Air pollution control and purification treatment device

Abstract

The invention discloses an atmospheric pollution control and purification treatment device, and particularly relates to the technical field of atmospheric treatment.The atmospheric pollution control and purification treatment device comprises a first treatment barrel and a second treatment barrel, a pickling assembly is arranged on the upper portion of the inner surface of the first treatment barrel, a first collecting assembly is arranged in the middle of the inner surface of the first treatment barrel, and an adsorption assembly is arranged in the middle of the inner surface of the second treatment barrel; a second collecting assembly is arranged on the lower middle portion of the inner surface of the second treatment barrel, and a water cooling assembly is arranged on the upper middle portion of the inner surface of the second treatment barrel. Through cooperation of a second guide plate and a third guide plate, a mixed solution generated by pickling is collected and conveyed, waste heat generated in the treatment process is utilized to achieve the purpose of heat exchange with dilute phosphoric acid in the liquid storage barrel, energy is saved while the dilute phosphoric acid is heated, treatment liquid is mixed, the mixed solution is intermittently and slowly sprayed, and the treatment effect is improved. While a nitrogen source and a phosphorus source required by facultative sulfur-oxidizing bacteria are accurately supplemented, the metabolic activity of flora is promoted, and the overall treatment efficiency of hydrogen sulfide is improved.

Description

TECHNICAL FIELD

[0001] The present application relates to the technical field of atmospheric treatment, in particular to an atmospheric pollution control and purification treatment device. BACKGROUND

[0002] Atmospheric treatment is a comprehensive environmental protection field, mainly focusing on improving air quality, reducing pollutant emissions, and treating air pollution, etc. It covers multiple urban life and traffic pollution source treatment, agricultural and livestock pollution source treatment scenarios, such as livestock farming, livestock farms (e.g. cattle farms), which produce waste gas and manure treatment waste gas containing ammonia, hydrogen sulfide, methane, carbon dioxide, volatile organic compounds, dust, and water vapor, etc. From an environmental perspective, ammonia and hydrogen sulfide in waste gas pollute the atmosphere, methane exacerbates global warming, and untreated emissions will destroy the ecological balance and affect the atmospheric environment; from a health perspective, irritating and toxic gases not only harm farm workers, but also affect surrounding residents and cause respiratory diseases or even poisoning.

[0003] Chinese Patent No. CN116550069B discloses an atmospheric pollution control and purification treatment device, which relates to the technical field of atmospheric pollution purification, comprising a device main body with a brake wheel installed at the four corners of the bottom outer wall, a plurality of air inlets are formed on one side of the device main body, and an air outlet is formed on the other side of the device main body. It also includes an air inlet filtering assembly, which includes a plurality of semi-circular air inlet cylinders fixedly installed in the air inlet; the multiple circular filter discs provided in this patent can filter and remove most of the dust and particles in the air when the semi-circular air inlet cylinders are in the air inlet, and can rotate the driven worm gear ring and the circular filter disc by rotating the auger worm, so that the upper half of the circular filter disc filters the air, while the lower half of the circular filter disc is placed inside the cleaning tank, and the cleaning unit can ensure the cleanliness of the circular filter disc to ensure its long-term filtering effect.

[0004] The above device can process air while achieving self-cleaning effect by using the cleaning tank during operation, but the above patent lacks targeted and staged treatment of multiple pollutants (such as ammonia and hydrogen sulfide) in waste gas, and cannot utilize waste heat during waste gas treatment. SUMMARY

[0005] The main purpose of the present application is to provide an atmospheric pollution control and purification treatment device, which can effectively solve the problem of not being able to target and stage the treatment of multiple pollutants in waste gas, and also can utilize waste heat and treatment liquid during waste gas treatment to achieve self-cleaning.

[0006] To achieve the above purpose, the technical solution adopted by the present application is:

[0007] The application discloses an atmospheric pollution control and purification device, which comprises a processing cylinder I and a processing cylinder II, wherein the processing cylinder I and the processing cylinder II are arranged on the ground, an acid washing assembly is arranged on the upper part of the inner surface of the processing cylinder I, a collecting assembly I is arranged on the middle part of the inner surface of the processing cylinder I, a flushing assembly is arranged on the middle upper part of the inner surface of the processing cylinder I, an adsorption assembly is arranged on the middle part of the inner surface of the processing cylinder II, a collecting assembly II is arranged on the middle lower part of the inner surface of the processing cylinder II, a water cooling assembly is arranged on the middle upper part of the inner surface of the processing cylinder II, and a rotating assembly is arranged on the lower part of the collecting assembly II.

[0008] Preferably, the upper part of the inner surface of the processing cylinder I is fixedly connected with a gas conveying pipe, a plurality of gas inlet pipes are arranged in an annular array on the lower side of the inner surface of the processing cylinder I, a rotating rod is rotatably connected to the middle part of the bottom wall of the inner surface of the processing cylinder I, a plurality of spiral blades are arranged in an annular array on the outer surface of the rotating rod, the spiral blades are distributed in a spiral ascending manner, and the spiral blades are fixedly connected with flow guide plates on the side away from the rotating rod.

[0009] Preferably, one end of the gas conveying pipe away from the processing cylinder I is fixedly connected with the inner surface of the processing cylinder II, and a plurality of spiral condensing plates are arranged in a spiral array on the upper part of the inner surface of the processing cylinder II.

[0010] Preferably, the acid washing assembly comprises a dispersion filler I fixedly connected with the upper part of the inner surface of the processing cylinder I, an acid washing pipe II fixedly connected with the inner surface of the processing cylinder I above the dispersion filler I, a dispersion filler II fixedly connected with the inner surface of the processing cylinder I above the acid washing pipe II, and an acid washing pipe I fixedly connected with the inner surface of the processing cylinder I above the dispersion filler II.

[0011] Preferably, the collecting assembly I comprises a guide plate II fixedly connected with the inner surface of the processing cylinder I, the guide plate II is arranged below the dispersion filler II, a guide plate III is fixedly connected with the inner surface of the processing cylinder I below the dispersion filler II, the guide plate II and the guide plate III are fixedly connected with a collecting pipe I, one end of the collecting pipe I away from the guide plate II is fixedly connected with a spiral heat dissipation pipe, the outer surface of one end of the spiral heat dissipation pipe away from the collecting pipe I is provided with a collecting barrel I, and the outer surface of the collecting barrel I is provided with a liquid outlet pipe II.

[0012] Preferably, the flushing assembly comprises a flushing pipe I fixedly connected with the inner surface of the processing cylinder I, the flushing pipe I is arranged between the dispersion filler I and the guide plate III, a flushing pipe II is fixedly connected with the inner surface of the processing cylinder I between the dispersion filler II and the guide plate II, the flushing pipe I and the flushing pipe II are fixedly connected with a liquid guide pipe I, one end of the liquid guide pipe I away from the processing cylinder I is fixedly connected with a liquid pump I, the outer surface of the liquid pump I is provided with a liquid storage barrel, and the spiral heat dissipation pipe is arranged in the liquid storage barrel.

