CN108905564B - Photocatalysis and biological bed combined type VOCs clarification plant - Google Patents
Photocatalysis and biological bed combined type VOCs clarification plant Download PDFInfo
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- CN108905564B CN108905564B CN201810817934.2A CN201810817934A CN108905564B CN 108905564 B CN108905564 B CN 108905564B CN 201810817934 A CN201810817934 A CN 201810817934A CN 108905564 B CN108905564 B CN 108905564B
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
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- B01D53/007—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by irradiation
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
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- B01D53/34—Chemical or biological purification of waste gases
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D—SEPARATION
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- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/88—Handling or mounting catalysts
- B01D53/885—Devices in general for catalytic purification of waste gases
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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Abstract
The invention belongs to the technical field of waste gas purification, and particularly relates to photocatalysis and biological bed combined VOCs (volatile organic compounds) purification equipment which comprises a reaction cavity, an elution pool, a photocatalysis device, a biodegradation layer, a biofiltration layer, a spray head, an air inlet pipeline, an air outlet and a feedback regulation device, wherein the reaction cavity is provided with a reaction cavity; the elution pool is positioned in the reaction cavity and at the bottom of the reaction cavity; the photocatalytic device is positioned in the reaction cavity and is positioned above the elution pool; the biodegradable layer is positioned in the reaction cavity and is used for biodegrading VOCs gas; the biological filter layer is positioned in the reaction cavity; the spray heads are positioned in the reaction cavity and divided into two groups, one group of spray heads is positioned between the biological degradation layer and the biological filtration layer, and the other group of spray heads is positioned above the biological filtration layer; the gas inlet pipeline is positioned below the elution pool and is used for injecting VOCs gas into the elution pool; the gas outlet is positioned at the upper part of the reaction cavity and used for discharging the evolved gas out of the reaction cavity.
Description
Technical Field
The invention belongs to the technical field of waste gas purification, and particularly relates to a photocatalysis and biological bed combined type VOCs purification device.
Background
In the production process of the industrial industry, a large amount of waste gas containing VOCs is generated, and if the waste gas is directly discharged into the atmosphere, not only air pollution is caused, but also material waste is caused, and the production cost is increased. In recent years, the work of treating the emission of VOCs has been developed in various places, and the commonly used technologies for treating VOCs include combustion methods, biological methods, absorption methods, adsorption methods, photocatalytic methods, etc., which all have certain effects on the treatment of VOCs, but all have respective disadvantages.
Patent document one: a composite biological bed purifying equipment for VOCs, application number: 2016204411534
In the above patent document 1, the present invention can effectively treat the VOCs gas by a method of elution oxidation and biodegradation absorption, but the content of the VOCs treated in a unit time is constant, and the present invention does not consider how to solve the problem of variation in the amount of gas introduced into the purification equipment in a unit time, and when the gas is introduced too much, the purification equipment cannot purify in time, and thus the purification of the VOCs is not complete.
Disclosure of Invention
In order to make up the defects of the prior art, the invention provides the photocatalysis and biological bed combined type VOCs purification equipment, which is provided with the elution pool, the photocatalysis device, the biodegradation layer and the biological filter layer, so that VOCs are purified by four layers, the purification efficiency is improved, and the purification speed is improved, thereby realizing the purification of a large amount of VOCs gas; the invention ensures that the gas in the reaction cavity is always kept in a constant state by arranging the feedback adjusting device, thereby avoiding incomplete purification caused by sudden increase of the gas in the reaction cavity.
