CN103673091B

CN103673091B - Oxygen-enriched air purifier capable of removing haze, organic nitrogen, sulfur, bacteria and carbon dioxide

Info

Publication number: CN103673091B
Application number: CN201310075749.8A
Authority: CN
Inventors: 蔡欣; 蔡海德
Original assignee: Individual
Current assignee: Individual
Priority date: 2013-03-11
Filing date: 2013-03-11
Publication date: 2020-11-24
Anticipated expiration: 2033-03-11
Also published as: CN103673091A

Abstract

The invention relates to an oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide. Haze, peculiar smell, carbon dioxide, nitric oxide, organic nitrogen, formaldehyde, organic benzenes, sulfides and pathogenic microorganisms of infectious diseases in the air are not only uncomfortable, but also harm the body of people, cause traffic accidents and interfere the beautiful life of people. The invention aims to purify the harmful substances in the air, and provides clean air which is free of pathogenic microorganisms, dust-free, low in carbon dioxide, oxygen-rich and pollution-free for people to breathe, so that people are happy, and the health care and life prolonging effects are achieved. The invention describes the equipment manufacturing and installation size, the flow operation and the application.

Description

Oxygen-enriched air purifier capable of removing haze, organic nitrogen, sulfur, bacteria and carbon dioxide

Technical Field

The invention relates to an air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide and enriching oxygen.

Background

Haze, peculiar smell, carbon dioxide, nitric oxide, organic nitrogen, formaldehyde, organic benzenes, sulfides and pathogenic microorganisms of infectious diseases in the air are not only uncomfortable, but also harm the body of people, cause traffic accidents and interfere the beautiful life of people. The invention aims to purify the harmful substances in the air, and provides clean air which is free of pathogenic microorganisms, dust-free, low in carbon dioxide, oxygen-rich and pollution-free for people to breathe, so that people are happy, and the health care and life prolonging effects are achieved.

Disclosure of Invention

The main purposes of the invention are as follows: the air purifier eliminates the root cause of air haze, removes various peculiar smells in the air, removes carbon dioxide in the air, kills pathogenic microorganisms of infectious diseases in the air, removes harmful chemical substances and particles in the air, removes PM2.5 particles, enriches oxygen in the air, and enables people to live a beautiful life of absorbing fresh, clean and oxygen-enriched air.

The invention is realized by the following technical scheme:

the invention relates to an air purifier for treating air haze peculiar smell and removing carbon dioxide and infectious disease epidemic particles and enriching oxygen, wherein ozone in the air purifier oxidizes organic or inorganic nitrogen oxides, sulfides, amides and peculiar smell in the air to kill pathogenic microorganisms, and unreacted ozone is decomposed into oxygen to enrich the oxygen in the air; the water in the air purifier absorbs and automatically separates nitrate and sulfate generated by nitric oxide and sulfide, and dust particles in the air are precipitated; the saturated calcium hydroxide emulsion in the air purifier absorbs purified carbon dioxide to generate calcium bicarbonate, the calcium bicarbonate takes calcium oxide as a raw material, 1 kilogram of calcium oxide can prepare 1.5 kilograms of refined calcium bicarbonate, the value is increased by 150 times, the cost for air purification is offset, and the industrial chain profit is also realized, one molecule of calcium oxide can absorb 2 molecules of carbon dioxide, and the calcium oxide can absorb 1 molecule of carbon dioxide released by preparing 1 molecule of calcium oxide when calcining calcium carbonate to prepare calcium oxide besides absorbing air carbon dioxide, and the processes of high cost, high energy consumption and high pollution of the calcium bicarbonate preparation are eliminated. The calcium bicarbonate industrial operation raw material and calcium supplement medicine auxiliary material are widely used, especially substances which can develop and enhance photosynthesis of plants, vegetables and crops, supply carbon sources for increasing carbon chains needed by growth of the plants, vegetables and crops and supply energy and energy needed by growth and metabolism of the plants, vegetables and crops are defined as energy fertilizers, and the calcium bicarbonate industrial operation raw material and the calcium supplement medicine auxiliary material are novel fertilizers. The air purifier for treating the air haze peculiar smell and removing the carbon dioxide and infectious disease epidemic particles and enriching the oxygen has good economic and social benefits.

In order to realize the technical scheme, the invention provides the air purifier for treating the air haze peculiar smell and removing carbon dioxide and epidemic infectious diseases and the process operation.

The utility model provides a remove haze and remove organic nitrogen and remove sulphur and remove infectious germ and remove carbon dioxide oxygen boosting air purifier, comprises following interconnect's part: ozone generator, ozone concentration verification flowmeter, ozone delivery pipe, upper valve of ozone delivery pipe of de-oxidizer, upper valve of ozone delivery pipe of de-carbonator, oxidizer, straight pipeline of polluted air inlet channel, cooling water spray pipe of polluted air inlet channel, inclined pipeline of polluted air inlet channel, pipeline of polluted air inlet oxidizer, cylinder of oxidizer, acid gas dissolving and absorbing chamber of oxidizer, acid water storing and cooling chamber, cooling coil, acid water discharge pipe, ash discharging hopper of oxidizer, spiral propeller shaft and blade of ash discharging hopper of oxidizer, spiral propeller reduction box of ash discharging hopper of oxidizer, spiral propeller motor of ash discharging hopper of oxidizer, electric contact controller wire, inclined pipe of ash discharging hopper of oxidizer, electric control valve A of inclined pipe of ash discharging hopper of oxidizer, electric control valve B of electric control valve of inclined pipe of ash discharging hopper of oxidizer, electric control valve B, Straight pipe of ash hopper of oxidizer, electric contact probe of closing valve, electric control valve, ash hopper of air inlet channel of polluted air, spiral propeller shaft and blade of ash hopper of air inlet channel of oxidizer, reduction box of spiral propeller of ash hopper of air inlet channel of oxidizer, motor of spiral propeller of ash hopper of air inlet channel of oxidizer, inclined pipe of ash hopper of air inlet channel of oxidizer, electric control valve A of inclined pipe of ash hopper of air inlet channel of oxidizer, washing water pipe of inclined pipe of ash hopper of air inlet channel of oxidizer, electric control valve B of inclined pipe of ash hopper of air inlet channel of oxidizer, straight pipe of ash hopper of air inlet channel of oxidizer, window of ash hopper of air inlet channel of polluted air, electric contact probe of opening valve, ozone decomposition chamber, isolation plate of ozone decomposition chamber, air outlet cyclone separator of oxidation chamber, air inlet pipe of air outlet cyclone separator of oxidation chamber, air outlet pipe of cyclone separator, 65 parts of an outlet pipe of an air outlet cyclone separator of the oxidation chamber, a clapboard between the ozone decomposition chamber and the air outlet chamber of the oxidizer, a drain pipe of the ozone decomposition chamber, an air outlet pipe of the oxidation chamber, a drain pipe of the air outlet chamber of the oxidation chamber, a carbon-containing air delivery pipe, a carbon-containing air inlet and carbon removal device mixing pipe inlet pipe, a carbon-containing air and ozone gas mixing gas inlet pipe, a carbon removal reaction chamber, a cover cap and a cover plate, an aseptic oxygen-enriched clean air water removal chamber, an aseptic oxygen-enriched clean air outlet chamber, a solid reactant inlet, a feed opening, a condensate water return pipe, a water feeding pipe and a;

one end of the ozone concentration verification flowmeter is connected with the ozone generator pipe; the other end of the ozone concentration verification flowmeter is connected with the oxidizer acid gas dissolving and absorbing chamber and the acid water storage and cooling chamber through the ozone conveying pipe; the ozone delivery pipe is provided with a valve for removing the ozone delivery pipe of the oxidizer; the oxidizer acid gas dissolving and absorbing chamber and the acid water storage and cooling chamber are internally provided with a pipeline for the polluted air to enter the oxidizer; the polluted air inlet inclined pipeline and the polluted air inlet straight pipeline which are sequentially arranged on the outer side walls of the polluted air inlet oxidizer pipeline, the oxidizer acid gas dissolving and absorbing chamber and the acid water storage cooling chamber are communicated; the inner wall of the polluted air inlet inclined pipeline is provided with the cooling water spray pipe of the polluted air inlet channel; cooling coils are arranged in the oxidizer acid gas dissolving and absorbing chamber and the acid water storage and cooling chamber; the side wall of the cylinder body of the oxidizer cylinder is communicated with the acid water discharge pipe and the electric control valve; the side wall of the cylinder body of the oxidizer cylinder is provided with an open valve electric contact probe and a close valve electric contact probe; the valve closing electric contact probe is positioned below the valve opening electric contact probe; the bottom of the oxidizer cylinder body is a conical oxidizer ash discharging hopper; a spiral propeller is arranged in the oxidizer ash discharging hopper; the screw propeller is sequentially connected with a screw propeller shaft and blades of the ash discharging hopper of the oxidizer, a reduction box of the screw propeller of the ash discharging hopper of the oxidizer, a motor of the screw propeller of the ash discharging hopper of the oxidizer and the electric contact controller; the bottom of the oxidizer ash slag discharging hopper is sequentially connected with the oxidizer ash slag discharging hopper straight pipe, the oxidizer ash slag discharging hopper inclined pipe electric control valve A, the oxidizer ash slag discharging hopper inclined pipe flushing water pipe and the oxidizer ash slag discharging hopper inclined pipe electric control valve B; the lower part of a polluted air inlet oxidizer pipeline communicated with the outer side wall of the oxidizer cylinder is communicated with the ash discharging hopper of the polluted air inlet channel; a screw propeller is arranged in the ash discharging hopper, and the screw propeller is sequentially connected with a screw propeller shaft and blades of the ash discharging hopper of the oxidizer, a reduction box of the screw propeller of the ash discharging hopper of the air inlet passage of the oxidizer and a motor of the screw propeller of the ash discharging hopper of the air inlet passage of the oxidizer; the bottom of the oxidizer ash discharging hopper is sequentially connected with the oxidizer air inlet ash discharging hopper straight pipe, the oxidizer air inlet ash discharging hopper inclined pipe electric control valve A, the oxidizer air inlet ash discharging hopper inclined pipe flushing water pipe and the oxidizer air inlet ash discharging hopper inclined pipe electric control valve B; the upper part of the cylinder body of the oxidizer cylinder is sequentially provided with the oxidizer, the air outlet cyclone separator of the oxidation chamber, the ozone decomposition chamber and the air outlet chamber of the oxidizer; the bottom of the ozone decomposition chamber is communicated with a drain pipe of the ozone decomposition chamber; the ozone decomposition chamber is provided with an oxidizer air outlet chamber partition plate and the ozone decomposition chamber partition plate; the upper part of the ozone decomposition chamber is communicated with an air outlet pipe of the ozone decomposition chamber; the air outlet pipe of the ozone decomposition chamber penetrates through the ozone decomposition chamber and the clapboard of the air outlet chamber of the oxidizer and extends into the air outlet chamber of the oxidizer; the bottom of the oxidizer gas outlet chamber is communicated with a drain pipe of the oxidizer gas outlet chamber; the upper part of the oxidation chamber air outlet cyclone separator is provided with an air outlet pipe of the oxidation chamber air outlet cyclone separator; the air outlet pipe of the air outlet cyclone separator of the oxidation chamber; the ozone decomposition chamber isolation plate penetrates through the ozone decomposition chamber and extends into the ozone decomposition chamber; the right side wall of the oxidation chamber air outlet cyclone separator is communicated with an air inlet pipe of the oxidation chamber air outlet cyclone separator; the bottom of the oxidation chamber air outlet cyclone separator is communicated with an air outlet pipe of the oxidation chamber air outlet cyclone separator; the top of the cylinder body of the oxidizer cylinder is communicated with the oxidizer gas outlet pipe; the air outlet pipe of the oxidizer is communicated with one end of the air inlet pipe of the mixing pipe of the carbon remover through the carbon-containing air conveying pipe; the other end of the carbon remover mixing tube air inlet tube is communicated with one end of the carbon-containing air and ozone gas mixed gas inlet tube; the other end of the ozone gas mixed gas inlet pipe extends into the decarbonization reaction chamber; the upper part of the decarbonization reaction chamber is provided with the cover cap and the cover plate; the side wall of the decarbonization reaction chamber is communicated with the water overflow pipe; the bottom of the decarbonization reaction chamber is communicated with the feed opening; the side wall of the other side of the carbon removal reaction chamber is communicated with the solid reactant feeding port; the sterile oxygen-enriched clean air water removing chamber and the sterile oxygen-enriched clean air outlet chamber are sequentially arranged above the decarbonization reaction chamber; the side wall of the sterile oxygen-enriched clean air outlet chamber is communicated with the condensed water return pipe; the condensed water return pipe is communicated with the water feeding pipe.

Preferably, the oxidizer is comprised of the following interconnected parts:

ozone generator, ozone concentration verification flowmeter, ozone delivery pipe, upper valve of ozone delivery pipe of de-oxidizer, upper valve of ozone delivery pipe of de-carbonator, oxidizer, straight pipeline of polluted air inlet channel, cooling water spray pipe of polluted air inlet channel, inclined pipeline of polluted air inlet channel, pipeline of polluted air inlet oxidizer, cylinder of oxidizer, acid gas dissolving and absorbing chamber of oxidizer, acid water storing and cooling chamber, cooling coil, acid water discharge pipe, ash discharging hopper of oxidizer, spiral propeller shaft and blade of ash discharging hopper of oxidizer, spiral propeller reduction box of ash discharging hopper of oxidizer, spiral propeller motor of ash discharging hopper of oxidizer, electric contact controller wire, inclined pipe of ash discharging hopper of oxidizer, electric control valve A of inclined pipe of ash discharging hopper of oxidizer, electric control valve B of electric control valve of inclined pipe of ash discharging hopper of oxidizer, electric control valve B, Straight tube of ash hopper of oxidizer, electric contact probe of closing valve, electric control valve, ash hopper of air inlet channel of polluted air, screw propeller shaft and blade of ash hopper of air inlet channel of oxidizer, reduction box of screw propeller of ash hopper of air inlet channel of oxidizer, motor of screw propeller of ash hopper of air inlet channel of oxidizer, inclined tube of ash hopper of air inlet channel of oxidizer, electric control valve A of inclined tube of ash hopper of air inlet channel of oxidizer, electric control valve B of inclined tube of ash hopper of air inlet channel of oxidizer, straight tube of ash hopper of air inlet channel of oxidizer, window of ash hopper of air inlet channel of polluted air, motor of screw propeller of ash hopper of air inlet channel of oxidizer, electric control valve A of inclined tube of ash hopper of air inlet channel of oxidizer, electric control valve B of electric control valve of inclined tube of ash hopper of oxidizer, electric control valve A of inclined tube of ash hopper of oxidizer, electric control, The device comprises an ozonolysis chamber, an ozonolysis chamber partition board, an oxidation chamber air outlet cyclone separator air inlet pipe, an oxidation chamber air outlet cyclone separator air outlet pipe, an oxidation chamber air outlet cyclone separator water outlet pipe, an ozonolysis chamber and oxidation device air outlet chamber partition board, an ozonolysis chamber drain pipe, an oxidation device air outlet chamber, an ozonolysis chamber air outlet pipe, an oxidation device air outlet chamber drain pipe, a carbon-containing air gas conveying pipe and a carbon-containing air inlet decarbonizer mixing pipe air inlet pipe which are connected with one another.

Preferably, the decarbonizer is composed of the following interconnected parts: the device comprises a carbon remover mixing tube air inlet pipe, a carbon-containing air and ozone gas mixed gas inlet pipe, a carbon removal reaction chamber, a cover cap, a cover plate, a sterile oxygen-enriched clean air water removal chamber, a sterile oxygen-enriched clean air outlet chamber, a solid reactant feeding port, a feed opening, a condensed water return pipe, a water feeding pipe and a water overflow pipe which are connected with one another.