[0013] Preferably, the collecting assembly two comprises a dispersion plate fixedly connected to the lower side of the inner surface of the processing cylinder two, a guide plate four fixedly connected to the inner surface of the processing cylinder two above the dispersion plate, an aeration pipe fixedly connected to the inner surface of the processing cylinder two above the guide plate four, and a hose fixedly connected to one side of the aeration pipe, wherein one end of the hose away from the aeration pipe penetrates through the inner surface of the processing cylinder two and extends to the outer surface.

[0014] Preferably, the adsorbing assembly comprises adsorbing filler one fixedly connected to the inner surface of the processing cylinder two, wherein the adsorbing filler one is above the aeration pipe, the inner surface of the processing cylinder two is fixedly connected with adsorbing filler two above the adsorbing filler one, the inner surface of the processing cylinder two is fixedly connected with adsorbing filler three above the adsorbing filler two, the inner surface of the processing cylinder two is fixedly connected with flushing pipe three above the adsorbing filler three, one side of the flushing pipe three is fixedly connected with liquid guide pipe two, one end of the liquid guide pipe two away from the flushing pipe three penetrates through the inner surface of the processing cylinder two and extends to the outer surface, and the outer surface of one end of the liquid guide pipe two away from the processing cylinder two is fixedly connected with liquid pump two, and the outer surface of the liquid pump two is provided with a storage cylinder.

[0015] Preferably, the water cooling assembly comprises guide plate one fixedly connected to the inner surface of the processing cylinder two, wherein the guide plate one is below a plurality of spiral condensing plates, the inner surface of the processing cylinder two is fixedly connected with water cooling plate between the adsorbing filler two and the adsorbing filler three, one side of the guide plate one and the water cooling plate is fixedly connected with U-shaped pipe, one side of the water cooling plate away from the U-shaped pipe is fixedly connected with drainage tube, the outer surface of one end of the drainage tube away from the processing cylinder two is provided with collecting cylinder, and one side of the outer surface of the collecting cylinder is fixedly connected with liquid outlet pipe one.

[0016] Preferably, the rotating assembly comprises rotating roller in transmission connection with the outer surface of the lower side of the rotating rod, the outer surface of the upper part of the rotating roller is fixedly connected with cam, one end of the hose away from the processing cylinder two is fixedly connected with air bag, one side of the outer surface of the air bag is fixedly connected with air inlet, one end of the air bag close to the processing cylinder two is fixedly connected with fixed plate, one end of the air bag away from the processing cylinder two is fixedly connected with sliding plate, the lower end of the sliding plate is slidingly connected with rectangular groove, and one end of the sliding plate close to the processing cylinder two is fixedly connected with a plurality of springs.

[0017] Compared with the prior art, the present application has the following beneficial effects:

[0018] 1、The acid washing assembly cooperates with the collecting assembly to complete the acid washing of ammonia in the air and the collection of salt solution at the same time, and can also realize self-cleaning of the acid washing assembly by cooperating with the flushing assembly by using neutralization heat, the collecting assembly two, the rotating assembly and the adsorption assembly are matched, the hydrogen sulfide in the waste gas is adsorbed and treated, and the water cooling assembly and the adsorption assembly are matched, the temperature of the cooling waste gas is lowered, and the spray and permeation of the treatment structure in the adsorption assembly are realized, so that the service life of the structure in the adsorption assembly is further prolonged, and various pollutants (such as ammonia and hydrogen sulfide) in the waste gas are treated in stages, so that the air pollution degree around the farm is further reduced.

[0019] 2、The preliminary waste gas is dispersed and upwardly guided by the rotating rod cooperating with a plurality of spiral blades, the waste gas is dispersed and the ascending speed of the waste gas is reduced by the cooperation of the dispersion filler one and the dispersion filler two, so that the waste gas is fully reacted with the acid washing liquid, the mixed liquid generated by acid washing is collected and transported by the cooperation of the guide plate two and the guide plate three, the neutralization heat in the acid washing process is used to cooperate with the spiral heat dissipation pipe to achieve heat exchange with the dilute phosphoric acid in the inside of the liquid storage barrel, the dilute phosphoric acid in the inside of the liquid storage barrel is heated, and energy is saved, and then the dilute phosphoric acid is used to wash the dispersion filler one and the dispersion filler two from bottom to top, the dissolved product is crystallized, and the self-cleaning effect is realized, the acid washing treatment of ammonia in the waste gas, solution collection and backflushing cleaning are realized by the cooperation of the dispersion filler one and the dispersion filler two, the guide plate two and the guide plate three, the flushing pipe one and the flushing pipe two and other structures, the air waste gas treatment efficiency is further improved, and energy is saved.

[0020] 3、The water vapor in the waste gas is condensed and guided by the cooperation of a plurality of spiral condensing plates, and is gathered, and the waste gas in the treatment of the facultative sulfur-oxidizing bacteria is also cooled in the condensate delivery process by the cooperation of the water cooling plate and other structures, so as to ensure the activity of the facultative sulfur-oxidizing bacteria and the treatment effect of hydrogen sulfide, and the air is continuously delivered into the inside of the treatment cylinder two by the cooperation of the cam and the sliding plate and the hose and other structures, the facultative sulfur-oxidizing bacteria in the inside of the adsorption filler one and the adsorption filler two and the adsorption filler three are used to realize the conversion of part of the sulfur single element generated by the treatment of hydrogen sulfide into sulfate, which is dissolved in the water solution on the surface of the adapted volcanic bed, and the probability of blockage of the adsorption filler one and the adsorption filler two and the adsorption filler three is further reduced.

[0021] 4、The present application is through the cooperation of the liquid outlet pipe two and the storage cylinder and the liquid outlet pipe one, the condensate water and the ammonium dihydrogen phosphate are quantitatively mixed, and through the cooperation of the liquid guide pipe two and the flushing pipe three, the mixed liquid is intermittently and slowly sprayed on the adsorption filler three, the nitrogen source and the phosphorus source required by the facultative sulfur-oxidizing bacteria are accurately supplemented, the internal pH of the adsorption filler is adjusted to the optimum range of the bacterial population, and the internal temperature of the adsorption filler two and the adsorption filler one is also reduced, the metabolic activity of the bacterial population is promoted, and the overall treatment efficiency of hydrogen sulfide is improved. BRIEF DESCRIPTION OF DRAWINGS

[0022] Figure 1 It is the overall structure schematic diagram of the present application;

[0023] Figure 2 It is the overall internal structure schematic diagram of the present application;

[0024] Figure 3 It is the partial structure schematic diagram of the processing cylinder one of the present application;

[0025] Figure 4 It is the acid washing assembly structure schematic diagram of the present application;

[0026] Figure 5 It is the collection assembly one structure schematic diagram of the present application;

[0027] Figure 6 It is the flushing assembly structure schematic diagram of the present application;

[0028] Figure 7 It is the collection assembly two structure schematic diagram of the present application;

[0029] Figure 8 It is the rotating assembly structure schematic diagram of the present application;

[0030] Figure 9 It is the adsorption assembly structure schematic diagram of the present application;

[0031] Figure 10 It is the water cooling assembly structure schematic diagram of the present application.