The technical scheme adopted by the invention for solving the technical problems is as follows: the invention relates to photocatalysis and biological bed combined VOCs purification equipment, which comprises a reaction chamber, an elution pool, a photocatalysis device, a biodegradation layer, a biological filter layer, a spray head, an air inlet pipeline, an air outlet and a feedback adjusting device, wherein the reaction chamber is provided with a reaction chamber and a reaction chamber; the elution pool is positioned in the reaction cavity, the elution pool is positioned at the bottom of the reaction cavity, and the elution pool is used for carrying out oxidation treatment on VOCs gas to realize first-layer treatment on the VOCs gas; the photocatalytic device is positioned in the reaction cavity, positioned above the elution pool and used for catalytically degrading VOCs gas to realize second-layer treatment on the VOCs gas; the biodegradation layer is positioned in the reaction cavity and is used for carrying out biodegradation on VOCs gas so as to realize third-layer treatment on the VOCs gas; the biological filter layer is positioned in the reaction cavity and is used for carrying out final absorption treatment on VOCs gas, so that VOCs are completely purified; the spray heads are positioned in the reaction cavity and divided into two groups, one group of spray heads is positioned between the biological degradation layer and the biological filtration layer, the other group of spray heads is positioned above the biological filtration layer, and the spray heads are used for adding nutrient solution to the biological filtration layer and the biological degradation layer so as to ensure the quantity and activity of microorganisms in the biological degradation layer and the biological filtration layer, so that the biological degradation layer and the biological filtration layer can work continuously and efficiently; the gas inlet pipeline is positioned below the elution pool and used for injecting VOCs gas into the elution pool, so that the VOCs gas is directly contacted with the elution liquid, and the oxidation treatment efficiency of the elution pool on the VOCs gas is improved; the gas outlet is positioned at the upper part of the reaction cavity and used for discharging the purified gas out of the reaction cavity; the feedback adjusting device comprises an extrusion ring, a liquid storage pipe and a piston; the extrusion ring is positioned outside the air inlet pipeline, a cavity is arranged in the extrusion ring, water is filled in the cavity, and the extrusion ring is used for extruding the air inlet pipeline; one end of the liquid storage pipe is connected with the reaction cavity, the other end of the liquid storage pipe is connected with the extrusion ring, water is stored in the liquid storage pipe, and the liquid storage pipe is used for injecting water into the extrusion ring; the piston is located in the liquid storage pipe and used for extruding water in the liquid storage pipe. When the device works, VOCs gas is introduced into the elution pool from the gas inlet pipeline for oxidation treatment, so that first-layer treatment is realized; the eluted gas enters a space between the elution pool and the biodegradable layer, and the VOCs gas is subjected to photocatalytic treatment through a photocatalytic device to realize second-layer treatment; the gas after photocatalysis enters a biodegradation layer to be subjected to microbial degradation treatment, so that the third layer treatment of the VOCs gas is realized; the degraded gas enters a biological filter layer to be subjected to final absorption treatment, so that the fourth layer treatment is realized, the VOCs gas is fully purified through the fourth layer treatment, the purification efficiency is high, and finally, the purified gas is discharged out of the reaction chamber through a gas outlet; in the process, the spray head sprays nutrient solution to the biological filter layer and the biological degradation layer, so that the quantity and activity of microorganisms in the biological filter layer and the biological degradation layer are ensured, and the microorganisms in the biological filter layer and the biological degradation layer are ensured to treat VOCs gas at high efficiency all the time; when the gas content in the space between biodegradable layer and the elution pool is too much, gaseous piston motion among the promotion feedback control device, water in the liquid storage pipe is extruded to the piston, thereby make the water in the extrusion ring receive the extrusion, finally realize the extrusion ring extrusion admission line, reduce the speed of admitting air, it is unchangeable to guarantee to elute the gas content between pool and the biodegradable layer, make photocatalytic unit can carry out abundant photocatalysis to VOCs gas, share purification pressure for biodegradable layer and biofiltration layer simultaneously, make the gaseous more complete that purifies of VOCs.
The air inlet pipe is internally provided with an air permeable block which is of a cylindrical structure, the air permeable block is fixed in the air inlet pipe and is provided with air holes, and the air permeable block is used for changing the size of air flow. During operation, the air permeable block shrinks under the extrusion effect of the extrusion ring, so that the air permeable holes on the air permeable block shrink, the speed of gas entering the reaction cavity is reduced, the gas in the reaction cavity is always kept at a constant value, and the gas in the reaction cavity is purified more completely.
Be equipped with the pellicle on the admission line, the pellicle is located the intercommunication department of admission line and elution pond, and the pellicle is used for making VOCs gaseous entering elution pond, and the pellicle is used for preventing the eluant inflow admission line. In operation, the selectively permeable nature of the semi-permeable membrane allows gas to enter the stripper while preventing liquid from the stripper from entering the gas inlet line.
The photocatalytic device comprises a catalytic light source and a catalytic ring; the catalytic light source is obtained by combining a vertical light source and a plurality of disc light sources, the top end of the catalytic light source is fixed at the bottom of the biodegradable layer, and the catalytic light source is used for providing illumination required by catalysis; the catalytic rings and the disc light sources of the catalytic light sources are alternately arranged, the number of the catalytic rings is one less than that of the disc light sources, and the catalytic rings are used for bearing catalysts. During operation, the catalysis light source provides the catalysis light to the catalysis ring for VOCs gas takes place the photocatalytic reaction on the catalysis ring, has realized the gaseous photocatalytic degradation of VOCs, and in-process, the vertical light source of catalysis light source and the existence of disc light source make the catalysis ring obtain abundant irradiation of catalysis light, have improved the speed of photocatalytic degradation.