Preferably, the basic process flow and operation are as follows:

ozone is output by an ozone generator, after the concentration detected in an ozone detection flowmeter is qualified, the concentration is determined in an ozone quantitative detection meter, the ozone enters an ozone delivery pipe through a valve on an ozone delivery pipe of a deoxidation device, the polluted air which enters an acid gas dissolving and absorbing chamber of the deoxidation device and an acid water storing and cooling chamber enters an outlet of a pipeline of the deoxidation device, the ozone is mixed with the polluted air, oxidation inorganic and organic nitrogen oxide, inorganic sulfide, organic sulfide, formaldehyde and benzene are oxidized due to high oxidation potential in acid water, and products comprise dinitrogen pentoxide, sulfur trioxide and organic acid; ozone oxidizes pyrogen produced by live, dead, pathogenic microorganisms; in the acid gas dissolving and absorbing chamber, the gas of dinitrogen pentoxide, sulfur trioxide or sulfur dioxide correspondingly generated by ozonized nitride and sulfide is dissolved and absorbed by water to correspondingly generate nitric acid, sulfuric acid or sulfurous acid aqueous solution, the water becomes acid water, and the acid water washes away tiny dust particles in the air; air for removing dust, nitride, sulfide and organic matters is separated out in acid water and enters an ozone decomposition chamber; the unreacted ozone is decomposed into oxygen in the ozone decomposition chamber, so that the air is enriched with oxygen; removing nitrogen, sulfur, organic matters, pathogenic microorganisms, dust and clean oxygen-enriched carbon-containing air, introducing the air into an air outlet cyclone separator of an oxidation chamber to separate acid water vapor, and introducing the air into an air outlet pipe of an ozone decomposition chamber to be introduced into an air outlet chamber of the oxidation chamber; nitrogen removal, sulfur removal, organic matter removal, pathogenic microorganism removal, dust removal, clean oxygen-enriched carbon-containing air suddenly enters an expanding air outlet chamber, the volume of the air expands to separate out water, and the separated water is discharged into a water discharge pipe of an ozone decomposition chamber from a water discharge pipe of an oxidizer air outlet chamber and then is discharged into an oxidizer acid gas dissolving and absorbing chamber and an acid water storage cooling chamber; if the polluted air is flue gas, the polluted air is high-temperature gas, the temperature of acid water is increased, cooling water is introduced into the polluted air through a cooling coil immersed in the acid water in an acid water storage cooling chamber for heat exchange and cooling, and the temperature of the acid water is not higher than 40 ℃; the acidic water in the acidic water storage chamber is controlled and discharged by an acidic water discharge pipe and an electric control valve, when the acidic water level reaches an open valve electric contact probe, the electric control valve is opened, the acidic water is discharged until the acidic water level is below the position of the acidic water discharge pipe, the acidic water stops being discharged, and when no acidic water is discharged, the electric control valve is automatically closed; neutralizing the discharged acid water with calcium oxide to generate calcium fluid and organic acid calcium precipitate, and dissolving the calcium nitrate generated by nitric acid in water to prepare a chemical product; defining the process flow and operation of the system as the process flow and operation of the oxidizer;

the carbon-containing air led out by the carbon-containing air enters the mixing pipe of the carbon-containing air inlet carbon remover through the carbon-containing air conveying pipeThe ozone is mixed with the carbon-containing air and enters a gas inlet pipe for mixing the carbon-containing air with the ozone, the mixture is guided into a decarbonization reaction chamber, the chamber is provided with a cover and a cover plate to separate the decarbonization reaction chamber into an oxidation and decarbonization chamber, the ozone further carries out the oxidation reaction in an oxidizer to remove harmful impurities and remove carbon, supersaturated calcium hydroxide emulsion in the chamber absorbs carbon dioxide to generate calcium carbonate, the calcium carbonate further absorbs the carbon dioxide to generate calcium bicarbonate, 70 to 90 percent of the carbon dioxide can be removed, the calcium hydroxide can further corrode and dissolve pathogenic microorganisms and remove peculiar smell, Ca in reaction liquid²⁺Calcium oxide in emulsified state in water is continuously dissolved in water for supplement; removing carbon dioxide from the oxygen-enriched air to obtain carbon-dioxide-removed oxygen-enriched clean air, making the carbon-dioxide-removed oxygen-enriched air enter into the sterile oxygen-enriched clean air water removing chamber from the tangential direction, due to the action of impacting the wall of the air outlet pipe and rotating separation, dropping water into the liquid discharge pipe at the lower part of the cyclone separator, making the air enter from the lower port of the air outlet pipe of the cyclone separator, suddenly expanding, absorbing heat and condensing from the upper port of the air outlet pipe, further removing water, discharging into the sterile oxygen-enriched clean air outlet chamber, discharging the water condensed in the air outlet chamber to the outside, making the water flow into the alkali liquor in the mixed gas reaction chamber by the condensed water return pipe, removing the sealing flange of the lower port after each batch of fermentation is finished, removing the alkali liquor and solid particles in the mixed gas reaction chamber, removing the liquid and solid particles in the mixed gas reaction chamber, recovering calcium nitrate, replacing the removed, calcium sulfate is insoluble, calcium sulfate is obtained by separation, calcium bicarbonate solution is used for preparing solid calcium bicarbonate by a conventional method, a feed opening sealing flange is closed, solid calcium oxide is added into water in a decarbonization reaction chamber and an ozonolysis chamber from a solid reactant adding opening, tap water is added into the decarbonization reaction chamber and the ozonolysis chamber from a water adding pipe while adding water, the calcium oxide is added after the calcium oxide is completely changed into calcium hydroxide, the water is adjusted and added into a water overflow pipe, and the water is added until the water flows out from the water overflow pipe and is stopped, and the operation can be carried out again; the sterile, dustless, low-carbon dioxide and oxygen-enriched clean air outlet pipe from the sterile oxygen-enriched air outlet chamber is discharged into the atmosphere by a common exhaust fan, and is used for providing people with breathing sterile, dustless, low-carbon dioxide and rich airThe technological process and operation are defined as carbon removal technological process and operation for oxygen clean air;

if the polluted air is flue gas, the polluted air is high-temperature gas, cooling water is introduced from a cooling water spray pipe of a polluted air inlet channel to pre-cool the polluted air and the cooling water in a cooling coil pipe to carry out heat exchange and temperature reduction, and the temperature of acid water in an acid gas dissolving and absorbing chamber of the oxidizer and an acid water storage and cooling chamber is not higher than 40 ℃; the cooling water in the cooling coil is soft water, and enters the boiler to be gasified after the temperature is raised, so that energy is saved; when the acid water level in the acid water storage chamber is above an open valve electric contact probe, the spiral propeller motor of the ash and slag discharging hopper of the oxidizer, the electric control valve A of the inclined pipe of the ash and slag discharging hopper of the oxidizer and the electric control valve B of the inclined pipe of the ash and slag discharging hopper of the oxidizer are started, the acid water level is reduced, when the acid water level is below a closed valve electric contact probe, the spiral propeller motor of the ash and slag discharging hopper of the oxidizer is firstly stopped, the electric control valve A of the inclined pipe of the ash and slag discharging hopper of the oxidizer is closed, at the moment, the electric control valve of the washing water pipe of the inclined pipe of the ash and slag discharging hopper of the oxidizer is automatically opened for washing for 2 minutes, the electric control valve B of the inclined pipe;

when the position of ash in a window of an ash discharging hopper of a polluted air inlet channel in a flue exceeds the glass median line of the window, opening a spiral propeller motor of the ash discharging hopper of the air inlet channel of an oxidizer, an electric control valve A of the ash discharging hopper of the air inlet channel of the oxidizer and an electric control valve B of the ash discharging hopper of the air inlet channel of the oxidizer, discharging the ash, and when the ash position descends to the point that the window of the ash discharging hopper of the polluted air inlet channel cannot be seen, stopping the work of the spiral propeller motor of the ash discharging hopper of the air inlet channel of the oxidizer, closing the electric control valve A of the ash discharging hopper of the air inlet channel of the oxidizer, automatically opening an electric valve on a washing water pipe of the ash discharging hopper of the air inlet channel of the oxidizer for washing for 2 minutes, closing the electric control;

aseptic, dustless, low carbon dioxide, the water of oxygen boosting clean air outlet chamber condensation flows to the decarbonization alkali lye by the comdenstion water return line, each batch of reaction is accomplished, pull down feed opening sealing flange, decarbonization reaction chamber alkali lye and solid grain can clear away soon, the liquid of cleaing away is used for retrieving and refines and obtains high-purity calcium bicarbonate, seal the feed opening flange, add solid calcium oxide to the decarbonization reaction chamber in solid reactant adds the mouth, from the filler pipe with water level to the water overflow pipe just outflow water stop adding water, seal the charge door, can continue to carry out air purification and use.

Preferably, the equipment and the basic process flow and operation are expanded, and the equipment and the basic process flow and operation are used for expanding the process flows and operations of dust removal, nitrogen removal, sulfur removal, harmful flue gas removal and carbon removal of a coal-fired power plant or garbage combustion power generation: the flue gas discharged from boiler is used as polluted air, and is operated according to the above-mentioned basic technological process and operation, and the flue gas treated by oxidation device is fed into carbon-removing device, and the flue gas after carbon-removing is changed into sterile dust-free low-carbon dioxide, oxygen-rich and clean air, and discharged into atmosphere by means of general-purpose exhaust fan, and said expanded technological process oxidation device and carbon-removing device must be combined for use.

Preferably, the equipment and the basic process flow and operation are expanded, and the equipment and the basic process flow and operation are used for expanding the central air conditioner of a large place for people to move, work and live: the mixed gas of return air and fresh air sucked from large places of people's activities, works and lives is used as polluted air, a mixing pipe and an air inlet pipe are added according to the conventional method, the operation is carried out according to the basic process flow and the operation, the air treated by an oxidizer is further fed into a carbon remover, the air after carbon removal is changed into sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air, the sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air is discharged into the large places of people's activities, works and lives by a common exhaust fan for people to breathe, the sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air can be connected to the air inlet of a common central air conditioning unit in winter and summer, the air conditioner unit is used for temperature regulation and humidity regulation, and then discharged into the large places of people's activities, works and lives for people to breathe, particularly a pharmaceutical preparation workshop, the air purifier and, The european union GMP certifies the requirements for air purification.

Preferably, the equipment and the basic process flow and operation are expanded, and the air conditioner is used for expanding the air conditioner of people in activities, work and living and family places: the air conditioner is combined with a household air conditioning unit according to a normal method, and sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air can be obtained and used for breathing of household people; expanding the equipment and the basic process flow and operation, reducing the sizes of the oxidizer and the decarbonizer according to a conventional method, connecting the gas discharged from an exhaust pipe of a gas vehicle into the oxidizer, then into the decarbonizer, then into an exhaust fan, and discharging sterile, dustless, low-carbon dioxide, oxygen-enriched and clean air into the atmosphere by the exhaust fan; the equipment, the basic process flow and the operation are expanded to the places of cattle raising, horse raising, sheep raising, deer raising and other livestock raising, and sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air for livestock to breathe can be obtained.

The basic technological process and operation of the equipment are expanded, calcium nitrate, calcium sulfate and calcium bicarbonate can be prepared, the calcium bicarbonate is refined into medicine auxiliary materials, and ash can be prepared into cement bricks, decoloration adsorbents, heat insulating agents and novel plastic material fillers.

Preferably, the reaction principle of air purification, the calculation formula, the equipment manufacture and the installation size are as follows:

firstly, a reaction principle;

air reacts under an electric spark:

oxygen in the air becomes ozone: 3O₂→2O₃，O₃→O₂+[O]

Nitrogen in air becomes dinitrogen pentoxide: 2N₂+5[O]→2N₂O₅

Ozone peculiar smell removing reaction:

O₃→O₂+[O]

[ O ] is a strong oxidant;

[ O ] + bacterial cells or cadaver fragments thereof → odorless oxidation products

[O]+ amine Compound → N₂+NO₂

[O]+H₂S→SO₃+H₂O

[O]+[NH₄]₂S→SO₃+NO₂+H₂O

[O]+2 NO₂→N₂O₅

Reaction in alkaline solution:

O₃+H₂O→H₂O₂+O₂→H₂O+O₂+[O]

H₂O₂also has [ O ]]The above-mentioned reaction for removing an offensive odor; it can be seen that ozone has a greater ability to deodorize in aqueous solutions because of the H produced by ozone₂O₂More [ O ] can be generated]The capability of removing peculiar smell is stronger;

CaO+H₂O→Ca(OH)₂→Ca²⁺+2OH^-

OH^-+ bacterial cells and their fragment oxidation products → water-soluble peptide amino acids and the like

SO₃+H₂O→H₂SO₄

H₂SO₄+Ca²⁺+2OH^-→CaSO₄↓+2H₂O

N₂O₅+H₂O→2 HNO₃

HNO₃+OH^-→NO₃ ^-+H₂O

CO₂+2OH^-→CO² ₃ ^-+H₂O

Ca²⁺+CO₃ ^2-→CaCO₃↓

Calcium sulfate and calcium carbonate can be seen to precipitate, and calcium nitrate can be naturally separated in the solution; recovering calcium nitrate from the solution, wherein calcium carbonate and calcium sulfate can be placed in carbon dioxide solution again, calcium carbonate is changed into calcium bicarbonate to be dissolved in water, calcium sulfate is not dissolved, and the calcium carbonate are separated; the calcium bicarbonate solution is prepared into solid calcium bicarbonate by a common industrial method;

CaCO₃+CO₂+H₂O→2Ca(HCO₃)₂

the decomposition of the excess ozone releases an oxygen reaction:

O₃→O₂+[O]

2[O]→O₂

secondly, quantitatively calculating the required ozone amount:

the quantitative calculation formula of the required ozone amount is as follows:

the ozone is used for sterilizing, deodorizing and decomposing the fermentation tail gas to release oxygen, and the concentration of the ozone required for treating the fermentation tail gas is 31 multiplied by 10^-6(V/V) since the ozone generators are all specified in terms of the weight of ozone produced per hour, the weight concentration of the ozone required in terms of conversion is 0.06085g/m³The natural decay rate of ozone is 62.25%, and the effective rate of ozone is 1-62.25%, namely 37.75%; the calculation formula of ozone is as follows:

Q＝C×V×60/37.75％

q: the required ozone amount per hour, g/h;

c: the concentration of ozone required for removing peculiar smell and sterilizing in tail gas is 0.06085g/m³；

V: output of fermentation tail gas m per minute³/min；

Thirdly, the calculation formula of the calcium oxide requirement is as follows:

and (3) calculating the carbon dioxide removal amount:

fermenting with antibiotics to produce carbon dioxide with amount of 0.03% of carbon dioxide in air being less than 2% of oxygen in air entering into the fermentation tank; at normal temperature, oxygen is 20.93% of air, and the density of fermentation tail gas is 1.3kg/m after fermentation in a fermentation tank³Then, the empirical formula for removing the carbon dioxide amount in the fermentation tail gas in the whole fermentation period is as follows:

W＝V×1.3×20.9％×2％×η×60×h

w: the amount of carbon dioxide removed in the whole fermentation period is kg;

v: amount of exhaust gas discharged from fermentation, m³/min；

Eta: the efficiency of carbon dioxide removal; 70% -99.9%;

h: the whole fermentation cycle time;

5.3.2 calculation of the amount of calcium oxide required:

the reaction formula is as follows: CaO + H₂O→Ca^2*+2OH^-

CO₂+2OH^-+Ca²⁺→CaCO₃↓+H₂O

Namely: CaO + CO₂→CaCO₃↓

56 44

G W

44/56＝W/G

G＝W×56/44

G: amount of calcium oxide required

W: the amount of carbon dioxide to be removed

Fourthly, the model of the air purifier for treating the air haze peculiar smell and removing carbon dioxide and infectious disease epidemic particles and more oxygen-enriched air, the model of the oxidizer and the model defined by the carbon remover model are as follows: air purifier model definition: KQJ-YH-CT-X, wherein KQJ is the Chinese phonetic alphabet consonant of the air purifier, YH is the oxidized Chinese phonetic alphabet consonant, CT is the carbon-removed Chinese phonetic alphabet consonant, and X is the polluted air which needs to be purified when the person is transported per minute; the middle of the flow range; definition of the oxidizer type: YHQ-X, HYQ is the Chinese phonetic alphabet of the oxidizer, and X is the polluted air which needs to be purified by inputting people every minute; the middle of the flow range; carbon remover type number definition: WQJ-X is tail gas purification Chinese phonetic alphabet initial consonant, and X is the air pollution purification requirement for people to be transported per minute; the middle of the flow range;

fifthly, specification comparison tables of air purifier, oxidizer and decarbonizer types are as follows:

sixthly, manufacturing and mounting size of the oxidizer equipment: the sizes of the oxidizer cylinder, the cone seal head and the air inlet and outlet are as follows: unit mm, design working pressure ±.09 MPa:

seventhly, the sizes of the polluted air inlet pipeline, the cooling system and the ash removal system are as follows: unit mm, design working pressure ± 0.09 MPa:

eighthly, the sizes of the acid gas dissolving and absorbing chamber of the oxidizer, the acid water storage and cooling chamber and the air outlet cyclone separator system of the oxidation chamber are as follows: unit mm, design working pressure ± 0.09 MPa:

ninth, the manufacturing and installation sizes of the air outlet cyclone separator of the oxidation chamber and the ozonolysis chamber of the oxidizer are as follows: unit mm, design working pressure ± 0.09 MPa:

tenth, ozone decomposition chamber and oxidizer gas outlet chamber manufacturing installation size: unit mm, design working pressure ± 0.09 MPa:

eleventh, equipment material parameter table:

twelfth, the equipment relates to the parameters of the thickness of the cylinder body, the thickness of the cone seal head, the ash blanking hopper, the partition plate and the thickness of the pipe wall: mm is

Thirteen, equipment-related angle parameters: unit: degree of rotation

The power of the motor of the spiral propeller of the ash discharging hopper for discharging the ash slag is more than 4.5 kilowatts, and the power is selected according to the material quantity and the viscosity.