[0032] Figure: 1, processing cylinder one; 11, gas pipe; 12, gas inlet pipe; 13, rotating rod; 14, spiral blade; 141, guide plate; 2, processing cylinder two; 21, spiral condensing plate; 3, flushing assembly; 31, flushing pipe one; 32, flushing pipe two; 33, liquid guide pipe one; 34, liquid storage barrel; 35, liquid pump one; 4, rotating assembly; 41, motor; 42, cam; 43, rotating roller; 44, rectangular groove; 45, fixed plate; 46, sliding plate; 47, air bag; 471, air inlet; 48, spring; 5, water cooling assembly; 51, guide plate one; 52, U-shaped pipe; 53, water cooling plate; 54, drainage pipe; 55, collection cylinder; 56, liquid outlet pipe one; 6, pickling assembly; 61, dispersed filler one; 62, dispersed filler two; 63, pickling pipe one; 64, pickling pipe two; 7, collection assembly one; 71, guide plate two; 72, guide plate three; 73, collection pipe one; 74, spiral heat dissipation pipe; 75, collection barrel one; 76, liquid outlet pipe two; 8, adsorption assembly; 81, adsorption filler one; 82, adsorption filler two; 83, adsorption filler three; 84, flushing pipe three; 85, liquid guide pipe two; 86, liquid pump two; 87, storage cylinder; 9, collection assembly two; 91, dispersion plate; 92, guide plate four; 93, aeration pipe; 94, hose. DETAILED DESCRIPTION

[0033] In order to make the technical means, creative features, purposes and effects of the present application easy to understand, the present application is further described below in conjunction with specific embodiments.

[0034] Embodiment one, as shown in Figure 1 and Figure 2 , an atmospheric pollution control and purification treatment device, comprising a processing cylinder one 1 and a processing cylinder two 2, the processing cylinder one 1 and the processing cylinder two 2 are both arranged on the ground, the pickling assembly 6 is arranged on the upper part of the inner surface of the processing cylinder one 1, the collection assembly one 7 is arranged on the middle part of the inner surface of the processing cylinder one 1, the flushing assembly 3 is arranged on the middle upper part of the inner surface of the processing cylinder one 1, the adsorption assembly 8 is arranged on the middle part of the inner surface of the processing cylinder two 2, the collection assembly two 9 is arranged on the middle lower part of the inner surface of the processing cylinder two 2, the water cooling assembly 5 is arranged on the middle upper part of the inner surface of the processing cylinder two 2, and the rotating assembly 4 is arranged below the collection assembly two 9.

[0035] For the mixed exhaust gas in the process of cattle farm breeding, after being collected by the existing ventilation collection system, the mixed exhaust gas is transported to the cyclone dust collector to remove the dust particles in the mixed exhaust gas, and then the mixed exhaust gas is transported to the inside of the treatment cylinder 1, and the ammonia in the mixed exhaust gas is treated by pickling through the pickling assembly 6 arranged inside the treatment cylinder 1, and the salt solution generated in the pickling process is collected by the collection assembly 1 7, and the salt solution is transported to the outer surface of the treatment cylinder 1 for storage. During the process of transporting the salt solution by the collection assembly 1 7, the part of the washing assembly 3 is continuously heated by the neutralization heat generated in the pickling process, which can intermittently realize the backwashing of the pickling assembly 6 by using the warm dilute acid solution, realize the self-cleaning effect of the pickling assembly 6 in the process of treating ammonia, and can also save resources;

[0036] After the mixed exhaust gas is treated by pickling through the pickling assembly 6, it is transported to the inner surface of the treatment cylinder 2, and through the cooperation of the rotating assembly 4 and the collection assembly 2 9, air is continuously transported to the inner surface of the treatment cylinder 2 during the further treatment of the mixed exhaust gas, and the hydrogen sulfide in the mixed exhaust gas is treated by adsorption through the cooperation of the oxygen in the air and the adsorption assembly 8. After the hydrogen sulfide adsorption treatment, the mixed exhaust gas passes through the upper part of the inner surface of the treatment cylinder 2, and the water vapor in the mixed exhaust gas is condensed into small water droplets and collected by the water cooling assembly 5. During the process of collecting and transporting the condensed water by the water cooling assembly 5, part of the structure of the water cooling assembly 5 can cool the exhaust gas after hydrogen sulfide treatment by cooperating with the transported condensed water, so as to avoid the influence of the exhaust gas with too high temperature on the treatment effect of the adsorption assembly 8;

[0037] During the treatment of the mixed exhaust gas, part of the condensed water collected and transported by the water cooling assembly 5 and part of the salt solution collected and transported by the collection assembly 1 7 are mixed, and the mixed liquid is slowly transported to the upper part of the adsorption assembly 8, so as to realize the slow penetration of the mixed liquid from the upper part of the adsorption assembly 8, and to penetrate and cool part of the structure of the adsorption assembly 8, thereby prolonging the service life of the adsorption assembly 8;

[0038] After the mixed exhaust gas is treated by pickling, adsorption and condensation, the remaining mixed exhaust gas is output through the upper part of the inner surface of the treatment cylinder 2 for subsequent treatment.

[0039] During the operation of the embodiment, the acid washing assembly 6 cooperates with the collection assembly one 7 to complete the acid washing of ammonia in the air and the collection of the salt solution, and the neutralization heat cooperates with the flushing assembly 3 to realize the self-cleaning of the acid washing assembly 6. Through the cooperation of the collection assembly two 9, the rotating assembly 4, and the adsorption assembly 8, the hydrogen sulfide adsorption treatment is completed. At the same time, the water cooling assembly 5 and the adsorption assembly 8 cooperate to cool the exhaust gas temperature and realize the spraying and permeation of the treatment structure in the adsorption assembly 8, further prolonging the service life of the structure in the adsorption assembly 8. Through the cooperation of various assemblies, various pollutants (such as ammonia and hydrogen sulfide) in the exhaust gas are treated in stages, further reducing the air pollution around the farm.

[0040] In the second embodiment, based on the first embodiment, the acid washing of ammonia in the acid washing exhaust gas is realized, and the neutralization heat of the acid washing is used for heat exchange, and the self-cleaning effect of the equipment is realized.

[0041] Referring to Figure 2 and Figure 3 , the inner surface of the treatment cylinder one 1 is fixedly connected with a gas inlet pipe 11 at the upper part, and a plurality of gas inlet pipes 12 are arranged in an annular array at the lower side of the inner surface of the treatment cylinder one 1. A rotating rod 13 is rotatably connected to the middle of the bottom wall of the inner surface of the treatment cylinder one 1, and a plurality of spiral blades 14 are arranged in an annular array on the outer surface of the rotating rod 13. The plurality of spiral blades 14 are distributed in a spiral upward manner, and each of the plurality of spiral blades 14 is fixedly connected with a flow guide plate 141 away from the rotating rod 13.

[0042] The rotating direction of the rotating rod 13 matches the spiral direction of the plurality of spiral blades 14, and the plurality of spiral blades 14 can be used to transport the exhaust gas upward during the rotation of the rotating rod 13.

[0043] The exhaust gas separated by the cyclone dust collector in the prior art is introduced into the lower part of the inner surface of the treatment cylinder one 1 through the plurality of gas inlet pipes 12. At this time, the rotating rod 13 is constantly rotating to drive the plurality of spiral blades 14 to rotate. After the mixed exhaust gas is introduced into the inner surface of the treatment cylinder one 1 through the plurality of gas inlet pipes 12, the plurality of spiral blades 14 are scattered, and the scattered exhaust gas is uniformly guided upward by the matched flow guide plates 141.