The catalytic ring is composed of two semi-elliptical rings, the two semi-elliptical rings are connected together through a spring, and the spring is coated with a catalyst. During operation, the spring constitutes an elliptical ring with two semi-elliptical rings, and the catalyst of paining on the spring has improved photocatalytic device's effective catalysis area simultaneously, has improved photocatalytic device's catalytic efficiency for VOCs is gaseous obtains abundant photodegradation and handles.
A pull rope and a VOCs gas detector are also arranged in the reaction cavity; the stay ropes are divided into two groups, one group of stay ropes is positioned on the right side of the catalytic ring, the right end of the catalytic ring is connected with the inner wall of the reaction cavity through the stay ropes, the other group of stay ropes is positioned on the left side of the catalytic ring, the stay ropes are connected with the left end of the catalytic ring, and the stay ropes are used for fixing the catalytic ring in the reaction cavity; the VOCs gas detector is fixed at the bottom of the biodegradable layer and is used for detecting the VOCs content of gas entering the biodegradable layer; a hollow channel is arranged in the catalysis ring, a catalysis rod is arranged in the hollow channel, and the catalysis rod is used for changing the size of the catalysis ring; rectangular lugs are arranged at two ends of the catalytic rod and are used for connecting the catalytic rod and the catalytic ring together; the outside of the reaction cavity is also provided with a winder, the winder is connected with the pull rope at the left end of the catalytic ring, and the winder is used for winding the pull rope. The during operation, the gaseous detector of VOCs detects the content of the VOCs who gets into the gas on biodegradable layer, thereby judge whether biodegradable layer and biofiltration layer can detach the VOCs gas in the gas completely, when VOCs content is too high in the gas that gets into biodegradable layer, through winder rolling stay cord, make two semielliptical rings of stay cord pulling catalysis ring, the catalysis pole constitutes not unidimensional catalysis ring with two semielliptical rings under the effect of stay cord, the size regulation of catalysis ring has been realized, catalytic area has been changed, realized handling the gaseous more efficient of VOCs, the strict control has got into the content of the VOCs of the gas on biodegradable layer.
The catalytic light source is also provided with a splayed through hole, the splayed through hole is positioned on the disc light source part of the catalytic light source, and the splayed through hole is used for reducing the ascending speed of VOCs gas below the disc light source. During operation, the arrangement of the splayed holes increases the gas pressure on the upper parts of the splayed holes, so that the speed of gas is reduced when the gas rises from the lower part of the disc light source of the catalytic light source, the VOCs gas is degraded by photocatalysis more thoroughly, and the purification rate of the purification equipment is effectively improved.
The invention has the following beneficial effects:
1. according to the photocatalysis and biological bed combined VOCs purification equipment, the elution pool, the photocatalysis device, the biodegradation layer and the biological filter layer are arranged, so that VOCs are purified by four layers, the purification rate is improved, and the purification speed is improved, so that a large amount of VOCs gas is purified; according to the invention, the feedback adjusting device is arranged, so that the gas in the reaction cavity is always kept in a constant state, incomplete purification caused by sudden increase of the gas in the reaction cavity is avoided, and the purification rate of the VOCs gas is improved.
2. This method is bright a photocatalysis and biological bed combined type VOCs clarification plant, mutually support through catalysis ring, spring, catalysis pole, stay cord and coiler and realized the size regulation of catalysis ring, the gaseous VOCs gaseous content that makes to get into the biodegradable layer of mutually supporting of catalysis ring and VOCs of adjustable size is invariable to realize that biodegradable layer and biofiltration layer purify VOCs gas completely, improved the purification rate.
3. This method is said a photocatalysis and biological bed combined type VOCs clarification plant, through scribbling the catalyst on the spring of connecting the catalysis ring, the effectual area that increases the photocatalysis has improved the efficiency to the gaseous photodegradation of VOCs.
Drawings
FIG. 1 is a front view of the present invention;
FIG. 2 is a cross-sectional view A-A of FIG. 1;
FIG. 3 is an enlarged view of a portion of FIG. 1 at C;
FIG. 4 is a cross-sectional view B-B of FIG. 1;
in the figure: the device comprises a reaction cavity 1, an elution pool 2, a photocatalytic device 3, a biodegradable layer 4, a biological filter layer 5, a spray head 6, an air inlet pipeline 7, an air outlet 8, a feedback adjusting device 9, a pull rope 11, a VOCs gas detector 12, a winder 13, a catalytic light source 31, a catalytic ring 32, a spring 33, a catalytic rod 34, a gas permeable block 71, a semipermeable membrane 72, an extrusion ring 91, a liquid storage pipe 92 and a piston 93.
