltage is, the more ozone is out of proportion than the required amount, which is a counter effect. Therefore, the unnecessary ozone is reduced by about 90% by the catalyst mixture (2aa) (2ba) of the catalyst mixture molding, and the remaining 10 % Of ozone will decompose harmful gases.

Next, the reaction relationship between ozone generated in the air and the harmful gases in the air will be described first, and then the reaction relationship between the catalyst mixtures 2aa and 2ba in the anode 2a and the cathode 2b and the harmful gases in the air will be described. Next, a description will be given regarding the collection and removal of solid particles such as various dusts and dusts in the air.

Ozone is generated by high voltage, the removal of cyanide using ozone is a well-known chemical reaction, and the ozone prescription of cyanide is known as the most suitable method for the following reasons. It works well in the presence of other contaminants. The first chemical reaction converts cyanide to cyanide, and the properties of cyanates are only 1 / 1000th of cyanide.

_{^{CN - + O 2 → CNO -}} + O 2

Next, ammonia and carbon dioxide are generated through general biological decomposition, and ammonia reacts with ozone again.

2NH ₃ + O ₂ → N ₂ + 3H ₂ O + 3O ₂

Two ammonia molecules combine with three ozone molecules to convert into one nitrogen molecule, three water molecules, and three oxygen molecules, all three of which are generally natural and are not pollutants in the atmosphere. admit.

That is, organic acids, alcohols, aldehydes and ketones (acetone types) react with ozone to generate carbon dioxide, water vapor, and oxygen, and aromatic compounds such as benzene and camphor (slight moth) react with ozone to generate carbon dioxide water vapor and oxygen. Aliphatic compounds such as butane and mineral alcohol react with ozone to produce carbon dioxide, water vapor and oxygen, and chlorides such as methyl chloride react with ozone to form hypochlorous acid, which is an intermediate process, and then produce carbon dioxide, water vapor and oxygen. Nitrogen compounds such as cyanide react with ozone to produce carbon dioxide, water vapor and nitrogen and oxygen, and sulfides such as triglycolate ammonium react with ozone to produce carbon dioxide water vapor and sulfur trioxide and oxygen, and other alkylated silicates and ionic detergents. Reacts with ozone to produce carbon dioxide vapor Hitting and generates oxygen.

Of course, these compounds do not fully cover all the classes that exist in homes and workplaces. As long as the pollution level is low, even a little ozone is enough to break them down to a level that greatly reduces the body's exposure to substances.

In addition, the results for bacteria in other common households were as follows.

Fungi, spores, and fungi can be significantly reduced by providing approximately 50 ppb of ozone in a typical home environment.

The noxious gas is caused by the reaction of the catalyst mixture 2aa and 2ba in the anode mixture 2a and the cathode 2b to which the catalyst mixture compact is attached and the harmful gas introduced in a state in which the catalyst mixture unit 1 is not decomposed. The reaction process of removing is already the same as the reaction process of removing the harmful gas by the catalyst mixture (1a) in the catalyst filter unit 1 will be omitted.

High-pressure dust collectors generate electricity by applying an electric field to dust suspended in the inflowing air, collecting particles with electrostatic force, and cleaning the gas. High DC voltage is required to collect the electricity.

Air passing through the high pressure dust collecting and ozone generating unit 2 passes through the gas purifying unit 3 and collides with the straw piece 3a in the state where gaseous iodine penetrates into the wall, thereby physically vibrating the molecule. While the harmful gases contained in the air are decomposed and purified, the protein is decomposed by the gaseous iodine penetrated into the straw piece 3a. First, allylglycine is introduced at a specific position and reacted with the iodine. Ring intermediates are formed, which react with water to split into two peptides with lactones and amines.

This decomposition depends largely on the location of allylglycine introduced, which is determined by how well the water in the air is accessible. This reaction converts trypsinogen, a precursor protein, to trypsin, an active protein.

The air which has passed through the gas purifying part 3 passes through the tertiary purge air supply part 4, and the third purified air is contacted with the water of the water tank 5 while the third purged air is contacted with the water of the water tank 5. After the remaining ozone, dust or other substances are removed, the fourth purified air is discharged to the outside through the exhaust hole 12ba.

On the other hand, contaminated water (5a) in the water tank (5) in which the polluted water is stored as ozone, dust, and the like remaining in the third purified air comes into contact with the water in the water tank (5) by the pump (8a). It is introduced into the water purification unit 9 through the water pipe (7).

The contaminated water flowing into the water purification unit 9 through the water pipe 7 is purified while passing through the water purification unit 9, and the existing adsorption / desorption process is changed by pressure (or concentration) and temperature change. On the other hand, electrosorption and desorption is a new control factor using a principle of charging or discharging the electric ion layer generated on the electrode surface by applying electric potential to the electrode of high surface area in solution as a new control factor. Since the electrical potential at the interface and the electrical properties affect the adsorption of ionic species or nonionic species from the solution, it is possible to polarize the electroconductive carbon bodies to adjust the interface potential, that is, the surface adsorption capacity. When the electrosorption and desorption process is applied to the purification of the waste liquid containing the ionic species, the ionic species in the waste liquid may be electrostatically adsorbed to the electric double layer of the electrode without a phase change when the electrical conductor is supplied with electricity.