[0044] Referring to Figure 4 , the acid washing assembly 6 includes a dispersion filler one 61 fixedly connected to the upper part of the inner surface of the treatment cylinder one 1. An acid washing pipe two 64 is fixedly connected to the inner surface of the treatment cylinder one 1 above the dispersion filler one 61. A dispersion filler two 62 is fixedly connected to the inner surface of the treatment cylinder one 1 above the acid washing pipe two 64. An acid washing pipe one 63 is fixedly connected to the inner surface of the treatment cylinder one 1 above the dispersion filler two 62.

[0045] The ceramic particles filled in the dispersion filler one 61 and the dispersion filler two 62 can disperse the exhaust gas and slow down the rising speed of the exhaust gas during the process that the mixed exhaust gas passes through the dispersion filler one 61 and the dispersion filler two 62.

[0046] The acid washing pipe one 63 and the acid washing pipe two 64 are fixedly connected with a plurality of spray heads at the lower side of the outer surface, and the acid washing pipe one 63 and the acid washing pipe two 64 are connected with the external phosphoric acid solution source. During the process of treating the exhaust gas, the low-concentration phosphoric acid is continuously sprayed downward through the plurality of spray heads.

[0047] The acid washing pipe one 63 and the acid washing pipe two 64 and the plurality of spray heads are made of polypropylene which is commonly used in the prior art and has the corrosion resistance and does not react with the phosphoric acid and the ammonia gas.

[0048] After the mixed exhaust gas is uniformly delivered by the plurality of spiral blades 14, the low-concentration phosphoric acid is continuously sprayed downward through the acid washing pipe one 63 and the acid washing pipe two 64, and the ceramic filler in the dispersion filler one 61 and the dispersion filler two 62 disperses and reduces the rising speed of the exhaust gas, so that the low-concentration phosphoric acid can fully react with the ammonia gas in the exhaust gas, and most of the reaction products are ammonium dihydrogen phosphate, and the reaction ammonium dihydrogen phosphate can be collected together with the descending low-concentration phosphoric acid solution.

[0049] The low-concentration phosphoric acid solution is calculated in advance according to the ammonia gas concentration in the exhaust gas, and the spraying amount of the acid washing pipe one 63 and the acid washing pipe two 64 and the resistance and speed reduction of the dispersion filler two 62 and the dispersion filler one 61 to the exhaust gas can ensure that the low-concentration phosphoric acid solution can completely neutralize the ammonia gas in the exhaust gas, and the reaction product is mainly monoammonium salt of ammonium dihydrogen phosphate which has good water solubility and is not easy to crystallize, so that the product can avoid blocking the dispersion filler one 61 and the dispersion filler two 62.

[0050] Referring to Figure 5 The collection assembly one 7 includes a guide plate two 71 fixedly connected with the inner surface of the treatment cylinder one 1, the guide plate two 71 is located below the dispersion filler two 62, a guide plate three 72 is fixedly connected with the inner surface of the treatment cylinder one 1 below the dispersion filler one 61, the guide plate two 71 and the guide plate three 72 are fixedly connected with a collection pipe one 73, one end of the collection pipe one 73 away from the guide plate two 71 is fixedly connected with a spiral heat dissipation pipe 74, the outer surface of one end of the spiral heat dissipation pipe 74 away from the collection pipe one 73 is provided with a collection bucket one 75, and the outer surface of the collection bucket one 75 is provided with a liquid outlet pipe two 76.

[0051] The material of the guide plate two 71 and the guide plate three 72 is a polytetrafluoroethylene PTFE film in the prior art, which has extremely low surface energy and cannot permeate liquid water, and only allows gas to pass through, with small resistance and high permeability to gases such as methane, carbon dioxide, VOCs, etc. Through the cooperation of the guide plate two 71 and the guide plate three 72, the rising of the waste gas is not blocked, and the excess low-concentration phosphoric acid and the product ammonium dihydrogen phosphate in the pickling process are also collected above the guide plate two 71 and the guide plate three 72.

[0052] The collection barrel one 75 is arranged on the ground, and the end of the spiral heat dissipation pipe 74 away from the collection pipe one 73 is located in the upper middle part of the inner surface of the collection barrel one 75. In addition, the collection barrel one 75 is internally provided with a stirrer commonly used in the prior art, which continuously stirs in the collection barrel one 75 during the waste gas treatment process, so that the collected phosphoric acid solution and ammonium dihydrogen phosphate solution are fully mixed. The collection barrel one 75 is in communication with the external salt solution treatment device. During the mixing of phosphoric acid and ammonium dihydrogen phosphate in the collection barrel one 75, the mixed solution is continuously transported to the outside for the next operation, and the overflow of the mixed solution in the collection barrel one 75 during the waste gas treatment process is avoided.

[0053] The liquid outlet pipe two 76 is internally provided with a timing valve near one end of the collection barrel one 75. The timing valve is commonly used in the prior art and can be opened every interval time by setting control, and is immediately closed after a certain time, thereby realizing the intermittent quantitative delivery of the mixed liquid in the collection barrel one 75 through the liquid outlet pipe two 76.

[0054] The guide plate two 71 and the guide plate three 72 are both arranged obliquely. During the pickling process, the excess low-concentration phosphoric acid and the ammonium dihydrogen phosphate solution generated by pickling are collected and converged by the guide plate two 71 and the guide plate three 72 into the collection pipe one 73, and then transported to the spiral heat dissipation pipe 74 through the collection pipe one 73. Since the connection part of the collection pipe one 73 and the guide plate three 72 is higher than the upper surface of the spiral heat dissipation pipe 74, when the collected mixed solution is transported by the collection pipe one 73, the liquid in the collection pipe one 73 can be automatically pressed into the spiral heat dissipation pipe 74 through the height difference, and then flow from the end of the spiral heat dissipation pipe 74 away from the collection pipe one 73 to the inside of the collection barrel one 75.

[0055] Through continuous treatment of the waste gas, the liquid level in the collection barrel one 75 is always slightly higher than the upper part of the inner surface of the liquid outlet pipe two 76.

[0056] Referring to Figure 6, the flushing assembly 3 includes the flushing pipe one 31 fixedly connected with the inner surface of the processing cylinder one 1, the flushing pipe one 31 is located between the dispersion filler one 61 and the guide plate three 72, the flushing pipe two 32 is fixedly connected with the inner surface of the processing cylinder one 1 between the dispersion filler two 62 and the guide plate two 71, the flushing pipe one 31 and the flushing pipe two 32 are fixedly connected with the liquid guide pipe one 33, the liquid guide pipe one 33 is fixedly connected with the liquid pump one 35 at the end away from the processing cylinder one 1, the liquid pump one 35 is provided with the liquid storage barrel 34 on the outer surface, and the spiral heat dissipation pipe 74 is located in the liquid storage barrel 34.

[0057] The above-mentioned liquid storage barrel 34 is arranged on the ground, and the above-mentioned liquid storage barrel 34 is connected with the outside dilute phosphoric acid source, and the dilute phosphoric acid solution is periodically supplemented into the liquid storage barrel 34.