Detailed Description
The structure of the apparatus for purifying VOCs by combining photocatalysis and bio-bed according to an embodiment of the present invention will be described below with reference to fig. 1 to 4.
As shown in fig. 1, the purification apparatus for VOCs of the present invention comprises a reaction chamber 1, an elution pool 2, a photocatalytic device 3, a biodegradable layer 4, a bio-filter layer 5, a nozzle 6, an air inlet pipe 7, an air outlet 8 and a feedback adjustment device 9; the elution pool 2 is positioned in the reaction cavity 1, the elution pool 2 is positioned at the bottom of the reaction cavity 1, and the elution pool 2 is used for carrying out oxidation treatment on VOCs gas to realize first-layer treatment on the VOCs gas; the photocatalytic device 3 is positioned in the reaction chamber 1, the photocatalytic device 3 is positioned above the elution pool 2, and the photocatalytic device 3 is used for catalytically degrading VOCs gas to realize second-layer treatment of the VOCs gas; the biodegradable layer 4 is positioned in the reaction cavity 1, and the biodegradable layer 4 is used for carrying out biodegradation on VOCs gas to realize third-layer treatment on the VOCs gas; the biological filter layer 5 is positioned in the reaction chamber 1, and the biological filter layer 5 is used for carrying out final absorption treatment on VOCs gas, so that VOCs are completely purified; the spray heads 6 are positioned in the reaction cavity 1, the spray heads 6 are divided into two groups, one group of spray heads 6 is positioned between the biological degradation layer 4 and the biological filtration layer 5, the other group of spray heads 6 is positioned above the biological filtration layer 5, and the spray heads 6 are used for adding nutrient solution to the biological filtration layer 5 and the biological degradation layer 4, so that the number and activity of microorganisms in the biological degradation layer 4 and the biological filtration layer 5 are ensured, and the biological degradation layer 4 and the biological filtration layer 5 can work continuously and efficiently; the gas inlet pipeline 7 is positioned below the elution pool 2, and the gas inlet pipeline 7 is used for injecting VOCs gas into the elution pool 2, so that the VOCs gas is directly contacted with the elution liquid, and the oxidation treatment efficiency of the elution pool 2 on the VOCs gas is improved; the gas outlet 8 is positioned at the upper part of the reaction chamber 1, and the gas outlet 8 is used for discharging the purified gas out of the reaction chamber 1; the feedback adjusting device 9 comprises a squeezing ring 91, a liquid storage pipe 92 and a piston 93; the extrusion ring 91 is positioned outside the air inlet pipeline 7, a cavity is arranged in the extrusion ring 91, water is filled in the cavity, and the extrusion ring 91 is used for extruding the air inlet pipeline 7; one end of the liquid storage tube 92 is connected with the reaction chamber 1, the other end of the liquid storage tube 92 is connected with the extrusion ring 91, water is stored in the liquid storage tube 92, and the liquid storage tube 92 is used for injecting water into the extrusion ring 91; the piston 93 is located in the reservoir 92, and the piston 93 is used to squeeze water in the reservoir 92. When the device works, VOCs gas is introduced into the elution pool 2 from the gas inlet pipeline 7 for oxidation treatment, so that first-layer treatment is realized; the eluted gas enters a space between the elution pool 2 and the biodegradable layer 4, and the VOCs gas is subjected to photocatalytic treatment through the photocatalytic device 3 to realize second-layer treatment; the gas after photocatalysis enters a biodegradation layer 4 for carrying out microbial degradation treatment, so that the third layer treatment of VOCs gas is realized; the degraded gas enters a biological filter layer 5 for final absorption treatment, so that the fourth layer treatment is realized, the VOCs gas is fully purified through the fourth layer treatment, the purification efficiency is high, and finally, the purified gas is discharged out of the reaction chamber 1 through a gas outlet 8; in the process, the spray head 6 sprays nutrient solution to the biological filter layer 5 and the biological degradation layer 4, so that the number and activity of microorganisms in the biological filter layer 5 and the biological degradation layer 4 are ensured, and the microorganisms in the biological filter layer 5 and the biological degradation layer 4 are ensured to treat VOCs gas at high efficiency all the time; when the gas content in the space between biodegradable layer 4 and the elution pool 2 is too much, gaseous piston 93 that promotes among the feedback adjusting device 9 moves, water in piston 93 extrusion liquid storage tube 92, thereby make the water in the extrusion ring 91 receive the extrusion, finally realize extrusion ring 91 extrusion admission line 7, reduce the speed of admitting air, guarantee that the gas content between elution pool 2 and the biodegradable layer 4 is unchangeable, make photocatalytic unit 3 can carry out abundant photocatalytic treatment to VOCs gas, purified pressure has been shared for biodegradable layer 4 and biofiltration layer 5 simultaneously, make the gaseous more complete of VOCs.