The possibility of cation exchange can be predicted based on the amphotericity of the functional groups and the ion exchange capacity is a function of solution pH. On the other hand, the available potential can cause desalination from the dilute aqueous solution. This process has a great effect on the electrodes with reversible and acidic functional groups.

The equilibrium form of protonation and deprotonation commonly used to explain surface charge development on surfaces containing amphoteric oxidative functional groups is as follows.

MOH ⁺ ₂ MOH + H ⁺ (1)

MOH MO ^{- +} H + (2)

MOH represents the surface group oxidized on the carbon body surface here. If the properties of the carbon body surface depend on the MOH group, the overall charge of the carbon body at a given pH of the aqueous solution will be positive, neutral or negative.

During electrosorption, hydrogen ions are selectively adsorbed on the negatively charged carbon surface.

_{2H 2 O + 2e → 2H +} 2OH - (3)

Acidic groups can be ionized by decreasing the proton concentration in the bulk solution. therefore

^{2M OH + 2OH - → 2M +} O - + 2H 2 O (4)

M OH represents a neutral group here.

In Reaction Scheme (4), M OH removes ozone ions from contaminated water.

2M O + O ₃ (MO) ₂ + O ₂ (5)

On the other hand, the reaction formula at the counter electrode can be expected as follows.

H ₂ O H ⁺ ₂ + 1/2 O ₂ + e-

In general, the adsorption equilibrium at the unusable potential was reduced from the initial concentration of 29.5ppm to 10ppm after the solution contact for 32 hours, the adsorption equilibrium time was 6 hours. When three negative potentials of -0.05, -0.1, and -0.2V were available, the solution was able to completely remove O ₃ ions in all three conditions, but the adsorption rate tended to increase as the negative potential increased.

Table 1 compares the amount of O ₃ adsorption obtained at various soluble potentials after 6 hours of adsorption. From this table, the adsorption amount of O ₃ adsorbed at -0.05V and -0.2V increased by 33% and 72%, respectively.

The difference in adsorption amount between OCP and -0.2V was 1.19 mg / g, which was relatively high.

The increase in the cation adsorption capacity at the negative potential is considered to be an electrostatic effect. The increase in the amount of adsorption on carbon bodies under potential availability has also been reported in other studies.

Table 1.

Applied Potential Potential (vs. SCE) OCP -0.05V -0.1V -0.2V Adsorbed Volume (mg / g) 1.68 2.23 2.52 2.87

When a material absorbs light, a chemical reaction occurs by the energy of that light. According to quantum theory, the energy of photon E is related to its frequency (V), where E = hv and h is Planck's constant (6.6239 × 10 ^-27 erg).

Also, the frequency v is the wavelength i and i = Where C is 2.279 × 10 ¹⁰ cm / sec at the speed of light.

E of ultraviolet (uv line) having a wavelength of 100 to 400 mm is easily calculated from the above equation.

Ultraviolet rays generated from the ultraviolet lamp 16 react with ozone to produce hydroxy radicals (.OH) which are very oxidizing, and these radicals cleave C = C double bonds.

Formaldehyde is generated by photochemical reactions in the following reactions.

CHCO + hv → H ₂ + CO → H + HCO

HCHO + OH → HCO + H ₂ O

HCO + O ₂ → HO ₂ + CO

CH ₃ COOH + hv → CH ₃ O + OH

CH ₄ + OH → CH ₃ + H ₂ O

In addition to the above chemical reaction, ultraviolet rays have a bactericidal action, and have a bactericidal power, and when 1 minute of ultraviolet rays having an intensity of 100㎼ per 1 cm ² are killed for 1 minute, Escherichia coli, diphtheria bacteria, and dysentery bacteria are killed 99% and water is relatively good at ultraviolet rays. Ultraviolet irradiation is effective for sterilization and disinfection of water because of permeation.

The purified water passing through the water purification unit 9 falls into the water tank 5, and the contaminated water in the water tank 5 continues through the water pipe 7 by the pump 8a. 9) Repeat the process of supplying to the water to continue to purify the water contaminated by air.

As described above, the present invention provides a catalyst filter unit 1 configured to apply a direct current electric current in a mixed state of carbon, iodine, and magnesium as a catalyst, and a cathode 2a having a catalyst mixture molding. And the gas purifying part 3 and the water tank 5 in which the high-pressure dust collecting and ozone generating part 2, in which the negative electrode 2b is installed, and the straw piece 3a in which iodine vapor has penetrated are embedded. It is configured to remove harmful gases such as dust and ozone in tertiary purified air, and in particular, a catalyst mixture (1a) (2aa) (2ba) mixed with carbon, iodine and magnesium is used for continuous catalytic reaction. Since the contaminated air can be efficiently purified, the catalyst mixtures 1a, 2aa and 2ba can be used semi-permanently.