[0058] The above-mentioned liquid pump one 35 is a conventional design in the prior art, the liquid pump one 35 has certain acid resistance and will not be corroded by the dilute phosphoric acid in the liquid storage barrel 34, and the phosphoric acid in the liquid storage barrel 34 can be transported to the inner surface of the liquid guide pipe one 33 through the cooperation of the liquid pump one 35 and continue to be transported upwards.

[0059] The materials of the above-mentioned flushing pipe one 31, the flushing pipe two 32, the liquid guide pipe one 33 and the liquid storage barrel 34 are the same as those of the pickling pipe one 63 and the pickling pipe two 64, and a plurality of spray heads are arranged on the upper part of the outer surface of the flushing pipe one 31 and the flushing pipe two 32, and a one-way valve is arranged at the connection position of the plurality of spray heads and the flushing pipe one 31 and the flushing pipe two 32, so that the descending mixed liquid cannot enter the inside of the flushing pipe one 31 or the flushing pipe two 32 through the spray heads, and the liquid in the inside of the flushing pipe one 31 and the flushing pipe two 32 can be sprayed out through the one-way valve.

[0060] In the process of spraying low-concentration dilute phosphoric acid through the pickling pipe one 63 and the pickling pipe two 64 to carry out pickling and ammonia gas, ammonium dihydrogen phosphate is generated, and a certain amount of heat is also generated, so that the temperature of the product mixed liquid is higher than the normal temperature, and as the waste gas is continuously treated, the phosphoric acid continuously reacts with the ammonia gas, the generated neutralization heat gradually accumulates and increases, and the temperature of the product mixed liquid increases;

[0061] In the process of transporting the mixed liquid generated by pickling by using the collecting pipe one 73 and the spiral heat dissipation pipe 74, the mixed liquid is extruded and spirally rises in the process of passing through the spiral heat dissipation pipe 74, and then the mixed liquid exchanges heat with the dilute phosphoric acid in the inside of the spiral heat dissipation pipe 74 and the liquid storage barrel 34, so that the temperature of the mixed liquid itself is reduced, the dilute phosphoric acid is slowly heated by using the neutralization heat, and after a period of time, the overall temperature of the dilute phosphoric acid solution in the inside of the liquid storage barrel 34 is higher than the normal temperature.

[0062] In the process of waste gas treatment, using phosphoric acid pickling ammonia, in addition to produce ammonium dihydrogen phosphate, there will be a certain amount of diammonium hydrogen phosphate crystallization, may gradually block the ceramic filler inside the dispersion filler one 61 and dispersion filler two 62.

[0063] After a period of time after the waste gas treatment, by stimulating liquid pump one 35, the temperature of the phosphoric acid solution inside the liquid storage barrel 34 is higher than the normal temperature, which flows from the liquid guide pipe one 33 to the liquid guide pipe two 32 and is uniformly sprayed upward from the nozzle on the outer surface of the flushing pipe one 31 and the flushing pipe two 32, and the temperature of the phosphoric acid solution is slightly higher, which can dissolve the diammonium hydrogen phosphate crystallization inside the dispersion filler one 61 and the dispersion filler two 62 more quickly, realize the self-cleaning of the dispersion filler one 61 and the dispersion filler two 62, and assist the phosphoric acid in the acid washing pipe one 63 and the acid washing pipe two 64 to spray the ammonia gas in the waste gas.

[0064] Similarly, the washed phosphoric acid mixed reaction product is guided by the guide plate two 71 and the guide plate three 72 to be collected in the collection barrel one 75.

[0065] Therefore, the present scheme realizes the dispersion and upward flow of the initially introduced waste gas by the rotating rod 13 cooperating with a plurality of spiral blades 14, disperses the waste gas and reduces the upward speed of the waste gas by the cooperation of the dispersion filler one 61 and the dispersion filler two 62, makes the waste gas fully react with the pickling liquid, collects and transports the mixed liquid produced by pickling by the cooperation of the guide plate two 71 and the guide plate three 72, uses the neutralization heat in the pickling process to cooperate with the spiral heat dissipation pipe 74 to achieve heat exchange with the dilute phosphoric acid inside the liquid storage barrel 34, realizes the effect of heating the dilute phosphoric acid inside the liquid storage barrel 34, saves energy, and further realizes the effect of washing the dispersion filler one 61 and the dispersion filler two 62 from bottom to top by using dilute phosphoric acid, dissolving the product crystallization while self-cleaning, and realizes the efficient circulation of ammonia gas pickling treatment, solution collection and back flushing by the cooperation of the dispersion filler one 61 and the dispersion filler two 62, the guide plate two 71 and the guide plate three 72, the flushing pipe one 31 and the flushing pipe two 32 and other structures, further improves the waste gas treatment efficiency while saving energy.

[0066] In example three, based on examples one and two, the effect of using facultative sulfur-oxidizing bacteria to treat hydrogen sulfide gas in waste gas while using condensed water to reduce the temperature of waste gas is realized, and the effect of using condensed water to prepare mixed liquid to provide nutrients required by facultative sulfur-oxidizing bacteria is also realized.

[0067] Referring to Figure 2 , the gas conveying pipe 11 is fixedly connected to the lower side of the inner surface of the treatment cylinder two 2 away from the one end of the treatment cylinder one 1, and the spiral array of the spiral condensing plate 21 is arranged on the upper part of the inner surface of the treatment cylinder two 2.

[0068] The waste gas after the acid washing treatment is transported to the lower part of the inner surface of the treatment cylinder two 2 through the gas pipe 11 and moves upward along the inner surface of the treatment cylinder two 2.

[0069] The plurality of spiral condensing plates 21 are conventional designs in the prior art, and the plurality of spiral condensing plates 21 are distributed in a spiral upward manner, so that when the waste gas passes through the plurality of spiral condensing plates 21 in sequence, the water vapor in the waste gas is condensed into water droplets, and the condensed water droplets flow downward along the spiral condensing plates 21 and converge.

[0070] Referring to Figure 7 , the collecting assembly two 9 includes a dispersion plate 91 fixedly connected to the lower side of the inner surface of the treatment cylinder two 2, a guide plate four 92 fixedly connected to the inner surface of the treatment cylinder two 2 above the dispersion plate 91, an aeration pipe 93 fixedly connected to the inner surface of the treatment cylinder two 2 above the guide plate four 92, a hose 94 fixedly connected to one side of the aeration pipe 93, and an end of the hose 94 away from the aeration pipe 93 penetrating through the inner surface of the treatment cylinder two 2 and extending to the outer surface.

[0071] The dispersion plate 91 is internally provided with a ceramic particle filler, which disperses the waste gas and slows down the upward speed of the waste gas.

[0072] The guide plate four 92 is made of the same material as the guide plate two 71 and the guide plate three 72, and will not be described in detail in this scheme. The guide plate four 92 is arranged in an inclined manner, and the lower side of the guide plate four 92 is connected to the external conveying pipe.

[0073] The aeration pipe 93 is provided with a plurality of spray heads on the outer surface, and a one-way valve is arranged at the connection between the aeration pipe 93 and the plurality of spray heads, so that the gas in the aeration pipe 93 can be sprayed outward through the one-way valve and the spray heads, and the gas or liquid from the outside cannot enter the inside of the aeration pipe 93 through the spray heads.