As shown in fig. 3 and 4, a ventilation block 71 is arranged in the air inlet pipe 7, the ventilation block 71 is of a cylindrical structure, the ventilation block 71 is fixed in the air inlet pipe, ventilation holes are formed in the ventilation block 71, and the ventilation block 71 is used for changing the size of air flow. During operation, the air permeable block 71 contracts under the extrusion action of the extrusion ring 91, so that the air holes in the air permeable block 71 contract, the speed of gas entering the reaction cavity 1 is reduced, the gas in the reaction cavity 1 is always kept at a constant value, and the gas in the reaction cavity 1 is purified more completely.
As shown in fig. 1 and 3, a semi-permeable membrane 72 is disposed on the gas inlet pipe 7, the semi-permeable membrane 72 is located at a communication position between the gas inlet pipe 7 and the elution tank 2, the semi-permeable membrane 72 is used for allowing VOCs gas to enter the elution tank 2, and the semi-permeable membrane 72 is used for preventing eluent from flowing into the gas inlet pipe 7. In operation, the selectively permeable nature of the semi-permeable membrane 72 allows gas to enter the stripper cell 2 while preventing liquid from the stripper cell 2 from entering the gas inlet conduit 7.
As shown in fig. 1, the photocatalytic device 3 includes a catalytic light source 31 and a catalytic ring 32; the catalytic light source 31 is obtained by combining a vertical light source and a plurality of disc light sources, the top end of the catalytic light source 31 is fixed at the bottom of the biodegradable layer 4, and the catalytic light source 31 is used for providing illumination required by catalysis; the catalytic rings 32 and the disk light sources of the catalytic light sources 31 are alternately arranged, the number of the catalytic rings 32 is one less than that of the disk light sources, and the catalytic rings 32 are used for bearing catalysts. During operation, catalysis light source 31 provides the catalysis light to catalysis ring 32 for the gaseous photocatalytic reaction takes place for VOCs on catalysis ring 32, has realized the gaseous photocatalytic degradation of VOCs, and in-process, the vertical light source of catalysis light source 31 and the existence of disc light source make catalysis ring 32 obtain the shining of abundant catalytic light, have improved the rate of photocatalytic degradation.
As shown in fig. 1 and 2, the catalytic ring 32 is composed of two semi-elliptical rings, the two semi-elliptical rings are connected together by a spring 33, and the spring 33 is coated with a catalyst. During operation, spring 33 constitutes an elliptical ring with two semi-elliptical rings, and the catalyst of paining on spring 33 has improved photocatalytic device 3's effective catalytic area simultaneously, has improved photocatalytic device 3's catalytic efficiency for VOCs is gaseous obtains abundant photodegradation and handles.
As shown in fig. 1, a pull rope 11 and a VOCs gas detector 12 are further arranged in the reaction chamber 1; the pull ropes 11 are divided into two groups, one group of pull ropes 11 is positioned on the right side of the catalytic ring 32, the right end of the catalytic ring 32 is connected with the inner wall of the reaction chamber 1 through the pull ropes 11, the other group of pull ropes 11 is positioned on the left side of the catalytic ring 32, the pull ropes 11 are connected with the left end of the catalytic ring 32, and the pull ropes 11 are used for fixing the catalytic ring 32 in the reaction chamber 1; the VOCs gas detector 12 is fixed at the bottom of the biodegradable layer 4, and the VOCs gas detector 12 is used for detecting the VOCs content of the gas entering the biodegradable layer 4; a hollow channel is arranged in the catalysis ring 32, a catalysis rod 34 is arranged in the hollow channel, and the catalysis rod 34 is used for changing the size of the catalysis ring 32; rectangular lugs are arranged at two ends of the catalytic rod 34 and are used for connecting the catalytic rod 34 and the catalytic ring 32 together; the reaction chamber 1 is also provided with a winder 13 outside, the winder 13 is connected with the pull rope 11 at the left end of the catalytic ring 32, and the winder 13 is used for winding the pull rope 11. During operation, the gaseous VOCs's that detects meter 12 detects the gaseous VOCs's that gets into biodegradable layer 4 content, thereby judge that whether biodegradable layer 4 and bio-filter layer 5 can detach the VOCs gas in the gas completely, when VOCs content is too high in the gas that gets into biodegradable layer 4, through 13 rolling stay cords of winder 11, make two semielliptical rings of stay cord 11 pulling catalysis ring 32, catalysis pole 34 constitutes not unidimensional catalysis ring 32 with two semielliptical rings under the effect of stay cord 11, catalytic ring 32's size regulation has been realized, catalytic area has been changed, realized handling VOCs gas's more efficient, the strict control has got into the gaseous VOCs's of biodegradable layer 4 content.