Drawings

FIG. 1 is a schematic diagram of the structural components, basic process flow and operation, manufacture and installation dimensions of a haze-removing, organic nitrogen-removing, sulfur-removing, germ-removing and carbon dioxide-removing oxygen-enriched air purifier. The abstract figure and the specification figure of the patent document are shown.

Reference numerals

In the figure, 101, an ozone generator, 102, an ozone concentration verification flowmeter, 10002, an ozone delivery pipe, 10003, an upper valve of an ozone delivery pipe of a de-oxidizer, 10004, an upper valve of an ozone delivery pipe of a de-carbon device, 10000, an oxidizer, 300, a straight pipeline of a polluted air inlet, 301, a cooling water spray pipe of a polluted air inlet, 400, an inclined inlet pipeline of polluted air, 500, a pipeline of a polluted air inlet oxidizer, 600, a cylindrical barrel of the oxidizer, 601, an acid gas dissolving and absorbing chamber of the oxidizer and a cooling chamber of acid water storage, 701, a cooling coil, 702, an acid water discharge pipe, 703, ash, 800, an ash discharge hopper of the oxidizer, 801, a spiral propeller shaft and blades of the ash discharge hopper of the oxidizer, 802, a spiral propeller reduction box of the ash discharge hopper, 803, a spiral propeller motor of the ash discharge hopper of the oxidizer, 804, an electric contact point controller wire, 805, an inclined hopper discharge pipe of the oxidizer, 806. an oxidizer ash hopper inclined pipe electric control valve A, 807, an oxidizer ash hopper inclined pipe flushing water pipe, 808, an oxidizer ash hopper inclined pipe electric control valve B, 809, an oxidizer ash hopper straight pipe, 810, a closing valve electric contact probe, 811, an electric control valve, 8000, a polluted air inlet duct ash hopper, 8001, an oxidizer inlet duct ash hopper spiral propeller shaft and blades, 8002, an oxidizer inlet duct ash hopper spiral propeller reduction box, 8003, an oxidizer inlet duct ash hopper spiral propeller motor, 8005, an oxidizer inlet duct ash hopper inclined pipe, 8006, an oxidizer inlet duct ash hopper inclined pipe electric control valve A, 8007, an oxidizer inlet duct ash hopper inclined pipe flushing water pipe, 8008, an oxidizer inlet duct ash hopper inclined pipe electric control valve B, 8009, an oxidizer inlet duct ash hopper straight pipe, 80090, a polluted air ash hopper, 8019. an electric contact probe of a valve is opened, 900 parts of an ozone decomposition chamber, 901 parts of an ozone decomposition chamber partition board, 1000 parts of an oxidation chamber air outlet cyclone separator, 1001 parts of an oxidation chamber air outlet cyclone separator air inlet pipe, 1002 parts of an oxidation chamber air outlet cyclone separator air outlet pipe, 1003 parts of an oxidation chamber air outlet cyclone separator water outlet pipe, 1104 parts of an ozone decomposition chamber and an oxidation device air outlet chamber partition board, 1005 parts of an ozone decomposition chamber water outlet pipe, 1100 parts of an oxidation device air outlet chamber, 1101 parts of an ozone decomposition chamber air outlet pipe, 1102 parts of an oxidation device air outlet pipe, 1103 parts of an oxidation device air outlet chamber water outlet pipe, 1105 parts of a carbon-containing air gas conveying pipe, 10001 parts of carbon-containing air, 2 parts of a carbon remover mixing pipe air inlet pipe, 3 parts of carbon-containing air and ozone gas mixed gas inlet pipe, 4 parts of a carbon removal reaction chamber, 5 parts of a cover and a cover plate, 6 parts of a sterile oxygen-, 9. a feed opening, 10 a condensate water return pipe, 11 a water feeding pipe and 12 a water overflow pipe.

Detailed Description

Example 1:

(1) the flow of the polluted air entering the air inlet of the oxidizer is 1m³Min, taking the middle value of the flow range as 20m³The method comprises the following steps of (1) min equipment, determining equipment type high specification, manufacturing and installing size, angle, thickness and angle of each material:

the model specification comparison table of the air purifier, the oxidizer and the carbon remover in the table 7.1 shows that:

from table 8.1 it is known that: the sizes of the cylinder body, the cone seal head and the air inlet and outlet of the oxidizer are as follows: unit mm, design working pressure +/-0.09 MPa.

Table 8.2: contaminated air intake duct 300, cooling, ash removal system size: unit mm, design working pressure ± 0.09 MPa:

table 8.3: the system size of the oxidizer acid gas dissolving and absorbing chamber, the acid water storage and cooling chamber 601, and the oxidizer outlet cyclone 1000: unit mm, design working pressure ± 0.09 MPa:

table 8.4: the installation dimensions of the oxidation chamber outlet cyclone 1000 and the oxidizer ozonolysis chamber are: unit mm, design working pressure ± 0.09 MPa:

table 8.5: the ozonolysis chamber 900 and oxidizer outlet chamber 1100 were manufactured with the installation dimensions: unit mm, design working pressure ± 0.09 MPa:

8.6 Equipment Material parameter Table:

8.7 the parameters of the thickness of the closed cylinder body, the thickness of the cone seal head, the ash discharging hopper, the partition plate and the thickness of the pipe wall of the equipment in the figure 1 are as follows: mm is

Table 8.8 relevant angle parameters of the device of fig. 1: unit: degree of rotation

(2) Determining the required ozone input amount:

the empirical calculation formula is:

Q＝C×V×60/37.75％

q: the required ozone amount per hour, g/h;

c: the required ozone concentration in the tail gas is 0.06085g/m³；

V: output of fermentation tail gas m per minute³/min。

And (3) calculating:

Q＝0.06085×V×60/37.75％

＝0.06085×1×60÷37.5％

9.736(g/h), 10(g/h) was taken.

An ozone generator with the specification of 10g of ozone per hour needs to be configured.

(3) Determining the weight of the required calcium oxide or sodium hydroxide:

(3.1) the amount of carbon dioxide in the fermentation tail gas removed is as follows:

W＝V×1.3×20.9％×2％×η×60×h

w: the amount of carbon dioxide removed during the entire air purification period, kg;

v: amount of contaminated air, 1m³/min；

Eta: the efficiency of carbon dioxide removal; taking 99.9%;

h: and taking purified air for 50 hours in the whole fermentation period.

W＝1×1.3×20.9％×2％×99.9％×60×50

＝16.2857(kg)

(3.2) calculation of the amount of calcium oxide required:

the reaction formula is as follows: CaO + H₂O→Ca²⁺+2OH^-

CO₂+2OH^-+Ca²⁺→CaCO₃+H₂O

Namely: CaO + CO₂→CaCO₃↓

56 44

G W

44/56＝W/G

G＝W×56/44

＝16.2857×56÷44

20.73(kg), 21 kg.

The amount of calcium oxide required was 21 kg.

(4) The process and the operation are as follows: as described above.

(5) And the actual effect is as follows:

note: the percentages in this table are by volume.

Example 2

(1) The flow of the polluted air entering the air inlet of the oxidizer is 75m³And/min. Taking the flow range value as 80m³The method comprises the following steps of (1) min equipment, determining equipment type high specification, manufacturing and installing size, angle, thickness and angle of each material:

table 7.1 specification comparison table of air cleaner, oxidizer, decarbonizer types:

eighthly, manufacturing and installing size of the oxidizer equipment:

table 8.1: the sizes of the oxidizer cylinder, the cone seal head and the air inlet and outlet are as follows: unit mm, design working pressure +/-09 MPa

8.6 Equipment Material parameter Table:

(2) Determining the required ozone input amount:

the empirical calculation formula is:

Q＝C×V×60/37.75％

q: the required ozone amount per hour, g/h;

c: the required ozone concentration in the tail gas is 0.06085g/m³；

V: air input m of polluted air treated per minute³/min。

And (3) calculating:

Q＝0.06085×80×60/37.75％

＝0.06085×80×60÷37.5％

778.88(g/h), 800 (g/h).

An ozone generator with the specification of 800g of ozone per hour needs to be configured.

(3) Determining the weight of the required calcium oxide or sodium hydroxide:

W＝V×1.3×20.9％×2％×η×60×h

v: amount of contaminated air, 80m³/min；

Eta: the efficiency of carbon dioxide removal; taking 99.9%;

h: and taking purified air for 50 hours in the whole fermentation period.

W＝80×1.3×20.9％×2％×99.9％×60×50

＝12684.6(kg)

(3.2) calculation of the amount of calcium oxide required:

the reaction formula is as follows: CaO + H₂O→Ca²⁺+2OH^-

CO₂+2OH^-+Ca²⁺→CaCO₃↓+H₂O

Namely: CaO + CO₂→CaCO₃↓

56 44

G W

44/56＝W/G

G＝W×56/44

＝×56÷44

＝161444(kg)。

The amount of calcium oxide required was 16144 kg.

The process flow operation is as described above.

(4) The process flow and operation are the same as those described above.

(5) And the actual effect is as follows:

(5) note: the percentages in this table are by volume

Example 3

The flow rate of the polluted air entering the air inlet of the oxidizer is 200m 3/min. Taking equipment with a flow range value of 150m3/min, determining equipment type high specification, manufacturing and installing size, angle, thickness and angle of each material:

eighthly, manufacturing and installing size of the oxidizer equipment:

8.6 Equipment Material parameter Table:

(2) Determining the required ozone input amount:

the empirical calculation formula is:

Q＝C×V×60/37.75％

q: the required ozone amount per hour, g/h;

c: the required ozone concentration in the tail gas is 0.06085g/m³；

V: air input m of polluted air treated per minute³/min。

And (3) calculating:

Q＝0.06085×200×60/37.75％

＝0.06085×200×60÷37.5％

＝1947.2(g/h)。

(3) Determining the weight of the required calcium oxide or sodium hydroxide:

W＝V×1.3×20.9％×2％×η×60×h

w: the amount of carbon dioxide removed during the entire air purification period, kg; v: amount of contaminated air, 200m³/min；

Eta: the carbon dioxide removal efficiency is as follows: taking 99.9%;

h: and taking purified air for 50 hours in the whole fermentation period.

W＝200×1.3×20.9％×2％×99.9％×60×50

＝3257.1(kg)

(3.2) calculation of the amount of calcium oxide required:

the reaction formula is as follows: CaO + H₂O→Ca²⁺+2OH^-

CO₂+2OH^-+Ca²⁺→CaCO₃↓+H₂O

Namely: CaO + CO₂→CaCO³↓

56 44

G W

44/56＝W/G

G＝W×56/44

＝3257.1×56÷44

＝4145.5(kg)。

The amount of calcium oxide required was 16144 kg.

(4) The process flow operation is as described above.

(5) (5) actual effects:

note: the percentages in this table are by volume.

Claims

1. The utility model provides a remove organic nitrogen of haze and remove sulphur and remove infectious germ and remove carbon dioxide oxygen boosting air purifier, characterized by comprises following interconnect's part: ozone generator (101), ozone concentration verification flowmeter (102), ozone delivery pipe (10002), go up valve (10003) of oxidizer ozone delivery pipe, go up valve (10004) of carbon removal ware ozone delivery pipe, oxidizer (10000), contaminated air intake duct straight pipeline (300), contaminated air intake duct cooling water shower (301), contaminated air intake inclined pipeline (400), contaminated air advances oxidizer pipeline (500), oxidizer cylinder barrel (600), oxidizer sour gas dissolves absorption chamber and sour water storage cooling chamber (601), cooling coil (701), sour water discharge pipe (702), lime-ash (703), oxidizer lime-ash blanking fill (800), oxidizer lime-ash blanking fill screw propeller shaft and blade (801), oxidizer lime-ash blanking fill screw propeller reduction box (802), oxidizer lime-ash blanking fill screw propeller motor (803), electric contact controller wiring (804), An oxidizer ash hopper inclined pipe (805), an oxidizer ash hopper inclined pipe electric control valve A (806), an oxidizer ash hopper inclined pipe flushing water pipe (807), an oxidizer ash hopper inclined pipe electric control valve B (808), an oxidizer ash hopper straight pipe (809), a valve closing electric contact probe (810), an electric control valve (811), a polluted air inlet channel ash hopper (8000), an oxidizer inlet channel ash hopper spiral propeller shaft and blade (8001), an oxidizer inlet channel ash hopper spiral propeller reduction gearbox (8002), an oxidizer inlet channel ash hopper spiral propeller motor (8003), an oxidizer inlet channel ash hopper inclined pipe (8005), an oxidizer inlet channel ash hopper inclined pipe electric control valve A (8006), an oxidizer inlet channel ash hopper inclined pipe flushing water pipe (8007), an oxidizer inlet channel ash hopper inclined pipe electric control valve B (8008), Straight pipe (8009) of ash discharging hopper of air inlet channel of oxidizer, window (80090) of ash discharging hopper of air inlet channel of polluted air, probe (8019) of electric contact point of valve opening, ozonolysis chamber (900), partition board of ozonolysis chamber (901), cyclone separator (1000) of air outlet of oxidation chamber, cyclone separator air inlet pipe (1001) of air outlet of oxidation chamber, cyclone separator air outlet pipe (1002) of air outlet of oxidation chamber, cyclone separator water outlet pipe (1003) of air outlet of oxidation chamber, partition board (1104) of air outlet chamber of ozonolysis chamber and oxidizer, drain pipe (1005) of ozonolysis chamber, air outlet chamber of oxidizer (1100), air outlet pipe (1101) of ozone decomposition chamber, air outlet pipe (1102) of oxidizer, drain pipe (1103) of air outlet chamber of oxidizer, air conveying pipe (1105) of carbon-containing air (10001) in mixing pipe of carbon removing device, air inlet pipe (, 65 parts of a decarbonization reaction chamber (4), a cover cap and a cover plate (5), a sterile oxygen-enriched clean air water removal chamber (6), a sterile oxygen-enriched clean air outlet chamber (7), a solid reactant feeding port (8), a feeding port (9), a condensed water return pipe (10), a water feeding pipe (11) and a water overflow pipe (12) are connected with one another;