[0074] Referring to Figure 8 , the rotating assembly 4 includes a rotating roller 43 in transmission connection with the lower side of the outer surface of the rotating rod 13, a motor 41 fixedly connected to the upper end of the rotating roller 43, a cam 42 fixedly connected to the upper part of the outer surface of the rotating roller 43, an air bag 47 fixedly connected to an end of the hose 94 away from the treatment cylinder two 2, an air inlet 471 fixedly connected to one side of the outer surface of the air bag 47, a fixed plate 45 fixedly connected to an end of the air bag 47 close to the treatment cylinder two 2, a sliding plate 46 fixedly connected to an end of the air bag 47 away from the treatment cylinder two 2, a rectangular groove 44 in sliding connection with the lower end of the sliding plate 46, and a plurality of springs 48 fixedly connected to an end of the sliding plate 46 close to the treatment cylinder two 2.

[0075] The rotating rod 13 and the rotating roller 43 are in transmission connection through the commonly used belt pulley in the prior art. When the rotating roller 43 is driven to rotate, the rotating rod 13 continuously rotates.

[0076] The rectangular groove 44 and the fixed plate 45 are arranged on the ground.

[0077] The connection between the above-mentioned hose 94 and the air bag 47 is provided with a one-way air outlet valve, so that the gas inside the air bag 47 enters the inside of the hose 94 through the one-way air outlet valve, and the gas inside the hose 94 cannot enter the inside of the air bag 47 through the one-way air outlet valve. The connection between the above-mentioned air inlet 471 and the air bag 47 is provided with a one-way air inlet valve, so that external air can enter the inside of the air bag 47 through the cooperation of the air inlet 471 and the one-way air inlet valve, and the gas inside the air bag 47 cannot flow in the opposite direction.

[0078] Before the exhaust gas is treated, the excitation motor 41 is started to rotate the output end of the motor 41 to drive the rotating roller 43 to rotate continuously, and then the cam 42 rotates continuously.

[0079] During the rotation of the cam 42, the sliding plate 46 will be pushed towards the side close to the treatment cylinder two 2, and then the sliding plate 46 will slide along the inner surface of the rectangular groove 44 towards the side close to the treatment cylinder two 2;

[0080] During the sliding of the sliding plate 46 towards the side close to the treatment cylinder two 2, the air bag 47 and the spring 48 are continuously squeezed through the cooperation of the fixed plate 45. During the squeezing of the air bag 47, the gas inside the air bag 47 enters the aeration pipe 93 through the hose 94 and is sprayed upwards from the nozzle on the outer surface of the aeration pipe 93. After the cam 42 rotates and the sliding plate 46 is separated, the spring 48 that is squeezed at this time restores to its original state and pushes the sliding plate 46 away from the treatment cylinder two 2, and then the sliding plate 46 stretches the air bag 47, and at this time the external air enters the inside of the air bag 47 through the air inlet 471 and the one-way air inlet valve;

[0081] With the operation of the motor 41, the cam 42 rotates continuously, so that the external air is continuously introduced into the inner surface of the treatment cylinder two 2.

[0082] Referring to Figure 9 The adsorption assembly 8 includes the adsorption filler one 81 fixedly connected to the inner surface of the treatment cylinder two 2, the adsorption filler one 81 is located above the aeration pipe 93, the adsorption filler two 82 is fixedly connected to the inner surface of the treatment cylinder two 2 above the adsorption filler one 81, the adsorption filler three 83 is fixedly connected to the inner surface of the treatment cylinder two 2 above the adsorption filler two 82, the flushing pipe three 84 is fixedly connected to the inner surface of the treatment cylinder two 2 above the adsorption filler three 83, the liquid guide pipe two 85 is fixedly connected to one side of the flushing pipe three 84, one end of the liquid guide pipe two 85 away from the flushing pipe three 84 penetrates through the inner surface of the treatment cylinder two 2 and extends to the outer surface, the liquid pump two 86 is fixedly connected to the end of the liquid guide pipe two 85 away from the treatment cylinder two 2, and the liquid pump two 86 is provided with the storage cylinder 87 on the outer surface.

[0083] The outer surface of the above-mentioned flushing pipe three 84 is provided with a plurality of nozzles, the above-mentioned liquid pump two 86 and the liquid pump one 35 are designed in the same model, and the specific operation mode will not be described in detail.

[0084] The storage cylinder 87 is internally provided with a stirrer commonly used in the prior art, which continuously stirs and mixes during the waste gas treatment process.

[0085] The internal fillers of the adsorption filler one 81, the adsorption filler two 82, and the adsorption filler three 83 are all wet volcanic rocks, and the volcanic rocks are the substrates, and a large number of facultative sulfur-oxidizing bacteria are attached to the surfaces of the volcanic rocks. The facultative sulfur-oxidizing bacteria are microorganisms commonly used in the prior art for treating hydrogen sulfide gas.

[0086] During the waste gas treatment process, the facultative sulfur-oxidizing bacteria can treat the hydrogen sulfide in the waste gas into elemental sulfur, and through the cooperation of the oxygen in the air sprayed through the aeration pipe 93, part of the converted elemental sulfur is converted into sulfate by the facultative sulfur-oxidizing bacteria in cooperation with oxygen, dissolved in water, to avoid clogging the volcanic rock bed, and through the sequential treatment of the waste gas by the adsorption filler one 81, the adsorption filler two 82, and the adsorption filler three 83, the hydrogen sulfide in the waste gas is completely eliminated.

[0087] Referring to Figure 10 The water cooling assembly 5 includes a guide plate one 51 fixedly connected to the inner surface of the treatment cylinder two 2, the guide plate one 51 is located below the plurality of spiral condensing plates 21, the water cooling plate 53 is fixedly connected to the inner surface of the treatment cylinder two 2 between the adsorption filler two 82 and the adsorption filler three 83, the guide plate one 51 and the water cooling plate 53 are fixedly connected together on one side of the U-shaped pipe 52, the water cooling plate 53 is fixedly connected to the drainage pipe 54 on the side away from the U-shaped pipe 52, the drainage pipe 54 is provided with a collection cylinder 55 on the outer surface of the end away from the treatment cylinder two 2, and the collection cylinder 55 is fixedly connected to the liquid outlet pipe one 56 on one side of the outer surface.

[0088] The material of the guide plate one 51 is the same as that of the guide plate two 71 and the guide plate three 72, and the present scheme will not be described in detail.

[0089] The water cooling plate 53 is internally provided with a curved water flow channel, the condensate water is guided into the inside of the U-shaped pipe 52 through the guide plate one 51, then enters the internal curved pipe of the water cooling plate 53, and finally flows out from the outlet on the side of the water cooling plate 53 away from the U-shaped pipe 52.

[0090] The collection cylinder 55 is arranged on the ground, and the end of the drainage pipe 54 away from the water cooling plate 53 is located on the upper part of the inner surface of the collection cylinder 55. Similarly, a timing valve is arranged at the connection between the liquid outlet pipe one 56 and the collection cylinder 55, the timing valve is commonly used in the prior art, and the timing valve can be opened every interval time through setting control, and is immediately closed after being opened for a certain time, thereby realizing the intermittent quantitative delivery of the condensate water in the collection cylinder 55 through the liquid outlet pipe one 56.