As shown in fig. 1, the catalytic light source 31 is further provided with a "figure-of-eight" through hole, the "figure-of-eight" through hole is located in the disc light source part of the catalytic light source 31, and the "figure-of-eight" through hole is used for reducing the ascending speed of the VOCs gas below the disc light source. During operation, the arrangement of the splayed holes increases the gas pressure on the upper parts of the splayed holes, so that the gas rises from the lower part of the disc light source of the catalytic light source 31 at a lower speed, the VOCs gas is degraded by photocatalysis more thoroughly, and the purification rate of the purification equipment is effectively improved.
The specific working process is as follows:
when the device works, VOCs gas is introduced into the elution pool 2 from the gas inlet pipeline 7 for oxidation treatment, so that the first layer treatment is realized, and the selective permeation characteristic of the semi-permeable membrane 72 enables the gas to enter the elution pool 2 and prevents liquid in the elution pool 2 from entering the gas inlet pipeline 7; the eluted gas enters a space between the elution pool 2 and the biodegradable layer 4, and the VOCs gas is subjected to photocatalytic treatment through the photocatalytic device 3 to realize second-layer treatment; the gas after photocatalysis enters a biodegradation layer 4 for carrying out microbial degradation treatment, so that the third layer treatment of VOCs gas is realized; the gas after degradation gets into biological filter layer 5 and carries out final absorption treatment to realize that the fourth layer is handled, handle through the four layers, make VOCs gaseous abundant purification treatment that obtains, purification efficiency is high, and the gas after the final purification passes through gas outlet 8 discharge reaction chamber 1.
In the process, the spray head 6 sprays nutrient solution to the biological filter layer 5 and the biological degradation layer 4, so that the number and activity of microorganisms in the biological filter layer 5 and the biological degradation layer 4 are ensured, and the microorganisms in the biological filter layer 5 and the biological degradation layer 4 are ensured to treat VOCs gas at high efficiency all the time; when the gas content in the space between the biodegradable layer 4 and the elution pool 2 is too much, the gas pushes the piston 93 in the feedback adjusting device 9 to move, the piston 93 extrudes the water in the liquid storage pipe 92, thereby the water in the extrusion ring 91 is extruded, the extrusion ring 91 extrudes the air inlet pipeline 7 finally, the air permeable block 71 in the air inlet pipeline 7 is contracted under the extrusion action of the extrusion ring 91, the air holes in the air permeable block 71 are contracted, the speed of the gas entering the reaction cavity 1 is slowed down, the gas content between the elution pool 2 and the biodegradable layer 4 is unchanged, the photocatalysis device 3 can perform sufficient photocatalysis treatment on the VOCs gas, meanwhile, the purification pressure is shared by the biodegradable layer 4 and the biological filter layer 5, and the VOCs gas is purified more completely. The catalytic light source 31 provides catalytic light for the catalytic ring 32, so that the VOCs gas generates a photocatalytic reaction on the catalytic ring 32, and the photocatalytic degradation of the VOCs gas is realized; the existence of the vertical light source and the disc light source of the catalytic light source 31 enables the catalytic ring 32 to be irradiated by sufficient catalytic light, so that the rate of photocatalytic degradation is improved; the two semi-elliptical rings of the catalytic ring 32 are connected together through the spring 33, and the catalyst coated on the spring 33 improves the effective catalytic area of the photocatalytic device 3, improves the catalytic efficiency of the photocatalytic device 3, and enables VOCs gas to be subjected to sufficient photodegradation treatment; the gaseous detector 12 of VOCs detects the content of the gaseous VOCs who gets into biodegradable layer 4, thereby judge whether biodegradable layer 4 can get rid of the VOCs gas in the gas completely with biological filter layer 5, when VOCs content is too high in the gas that gets into biodegradable layer 4, through 13 rolling stay cords of winder 11, make two semielliptical rings of 11 pulling catalysis rings 32 of stay cord, catalytic rod 34 constitutes unidimensional catalysis ring 32 with two semielliptical rings under the effect of stay cord 11, catalytic ring 32's size regulation has been realized, catalytic area has been changed, realized handling VOCs gas's more efficient, the strict control has got into the gaseous VOCs's of biodegradable layer 4 content. The setting in "eight" font hole on the catalysis light source 31 has increased the gas pressure on "eight" font hole upper portion for gaseous speed slows down when rising from the below of the disc light source of catalysis light source 31, makes VOCs gas more thorough by photocatalytic degradation, thereby effectual clarification plant's purification efficiency that has improved.