In addition, the contaminated water in the contaminated water tank 5 passes through the water purification unit 9, and in particular, a catalyst mixture 9c and an electrode in which carbon, iodine, and magnesium are mixed so that the catalytic reaction occurs continuously. Since it consists of three elements of 9d and the ultraviolet lamp 16, the catalyst mixture 9c can be used semi-permanently while being able to efficiently purify the water contaminated by the tertiary purified air and continue to use it. .

In addition, some of the purified water drops purified by the water purification unit 9 together with the fourth purified air discharged through the exhaust hole 12ba of the lower body 12b may be discharged through the exhaust hole 12ba. Because it is configured to have a humidification function, there is an effect that can be used semi-permanently the device of the present invention.

Claims (6)

Activated charcoal is built in, high pressure dust collector and ozone generator are installed, pump is installed to move the water in the tank to purify the water in the tank and the power supply is installed to supply the voltage. In which the purified air is discharged through the exhaust hole after the outside air is sucked and purified by the air, A catalyst filter unit 1 in which a catalyst mixture 1a is built and the electrode 1b is installed so as to purify the outside polluted air primarily; A high pressure dust collector and an ozone generator (2) installed under the catalyst filter unit (1) and provided with a cathode mixture (2a) and a cathode (2b), each of which has a catalyst mixture molded body so as to purify the air secondaryly; A gas purifying part 3 installed under the high pressure dust collecting and ozone generating part 2 and having a straw piece 3a embedded therein to purify the air in a third order; 3, which is installed under the gas purifying part 3, and has a third air 4a installed to send the third purified air downward to contact the water of the lower tank 5 to purify the tertiary purification air. A primary purifying air supply unit 4; The catalyst mixture 9c is embedded to purify the contaminated water flowing through the water pipe 7 by a pump 8a installed on one side of the water tank 5 while being installed above the water tank 5, and the electrode ( 9d) and the water purification part 9 provided with the ultraviolet lamp 16; The catalyst filter unit 1, the high pressure dust collecting and ozone generating unit 2, the gas purifying unit 3, and the tertiary purification air supply unit 4 are configured in the body 11 installed in the main body 12. Air, characterized in that the body 11 and the power supply 13 is installed on one side of the upper surface of the support plate 15 is formed with a fixing hole (15b) so that the water purification unit 9 is inserted and fixed, Air and water purification equipment using catalyst mixture for water purification 2. The apparatus for purifying air according to claim 1, wherein the straw pieces (3a) of the gas purifying part (3) are characterized in that gaseous iodine penetrates into the wall. The catalyst mixture (1a) (2aa) (2ba) (9c) contained in the catalyst filter (1), the high pressure dust collecting and ozone generating unit (2), and the water purification unit (9), respectively. Air, water purification apparatus using a catalyst mixture for air, water purification, characterized in that 80 to 90% by weight activated carbon, 5 to 10% by weight iodine, 5 to 10% by weight magnesium. The method of claim 1, wherein the body 11 is formed by a rectangular mesh 10, the catalyst filter unit 1, the high pressure dust collection and ozone generating unit 2, the gas purification unit 3, the third purification air supply unit ( 4) is formed to be partitioned into a four-layer layer consisting of the support 10 (11a) is formed on each of the inner surface to be fixed by mounting the network 10 is formed in a box shape with the upper and lower sides open Air, characterized in that the air used for the water purification catalyst mixture, water purification device. According to claim 1, wherein the main body 12 has a support protrusion 12aa is formed at the lower end of the inner surface so that the support plate 15 is fixed on the body 11, the power supply device 13, water purification The upper part of the part 9 is built-in, the lower side is open, and the upper body 12a of the hexahedron shape in which the intake hole 12ab is formed in one side of the upper surface, the purifying air accommodating part 6, and the water purification part 9 The lower part, the water tank (5), the pump chamber (8) has a built-in exhaust hole (12ba) is formed at regular intervals on the three sides of the side portion and the support projections (12bb) on the inner surface so that the water purification section (9) is fixed An inner doltte formed along a rim of the upper body of the lower body 12b in an outer dolce 12ac formed along a rim of the lower end of the upper body 12a while being formed in an open hexahedral shape. Air characterized in that 12bc is inserted and fixed, Air and water purification equipment using catalyst mixture for water purification The catalyst mixture mixture according to claim 1, wherein the catalyst mixture molding is formed by mixing 70 wt% of a catalyst mixture (2aa) (2ba) and 30 wt% of coal tar and heating them at 70 ° C to 90 ° C. Used air, water purification device