[0091] The collection cylinder 55 is connected to the external water source, and during the continuous treatment of the exhaust gas, the collection cylinder 55 slowly delivers condensed water to the external water source, so that the water level inside the collection cylinder 55 is slightly higher than the upper part of the inner surface of the liquid outlet pipe 56.

[0092] After the exhaust gas is treated by the adsorption filler 81, the adsorption filler 82 and the adsorption filler 83, it continues to rise through the water cooling plate 53 and the guide plate 51, and is removed by the cooperation of the spiral condensing plates 21, and the water vapor in the exhaust gas is condensed, and the condensed water is collected above the guide plate 51 and enters the inside of the water cooling plate 53 through the U-shaped pipe 52.

[0093] When the exhaust gas is treated by the adsorption filler 81, the adsorption filler 82 and the adsorption filler 83 in turn, the overall exhaust gas temperature slowly rises after being treated by the adsorption filler 81 and the adsorption filler 82, because the hydrogen sulfide is oxidized by the facultative sulfur-oxidizing bacteria to an exothermic reaction;

[0094] With the continuous treatment of the exhaust gas, the exhaust gas temperature slowly rises after passing through the adsorption filler 81 and the adsorption filler 82, at the same time, the condensed water in the exhaust gas is guided into the U-shaped pipe 52 and the inside of the water cooling plate 53 through the guide plate 51, and flows out from the drainage pipe 54, after a large amount of exhaust gas is treated by the cooperation of the spiral condensing plates 21, the condensed water flows into the inside of the collection cylinder 55 through the drainage pipe 54.

[0095] During the flow of condensed water in the water cooling plate 53, the exhaust gas rising through the adsorption filler 82 is slowly cooled to avoid the influence of high exhaust gas on the activity of the facultative sulfur-oxidizing bacteria in the adsorption filler 83, thereby avoiding the influence on the treatment effect of hydrogen sulfide.

[0096] Therefore, the present application can condense and guide the water vapor in the exhaust gas through the cooperation of the spiral condensing plates 21, and at the same time, the facultative sulfur-oxidizing bacteria in the exhaust gas can be cooled during the delivery of the condensed water through the cooperation of the water cooling plate 53 and other structures, so as to ensure the activity of the facultative sulfur-oxidizing bacteria and the treatment effect of hydrogen sulfide, and at the same time, the air is continuously delivered into the treatment cylinder 2 through the cooperation of the cam 42, the sliding plate 46 and the hose 94, and the oxygen in the air cooperates with the facultative sulfur-oxidizing bacteria in the adsorption filler 81, the adsorption filler 82 and the adsorption filler 83 to convert part of the sulfur produced by the treatment of hydrogen sulfide into sulfate, which is dissolved in the water solution on the surface of the adapted volcanic rock bed, thereby further reducing the probability of clogging of the adsorption filler 81, the adsorption filler 82 and the adsorption filler 83.

[0097] In the above embodiment, the liquid outlet pipe 56, the liquid outlet pipe 76 and the liquid guide pipe 85 and other structures can realize the effect of quantitatively spraying the required nutrients to the facultative sulfur-oxidizing bacteria during operation;

[0098] The specific steps of this effect are: through the cooperation of liquid outlet pipe two 76 with the timing valve, the ammonium dihydrogen phosphate solution inside the collection barrel one 75 is intermittently released into the storage cylinder 87, at the same time, the condensate water inside the collection cylinder 55 is released into the storage cylinder 87 through the cooperation of liquid outlet pipe one 56 with the timing valve, and the two solutions are fully mixed by the stirrer inside the storage cylinder 87;

[0099] Then, through the operation of liquid pump two 86, the mixed solution inside the storage cylinder 87 enters the flushing pipe three 84 through the liquid guide pipe two 85 and is intermittently sprayed down slowly, and the mixed solution sprayed down through the flushing pipe three 84 penetrates downward through the water-cooled plate 53, the adsorption filler three 83, the adsorption filler two 82 and the adsorption filler one 81 in turn;

[0100] During the downward penetration process, the nitrogen source and the phosphorus source required by the compatible sulfur-oxidizing bacteria inside the adsorption filler three 83, the adsorption filler two 82 and the adsorption filler one 81 can be accurately supplemented, the metabolic activity of the bacterial flora is promoted, and the hydrogen sulfide treatment efficiency is improved;

[0101] In addition, during the penetration process, the PH inside the adsorption filler three 83, the adsorption filler two 82 and the adsorption filler one 81 can also be slowly adjusted, so that the overall PH is stable in the most suitable range of compatible sulfur-oxidizing bacteria. Similarly, during the penetration process, the mixed solution can also reduce the temperature inside the adsorption filler two 82 and the adsorption filler one 81, so as to avoid the phenomenon that the compatible sulfur-oxidizing bacteria are inactivated due to too high temperature.

[0102] The ammonium dihydrogen phosphate mixed solution released by the liquid outlet pipe two 76 and the condensate water released by the liquid outlet pipe one 56 are calculated in advance to release the amount respectively, so that the final mixed solution is suitable for the penetration of the adsorption filler three 83, the adsorption filler two 82 and the adsorption filler one 81.

[0103] Further, the slowly penetrating mixed solution is finally guided by the guide plate four 92 and is uniformly collected and treated.

[0104] After the acid washing treatment of ammonia gas, the sulfur-oxidizing bacteria treatment of hydrogen sulfide gas and the condensation removal of water vapor, the waste gas is output from the inner surface of the treatment cylinder two 2 and is guided to the activated carbon adsorption layer commonly used in the prior art for next step processing operation. After the waste gas treatment is completed and the detection reaches the standard, it is discharged.

[0105] Further, the scheme quantitatively mixes the condensed water and the ammonium dihydrogen phosphate through the cooperation of the liquid outlet pipe two 76, the storage cylinder 87 and the liquid outlet pipe one 56, and intermittently and slowly sprays the mixed liquid on the adsorption filler three 83 through the cooperation of the liquid guide pipe two 85 and the flushing pipe three 84, so as to precisely supplement the nitrogen source and the phosphorus source required by the facultative sulfur-oxidizing bacteria, adjust the internal pH of the adsorption filler to the optimum range of the bacterial flora, and also reduce the internal temperature of the adsorption filler two 82 and the adsorption filler one 81, promote the metabolic activity of the bacterial flora, and improve the overall treatment efficiency of hydrogen sulfide.

[0106] It should be particularly pointed out that the specific installation mode of the motor 41, the connection mode of the circuit and the control method used in the present application all belong to the conventional design, and the present application will not be described in detail.

[0107] The basic principles and main features of the present application and the advantages of the present application are shown and described above. It should be understood by those skilled in the art that the present application is not limited by the above examples, and the above examples and descriptions in the specification are only to illustrate the principles of the present application. Without departing from the spirit and scope of the present application, various changes and improvements can be made to the present application, and these changes and improvements all fall within the scope of the present application. The scope of protection of the present application is defined by the appended claims and their equivalents.