While one embodiment of the present invention has been described above, the present invention is not limited to the above embodiment, and various modifications can be made without departing from the scope of the present invention.
(A) In the above embodiment, the water is added into the liquid storage pipe and the extrusion ring to drive the piston to extrude the water in the liquid storage pipe and the extrusion ring to enter the air inlet pipeline, but the invention is not limited thereto, and other liquid or gas can be added to realize the function.
(B) In the above embodiments, the catalytic ring has an elliptical structure, but is not limited thereto, and the catalytic ring may have other shapes.
Industrial applicability
According to the invention, the photocatalysis and biological bed combined type VOCs purification equipment can successfully purify VOCs gas in waste gas, so that the photocatalysis and biological bed combined type VOCs purification equipment is useful in the technical field of waste gas purification.
Claims (1)
1. A photocatalysis and biological bed combined VOCs purifying device comprises a reaction chamber (1), an elution pool (2), a photocatalysis device (3), a biodegradation layer (4), a biological filter layer (5), a spray head (6), an air inlet pipeline (7), an air outlet (8) and a feedback adjusting device (9); the elution pool (2) is positioned in the reaction cavity (1), the elution pool (2) is positioned at the bottom of the reaction cavity (1), and the elution pool (2) is used for carrying out oxidation treatment on VOCs gas; the photocatalytic device (3) is positioned in the reaction chamber (1), the photocatalytic device (3) is positioned above the elution pool (2), and the photocatalytic device (3) is used for catalyzing VOCs gas; the biodegradable layer (4) is positioned in the reaction cavity (1), and the biodegradable layer (4) is used for biodegrading VOCs gas; the biological filter layer (5) is positioned in the reaction cavity (1), and the biological filter layer (5) is used for carrying out final absorption treatment on VOCs gas; the spray heads (6) are positioned in the reaction cavity (1), the spray heads (6) are divided into two groups, one group of spray heads (6) is positioned between the biological degradation layer (4) and the biological filtration layer (5), the other group of spray heads (6) is positioned above the biological filtration layer (5), and the spray heads (6) are used for adding nutrient solution to the biological filtration layer (5) and the biological degradation layer (4); the gas inlet pipeline (7) is positioned below the elution pool (2), and the gas inlet pipeline (7) is used for injecting VOCs gas into the elution pool (2); the gas outlet (8) is positioned at the upper part of the reaction cavity (1), and the gas outlet (8) is used for discharging the purified gas out of the reaction cavity (1); the method is characterized in that: the feedback adjusting device (9) comprises a squeezing ring (91), a liquid storage pipe (92) and a piston (93); the extrusion ring (91) is positioned outside the air inlet pipeline (7), a cavity is arranged in the extrusion ring (91), water is filled in the cavity, and the extrusion ring (91) is used for extruding the air inlet pipeline (7); one end of the liquid storage pipe (92) is connected with the reaction cavity (1), the other end of the liquid storage pipe (92) is connected with the extrusion ring (91), water is stored in the liquid storage pipe (92), and the liquid storage pipe (92) is used for injecting water into the extrusion ring (91); the piston (93) is positioned in the liquid storage pipe (92), and the piston (93) is used for extruding water in the liquid storage pipe (92);
a ventilation block (71) is arranged in the air inlet pipeline (7), the ventilation block (71) is of a cylindrical structure, the ventilation block (71) is fixed in the air inlet pipeline, ventilation holes are formed in the ventilation block (71), and the ventilation block (71) is used for changing the size of air flow;
the gas inlet pipeline (7) is provided with a semi-permeable membrane (72), the semi-permeable membrane (72) is positioned at the communication position of the gas inlet pipeline (7) and the elution pool (2), the semi-permeable membrane (72) is used for enabling VOCs gas to enter the elution pool (2), and the semi-permeable membrane (72) is used for preventing eluent from flowing into the gas inlet pipeline (7);
