CN220715317U - Dehumidification and ethanol recovery VOCS (volatile organic Compounds) purification zero emission system - Google Patents
Dehumidification and ethanol recovery VOCS (volatile organic Compounds) purification zero emission system Download PDFInfo
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- CN220715317U CN220715317U CN202322467303.1U CN202322467303U CN220715317U CN 220715317 U CN220715317 U CN 220715317U CN 202322467303 U CN202322467303 U CN 202322467303U CN 220715317 U CN220715317 U CN 220715317U
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- China
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- dehumidification
- pipe
- treatment cylinder
- fixedly arranged
- ethanol recovery
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 48
- 238000007791 dehumidification Methods 0.000 title claims description 32
- 238000011084 recovery Methods 0.000 title claims description 13
- 238000000746 purification Methods 0.000 title claims description 9
- 239000012855 volatile organic compound Substances 0.000 title description 13
- 239000012535 impurity Substances 0.000 claims abstract description 35
- 239000000463 material Substances 0.000 claims description 14
- 238000007599 discharging Methods 0.000 claims description 10
- 238000007790 scraping Methods 0.000 claims description 10
- 238000003756 stirring Methods 0.000 claims description 10
- 239000002893 slag Substances 0.000 claims description 9
- 238000007789 sealing Methods 0.000 claims description 8
- 238000013016 damping Methods 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims 8
- 235000017491 Bambusa tulda Nutrition 0.000 claims 8
- 241001330002 Bambuseae Species 0.000 claims 8
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims 8
- 239000011425 bamboo Substances 0.000 claims 8
- 238000004064 recycling Methods 0.000 abstract description 3
- 239000002912 waste gas Substances 0.000 abstract description 3
- 238000010521 absorption reaction Methods 0.000 description 12
- 230000000694 effects Effects 0.000 description 6
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 5
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
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- Drying Of Gases (AREA)
Abstract
The utility model discloses a dehumidifying and ethanol recycling VOCS purifying zero-emission system, which belongs to the technical field of waste gas treatment and comprises a treatment cylinder, wherein an air inlet pipe is fixedly arranged on one side of the treatment cylinder, an impurity filter plate is fixedly arranged in the treatment cylinder and positioned above the air inlet pipe, a dehumidifying component is fixedly arranged in the middle position of the interior of the treatment cylinder, a guide plate is fixedly arranged in the treatment cylinder and positioned above the dehumidifying component, a flow outlet pipe is fixedly arranged on one side of the treatment cylinder, a snake-shaped condensing pipe is fixedly arranged above the interior of the treatment cylinder, and an exhaust pipe is fixedly arranged at the upper end of the treatment cylinder.
Description
Technical Field
The utility model relates to a dehumidifying and ethanol recycling VOCS purifying zero-emission system, and belongs to the technical field of waste gas treatment.
Background
VOCS refers to volatile organic compounds, which are important precursors for forming secondary pollutants such as fine particles and ozone, and further cause the problems of dust haze, photochemical smog and other atmospheric environments. With the rapid development of industrialization and urban industry in China and the continuous growth of energy consumption, regional composite type air pollution featuring fine particles and ozone is increasingly prominent, the occurrence frequency of air heavy pollution phenomena in the region is increased, sustainable development of society and economy is seriously restricted, physical health of people is threatened, volatile organic matters can be generated in industrial production, the volatile organic matters are discharged after being treated, however, the traditional treatment system cannot systematically remove impurities, dehumidify and recycle ethanol when in use, the treatment needs to be transferred, the use is inconvenient, and meanwhile, the efficiency when dehumidification is carried out is low, and the efficiency of integral treatment is affected.
Disclosure of Invention
The utility model aims to solve the problems and provide a zero emission system for purifying VOCS (volatile organic Compounds) by dehumidification and ethanol recovery, which can finish impurity removal, dehumidification and ethanol recovery in the same treatment cylinder, is not required to be transferred during treatment, is convenient for a user to use, can scrape impurities from an impurity filter plate through an arc-shaped scraping plate during impurity removal, avoids blocking the impurity filter plate, and can stir a hygroscopic ball during dehumidification, thereby improving the hygroscopic efficiency.