Claims

1. An air pollution control purification treatment apparatus comprising a treatment cylinder I (1) and a treatment cylinder II (2), characterized in that: The processing cylinder one (1) and processing cylinder two (2) are arranged on the ground, the inner surface upper part of the processing cylinder one (1) is provided with pickling assembly (6), the inner surface middle part of the processing cylinder one (1) is provided with collection assembly one (7), the inner surface middle upper part of the processing cylinder one (1) is provided with flushing assembly (3), the inner surface middle part of the processing cylinder two (2) is provided with adsorption assembly (8), the inner surface middle lower part of the processing cylinder two (2) is provided with collection assembly two (9), the inner surface middle upper part of the processing cylinder two (2) is provided with water cooling assembly (5), the lower part of the collection assembly two (9) is provided with rotating assembly (4).

2. The device for cleaning and purifying air pollution according to claim 1, characterized in that: The inner surface upper part of the processing cylinder one (1) is fixedly connected with gas delivery pipe (11), the inner surface lower side of the processing cylinder one (1) is arranged with a plurality of gas inlet pipes (12) in annular array, the middle part of the bottom wall of the inner surface of the processing cylinder one (1) is rotatably connected with rotating rod (13), the outer surface of rotating rod (13) is arranged with a plurality of spiral blades (14) in annular array, a plurality of spiral blades (14) are distributed in spiral ascending manner, and the side, away from rotating rod (13), of a plurality of spiral blades (14) is fixedly connected with guide plate (141).

3. An air pollution control purification treatment device according to claim 2, characterized in that: The end, away from the processing cylinder one (1), of the gas delivery pipe (11) is fixedly connected with the inner surface lower side of the processing cylinder two (2), and the inner surface upper part of the processing cylinder two (2) is arranged with a plurality of spiral condensing plates (21) in spiral array.

4. The device for cleaning and purifying air pollution according to claim 1, characterized in that: The pickling assembly (6) comprises dispersion filler one (61) fixedly connected with the inner surface upper part of the processing cylinder one (1), pickling pipe two (64) fixedly connected with the inner surface of the processing cylinder one (1) above dispersion filler one (61), dispersion filler two (62) fixedly connected with the inner surface of the processing cylinder one (1) above pickling pipe two (64), and pickling pipe one (63) fixedly connected with the inner surface of the processing cylinder one (1) above dispersion filler two (62).

5. An air pollution control purification treatment device according to claim 4, characterized in that: The collection assembly one (7) comprises guide plate two (71) fixedly connected with the inner surface of the processing cylinder one (1), the guide plate two (71) is located below dispersion filler two (62), guide plate three (72) is fixedly connected with the inner surface of the processing cylinder one (1) below dispersion filler one (61), the guide plate two (71) and the guide plate three (72) are fixedly connected with collection pipe one (73) together, the end, away from the guide plate two (71), of the collection pipe one (73) is fixedly connected with spiral heat dissipation pipe (74), the outer surface of the end, away from the collection pipe one (73), of the spiral heat dissipation pipe (74) is provided with collection bucket one (75), and the outer surface of the collection bucket one (75) is provided with liquid outlet pipe two (76).

6. An air pollution control purification treatment device according to claim 5, characterized in that: The flushing assembly (3) includes a flushing pipe I (31) fixedly connected with the inner surface of the processing cylinder I (1), which is located between the dispersion filler I (61) and the guide plate III (72), and between the dispersion filler II (62) and the guide plate II (71); the inner surface of the processing cylinder I (1) is fixedly connected with a flushing pipe II (32); the flushing pipe I (31) and the flushing pipe II (32) are fixedly connected with a liquid guide pipe I (33) together; one end of the liquid guide pipe I (33) away from the processing cylinder I (1) is fixedly connected with a liquid pump I (35); the outer surface of the liquid pump I (35) is provided with a liquid storage barrel (34); and the spiral heat dissipation pipe (74) is located inside the liquid storage barrel (34).

7. An air pollution control purification treatment device according to claim 3, characterized by: The collection assembly II (9) includes a dispersion plate (91) fixedly connected with the inner surface of the lower side of the processing cylinder II (2); the inner surface of the processing cylinder II (2) is fixedly connected with a guide plate IV (92) above the dispersion plate (91); the inner surface of the processing cylinder II (2) is fixedly connected with an aeration pipe (93) above the guide plate IV (92); one side of the aeration pipe (93) is fixedly connected with a hose (94); and one end of the hose (94) away from the aeration pipe (93) penetrates through the inner surface of the processing cylinder II (2) and extends to the outer surface.

8. An air pollution control purification treatment device according to claim 7, characterized in that: The adsorption assembly (8) includes an adsorption filler I (81) fixedly connected with the inner surface of the processing cylinder II (2); the adsorption filler I (81) is located above the aeration pipe (93); the inner surface of the processing cylinder II (2) is fixedly connected with an adsorption filler II (82) above the adsorption filler I (81); the inner surface of the processing cylinder II (2) is fixedly connected with an adsorption filler III (83) above the adsorption filler II (82); the inner surface of the processing cylinder II (2) is fixedly connected with a flushing pipe III (84) above the adsorption filler III (83); one side of the flushing pipe III (84) is fixedly connected with a liquid guide pipe II (85); one end of the liquid guide pipe II (85) away from the flushing pipe III (84) penetrates through the inner surface of the processing cylinder II (2) and extends to the outer surface; one end of the liquid guide pipe II (85) away from the processing cylinder II (2) is fixedly connected with a liquid pump II (86); and the outer surface of the liquid pump II (86) is provided with a storage cylinder (87).

9. An air pollution control purification treatment device according to claim 8, characterized in that: The water cooling assembly (5) includes a guide plate I (51) fixedly connected with the inner surface of the processing cylinder II (2); the guide plate I (51) is located below a plurality of spiral condensation plates (21); the inner surface of the processing cylinder II (2) is fixedly connected with a water cooling plate (53) between the adsorption filler II (82) and the adsorption filler III (83); one side of the guide plate I (51) and the water cooling plate (53) is fixedly connected with a U-shaped pipe (52) together; one side of the water cooling plate (53) away from the U-shaped pipe (52) is fixedly connected with a drainage pipe (54); the outer surface of one end of the drainage pipe (54) away from the processing cylinder II (2) is provided with a collection cylinder (55); and one side of the outer surface of the collection cylinder (55) is fixedly connected with a liquid outlet pipe I (56).

10. The device for cleaning and purifying air pollution according to claim 7, characterized in that: Said rotating component (4) includes the transmission connection with the outer surface lower side of the rotating rod (13) rotating roller (43), the upper end fixed connection of rotating roller (43) has motor (41), the outer surface upper part fixed connection of rotating roller (43) has cam (42), the one end fixed connection of hose (94) away from processing cylinder two (2) has air bag (47), the outer surface one side fixed connection of air bag (47) has air inlet (471), the one end fixed connection of air bag (47) close to processing cylinder two (2) has fixed plate (45), the one end fixed connection of air bag (47) away from processing cylinder two (2) has sliding plate (46), the lower end sliding connection of sliding plate (46) has rectangular groove (44), the one end fixed connection of sliding plate (46) close to processing cylinder two (2) has a plurality of spring (48).

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