one end of the ozone concentration verification flowmeter (102) is connected with the ozone generator (101) through a pipe; the other end of the ozone concentration verification flowmeter (102) is connected with the oxidizer acid gas dissolution absorption chamber and the acid water storage cooling chamber (601) through the ozone conveying pipe (10002); the ozone delivery pipe (10002) is provided with a valve (10003) for removing the ozone delivery pipe of the oxidizer; the oxidizer acid gas dissolving and absorbing chamber and the acid water storage and cooling chamber (601) are internally provided with a pipeline (500) for feeding the polluted air into the oxidizer; the polluted air inlet inclined pipeline (400) and the polluted air inlet straight pipeline (300) which are sequentially arranged on the outer side walls of the polluted air inlet oxidizer pipeline (500), the oxidizer acid gas dissolving and absorbing chamber and the acid water storage cooling chamber (601) are communicated; the inner wall of the polluted air inlet inclined pipeline (400) is provided with a cooling water spray pipe (301) of the polluted air inlet channel; cooling coils (701) are arranged in the oxidizer acid gas dissolving and absorbing chamber and the acid water storage and cooling chamber (601); the side wall of the cylindrical barrel (600) of the oxidizer is communicated with the acid water discharge pipe (702) and the electric control valve (811); the side wall of the oxidizer cylinder barrel (600) is provided with a valve opening electric contact probe (8019) and a valve closing electric contact probe (810); the valve-closing electrical contact probe (810) is located below the valve-opening electrical contact probe (8019); the bottom of the oxidizer cylinder body (600) is provided with a conical oxidizer ash discharging hopper (800); a screw propeller is arranged in the oxidizer ash discharging hopper (800); the screw propeller is sequentially connected with a screw propeller shaft and blades (801) of the ash discharging hopper of the oxidizer, a reduction box (802) of the screw propeller of the ash discharging hopper of the oxidizer, a motor (803) of the screw propeller of the ash discharging hopper of the oxidizer and the electric contact controller wire (804); the bottom of the oxidizer ash discharging hopper (800) is sequentially connected with the oxidizer ash discharging hopper straight pipe (809), the oxidizer ash discharging hopper inclined pipe (805), the oxidizer ash discharging hopper inclined pipe electric control valve A (806), the oxidizer ash discharging hopper inclined pipe flushing water pipe (807) and the oxidizer ash discharging hopper inclined pipe electric control valve B (808); the lower part of a polluted air inlet oxidizer pipeline communicated with the outer side wall of the oxidizer cylinder (600) is communicated with the ash and slag discharging hopper (8000) of the polluted air inlet channel; a screw propeller is arranged in the ash discharging hopper (8000), and is sequentially connected with a screw propeller shaft and blades (8001) of the ash discharging hopper of the oxidizer, a reduction box (8002) of the ash discharging hopper of the air inlet passage of the oxidizer and a motor (8003) of the ash discharging hopper of the air inlet passage of the oxidizer; the bottom of the oxidizer ash discharging hopper (800) is sequentially connected with the oxidizer air inlet ash discharging hopper straight pipe (8009), the oxidizer air inlet ash discharging hopper inclined pipe (8005), the oxidizer air inlet ash discharging hopper electric control valve A (8006), the oxidizer air inlet ash discharging hopper inclined pipe flushing water pipe (8007) and the oxidizer air inlet ash discharging hopper inclined pipe electric control valve B (8008); the upper part of the oxidizer cylinder body (600) is sequentially provided with the oxidizer (10000), the oxidation chamber gas outlet cyclone separator (1000), the ozone decomposition chamber (900) and the oxidizer gas outlet chamber (1100); the bottom of the ozone decomposition chamber (900) is communicated with the ozone decomposition chamber drain pipe (1005); the ozone decomposition chamber (900) is provided with an oxidizer outlet chamber partition plate (1104) and the ozone decomposition chamber partition plate (901); the upper part of the ozone decomposition chamber (900) is communicated with the ozone decomposition chamber air outlet pipe (1101); the ozone decomposition chamber gas outlet pipe (1101) penetrates through the ozone decomposition chamber and the oxidizer gas outlet chamber partition plate (1104) and extends into the oxidizer gas outlet chamber (1100); the bottom of the oxidizer gas outlet chamber (1100) is communicated with a gas outlet chamber drain pipe (1103) of the oxidizer; an air outlet pipe (1002) of the oxidation chamber air outlet cyclone separator is arranged at the upper part of the oxidation chamber air outlet cyclone separator (1000); an air outlet pipe (1002) of the oxidation chamber air outlet cyclone separator; extends into the ozonolysis chamber (900) through the ozonolysis chamber partition plate (901); the right side wall of the oxidation chamber air outlet cyclone separator (1000) is communicated with an air inlet pipe (1001) of the oxidation chamber air outlet cyclone separator; the bottom of the oxidation chamber air outlet cyclone separator (1000) is communicated with an oxidation chamber air outlet cyclone separator water outlet pipe (1003); the top of the oxidizer cylinder body (600) is communicated with the oxidizer gas outlet pipe (1102); the oxidizer air outlet pipe (1102) is communicated with one end of the carbon remover mixing pipe air inlet pipe (2) through the carbon-containing air conveying pipe (1105); the other end of the carbon remover mixing tube air inlet tube (2) is communicated with one end of the carbon-containing air and ozone gas mixed gas inlet tube (3); the other end of the ozone gas mixed gas inlet pipe (3) extends into the decarbonization reaction chamber (4); the upper part of the decarbonization reaction chamber (4) is provided with the cover cap and the cover plate (5); the side wall of the decarbonization reaction chamber (4) is communicated with the water overflow pipe (12); the bottom of the decarbonization reaction chamber (4) is communicated with the feed opening (9); the side wall of the other surface of the carbon removal reaction chamber (4) is communicated with the solid reactant adding port (8); the sterile oxygen-enriched clean air water removing chamber (6) and the sterile oxygen-enriched clean air outlet chamber (7) are sequentially arranged above the decarbonization reaction chamber (4); the side wall of the sterile oxygen-enriched clean air outlet chamber (7) is communicated with the condensed water return pipe (10); the condensed water return pipe (10) is communicated with the water feeding pipe (11).

2. The oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide as claimed in claim 1, wherein the oxidizer comprises the following interconnected components:

ozone generator (101), ozone concentration verification flowmeter (102), ozone delivery pipe (10002), go up valve (10003) of oxidizer ozone delivery pipe, go up valve (10004) of carbon removal ware ozone delivery pipe, oxidizer (10000), contaminated air intake duct straight pipeline (300), contaminated air intake duct cooling water shower (301), contaminated air intake inclined pipeline (400), contaminated air advances oxidizer pipeline (500), oxidizer cylinder barrel (600), oxidizer sour gas dissolves absorption chamber and sour water storage cooling chamber (601), cooling coil (701), sour water discharge pipe (702), lime-ash (703), oxidizer lime-ash blanking fill (800), oxidizer lime-ash blanking fill screw propeller shaft and blade (801), oxidizer lime-ash blanking fill screw propeller reduction box (802), oxidizer lime-ash blanking fill screw propeller motor (803), electric contact controller wiring (804), An oxidizer ash hopper inclined pipe (805), an oxidizer ash hopper inclined pipe electric control valve A (806), an oxidizer ash hopper inclined pipe flushing water pipe (807), an oxidizer ash hopper inclined pipe electric control valve B (808), an oxidizer ash hopper straight pipe (809), a valve closing electric contact probe (810), an electric control valve (811), a polluted air inlet channel ash hopper (8000), an oxidizer inlet channel ash hopper spiral propeller shaft and blade (8001), an oxidizer inlet channel ash hopper spiral propeller reduction gearbox (8002), an oxidizer inlet channel ash hopper spiral propeller motor (8003), an oxidizer inlet channel ash hopper inclined pipe (8005), an oxidizer inlet channel ash hopper inclined pipe electric control valve A (8006), an oxidizer inlet channel ash hopper inclined pipe flushing water pipe (8007), an oxidizer inlet channel ash hopper inclined pipe electric control valve B (8008), An oxidizer inlet channel ash discharging hopper straight pipe (8009), a polluted air inlet channel ash discharging hopper window (80090), an oxidizer inlet channel ash discharging hopper screw propeller motor (8003), an oxidizer inlet channel ash discharging hopper inclined pipe electric control valve A (8006), an oxidizer inlet channel ash discharging hopper inclined pipe electric control valve B (8008), an oxidizer inlet channel ash discharging hopper inclined pipe electric control valve A (8006) and a valve opening electric contact probe (8019), an ozone decomposition chamber (900), an ozone decomposition chamber partition plate (901), an oxidation chamber air outlet cyclone separator (1000), an oxidation chamber air outlet cyclone separator air inlet pipe (1001), an oxidation chamber air outlet cyclone separator air outlet pipe (1002), an oxidation chamber air outlet cyclone separator water outlet pipe (1003), an ozone decomposition chamber and an oxidizer air outlet chamber partition plate (1104), an ozone decomposition chamber water outlet pipe (1005), an oxidizer air outlet chamber (1100), The ozone decomposition chamber comprises an ozone decomposition chamber air outlet pipe (1101), an oxidizer air outlet pipe (1102), an oxidizer air outlet chamber drain pipe (1103), a carbon-containing air conveying pipe (1105) and carbon-containing air (10001) which enter a carbon remover mixing pipe air inlet pipe (2) which are connected with one another.

3. The oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide as claimed in claim 1, wherein the carbon remover comprises the following interconnected components: the device comprises a carbon remover mixing tube air inlet pipe (2), a carbon-containing air and ozone mixed gas air inlet pipe (3), a carbon removal reaction chamber (4), a cover cap and a cover plate (5), an aseptic oxygen-enriched clean air water removal chamber (6), an aseptic oxygen-enriched clean air outlet chamber (7), a solid reactant feeding port (8), a feeding port (9), a condensed water return pipe (10), a water feeding pipe (11) and a water overflow pipe (12) which are connected with one another.

4. The oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide according to claim 1, which is characterized by comprising the following basic process flows and operations:

ozone is output by an ozone generator (101), after the concentration detected by an ozone detection flowmeter (102) is qualified, the concentration is determined by an ozone quantitative detection meter, the polluted air which enters an ozone conveying pipe (10002) through a valve (10003) on an ozone conveying pipe of a deoxidizer to an oxidizer acid gas dissolving and absorbing chamber and an acid water storage and cooling chamber (601) enters an outlet of an oxidizer pipeline (500), the ozone is mixed with the polluted air, oxidation inorganic, organic nitrogen oxide, inorganic sulfide, organic sulfide, formaldehyde and benzene are oxidized due to high oxidation potential in acid water, and products comprise dinitrogen pentoxide, sulfur trioxide and organic acid; ozone oxidizes pyrogen produced by live, dead, pathogenic microorganisms; in the acid gas dissolving and absorbing chamber, the gas of dinitrogen pentoxide, sulfur trioxide or sulfur dioxide correspondingly generated by ozonized nitride and sulfide is dissolved and absorbed by water to correspondingly generate nitric acid, sulfuric acid or sulfurous acid aqueous solution, the water becomes acid water, and the acid water washes away tiny dust particles in the air; air for removing dust, nitride, sulfide and organic matters is separated out in acid water and enters an ozone decomposition chamber (900); the unreacted ozone is decomposed into oxygen in the ozone decomposition chamber, so that the air is enriched with oxygen; nitrogen removal, sulfur removal, organic matter removal, pathogenic microorganism removal, dust removal and clean oxygen-enriched carbon-containing air enter an oxidation chamber air outlet cyclone separator (1000) to separate acid water vapor, and then are guided into an ozone decomposition chamber air outlet pipe (1101) to be guided into an oxidation chamber air outlet chamber (1100); nitrogen removal, sulfur removal, organic matter removal, pathogenic microorganism removal, dust removal, clean oxygen-enriched carbon-containing air suddenly enters an expanding air outlet chamber, the volume of the air expands to separate out water, the separated water is discharged into a water discharge pipe (1005) of an ozone decomposition chamber through a water discharge pipe (1103) of an oxidizer air outlet chamber, and then is discharged into an oxidizer acid gas dissolving and absorbing chamber and an acid water storage cooling chamber (601); if the polluted air is flue gas, the polluted air is high-temperature gas, the temperature of acid water is increased, cooling water is introduced into the polluted air through a cooling coil (701) immersed in the acid water in an acid water storage cooling chamber for heat exchange and temperature reduction, and the temperature of the acid water is not higher than 40 ℃; acid water in the acid water storage chamber is discharged under the control of an acid water discharge pipe (702) and an electric control valve (811), when the water level of the acid water reaches a valve-opening electric contact probe (8019), the electric control valve (811) is opened, the acid water is discharged until the water level of the acid water is below the position of the acid water discharge pipe (702), the acid water stops being discharged, and when no acid water is discharged, the electric control valve (811) is automatically closed; neutralizing the discharged acid water with calcium oxide to generate calcium fluid and organic acid calcium precipitate, and dissolving the calcium nitrate generated by nitric acid in water to prepare a chemical product; defining the process flow and operation of the system as the process flow and operation of the oxidizer;

the carbon-containing air led out by the carbon-containing air enters the carbon-containing air (10001) through a carbon-containing air conveying pipe (1105) and enters a carbon-containing air inlet pipe (2), ozone is mixed with the carbon-containing air and enters a carbon-containing air and ozone mixed gas inlet pipe (3) and is guided into a carbon removal reaction chamber (4), the chamber is provided with a cover cap and a cover plate (5) to separate the carbon removal reaction chamber into an oxidation and carbon removal chamber, the ozone further carries out the oxidation reaction in the oxidizer to remove harmful impurities and remove carbon, supersaturated calcium hydroxide emulsion in the chamber absorbs the carbon dioxide to generate calcium carbonate, the calcium carbonate further absorbs the carbon dioxide to generate calcium bicarbonate, 70 to 90 percent of the carbon dioxide can be removed, the calcium hydroxide can further corrode and dissolve pathogenic microorganisms and remove peculiar smell, and Ca in the reaction liquid²⁺Calcium oxide in emulsified state in water is continuously dissolved in water for supplement; the oxygen-enriched air from which carbon dioxide is removed is changed into carbon-removing oxygen-enriched clean air, the carbon-removing oxygen-enriched clean air enters the sterile oxygen-enriched clean air water removing chamber (6) from the tangential direction, water drips into a liquid discharge pipe at the lower part of the cyclone separator and flows into alkali liquor due to the collision with the wall of the gas outlet pipe and the rotating separation effect, the gas enters from the lower port of the gas outlet pipe of the cyclone separator, the gas suddenly expands and absorbs heat and condenses from the upper port of the gas outlet pipe, further water is removed and is discharged into the sterile oxygen-enriched clean air gas outlet chamber (7) and is discharged outdoors, the water condensed in the gas outlet chamber flows into the alkali liquor in the mixed gas reaction chamber through a condensed water return pipe (10), after each batch of fermentation is finished, a sealing flange of a discharging port (9) is detached, the alkali liquor and solid particles in the mixed gas reaction chamber can be removed, the liquid and the solid, calcium carbonate is changed into calcium bicarbonate to be dissolved, calcium sulfate is not dissolved, calcium sulfate is obtained by separation, solid calcium bicarbonate is prepared by calcium bicarbonate solution by a conventional method, a feed opening is sealed by a flange, solid calcium oxide is added into water in a decarbonization reaction chamber (4) and an ozonolysis chamber through a solid reactant adding opening (8), tap water is added into the decarbonization reaction chamber (4) and the ozonolysis chamber through a water adding pipe (11), calcium oxide is added while adding water, after the calcium oxide is completely changed into calcium hydroxide, the water is adjusted to be added,adding the water into the effluent of the water overflow pipe (12), stopping adding the water, and then performing the operation; an air outlet pipe of sterile, dust-free, low-carbon dioxide and oxygen-enriched clean air from the sterile oxygen-enriched air outlet chamber (7) is exhausted into the atmosphere by a common exhaust fan and is used for people to breathe the sterile, dust-free, low-carbon dioxide and oxygen-enriched clean air, and the process flow and the operation are defined as a carbon removal process flow and operation;