the photocatalytic device (3) comprises a catalytic light source (31) and a catalytic ring (32); the catalytic light source (31) is obtained by combining a vertical light source and a plurality of disc light sources, the top end of the catalytic light source (31) is fixed at the bottom of the biodegradable layer (4), and the catalytic light source (31) is used for providing illumination required by catalysis; the catalytic rings (32) and the disc light sources of the catalytic light sources (31) are alternately arranged, the number of the catalytic rings (32) is one less than that of the disc light sources, and the catalytic rings (32) are used for bearing catalysts;
the catalytic ring (32) consists of two semi-elliptical rings, the two semi-elliptical rings are connected together through a spring (33), and the spring (33) is coated with a catalyst;
a pull rope (11) and a VOCs gas detector (12) are also arranged in the reaction cavity (1); the pull ropes (11) are divided into two groups, one group of pull ropes (11) is positioned on the right side of the catalytic ring (32), the right end of the catalytic ring (32) is connected with the inner wall of the reaction cavity (1) through the pull ropes (11), the other group of pull ropes (11) is positioned on the left side of the catalytic ring (32), the pull ropes (11) are connected with the left end of the catalytic ring (32), and the pull ropes (11) are used for fixing the catalytic ring (32) in the reaction cavity (1); the VOCs gas detector (12) is fixed at the bottom of the biodegradable layer (4), and the VOCs gas detector (12) is used for detecting the VOCs content of gas entering the biodegradable layer (4); a hollow channel is arranged in the catalysis ring (32), a catalysis rod (34) is arranged in the hollow channel, and the catalysis rod (34) is used for changing the size of the catalysis ring (32); rectangular lugs are arranged at two ends of the catalytic rod (34) and are used for connecting the catalytic rod (34) and the catalytic ring (32) together; a winder (13) is further arranged outside the reaction cavity (1), the winder (13) is connected with the pull rope (11) at the left end of the catalytic ring (32), and the winder (13) is used for winding the pull rope (11);
the catalytic light source (31) is also provided with a splayed through hole, the splayed through hole is positioned at the disc light source part of the catalytic light source (31), and the splayed through hole is used for reducing the ascending speed of VOCs gas below the disc light source;
when the gas content in the space between the biodegradable layer (4) and the elution tank (2) is excessive, the gas pushes a piston (93) in the feedback adjusting device (9) to move, the piston (93) extrudes the water in the liquid storage pipe (92), so that the water in the extrusion ring (91) is extruded, finally the extrusion ring (91) extrudes the air inlet pipeline (7), the air permeable block (71) in the air inlet pipeline (7) shrinks under the extrusion action of the extrusion ring (91), so that the air holes on the air permeable block (71) are contracted, the speed of the air entering the reaction cavity (1) is slowed down, so that the gas content between the elution pool (2) and the biodegradable layer (4) is not changed, so that the photocatalysis device (3) can carry out sufficient photocatalysis treatment on the VOCs gas, meanwhile, the purification pressure is shared by the biodegradable layer (4) and the biological filter layer (5), so that the VOCs gas is purified more completely.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US20020096479A1 (en) * | 2000-06-02 | 2002-07-25 | Butters Brian E. | System and method for photocatalytic treatment of contaminated media |
| US7651555B2 (en) * | 2005-08-17 | 2010-01-26 | Roseberry Jeffrey L | Onsite chemistry air filtration system |
| CN101099937A (en) * | 2006-07-06 | 2008-01-09 | 杨小明 | Thin-plate composite type optical catalyst carrier structure |
| CN101096014B (en) * | 2006-06-27 | 2011-01-05 | 杨小明 | Thin plate combined type photocatalyst carrier structure |
| CN103599684A (en) * | 2013-11-14 | 2014-02-26 | 深圳市利源水务设计咨询有限公司 | Photocatalysis oxidization and biological degradation deodorizing device and deodorizing process |
| CN204852487U (en) * | 2015-06-29 | 2015-12-09 | 温州市慧能机械科技有限公司 | Hose flow control valve |
| CN105396444B (en) * | 2015-12-16 | 2017-12-22 | 永康市禄祥环保科技有限公司 | Utilize ozone catalytic and the processing unit of biological oxidation VOC waste gas |
| CN206240298U (en) * | 2016-04-29 | 2017-06-13 | 广东工业大学 | A kind of odor removal |
| CN105833687B (en) * | 2016-04-29 | 2018-09-07 | 广东工业大学 | A kind of deodorization device |
| CN105817137B (en) * | 2016-05-16 | 2018-06-15 | 东莞市环境科学研究所 | A kind of compound bio bed cleaning equipment of VOCs |
| CN206682355U (en) * | 2017-04-11 | 2017-11-28 | 上海欧特莱阀门机械有限公司 | A kind of gas flow regulating valve and its pipeline |
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