The utility model realizes the aim through the following technical scheme that the VOCS purifying zero-emission system comprises a treatment cylinder, wherein an air inlet pipe is fixedly arranged on one side of the treatment cylinder, an impurity filter plate is fixedly arranged in the treatment cylinder, the impurity filter plate is positioned above the air inlet pipe, a dehumidifying component is fixedly arranged in the middle of the inside of the treatment cylinder, a guide plate is fixedly arranged in the treatment cylinder, the guide plate is positioned above the dehumidifying component, a flow outlet pipe is fixedly arranged on one side of the treatment cylinder, a snake-shaped condensing pipe is fixedly arranged above the inside of the treatment cylinder, an exhaust pipe is fixedly arranged at the upper end of the treatment cylinder, when the treatment cylinder is used, firstly, a moisture absorption ball is put into the dehumidifying component, then volatile organic matters are led into the treatment cylinder through the air inlet pipe, and then are filtered by the impurity filter plate, the moisture in the volatile organic matters are absorbed by the moisture absorption ball, the moisture absorption purpose of the volatile organic matters is achieved, meanwhile, the snake-shaped condensing pipe is communicated with an external air cooling device, when the volatile organic matters are contacted with the dehumidifying component, the snake-shaped condensing pipe is discharged out of the ethanol after the volatile organic matters are discharged through the exhaust pipe, and the ethanol is completely discharged out of the treatment cylinder after the ethanol is treated.
Preferably, in order to place the utility model at a use place, supporting feet are uniformly and fixedly arranged at the lower end of the outer part of the treatment cylinder, and damping rubber pads are fixedly arranged at the lower ends of the supporting feet.
Preferably, in order to drive the rotating shaft to rotate, a control motor is fixedly arranged at the lower end of the outer part of the treatment cylinder, a rotating shaft is fixedly arranged at the output end of the control motor, and one end of the rotating shaft extends to the interior of the dehumidification assembly.
Preferably, in order to scrape the impurity on the impurity filter, prevent the condition of jam, fixed mounting has the arc scraper blade in the pivot, the up end of arc scraper blade with the lower terminal surface of impurity filter contacts, just the upper end fixed mounting of pivot has the puddler, the puddler is located in the dehumidification subassembly.
Preferably, in order to facilitate the discharge of impurities, a slag discharging pipe is fixedly installed on one side of the outer portion of the treatment cylinder, the inner lower end face of the slag discharging pipe and the inner lower end face of the treatment cylinder are on the same horizontal plane, and a first sealing cover is installed at one end of the slag discharging pipe.
Preferably, in order to absorb moisture in the volatile organic compounds, the dehumidifying assembly comprises an upper dehumidifying filter plate and a lower dehumidifying filter plate, and the upper dehumidifying filter plate and the lower dehumidifying filter plate are fixedly installed inside the treatment cylinder.
Preferably, in order to facilitate replacement of the moisture absorption balls, a material exchange tube is fixedly mounted on one side of the outer portion of the treatment cylinder, the inner lower end face of the material exchange tube and the upper end face of the lower dehumidification filter plate are on the same horizontal plane, and a second sealing cover is mounted on the other end of the material exchange tube.
Preferably, in order to discharge the discharged waste gas, a cylinder cover is mounted at the upper end of the treatment cylinder, the exhaust pipe is fixedly mounted on the cylinder cover, and an air valve is fixedly mounted on the exhaust pipe.
The beneficial effects of the utility model are as follows: the impurity removal, dehumidification and ethanol recovery can be completed in the same treatment cylinder, the use of a user is facilitated without transferring during treatment, impurities can be scraped from the impurity removal filter plate through the arc-shaped scraping plate during impurity removal, blockage of the impurity removal filter plate is avoided, the hygroscopic balls can be stirred during dehumidification, and the hygroscopic efficiency is improved.
Drawings
Fig. 1 is a schematic diagram of the overall structure of the present utility model.