if the polluted air is flue gas, the polluted air is high-temperature gas, the polluted air is introduced into cooling water from a polluted air inlet cooling water spray pipe (301) for pre-cooling and is subjected to heat exchange cooling with cooling water in a cooling coil pipe (701) to reduce the temperature, and the acid water temperature in an oxidizer acid gas dissolution absorption chamber and an acid water storage cooling chamber (601) is not higher than 40 ℃; the cooling water in the cooling coil (701) is soft water, and enters the boiler to be gasified after the temperature is raised, so that energy is saved; when the acid water level in the acid water storage chamber is above a valve opening electric contact probe (8019), an oxidizer ash discharging hopper spiral propeller motor (803), an oxidizer ash discharging hopper inclined pipe electric control valve A (806) and an oxidizer ash discharging hopper inclined pipe electric control valve B (808) are started, ash is discharged, the acid water level is reduced, when the acid water level is below a valve closing electric contact probe (810), the oxidizer ash discharging hopper spiral propeller motor (803) is firstly stopped, the oxidizer ash discharging hopper inclined pipe electric control valve A (806) is closed, at the moment, an oxidizer ash discharging hopper inclined pipe flushing water pipe (807) is automatically opened for flushing for 2 minutes, an oxidizer ash discharging hopper inclined pipe electric control valve B (808) is closed again, and the valve is closed again after ash is cleaned;

when the position of the ash in a window (80090) of the ash hopper of the polluted air inlet channel in the flue exceeds the glass median of the window, opening an oxidizer inlet channel ash hopper screw propeller motor (8003), an oxidizer inlet channel ash hopper inclined pipe electric control valve A (8006) and an oxidizer inlet channel ash hopper inclined pipe electric control valve B (8008), discharging ash, descending the ash position until the ash hopper window (80090) of the polluted air inlet channel cannot see, an oxidizer inlet channel ash hopper screw propeller motor (8003) stops working, an oxidizer inlet channel ash hopper inclined pipe electric control valve A (8006) is closed, an electric valve on an oxidizer inlet channel ash hopper inclined pipe flushing water pipe (8007) is automatically opened for flushing for 2 minutes, an oxidizer inlet channel ash hopper inclined pipe electric control valve B (8008) is closed again, and the valve is closed again after ash is cleaned to achieve the sealing effect;

the water of the condensation of the sterile, dustless, low carbon dioxide, oxygen-enriched clean air outlet chamber flows into the decarbonization alkali liquor through the condensed water return pipe (10), each batch of reaction is finished, the feed opening sealing flange is disassembled, the decarbonization reaction chamber alkali liquor and solid particles can be quickly removed, the removed liquid is used for recovering and refining to obtain high-purity calcium bicarbonate, the feed opening flange is sealed, solid calcium oxide is added into the decarbonization reaction chamber through the solid reactant adding opening (8), water is just flowed out of the water overflow pipe (12) from the water adding pipe (11) to stop adding water, the feed opening is sealed, and air purification can be continuously carried out.

5. The oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide according to claim 1, which is characterized by expanding the basic process flow and operation, and is used for expanding the process flow and operation of dust removal, nitrogen removal, sulfur removal, harmful smoke removal and carbon removal of coal-fired power plants or garbage combustion power generation: the flue gas discharged from boiler is used as polluted air, and is operated according to the above-mentioned basic technological process and operation, and the flue gas treated by oxidation device is fed into carbon-removing device, and the flue gas after carbon-removing is changed into sterile dust-free low-carbon dioxide, oxygen-rich and clean air, and discharged into atmosphere by means of general-purpose exhaust fan, and said expanded technological process oxidation device and carbon-removing device must be combined for use.

6. The oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide as claimed in claim 1, wherein the device, the basic process flow and the operation are expanded, and the oxygen-enriched air purifier is used for expanding a central air conditioner in a large place for people to move, work and live:

the mixed gas of return air and fresh air sucked from large places of people's activities, works and lives is used as polluted air, a mixing pipe and an air inlet pipe are added according to the conventional method, the operation is carried out according to the basic process flow and the operation, the air treated by an oxidizer enters a carbon remover, the air after carbon removal is changed into sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air, the sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air is discharged into the large places of people's activities, works and lives by a common exhaust fan for people to breathe, the sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air can be connected to an air inlet of a common central air conditioning unit in winter and summer, the air conditioning unit is used for temperature adjustment and humidity adjustment and then is discharged into the large places of people's activities, works and lives for people to breathe, particularly, the haze removal, nitrogen removal, sulfur removal, infection germ removal, oxygen-enriched, can meet or exceed the requirements of GMP certification of America and European Union on air purification.

7. The oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide as claimed in claim 1, wherein the device, the basic process flow and the operation are expanded, and the oxygen-enriched air purifier is used for expanding air conditioners in activities, work and life families of people: the air conditioner is combined with a household air conditioning unit according to a normal method, and sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air can be obtained and used for breathing of household people; expanding the equipment and the basic process flow and operation, reducing the sizes of the oxidizer and the decarbonizer according to a conventional method, connecting the gas discharged from an exhaust pipe of a gas vehicle into the oxidizer, then into the decarbonizer, then into an exhaust fan, and discharging sterile, dustless, low-carbon dioxide, oxygen-enriched and clean air into the atmosphere by the exhaust fan; the equipment, the basic process flow and the operation are expanded to the places of cattle raising, horse raising, sheep raising, deer raising and other livestock raising, and sterile, dust-free, low-carbon dioxide, oxygen-enriched and clean air for livestock to breathe can be obtained.

8. The oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide as claimed in claim 1, wherein the reaction principle, the calculation formula, the equipment manufacturing and the installation size of the air purification are as follows:

firstly, a reaction principle;

air reacts under an electric spark:

oxygen in the air becomes ozone: 3O₂→2O₃，O₃→O₂+[O]

Nitrogen in air becomes dinitrogen pentoxide: 2N₂+5[O]→2N₂O₅

Ozone peculiar smell removing reaction:

O₃→O₂+[O]

[ O ] is a strong oxidant;

[O]+ amine Compound → N₂+NO₂

[O]+H₂S→SO₃+H₂O

[O]+[NH₄]₂S→SO₃+NO₂+H₂O

[O]+2NO₂→N₂O₅

Reaction in alkaline solution:

O₃+H₂O→H₂O₂+O₂→H₂O+O₂+[O]

CaO+H₂O→Ca(OH)₂→Ca²⁺+2OH^-

SO₃+H₂O→H₂SO₄

H₂SO₄+Ca²⁺+2OH^-→CaSO₄↓+2H₂O

N₂O₅+H₂O→2HNO₃

HNO₃+OH^-→NO₃ ^-+H₂O

CO₂+2OH^-→CO² ₃ ^-+H₂O

Ca²⁺+CO₃ ^2-→CaCO₃↓

CaCO₃+CO₂+H₂O→2Ca(HCO₃)₂

the decomposition of the excess ozone releases an oxygen reaction:

O₃→O₂+[O]

2[O]→O₂

secondly, quantitatively calculating the required ozone amount:

Q＝C×V×60/37.75％

q: the required ozone amount per hour, g/h;

V: output of fermentation tail gas m per minute³/min；

and (3) calculating the carbon dioxide removal amount:

fermenting with antibiotics to produce carbon dioxide with amount of 0.03% of carbon dioxide in air being less than 2% of oxygen in air entering into the fermentation tank; at normal temperature, oxygen is air20.93% of the components, and the density of fermentation tail gas is 1.3kg/m after the fermentation in a fermentation tank³Then, the empirical formula for removing the carbon dioxide amount in the fermentation tail gas in the whole fermentation period is as follows:

W＝V×1.3×20.9％×2％×η×60×h

w: the amount of carbon dioxide removed in the whole fermentation period is kg;

v: amount of exhaust gas discharged from fermentation, m³/min；

Eta: the efficiency of carbon dioxide removal; 70% -99.9%;

h: the whole fermentation cycle time;

5.3.2 calculation of the amount of calcium oxide required:

the reaction formula is as follows: CaO + H₂O→Ca^2*+2OH^-

CO₂+2OH^-+Ca²⁺→CaCO₃↓+H₂O

Namely: CaO + CO₂→CaCO₃↓

56 44

G W

44/56＝W/G

G＝W×56/44

G: amount of calcium oxide required

W: the amount of carbon dioxide to be removed

Fourthly, the model of the air purifier for treating the air haze peculiar smell and removing carbon dioxide and infectious disease epidemic particles and more oxygen-enriched air, the model of the oxidizer and the model defined by the carbon remover model are as follows: air purifier model definition: KQJ-YH-CT-X, wherein KQJ is the Chinese phonetic alphabet consonant of the air purifier, YH is the oxidized Chinese phonetic alphabet consonant, CT is the carbon-removed Chinese phonetic alphabet consonant, and X is the polluted air which needs to be purified when the person is transported per minute; taking a middle value of the flow range; definition of the oxidizer type: YHQ-X, HYQ is the Chinese phonetic alphabet of the oxidizer, and X is the polluted air which needs to be purified by inputting people every minute; taking a middle value of the flow range; carbon remover type number definition: WQJ-X is tail gas purification Chinese phonetic alphabet initial consonant, and X is the air pollution purification requirement for people to be transported per minute; taking a middle value of the flow range;

fifthly, the specifications of the matched air purifier, oxidizer and carbon remover are as follows:

KQJ-YH-CY-20 of an air purifier, YHQ-20 of an oxidizer and BQJ-B20 of a carbon remover, the design working pressure is +/-0.09 MPa, and the flow of input polluted air is 1-25m³Min, wherein the inner diameters of a BQJ-B-X air inlet flange and a pipe are DN200 mm;

KQJ-YH-CY-30 of the air purifier, YHQ-30 of the oxidizer and BQJ-B30 of the carbon remover, the design working pressure is +/-0.09 MPa, and the flow of the input polluted air is 30 +/-5 m³Min, wherein the inner diameters of a BQJ-B-X air inlet flange and a pipe are DN200 mm;

KQJ-YH-CY-40 of an air purifier, YHQ-40 of an oxidizer and BQJ-40 of a carbon remover, the design working pressure is +/-0.09 MPa, and the flow of input polluted air is 40 +/-5 m³Min, wherein the inner diameter of a BQJ-B-X air inlet flange and a pipe is DN300 mm;

KQJ-YH-CY-50 of an air purifier, YHQ-50 of an oxidizer and BQJ-50 of a carbon remover, the design working pressure is +/-0.09 MPa, and the flow of input polluted air is 50 +/-5 m³Min, wherein the inner diameter of a BQJ-B-X air inlet flange and a pipe is DN300 mm;

KQJ-YH-CY-60 of an air purifier, YHQ-60 of an oxidizer and BQJ-60 of a carbon remover, the design working pressure is +/-0.09 MPa, and the flow of input polluted air is 60 +/-m³Min, wherein the inner diameter of a BQJ-B-X air inlet flange and a pipe is DN300 mm;

KQJ-YH-CY-70 air purifier, YHQ-70 oxidizer and BQJ-70 carbon remover, the design working pressure is +/-0.09 MPa, and the flow of the input polluted air is 70 +/-5 m³Min, wherein the inner diameters of a BQJ-B-X air inlet flange and a pipe are DN400 mm;

KQJ-YH-CY-80 of an air purifier, YHQ-80 of an oxidizer and BQJ-80 of a carbon remover, the design working pressure is +/-0.09 MPa, and the flow of input polluted air is 80 +/-5 m³Min, wherein the inner diameters of a BQJ-B-X air inlet flange and a pipe are DN400 mm;

KQJ-YH-CY-90 of an air purifier, YHQ-90 of an oxidizer and BQJ-90 of a carbon remover, the design working pressure is +/-0.09 MPa, and the flow of input polluted air is 90 +/-5 m³Min, wherein the inner diameters of a BQJ-B-X air inlet flange and a pipe are DN400 mm;

KQJ-YH-CY-100 of an air purifier, YHQ-100 of an oxidizer and BQJ-100 of a carbon remover, the designed working pressure is +/-0.09 MPa, and the flow of input polluted air is 95-140m³/min，The inner diameters of the BQJ-B-X air inlet flange and the pipe are DN500 mm;

KQJ-YH-CY-150 of the air purifier, YHQ-150 of the oxidizer and BQJ-150 of the carbon remover, the design working pressure is +/-0.09 MPa, and the flow of the input polluted air is 140-200m³Min, wherein the inner diameters of a BQJ-B-X air inlet flange and a pipe are DN500 mm;

sixthly, manufacturing and installing dimensions of the oxidizer equipment are as follows:

the air purifier KQJ-YH-CY-20 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths and the widths of pipe openings of the polluted air inlet straight pipeline and the polluted air inlet oxidizer pipeline are 2000mm and 1200mm respectively; the diameter of the inside of a cylindrical barrel of an oxidizer (10000) is 2800 mm; the height of a cylindrical barrel of the oxidizer (10000) is 12000 mm; the height of an upper conical end socket of an oxidizer gas outlet chamber (1100) and the height of a lower conical end socket of an oxidizer ash discharge hopper (800) are 1200 mm; the distance between the horizontal central axis of the pipeline (500) of the polluted air entering the oxidizer and the horizontal line of the air outlet of the pipe is 3600 mm; the length of the bevel edge of the upper conical end socket of the oxidizer gas outlet chamber (1100) and the length of the bevel edge of the lower conical end socket of the oxidizer ash discharge hopper (800) are 1700 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN200 mm;

the air purifier KQJ-YH-CY-30 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths and the widths of pipe openings of the polluted air inlet straight pipeline and the polluted air inlet oxidizer pipeline are 2000mm and 1200mm respectively; the diameter of the inside of a cylindrical barrel of the oxidizer (10000) is 3200 mm; the height of the cylindrical barrel of the oxidizer (10000) is 14000 mm; the height of an upper conical end socket of an oxidizer gas outlet chamber (1100) and the height of a lower conical end socket of an oxidizer ash discharge hopper (800) are both 1400 mm; the distance between the horizontal central axis of the pipeline (500) of the polluted air entering the oxidizer and the horizontal line of the air outlet of the pipe is 3600 mm; the length of the bevel edge of the upper conical end socket of the gas outlet chamber (1100) of the oxidizer and the length of the bevel edge of the lower conical end socket of the ash hopper (800) of the oxidizer are both 1980 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN200 mm;

the air purifier KQJ-YH-CY-40 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths and the widths of pipe openings of the polluted air inlet straight pipeline and the polluted air inlet oxidizer pipeline are 2000mm and 1200mm respectively; the diameter of the inside of a cylindrical barrel of an oxidizer (10000) is 3600 mm; the height of the cylindrical barrel of the oxidizer (10000) is 16000 mm; the height of an upper conical end socket of an oxidizer gas outlet chamber (1100) and the height of a lower conical end socket of an oxidizer ash slag discharging hopper (800) are both 1600 mm; the distance between the horizontal central axis of the pipeline (500) of the polluted air entering the oxidizer and the horizontal line of the air outlet of the pipeline is 4800 mm; the length of the bevel edge of the upper conical end socket of the oxidizer gas outlet chamber (1100) and the length of the bevel edge of the lower conical end socket of the oxidizer ash discharge hopper (800) are both 2270 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN300 mm;

the air purifier KQJ-YH-CY-50 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths and the widths of pipe openings of the polluted air inlet straight pipeline and the polluted air inlet oxidizer pipeline are 2000mm and 1600mm respectively; the inner diameter of a cylindrical barrel of an oxidizer (10000) is 44000 mm; the height of the cylindrical barrel of the oxidizer (10000) is 18000 mm; the height of an upper conical end socket of an oxidizer gas outlet chamber (1100) and the height of a lower conical end socket of an oxidizer ash discharge hopper (800) are both 1800 mm; the distance between the horizontal central axis of the pipeline (500) of the polluted air entering the oxidizer and the horizontal line of the air outlet of the pipeline is 4800 mm; the length of the bevel edge of the upper conical end socket of the gas outlet chamber (1100) of the oxidizer and the length of the bevel edge of the lower conical end socket of the ash discharging hopper (800) of the oxidizer are both 2550 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN300 mm;

the air purifier KQJ-YH-CY-60 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths of pipe openings of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 2000mm, and the widths of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 1400 mm; the inner diameter of a cylindrical barrel of an oxidizer (10000) is 4400 mm; the height of the cylindrical barrel of the oxidizer (10000) is 20000 mm; the height of an upper conical end socket of an oxidizer gas outlet chamber (1100) and the height of a lower conical end socket of an oxidizer ash discharge hopper (800) are both 2000 mm; the distance between the horizontal central axis of the polluted air inlet pipeline (500) and the horizontal line of the air outlet of the pipeline is 6000 mm; the length of the bevel edge of the upper conical end socket of the gas outlet chamber (1100) of the oxidizer and the length of the bevel edge of the lower conical end socket of the ash discharging hopper (800) of the oxidizer are both 2830 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN300 mm;

the air purifier KQJ-YH-CY-70 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths of pipe openings of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 2000mm, and the widths of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 1400 mm; the diameter of the inside of a cylindrical barrel of the oxidizer (10000) is 4800 mm; the height of a cylindrical barrel of the oxidizer (10000) is 22000 mm; the height of an upper conical end socket of an oxidizer gas outlet chamber (1100) and the height of a lower conical end socket of an oxidizer ash discharge hopper (800) are 2200 mm; the distance between the horizontal central axis of the polluted air inlet pipeline (500) and the horizontal line of the air outlet of the pipeline is 6000 mm; the length of the bevel edge of the upper conical end socket of the oxidizer gas outlet chamber (1100) and the length of the bevel edge of the lower conical end socket of the oxidizer ash discharge hopper (800) are 3120 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN400 mm;

the air purifier KQJ-YH-CY-80 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths of pipe openings of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 2000mm, and the widths of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 1600 mm; the inner diameter of a cylindrical barrel of the oxidizer (10000) is 5200 mm; the height of the cylindrical barrel of the oxidizer (10000) is 24000 mm; the height of an upper conical end socket of an oxidizer gas outlet chamber (1100) and the height of a lower circular cone end socket of an oxidizer ash discharge hopper (800) are 2400 mm; the distance between the horizontal central axis of the polluted air inlet pipeline (500) and the horizontal line of the air outlet of the pipeline is 6500 mm; the length of the bevel edge of the upper conical end socket of the oxidizer gas outlet chamber (1100) and the length of the bevel edge of the lower conical end socket of the oxidizer ash discharge hopper (800) are 3400 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN400 mm;

the air purifier KQJ-YH-CY-90 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths of pipe openings of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 2000mm, and the widths of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 1600 mm; the diameter of the inside of a cylindrical barrel of the oxidizer (10000) is 5600 mm; the height of a cylindrical barrel of the oxidizer (10000) is 26000 mm; the heights of an upper conical end socket of an oxidizer gas outlet chamber (1100) and a lower conical end socket of an oxidizer ash discharge hopper (800) are 2600 mm; the distance between the horizontal central axis of the polluted air inlet pipeline (500) and the horizontal line of the air outlet of the pipeline is 6500 mm; the length of the bevel edge of the upper conical end socket of the gas outlet chamber (1100) of the oxidizer and the length of the bevel edge of the lower conical end socket of the ash discharging hopper (800) of the oxidizer are both 3680 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN400 mm;

the air purifier KQJ-YH-CY-100 is characterized in that the lengths of pipe openings of a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline are 2000mm, and the widths of the pipe openings are 1800 mm; the diameter of the inside of a cylindrical barrel of the oxidizer (10000) is 6000 mm; the height of the cylindrical barrel of the oxidizer (10000) is 28000 mm; the height of an upper conical end socket of an oxidizer gas outlet chamber (1100) and the height of a lower conical end socket of an oxidizer ash discharge hopper (800) are 2800 mm; the distance between the horizontal central axis of the polluted air inlet pipeline (500) and the horizontal line of the air outlet of the pipeline is 7000 mm; the length of the bevel edge of the upper conical end socket of the oxidizer gas outlet chamber (1100) and the length of the bevel edge of the lower conical end socket of the oxidizer ash hopper (800) are both 3970 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN500 mm;

the air purifier KQJ-YH-CY-150 comprises a polluted air inlet inclined pipeline (400), a polluted air inlet straight pipeline (300) and a polluted air inlet oxidizer pipeline, wherein the lengths of pipe openings of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 2000mm, and the widths of the polluted air inlet inclined pipeline and the polluted air inlet oxidizer pipeline are 1800 mm; the diameter of the inside of a cylindrical barrel of the oxidizer (10000) is 8000 mm; the height of the cylindrical barrel of the oxidizer (10000) is 38000 mm; the heights of an upper conical end socket of the oxidizer gas outlet chamber (1100) and a lower conical end socket of the oxidizer ash discharge hopper (800) are 3800 mm; the distance between the horizontal central axis of the polluted air inlet pipeline (500) and the horizontal line of the air outlet of the pipeline is 7000 mm; the length of the bevel edge of the upper conical end socket of the oxidizer gas outlet chamber (1100) and the length of the bevel edge of the lower conical end socket of the oxidizer ash hopper (800) are both 5380 mm; an oxidizer gas outlet pipe (1102), an oxidizer ash discharging hopper (800) and an ash discharging inclined pipe on an ash discharging hopper (8000) of a polluted air inlet channel, an electric valve, a flange and the inner diameter of the pipe are DN500 mm;

seventhly, the sizes of the polluted air inlet pipeline, the cooling system and the ash removal system are as follows: unit mm, working pressure ± 0.09 MPa:

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-20 is 5000mm, and the spraying amount of a polluted air inlet cooling water spraying pipe (301) is 0.20-0.35m³The length of the long side of an oxidizer ash hopper straight pipe (809) or an oxidizer air inlet channel ash hopper straight pipe (8009) and the length of the short side of an oxidizer ash hopper inclined pipe (805) or an oxidizer air inlet channel ash hopper inclined pipe (8005) are 500mm or 900mm, the axial length and the axial outer diameter of an oxidizer ash hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash hopper spiral propeller shaft and blades (8001) are 800mm and 80mm respectively, the rotating speed of an oxidizer ash hopper spiral propeller reduction box (802) and an oxidizer ash hopper spiral propeller motor (803) is reduced to 30-60 revolutions per minute, the length of an oxidizer ash hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash hopper inclined pipe flushing water pipe (8007) inserted into the inclined pipe is 200mm, the outer diameter of the ash pipe is 38mm, and the oxidizer ash hopper spiral propeller shaft and blades (801) or the oxidizer hopper spiral propeller shaft and blades (8005) and the oxidizer air inlet channel ash hopper inclined pipe outer diameter are 38mm (8001) The outer diameter of the impeller is 140 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-30 is 5000mm, and the spraying amount of a cooling water spraying pipe (301) of a polluted air inlet channel is 0.30-0.45m³The length of the long side of an oxidizer ash discharging hopper straight pipe (809) or an oxidizer air inlet channel ash discharging hopper straight pipe (8009) and the length of the short side of an oxidizer ash discharging hopper inclined pipe (805) or an oxidizer air inlet channel ash discharging hopper inclined pipe (8005) are 500mm or 900mm, the axial length and the axial outer diameter of an oxidizer ash discharging hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash discharging hopper spiral propeller shaft and blades (8001) are 800mm and 80mm respectively, the rotating speed of an oxidizer ash discharging hopper spiral propeller reduction box (802) and an oxidizer ash discharging hopper spiral propeller motor (803) is reduced to 30-60 revolutions per minute, and an oxidizer ash discharging hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash discharging hopper inclined pipe are reduced to 30-60 revolutions per minuteThe length of the flushing water pipe (8007) inserted into the inclined pipe is 200mm, the outer diameter of the pipe is 38mm, and the outer diameter of an impeller of an oxidizer ash discharging hopper screw propeller shaft and blades (801) or an oxidizer air inlet ash discharging hopper screw propeller shaft and blades (8001) is 140 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-40 is 5000mm, and the spraying amount of a cooling water spraying pipe (301) of a polluted air inlet channel is 0.40-0.55m³The length of the long side of an oxidizer ash hopper straight pipe (809) or an oxidizer air inlet channel ash hopper straight pipe (8009) and the length of the short side of an oxidizer ash hopper inclined pipe (805) or an oxidizer air inlet channel ash hopper inclined pipe (8005) are 500mm or 900mm, the axial length and the axial outer diameter of an oxidizer ash hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash hopper spiral propeller shaft and blades (8001) are 800mm and 80mm respectively, the rotating speed of an oxidizer ash hopper spiral propeller reduction box (802) and an oxidizer ash hopper spiral propeller motor (803) is reduced to 30-60 revolutions per minute, the length of an oxidizer ash hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash hopper inclined pipe flushing water pipe (8007) inserted into the inclined pipe is 200mm, the outer diameter of the ash pipe is 38mm, and the oxidizer ash hopper spiral propeller shaft and blades (801) or the oxidizer hopper spiral propeller shaft and blades (8005) and the oxidizer air inlet channel ash hopper inclined pipe outer diameter are 38mm (8001) The outer diameter of the impeller is 140 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-50 is 7000mm, and the spraying amount of a cooling water spraying pipe (301) of a polluted air inlet channel is 0.50-0.65m³Min, the length of the long side of an oxidizer ash hopper straight pipe (809) or an oxidizer air inlet channel ash hopper straight pipe (8009) and the length of the short side of an oxidizer ash hopper inclined pipe (805) or an oxidizer air inlet channel ash hopper inclined pipe (8005) are 600mm or 1100mm, the axial length and the axial outer diameter of an oxidizer ash hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash hopper spiral propeller shaft and blades (8001) are 1000mm and 90mm respectively, the rotating speeds of an oxidizer ash hopper spiral propeller reduction box (802) and an oxidizer ash hopper spiral propeller motor (803) are reduced to 30-60 revolutions per minute, and an oxidizer ash hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash hopper inclined pipe flushing water pipe (8007) are inserted into inclined pipesThe length is 200mm, the outer diameter of the pipe is 38mm, and the outer diameter of an impeller of an oxidizer ash discharging hopper screw propeller shaft and blades (801) or an oxidizer air inlet ash discharging hopper screw propeller shaft and blades (8001) is 140 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-60 is 7000mm, and the spraying amount of a cooling water spraying pipe (301) of a polluted air inlet channel is 0.60-0.75m³The length of the long side of an oxidizer ash hopper straight pipe (809) or an oxidizer air inlet channel ash hopper straight pipe (8009) and the length of the short side of an oxidizer ash hopper inclined pipe (805) or an oxidizer air inlet channel ash hopper inclined pipe (8005) are 600mm or 1100mm, the axial length and the axial outer diameter of an oxidizer ash hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash hopper spiral propeller shaft and blades (8001) are 1000mm and 90mm respectively, the rotating speed of an oxidizer ash hopper spiral propeller reduction box (802) and an oxidizer ash hopper spiral propeller motor (803) is reduced to 30-60 revolutions per minute, the length of an oxidizer ash hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash hopper inclined pipe flushing water pipe (8007) inserted into the inclined pipe is 200mm, the outer diameter of the ash pipe is 38mm, and the oxidizer ash hopper spiral propeller shaft and blades (801) or the oxidizer hopper spiral propeller shaft and blades (8005) and the oxidizer air inlet channel ash hopper inclined pipe outer diameter are 38mm (8001) The outer diameter of the impeller is 140 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-70 is 7000mm, and the spraying amount of a cooling water spraying pipe (301) of a polluted air inlet channel is 0.70-0.85m³Min, the length of the long side of an oxidizer ash hopper straight pipe (809) or an oxidizer air inlet channel ash hopper straight pipe (8009) and the length of the short side of an oxidizer ash hopper inclined pipe (805) or an oxidizer air inlet channel ash hopper inclined pipe (8005) are 600mm or 1100mm, the axial length and the axial outer diameter of an oxidizer ash hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash hopper spiral propeller shaft and blades (8001) are respectively 1000mm and 90mm, the rotating speeds of an oxidizer ash hopper spiral propeller reduction box (802) and an oxidizer ash hopper spiral propeller motor (803) are reduced to 30-60 r/m, the length of an oxidizer ash hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash hopper inclined pipe flushing water pipe (8007) inserted into the inclined pipes is 200mm, and the outer diameter of the pipes is 38mm,the outer diameter of an impeller of an oxidizer ash discharging hopper screw propeller shaft and blades (801) or an oxidizer air inlet ash discharging hopper screw propeller shaft and blades (8001) is 140 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-80 is 7000mm, and the spraying amount of a cooling water spraying pipe (301) of a polluted air inlet channel is 0.80-0.95m³The length of the long side of an oxidizer ash hopper straight pipe (809) or an oxidizer air inlet channel ash hopper straight pipe (8009) and the length of the short side of an oxidizer ash hopper inclined pipe (805) or an oxidizer air inlet channel ash hopper inclined pipe (8005) are 600mm or 1100mm, the axial length and the axial outer diameter of an oxidizer ash hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash hopper spiral propeller shaft and blades (8001) are 1000mm and 90mm respectively, the rotating speed of an oxidizer ash hopper spiral propeller reduction box (802) and an oxidizer ash hopper spiral propeller motor (803) is reduced to 30-60 revolutions per minute, the length of an oxidizer ash hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash hopper inclined pipe flushing water pipe (8007) inserted into the inclined pipe is 200mm, the outer diameter of the ash pipe is 38mm, and the oxidizer ash hopper spiral propeller shaft and blades (801) or the oxidizer hopper spiral propeller shaft and blades (8005) and the oxidizer air inlet channel ash hopper inclined pipe outer diameter are 38mm (8001) The outer diameter of the impeller is 140 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-90 is 9000mm, and the spraying amount of a polluted air inlet cooling water spraying pipe (301) is 0.90-1.15m³And min, the length of the long side of an oxidizer ash discharging hopper straight pipe (809) or an oxidizer air inlet channel ash discharging hopper straight pipe (8009) and the length of the short side of an oxidizer ash discharging hopper inclined pipe (805) or an oxidizer air inlet channel ash discharging hopper inclined pipe (8005) are 700mm or 1500mm, the axial length and the axial outer diameter of an oxidizer ash discharging hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash discharging hopper spiral propeller shaft and blades (8001) are 1200mm and 100mm respectively, the rotating speed of an oxidizer ash discharging hopper spiral propeller reduction box (802) and an oxidizer ash discharging hopper spiral propeller motor (803) is reduced to 30-60 r/min, the length of an oxidizer ash discharging hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash discharging inclined pipe flushing water pipe (8007) inserted into the ash inclined pipe is 200mm, the pipe outer diameter is 38mm, and the oxidizer ash discharging hopper spiral is pushed.The outer diameter of an impeller shaft and blades (801) or an impeller of an ash hopper screw propeller shaft and blades (8001) of an air inlet passage of the oxidizer is 150 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-100 is 9000mm, and the spraying amount of a polluted air inlet cooling water spraying pipe (301) is 1.0-1.25m³The length of the long side of an oxidizer ash hopper straight pipe (809) or an oxidizer air inlet channel ash hopper straight pipe (8009) and the length of the short side of an oxidizer ash hopper inclined pipe (805) or an oxidizer air inlet channel ash hopper inclined pipe (8005) are 700mm or 1500mm, the axial length and the axial outer diameter of an oxidizer ash hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash hopper spiral propeller shaft and blades (8001) are 1200mm and 100mm respectively, the rotating speed of an oxidizer ash hopper spiral propeller reduction box (802) and an oxidizer ash hopper spiral propeller motor (803) is reduced to 30-60 revolutions per minute, the length of an oxidizer ash hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel ash hopper inclined pipe flushing water pipe (8007) inserted into the inclined pipe is 200mm, the outer diameter of the ash pipe is 38mm, and the oxidizer ash hopper spiral propeller shaft and blades (801) or the oxidizer hopper spiral propeller shaft and blades (8005) and the oxidizer air inlet channel ash hopper inclined pipe outer diameter are 38mm (8001) The outer diameter of the impeller is 150 mm;

the length of a polluted air inlet inclined pipeline (400) of the oxidizer YHQ-150 is 9000mm, and the spraying amount of a polluted air inlet cooling water spraying pipe (301) is 1.50-1.75m³And min, the length of the long side of an oxidizer ash hopper straight pipe (809) or an oxidizer air inlet channel ash hopper straight pipe (8009) and the length of the short side of an oxidizer ash hopper inclined pipe (805) or an oxidizer air inlet channel ash hopper inclined pipe (8005) are 700mm or 1500mm, the axial length and the axial outer diameter of an oxidizer ash hopper spiral propeller shaft and blades (801) or an oxidizer air inlet channel ash hopper spiral propeller shaft and blades (8001) are 1200mm and 100mm respectively, the rotating speed of an oxidizer ash hopper spiral propeller reduction box (802) and an oxidizer ash hopper spiral propeller motor (803) is reduced to 30-60 rpm, the length of an oxidizer ash hopper inclined pipe flushing water pipe (807) and an oxidizer air inlet channel inclined pipe flushing water pipe (8007) inserted into the ash inclined pipe is 200mm, the pipe outer diameter is 38mm, and the oxidizer ash hopper spiral propeller shaft and blades (801) or oxidation.The outer diameters of the impeller shaft and the impeller (8001) of the ash discharging hopper screw propeller of the inlet channel are 150 mm;

eighthly, the sizes of the acid gas dissolving and absorbing chamber of the oxidizer, the acid water storage and cooling chamber and the air outlet cyclone separator system of the oxidation chamber are as follows: unit mm, working pressure ± 0.09 MPa:

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-20 was 4.0m³The distance between the horizontal central axis of the cooling coil (701) and the lower edge of the oxidizer cylinder barrel (600) is 200mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal axis of a spiral propeller motor or an electric control valve shutdown or valve closing electric contact probe (810) is 500mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an oxidizer ash slag discharging hopper spiral propeller motor (8019) is 1400mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an acid water discharging pipe (702) is 1200mm, and the distance between the horizontal central axis of an ozone decomposition chamber isolation plate (901) and the lower edge of the horizontal axis of the spiral propeller motor or the electric control valve shutdown or valve closing electric contact probe (810) is 3600;

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-30 is 4.0m³The distance between the horizontal central axis of the cooling coil (701) and the lower edge of the oxidizer cylinder barrel (600) is 200mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal axis of a spiral propeller motor or an electric control valve shutdown or valve closing electric contact probe (810) is 500mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an oxidizer ash slag discharging hopper spiral propeller motor (8019) is 1400mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an acid water discharging pipe (702) is 1200mm, and the distance between the horizontal central axis of an ozone decomposition chamber isolation plate (901) and the lower edge of the horizontal axis of the spiral propeller motor or the electric control valve shutdown or valve closing electric contact probe (810) is 3600;

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-40 was 7.0m³Min, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the cylindrical barrel (600) of the oxidizer is 200mm, and the horizontal central axis of the cooling coil (701) and a motor of a propeller or an electric control valveThe lower distance of the horizontal axis of a shutdown or valve closing electric contact probe (810) is 700mm, the lower distance of the horizontal central axis of a cooling coil (701) and the horizontal central axis of an oxidizer ash slag discharging hopper screw propeller motor (8019) is 1600mm, the lower distance of the horizontal central axis of the cooling coil (701) and the horizontal central axis of an acid water discharging pipe (702) is 1400mm, and the lower distance of the horizontal central axis of an ozone decomposition chamber isolation plate (901) and the lower distance of the horizontal axis of the screw propeller motor or an electric control valve shutdown or valve closing electric contact probe (810) is 4000 mm;

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-50 is 7.0m³The distance between the horizontal central axis of the cooling coil (701) and the lower edge of the oxidizer cylinder barrel (600) is 200mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal axis of a spiral propeller motor or an electric control valve shutdown or valve closing electric contact probe (810) is 700mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an oxidizer ash slag discharging hopper spiral propeller motor (8019) is 1600mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an acid water discharging pipe (702) is 1400mm, and the distance between the horizontal central axis of an ozone decomposition chamber isolation plate (901) and the lower edge of the horizontal axis of the spiral propeller motor or the electric control valve shutdown or valve closing electric contact probe (810) is 4000;

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-60 is 7.0m³The distance between the horizontal central axis of the cooling coil (701) and the lower edge of the oxidizer cylinder barrel (600) is 200mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal axis of a spiral propeller motor or an electric control valve shutdown or valve closing electric contact probe (810) is 700mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an oxidizer ash slag discharging hopper spiral propeller motor (8019) is 1600mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an acid water discharging pipe (702) is 1400mm, and the distance between the horizontal central axis of an ozone decomposition chamber isolation plate (901) and the lower edge of the horizontal axis of the spiral propeller motor or the electric control valve shutdown or valve closing electric contact probe (810) is 4000;

oxidizer YHQ-70, cooling coil (701)Cooling water amount of 9.0m³The horizontal central axis of the cooling coil (701) is 200mm away from the lower side of the oxidizer cylinder barrel (600), the horizontal central axis of the cooling coil (701) is 900mm away from the lower side of the horizontal axis of the electric contact probe (810) for stopping or closing the electric control valve or the spiral propeller motor, the horizontal central axis of the cooling coil (701) is 1800mm away from the lower side of the horizontal central axis of the spiral propeller motor (8019) of the ash residue discharging hopper of the oxidizer, the horizontal central axis of the cooling coil (701) is 1600mm away from the lower side of the horizontal central axis of the acid water discharging pipe (702), and the horizontal central axis of the partition plate (901) of the ozone decomposition chamber is 4200mm away from the lower side of the horizontal axis of the electric contact probe (810) for stopping or closing the electric control valve or the electric control valve;

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-80 was 9.0m³The horizontal central axis of the cooling coil (701) is 200mm away from the lower side of the oxidizer cylinder barrel (600), the horizontal central axis of the cooling coil (701) is 900mm away from the lower side of the horizontal axis of the electric contact probe (810) for stopping or closing the electric control valve or the spiral propeller motor, the horizontal central axis of the cooling coil (701) is 1800mm away from the lower side of the horizontal central axis of the spiral propeller motor (8019) of the ash residue discharging hopper of the oxidizer, the horizontal central axis of the cooling coil (701) is 1600mm away from the lower side of the horizontal central axis of the acid water discharging pipe (702), and the horizontal central axis of the partition plate (901) of the ozone decomposition chamber is 4200mm away from the lower side of the horizontal axis of the electric contact probe (810) for stopping or closing the electric control valve or the electric control valve;

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-90 is 12.0m³The distance between the horizontal central axis of the cooling coil (701) and the lower edge of the cylinder body (600) of the oxidizer cylinder is 200mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal axis of the electric contact probe (810) for stopping or closing the electric control valve or the spiral propeller motor, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of the spiral propeller motor (8019) of the ash residue discharging hopper of the oxidizer cylinder is 2000mm, the distance between the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of the acid water discharging pipe (702) is 1800mm, and the ozone decomposition chamber is isolatedThe distance between the horizontal central axis of the plate (901) and the lower edge of the horizontal axis of the screw propeller motor or the electric control valve shutdown or valve closing electric contact probe (810) is 4800 mm;

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-100 is 12.0m³The horizontal central axis of the cooling coil (701) and the lower edge of the oxidizer cylinder barrel (600) are 200mm, the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal axis of a spiral propeller motor or an electric control valve shutdown or valve closing electric contact probe (810) are 1000mm, the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an oxidizer ash slag discharging hopper spiral propeller motor (8019) are 2000mm, the horizontal central axis of the cooling coil (701) and the lower edge of the horizontal central axis of an acid water discharging pipe (702) are 1800mm, and the horizontal central axis of an ozone decomposition chamber isolation plate (901) and the lower edge of the horizontal axis of the spiral propeller motor or the electric control valve shutdown or valve closing electric contact probe (810) are 4800 mm;

the cooling water quantity of the cooling coil (701) of the oxidizer YHQ-150 is 16.0m³The horizontal central axis of the cooling coil (701) is 200mm away from the lower side of the cylinder (600) of the oxidizer cylinder, the horizontal central axis of the cooling coil (701) is 1500mm away from the lower side of the horizontal axis of the electric contact probe (810) for stopping or closing the electric control valve or the screw propeller motor, the horizontal central axis of the cooling coil (701) is 2600mm away from the lower side of the horizontal central axis of the screw propeller motor (8019) of the ash residue discharging hopper of the oxidizer, the horizontal central axis of the cooling coil (701) is 2400mm away from the lower side of the horizontal central axis of the acid water discharging pipe (702), and the horizontal central axis of the partition plate (901) of the ozone decomposition chamber is 6000mm away from the lower side of the horizontal axis of the electric contact probe (810) for stopping or closing the electric control valve or the electric control valve;

ninth, the manufacturing and installation sizes of the air outlet cyclone separator of the oxidation chamber and the ozonolysis chamber of the oxidizer are as follows: unit mm, working pressure ± 0.09 MPa:

the device comprises an oxidizer YHQ-20, wherein the height of a cone end socket or a cylinder of an oxidation chamber gas outlet cyclone separator (1000) is 720mm, the length of the inclined side of the cone end socket of the oxidation chamber gas outlet cyclone separator (1000) is 1020mm, the outer diameter of the cylinder of the oxidation chamber gas outlet cyclone separator (1000) is 1440mm, the height of an air inlet of an oxidation chamber gas outlet cyclone separator air inlet pipe (1001) is 720mm, the width of the air inlet of the oxidation chamber gas outlet cyclone separator air inlet pipe is 200mm, the length of an oxidation chamber gas outlet cyclone separator air outlet pipe (1002) is 1440mm, the length of the oxidation chamber gas outlet cyclone separator air outlet pipe (1002) in an ozone decomposition chamber (900) is 360mm, the inner diameter of an oxidation chamber gas outlet cyclone separator water outlet pipe (1003) is 50mm, and the length of the oxidation chamber gas outlet cyclone separator water outlet;

the device comprises an oxidizer YHQ-30, wherein the height of a cone end socket or a cylinder of an oxidation chamber gas outlet cyclone separator (1000) is 840mm, the length of the inclined side of the cone end socket of the oxidation chamber gas outlet cyclone separator (1000) is 1190mm, the outer diameter of the cylinder of the oxidation chamber gas outlet cyclone separator (1000) is 1680mm, the height of an air inlet of an oxidation chamber gas outlet cyclone separator air inlet pipe (1001) is 840mm and the width of the air inlet of the oxidation chamber gas outlet cyclone separator air inlet pipe is 200mm, the length of an oxidation chamber gas outlet cyclone separator air outlet pipe (1002) is 1680mm, the length of the oxidation chamber gas outlet cyclone separator air outlet pipe (1002) in an ozone decomposition chamber (900) is 420mm, the inner diameter of the oxidation chamber gas outlet cyclone separator water outlet pipe (1003) is 50mm, and the length of the oxidation chamber gas outlet cyclone separator water outlet;

the device comprises an oxidizer YHQ-40, wherein the height of a cone end socket or a cylinder of an oxidation chamber outlet cyclone separator (1000) is 960mm, the length of a slant edge of the cone end socket of the oxidation chamber outlet cyclone separator (1000) is 1360mm, the outer diameter of the cylinder of the oxidation chamber outlet cyclone separator (1000) is 1920mm, the height of an air inlet of an oxidation chamber outlet cyclone separator air inlet pipe (1001) is 960mm, the width of the air inlet of the oxidation chamber outlet cyclone separator air inlet pipe is 300mm, the length of an oxidation chamber outlet cyclone separator air outlet pipe (1002) is 1920mm, the length of the oxidation chamber outlet cyclone separator air outlet pipe (1002) in an ozone decomposition chamber (900) is 480mm, the inner diameter of an oxidation chamber outlet cyclone separator water outlet pipe (1003) is 50mm, and the length of the oxidation chamber outlet cyclone separator water outlet pipe (1003) is 200 mm;

the device comprises an oxidizer YHQ-50, wherein the height of a cone end socket or a cylinder of an oxidation chamber outlet cyclone separator (1000) is 1080mm, the length of an inclined side of the cone end socket of the oxidation chamber outlet cyclone separator (1000) is 1530mm, the outer diameter of the cylinder of the oxidation chamber outlet cyclone separator (1000) is 2160mm, the height of an air inlet of an oxidation chamber outlet cyclone separator air inlet pipe (1001) is 1080mm, the width of the air inlet of the oxidation chamber outlet cyclone separator air inlet pipe is 300mm, the length of an oxidation chamber outlet cyclone separator air outlet pipe (1002) is 2160mm, the length of the oxidation chamber outlet cyclone separator air outlet pipe (1002) in an ozone decomposition chamber (900) is 540mm, the inner diameter of an oxidation chamber outlet cyclone separator water outlet pipe (1003) is 75mm, and the length of the oxidation chamber outlet cyclone separator water outlet pipe (1003) is 200 mm;

the device comprises an oxidizer YHQ-60, wherein the height of a cone end socket or a cylinder of an oxidation chamber gas outlet cyclone separator (1000) is 1200mm, the length of an inclined side of the cone end socket of the oxidation chamber gas outlet cyclone separator (1000) is 1700mm, the outer diameter of the cylinder of the oxidation chamber gas outlet cyclone separator (1000) is 2400mm, the height of an air inlet of an oxidation chamber gas outlet cyclone separator air inlet pipe (1001) is 1200mm, the width of the air inlet of the oxidation chamber gas outlet cyclone separator air inlet pipe is 400mm, the pipe length of an oxidation chamber gas outlet cyclone separator air outlet pipe (1002) is 2400mm, the pipe length of the oxidation chamber gas outlet cyclone separator air outlet pipe (1002) in an ozone decomposition chamber (900) is 600mm, the inner diameter of an oxidation chamber gas outlet cyclone separator water outlet pipe (1003) is 75mm, and the length of the oxidation chamber gas outlet cyclone separator;

the device comprises an oxidizer YHQ-70, wherein the height of a cone end socket or a cylinder of an oxidation chamber gas outlet cyclone separator (1000) is 1320mm, the length of an inclined side of the cone end socket of the oxidation chamber gas outlet cyclone separator (1000) is 1870mm, the outer diameter of the cylinder of the oxidation chamber gas outlet cyclone separator (1000) is 2640mm, the height of an air inlet of an oxidation chamber gas outlet cyclone separator air inlet pipe (1001) is 1320mm, the width of the air inlet of the oxidation chamber gas outlet cyclone separator air inlet pipe is 400mm, the length of an air outlet pipe (1002) of the oxidation chamber gas outlet cyclone separator is 2640mm, the length of the air outlet pipe (1002) of the oxidation chamber gas outlet cyclone separator in an ozone decomposition chamber (900) is 660mm, the inner diameter of an oxidation chamber gas outlet cyclone separator water outlet pipe (1003) is 75mm, and the length of the oxidation chamber gas outlet;