Fig. 2 is a half cross-sectional view of the overall structure of the present utility model.
FIG. 3 is a schematic diagram illustrating the connection relationship of the rotating shafts according to the present utility model.
Fig. 4 is an enlarged view of the present utility model at a in fig. 2.
In the figure: 1. a treatment cylinder; 2. an air inlet pipe; 3. an impurity filter plate; 4. a dehumidifying component; 401. a top dehumidifying filter plate; 402. a lower dehumidifying filter plate; 5. a deflector; 6. a outflow pipe; 7. a serpentine condenser tube; 8. an exhaust pipe; 9. supporting feet; 10. a damping rubber pad; 11. controlling a motor; 12. a rotating shaft; 13. an arc-shaped scraping plate; 14. a stirring rod; 15. a slag discharge pipe; 16. a first sealing cover; 17. exchanging a material pipe; 18. a second sealing cover; 19. a cylinder cover; 20. and an air valve.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1-4, a zero emission system for purifying and recovering VOCS from ethanol comprises a treatment cylinder 1, wherein an air inlet pipe 2 is fixedly arranged at one side of the treatment cylinder 1, an impurity filter plate 3 is fixedly arranged in the treatment cylinder 1, the impurity filter plate 3 is positioned above the air inlet pipe 2, a dehumidification assembly 4 is fixedly arranged in the middle of the interior of the treatment cylinder 1, a guide plate 5 is fixedly arranged in the interior of the treatment cylinder 1, the guide plate 5 is positioned above the dehumidification assembly 4, an outlet pipe 6 is fixedly arranged at one side of the treatment cylinder 1, a serpentine condenser pipe 7 is fixedly arranged above the interior of the treatment cylinder 1, an exhaust pipe 8 is fixedly arranged at the upper end of the treatment cylinder 1, in use, firstly, a moisture absorption ball is put into the dehumidification assembly 4, then volatile organic matters are led into the treatment cylinder 1 through the air inlet pipe 2, the impurity filter plate 3 is filtered and then enter the dehumidification assembly 4, the moisture in the volatile organic matters is absorbed by the moisture absorption ball, the moisture absorption purpose of the volatile organic matters is achieved, the serpentine condenser pipe 7 is communicated with an external air conditioner, when the volatile organic matters are contacted with the condenser pipe 7, an exhaust pipe 6 is fixedly arranged at one side of the upper side of the treatment cylinder 1, an exhaust pipe 8 is fixedly arranged at the upper side of the interior of the treatment cylinder, an exhaust pipe 8 is discharged through the guide pipe 6, and then the exhaust pipe 8 is discharged after the ethanol is processed.
As shown in fig. 3, the supporting feet 9 are uniformly and fixedly installed at the lower end of the outer part of the treatment cylinder 1, the damping rubber pad 10 is fixedly installed at the lower end of the supporting feet 9, the control motor 11 is fixedly installed at the lower end of the outer part of the treatment cylinder 1, the rotating shaft 12 is fixedly installed at the output end of the control motor 11, one end of the rotating shaft 12 extends to the inside of the dehumidifying component 4, the arc-shaped scraping plate 13 is fixedly installed on the rotating shaft 12, the upper end face of the arc-shaped scraping plate 13 is contacted with the lower end face of the impurity filtering plate 3, the deslagging pipe 15 is fixedly installed at one side of the outer part of the treatment cylinder 1, the inner lower end face of the deslagging pipe 15 is on the same horizontal plane with the inner lower end face of the treatment cylinder 1, the first sealing cover 16 is installed at one end of the deslagging pipe 15, when in use, the utility model is firstly placed at a use place through the supporting feet 9, then the moisture absorbing balls are placed into the dehumidifying component 4 through the material exchanging pipe 17, then volatile organic matters enter the treatment cylinder 1 through the air inlet pipe 2, enter the dehumidifying component 4 after being filtered by the impurity 3, in the process, the control motor 11 is turned on, the control motor 11 is driven to rotate the rotating shaft 12, so that the arc-shaped scraping plate 13 can drive the rotating shaft to rotate, and the lower end of the scraping plate 3 to be on the same level, and the impurity can be prevented from being blocked by the impurity.