the device comprises an oxidizer YHQ-80, wherein the height of a cone end socket or a cylinder of an oxidation chamber outlet cyclone separator (1000) is 1440mm, the length of a slant edge of the cone end socket of the oxidation chamber outlet cyclone separator (1000) is 2040mm, the outer diameter of the cylinder of the oxidation chamber outlet cyclone separator (1000) is 2880mm, the height of an air inlet of an oxidation chamber outlet cyclone separator air inlet pipe (1001) is 1440mm, the width of the air inlet of the oxidation chamber outlet cyclone separator air inlet pipe is 600mm, the length of a pipe of an oxidation chamber outlet cyclone separator air outlet pipe (1002) is 2880mm, the length of the pipe of the oxidation chamber outlet cyclone separator air outlet pipe (1002) in an ozone decomposition chamber (900) is 570mm, the inner diameter of the oxidation chamber outlet cyclone separator water outlet pipe (1003) is 100mm, and the length of the oxidation chamber outlet cyclone separator water outlet pipe (1003;

the device comprises an oxidizer YHQ-90, wherein the height of a cone end socket or a cylinder of an oxidation chamber air outlet cyclone separator (1000) is 1560mm, the length of an inclined side of the cone end socket of the oxidation chamber air outlet cyclone separator (1000) is 2210mm, the outer diameter of the cylinder of the oxidation chamber air outlet cyclone separator (1000) is 3120mm, the height of an air inlet of an oxidation chamber air outlet cyclone separator air inlet pipe (1001) is 1560mm and the width of the air inlet of the oxidation chamber air outlet cyclone separator air inlet pipe is 600mm, the pipe length of an oxidation chamber air outlet cyclone separator air outlet pipe (1002) is 3120mm, the pipe length of the oxidation chamber air outlet cyclone separator air outlet pipe (1002) in an ozone decomposition chamber (900) is 780mm, the inner diameter of the oxidation chamber air outlet cyclone separator water outlet pipe (1003) is 100mm, and the length of the oxidation chamber air outlet cyclone separator;

the device comprises an oxidizer YHQ-100, wherein the height of a cone end socket or a cylinder of an oxidation chamber air outlet cyclone separator (1000) is 1680mm, the length of an inclined side of the cone end socket of the oxidation chamber air outlet cyclone separator (1000) is 2380mm, the outer diameter of the cylinder of the oxidation chamber air outlet cyclone separator (1000) is 3360mm, the height of an air inlet of an oxidation chamber air outlet cyclone separator air inlet pipe (1001) is 1680mm and the width of the air inlet of the oxidation chamber air outlet cyclone separator air inlet pipe is 800mm, the pipe length of an oxidation chamber air outlet cyclone separator air outlet pipe (1002) is 3360mm, the pipe length of the oxidation chamber air outlet cyclone separator air outlet pipe (1002) in an ozone decomposition chamber (900) is 840mm, the inner diameter of an oxidation chamber air outlet cyclone separator water outlet pipe (1003) is 100mm, and the length of the oxidation chamber air outlet cyclone separator;

the device comprises an oxidizer YHQ-150, wherein the height of a cone end socket or a cylinder of an oxidation chamber gas outlet cyclone separator (1000) is 2260mm, the length of the inclined side of the cone end socket of the oxidation chamber gas outlet cyclone separator (1000) is 3200mm, the outer diameter of the cylinder of the oxidation chamber gas outlet cyclone separator (1000) is 4520mm, the height of an air inlet of an oxidation chamber gas outlet cyclone separator air inlet pipe (1001) is 2260mm, the width of the air inlet of the oxidation chamber gas outlet cyclone separator air inlet pipe is 800mm, the pipe length of an oxidation chamber gas outlet pipe (1002) is 4520mm, the pipe length of the oxidation chamber gas outlet pipe (1002) in an ozone decomposition chamber (900) is 1130mm, the inner diameter of an oxidation chamber gas outlet cyclone separator water outlet pipe (1003) is 100mm, and the length of the oxidation chamber gas outlet cyclone separator water outlet pipe (1003) is 200;

tenth, ozone decomposition chamber and oxidizer gas outlet chamber manufacturing installation size: unit mm, working pressure ± 0.09 MPa:

the device comprises an oxidizer YHQ-20, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 200mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 720mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber in an ozone decomposition chamber (900) is 300mm, the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 200mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the pipe outer diameter is 55mm, the pipe length of a drain pipe (1103) of the oxidation chamber is 2600mm, the distance between an partition plate (901) of the ozone decomposition chamber and a partition plate (104) of the oxidation chamber is 2400mm, the pipe outer diameter of the drain pipe (1103) of the oxidation chamber is 25mm, and the pipe length of the air outlet pipe;

the device comprises an oxidizer YHQ-30, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 200mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 720mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber is 300mm in an ozone decomposition chamber (900), the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 200mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the pipe outer diameter is 55mm, the pipe length of a drain pipe (1103) of the oxidation chamber is 3000mm, the distance between an ozone decomposition chamber partition plate (901) and a partition plate (104) of the oxidation chamber is 2800mm, the pipe outer diameter of the drain pipe (1103) of the oxidation chamber is 25mm, and the pipe length of the air outlet pipe (1102);

the device comprises an oxidizer YHQ-40, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 300mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 720mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber is 300mm in an ozone decomposition chamber (900), the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 300mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the outer diameter of the pipe is 55mm, the pipe length of a water outlet pipe (1103) of the oxidation chamber is 3400mm, the distance between an ozone decomposition chamber partition plate (901) and a partition plate (104) of the oxidation chamber is 3200mm, the outer diameter of the water outlet pipe (1103) of the oxidation chamber is 25mm, and the pipe length of the air outlet pipe;

the device comprises an oxidizer YHQ-50, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 300mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 800mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber is 300mm in an ozone decomposition chamber (900), the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 300mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the outer diameter of the pipe is 81mm, the pipe length of a water outlet pipe (1103) of the oxidizer air outlet chamber is 3800mm, the distance between an ozone decomposition chamber partition plate (901) and a partition plate (104) of the oxidizer air outlet chamber is 3600mm, the outer diameter of the water outlet pipe (1103) of the oxidizer air outlet chamber is 38mm, and the pipe;

the device comprises an oxidizer YHQ-60, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 300mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 800mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber is 400mm in an ozone decomposition chamber (900), the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 300mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the outer diameter of the pipe is 81mm, the pipe length of a drain pipe (1103) of the oxidation chamber is 4200mm, the distance between an ozone decomposition chamber partition plate (901) and a partition plate (104) of the oxidation chamber is 4000mm, the outer diameter of the drain pipe (1103) of the oxidation chamber is 38mm, and the pipe length of the air outlet pipe (1102;

the device comprises an oxidizer YHQ-70, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 400mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 800mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber is 400mm in an ozone decomposition chamber (900), the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 400mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the outer diameter of the pipe is 81mm, the pipe length of a water outlet pipe (1103) of the oxidizer air outlet chamber is 4600mm, the distance between an ozone decomposition chamber partition plate (901) and an oxidizer air outlet chamber partition plate (104) is 4400mm, the outer diameter of the water outlet pipe (1103) of the oxidizer air outlet chamber is 38mm, and the pipe length of;

the device comprises an oxidizer YHQ-80, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 400mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 800mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber is 400mm in an ozone decomposition chamber (900), the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 400mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the pipe outer diameter is 108mm, the pipe length of a drain pipe (1103) of the oxidation outlet chamber is 5600mm, the distance between a partition plate (901) of the ozone decomposition chamber and a partition plate (104) of the oxidation outlet chamber is 2800mm, the pipe outer diameter of the drain pipe (1103) of the oxidation outlet chamber is 55mm, and the pipe length of the air;

the device comprises an oxidizer YHQ-90, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 400mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 1000mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber is 400mm in an ozone decomposition chamber (900), the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 400mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the pipe outer diameter is 108mm, the pipe length of a water outlet pipe (1103) of the oxidation chamber is 10400mm, the distance between an ozone decomposition chamber partition plate (901) and a partition plate (104) of the oxidation chamber is 5200mm, the pipe outer diameter of the water outlet pipe (1103) of the oxidation chamber is 55mm, and the pipe length of the air outlet pipe (;

the gas outlet pipe (1002) of the oxidation chamber outlet cyclone separator is 500mm in inner diameter, the gas outlet pipe (1101) of the ozone decomposition chamber is 1000mm in length, the gas outlet pipe (1101) of the ozone decomposition chamber is 400mm in length of the ozone decomposition chamber (900), the gas outlet pipe (1101) of the ozone decomposition chamber is 500mm in inner diameter, the gas outlet pipe (1101) of the ozone decomposition chamber is 5200mm in pipe length, the pipe outer diameter is 108mm, the pipe length of the gas outlet pipe (1103) of the oxidation chamber is 11200mm, the distance between the partition plate (901) of the ozone decomposition chamber and the partition plate (104) of the oxidation chamber is 5600mm, the pipe outer diameter of the gas outlet pipe (1103) of the oxidation chamber is 55mm, and the pipe length of the gas outlet pipe (1102) of the oxidation chamber is 300 mm;

the device comprises an oxidizer YHQ-150, wherein the inner diameter of an air outlet pipe (1002) of an air outlet cyclone separator of an oxidation chamber is 500mm, the length of an air outlet pipe (1101) of an ozone decomposition chamber is 1000mm, the length of the air outlet pipe (1101) of the ozone decomposition chamber in an ozone decomposition chamber (900) is 400mm, the inner diameter of the air outlet pipe (1101) of the ozone decomposition chamber is 500mm, the pipe length of the air outlet pipe (1101) of the ozone decomposition chamber is 5200mm, the pipe outer diameter is 108mm, the pipe length of a drain pipe (1103) of the oxidation chamber is 15200mm, the distance between an ozone decomposition chamber partition plate (901) and a partition plate (104) of the oxidation chamber is 7600mm, the pipe outer diameter of the drain pipe (1103) of the oxidation chamber is 55mm, and the pipe length of the air outlet pipe (1102;

eleventh, the equipment materials are as follows:

the device comprises an oxidizer YHQ-20, an oxidizer YHQ-30, an oxidizer YHQ-40, an oxidizer YHQ-50, an oxidizer YHQ-60, an oxidizer YHQ-70, an oxidizer YHQ-80, an oxidizer YHQ-90, an oxidizer YHQ-100 and an oxidizer YHQ-150, wherein a polluted air inlet straight pipeline (300) and a polluted air inlet inclined pipeline (400) are hooked by acid-resistant granite pyroxene powder phenolic resin, an oxidizer cylinder body (600) is hooked by acid-resistant granite pyroxene powder phenolic resin, a polluted air inlet cooling water spray pipe (301), a polluted air inlet oxidizer pipeline (500), a cooling coil pipe (701), an acid water discharge pipe (702), an oxidizer ash discharge hopper (800), an oxidizer ash discharge hopper screw propeller shaft and blades (801), an oxidizer ash discharge hopper inclined pipe (805), an oxidizer ash discharge hopper inclined pipe flushing water pipe (807), The material of the ash hopper inclined tube electric control valve B (808) of the oxidizer inlet channel, the ash hopper spiral propeller shaft and the blades (8001) of the oxidizer inlet channel, the ash hopper inclined tube (8005) of the oxidizer inlet channel, the ash hopper inclined tube flushing water pipe (8007) of the oxidizer inlet channel, the ash hopper inclined tube electric control valve B (8008) of the oxidizer inlet channel, the ash hopper straight tube (8009) of the oxidizer inlet channel, the ash hopper (8000) of the polluted air inlet channel, the ozone decomposition chamber partition board (901), the oxidation chamber air outlet cyclone separator (1000), the oxidation chamber air outlet cyclone separator air outlet pipe (1002), the oxidation chamber air outlet cyclone separator water outlet pipe (1003), the ozone decomposition chamber and oxidation chamber partition board (1104), the ozone decomposition chamber water outlet pipe (1005), the oxidation chamber air outlet chamber (1100), the ozone decomposition chamber air outlet pipe (1101), the oxidation chamber air outlet pipe (1102), the oxidation chamber air outlet pipe (1103) and the oxidation chamber air outlet (1100) adopts polytetrafluoroethylene, polypropylene, PVC or acid-resistant and temperature-resistant plastic plates and pipes with the temperature of more than 60 ℃, wherein the material adopted by the ash discharging hopper window (80090) of the polluted air inlet channel is acid-resistant, pressure-resistant and heat-resistant glass, and the ash discharging hopper window (80090) of the polluted air inlet channel has the length of 600mm, the width of 300mm and the height of 30 mm;

twelfth, the thickness of the relevant cylinder body, the thickness of the conical sealing head, the thickness of the ash discharging hopper and the thickness of the partition plate pipe wall of the equipment are as follows: unit mm:

the device comprises an oxidizer YHQ-20, wherein the thickness of an oxidizer cylinder body (600) is 150mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 20mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 20mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 25mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-30, wherein the thickness of an oxidizer cylinder body (600) is 150mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 20mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 20mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 25mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-40, wherein the thickness of an oxidizer cylinder body (600) is 240mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 25mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 25mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 30mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-50, wherein the thickness of an oxidizer cylinder body (600) is 240mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 25mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 25mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 30mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-60, wherein the thickness of an oxidizer cylinder body (600) is 240mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 25mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 25mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 30mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-70, wherein the thickness of an oxidizer cylinder body (600) is 240mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 30mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 30mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 30mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-80, wherein the thickness of an oxidizer cylinder body (600) is 240mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 30mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 30mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 35mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-90, wherein the thickness of an oxidizer cylinder body (600) is 380mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 35mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 35mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 35mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-100, wherein the thickness of an oxidizer cylinder body (600) is 380mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 35mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 35mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 40mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

the device comprises an oxidizer YHQ-150, wherein the thickness of an oxidizer cylinder body (600) is 380mm, the thickness of upper and lower cone seal heads of the oxidizer cylinder body (600) is 40mm, the thickness of a cone lower slag hopper of a polluted air inlet channel ash and slag lower hopper (8000) is 40mm, the thickness of an ozone decomposition chamber partition plate (901), an ozone decomposition chamber partition plate and an oxidizer air outlet chamber partition plate (1104) is 40mm, the pipe wall thickness of pipelines with inner and outer diameters less than or equal to 50 is 5mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 50 is 8mm, the pipe wall thickness of pipelines with inner and outer diameters greater than or less than 200 is 10mm, and the pipe wall thickness of pipelines with inner and outer diameters greater than 200 is 15 mm;

thirteen, the relevant angles of the equipment are as follows: unit: degree of rotation

The device comprises an oxidizer YHQ-20, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-30, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-40, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-50, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-60, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-70, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-80, a polluted air inlet inclined pipeline (400) and a horizontal ground form an included angle of 30 degrees, a polluted air inlet ash discharging hopper (8000) cone vertex angle is 60 degrees, an oxidizer cylinder body (600) upper cone vertex angle and a polluted air inlet ash discharging hopper lower cone vertex angle are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder body (600) and a horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between the cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-90, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-100, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

the device comprises an oxidizer YHQ-150, wherein an included angle between a polluted air inlet inclined pipeline (400) and the horizontal ground is 30 degrees, a cone vertex angle of a polluted air inlet ash discharging hopper (8000) is 60 degrees, upper and lower cone vertex angles of an oxidizer cylinder (600) are 90 degrees, an included angle between a cone inclined plane in the oxidizer cylinder (600) and the horizontal plane, an inclined angle of an oxidizer ash discharging hopper inclined pipe (805), an inclined angle of an oxidizer inlet ash discharging hopper inclined pipe (8005) and an included angle between a cone inclined plane of an oxidation chamber air outlet cyclone separator (1000) and the horizontal plane are both 45 degrees;

9. The oxygen-enriched air purifier for removing haze, organic nitrogen, sulfur, infectious germs and carbon dioxide according to claim 1, which is characterized in that the basic process flow and operation of the device are expanded to prepare calcium nitrate, calcium sulfate and calcium bicarbonate, the calcium bicarbonate is refined into pharmaceutical auxiliary materials, and ash can be made into cement bricks, decoloration adsorbents, heat insulators and novel plastic material fillers.