As shown in fig. 3, the dehumidifying assembly 4 includes an upper dehumidifying filter plate 401 and a lower dehumidifying filter plate 402, the upper dehumidifying filter plate 401 and the lower dehumidifying filter plate 402 are fixedly installed inside the processing cylinder 1, a stirring rod 14 is fixedly installed at the upper end of the rotating shaft 12, the stirring rod 14 is located in the dehumidifying assembly 4, a material exchanging pipe 17 is fixedly installed at one side of the outer part of the processing cylinder 1, the lower inner end face of the material exchanging pipe 17 and the upper end face of the lower dehumidifying filter plate 402 are located on the same horizontal plane, a second sealing cover 18 is installed at the other end of the material exchanging pipe 17, when the dehumidifying assembly is used, moisture in volatile organic compounds is absorbed by the moisture absorbing balls, the dehumidifying effect is achieved, meanwhile, the stirring rod 14 can stir the moisture absorbing balls, so that the dehumidifying effect can be improved, when the moisture absorbing balls are needed to be replaced, and then the unused moisture absorbing balls are replaced through the material exchanging pipe 17.
As shown in fig. 2, a deflector 5 is fixedly installed inside the treatment canister 1, the deflector 5 is located above the dehumidification assembly 4, a flow outlet pipe 6 is fixedly installed on one side of the treatment canister 1, a canister cover 19 is installed at the upper end of the treatment canister 1, an exhaust pipe 8 is fixedly installed on the canister cover 19, an air valve 20 is fixedly installed on the exhaust pipe 8, when the serpentine condenser 7 is encountered by volatile organic matters in use, the volatile organic matters in the volatile organic matters are condensed and then fall onto the deflector 5, and then are discharged through the flow outlet pipe 6, so that the effect of recovering the ethanol is achieved, and then the volatile organic matters after treatment are discharged through the exhaust pipe 8.
When the utility model is used, firstly, the utility model is placed at a use place through the supporting legs 9, then the moisture absorption balls are placed into the dehumidifying component 4 through the material exchanging pipe 17, then volatile organic matters enter the processing cylinder 1 through the air inlet pipe 2, are filtered by the impurity filtering plate 3 and enter the dehumidifying component 4, in the impurity removing process, the control motor 11 is opened, the control motor 11 drives the rotating shaft 12 to rotate, thereby the arc scraping plate 13 can be driven to scrape impurities at the lower end of the impurity filtering plate 3, the blocking condition is avoided, impurities can be discharged through the slag discharging pipe 15, the moisture absorption balls absorb moisture in the volatile organic matters to achieve the dehumidifying effect, meanwhile, the stirring rod 14 can stir the moisture absorption balls, thereby improving the dehumidifying effect, when the volatile organic matters need to be replaced, the moisture absorption balls which are used are taken out through the material exchanging pipe 17, then the unused moisture absorption balls are replaced, when the volatile organic matters meet the serpentine condensing pipe 7, the ethanol in the volatile organic matters are condensed and then fall onto the flow guiding plate 5, then are discharged through the discharging pipe 6, thereby achieving the ethanol recycling effect, and then the volatile organic matters which are processed through the discharging pipe 8.
It will be evident to those skilled in the art that the utility model is not limited to the details of the foregoing illustrative embodiments, and that the present utility model may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The present embodiments are, therefore, to be considered in all respects as illustrative and not restrictive, the scope of the utility model being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present disclosure describes embodiments, not every embodiment is provided with a separate embodiment, and that this description is provided for clarity only, and that the disclosure is not limited to the embodiments described in detail below, and that the embodiments described in the examples may be combined as appropriate to form other embodiments that will be apparent to those skilled in the art.
Claims (8)
1. The utility model provides a dehumidification and ethanol recovery VOCS purification zero release system which characterized in that: including handling section of thick bamboo (1), one side fixed mounting of handling section of thick bamboo (1) has intake pipe (2), the inside fixed impurity filter (3) that is equipped with of handling section of thick bamboo (1), impurity filter (3) are located the top of intake pipe (2), the inside intermediate position fixed mounting of handling section of thick bamboo (1) has dehumidification subassembly (4), the inside fixed mounting of handling section of thick bamboo (1) has guide plate (5), guide plate (5) are located the top of dehumidification subassembly (4), one side fixed mounting of handling section of thick bamboo (1) has outlet pipe (6), the inside top fixed mounting of handling section of thick bamboo (1) has snakelike condenser pipe (7), the upper end fixed mounting of handling section of thick bamboo (1) has blast pipe (8).
2. The zero emission dehumidification and ethanol recovery VOCS purification system of claim 1, wherein: the outer lower end of the treatment cylinder (1) is uniformly and fixedly provided with supporting feet (9), and the lower end of the supporting feet (9) is fixedly provided with damping rubber pads (10).
3. The zero emission dehumidification and ethanol recovery VOCS purification system of claim 1, wherein: the control motor (11) is fixedly arranged at the lower end of the outer part of the treatment cylinder (1), the rotating shaft (12) is fixedly arranged at the output end of the control motor (11), and one end of the rotating shaft (12) extends to the inner part of the dehumidification component (4).
4. A dehumidification and ethanol recovery VOCS clean zero release system according to claim 3, wherein: an arc scraping plate (13) is fixedly installed on the rotating shaft (12), the upper end face of the arc scraping plate (13) is in contact with the lower end face of the impurity filtering plate (3), a stirring rod (14) is fixedly installed at the upper end of the rotating shaft (12), and the stirring rod (14) is located in the dehumidifying component (4).
5. The zero emission dehumidification and ethanol recovery VOCS purification system of claim 1, wherein: the slag discharging device is characterized in that a slag discharging pipe (15) is fixedly arranged on one side of the outer portion of the treatment cylinder (1), the inner lower end face of the slag discharging pipe (15) and the inner lower end face of the treatment cylinder (1) are arranged on the same horizontal plane, and a first sealing cover (16) is arranged at one end of the slag discharging pipe (15).
6. The zero emission dehumidification and ethanol recovery VOCS purification system of claim 1, wherein: the dehumidification assembly (4) comprises an upper dehumidification filter plate (401) and a lower dehumidification filter plate (402), and the upper dehumidification filter plate (401) and the lower dehumidification filter plate (402) are fixedly installed inside the treatment cylinder (1).
7. The zero emission dehumidification and ethanol recovery VOCS purification system of claim 6, wherein: the novel wet-removing device is characterized in that a material changing pipe (17) is fixedly arranged on one side of the outer part of the treatment cylinder (1), the lower end face of the inner part of the material changing pipe (17) and the upper end face of the lower dehumidifying filter plate (402) are arranged on the same horizontal plane, and a second sealing cover (18) is arranged at the other end of the material changing pipe (17).
8. The zero emission dehumidification and ethanol recovery VOCS purification system of claim 1, wherein: the upper end of the treatment cylinder (1) is provided with a cylinder cover (19), the exhaust pipe (8) is fixedly arranged on the cylinder cover (19), and the exhaust pipe (8) is fixedly provided with an air valve (20).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322467303.1U CN220715317U (en) | 2023-09-12 | 2023-09-12 | Dehumidification and ethanol recovery VOCS (volatile organic Compounds) purification zero emission system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322467303.1U CN220715317U (en) | 2023-09-12 | 2023-09-12 | Dehumidification and ethanol recovery VOCS (volatile organic Compounds) purification zero emission system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220715317U true CN220715317U (en) | 2024-04-05 |
Family
ID=90486941
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322467303.1U Active CN220715317U (en) | 2023-09-12 | 2023-09-12 | Dehumidification and ethanol recovery VOCS (volatile organic Compounds) purification zero emission system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220715317U (en) |
-
2023
- 2023-09-12 CN CN202322467303.1U patent/CN220715317U/en active Active
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