CN220609755U - Runner concentration system degree of depth regenerating unit - Google Patents
Runner concentration system degree of depth regenerating unit Download PDFInfo
- Publication number
- CN220609755U CN220609755U CN202321991910.1U CN202321991910U CN220609755U CN 220609755 U CN220609755 U CN 220609755U CN 202321991910 U CN202321991910 U CN 202321991910U CN 220609755 U CN220609755 U CN 220609755U
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- Prior art keywords
- pipeline
- rotating wheel
- runner
- steam
- zone
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- 230000001172 regenerating effect Effects 0.000 title claims description 4
- 230000008929 regeneration Effects 0.000 claims abstract description 30
- 238000011069 regeneration method Methods 0.000 claims abstract description 30
- 238000001179 sorption measurement Methods 0.000 claims abstract description 23
- 238000003795 desorption Methods 0.000 claims abstract description 19
- 238000007789 sealing Methods 0.000 claims abstract description 8
- 239000007779 soft material Substances 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims description 8
- 239000002808 molecular sieve Substances 0.000 claims description 8
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 7
- 238000009434 installation Methods 0.000 claims description 5
- 238000010030 laminating Methods 0.000 claims description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000005192 partition Methods 0.000 claims 3
- 239000007921 spray Substances 0.000 claims 3
- 239000007789 gas Substances 0.000 description 6
- 239000002912 waste gas Substances 0.000 description 5
- 239000010815 organic waste Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The utility model discloses a deep regeneration device of a rotating wheel concentration system, which comprises a first pipeline, a filtering device, a second pipeline, a rotating wheel device, a heating reactor, an adsorption fan, a steam pipeline and a desorption fan, wherein the first pipeline is provided with an air inlet, the surface of the first pipeline is connected with the filtering device, the first pipeline is connected with the rotating wheel device through soft materials in a bonding and sealing contact manner, one end of the first pipeline is connected with the adsorption fan, a through groove is formed in the surface of the first pipeline, the second pipeline is connected with the rotating wheel device through soft materials in a bonding and sealing contact manner in a position corresponding to the through groove, the second pipeline is connected with the heating reactor, the through groove is formed in the surface of the second pipeline, the steam pipeline is connected with the corresponding position of the through groove, a valve is arranged in the corresponding position of the steam pipeline, one end of the second pipeline is connected with the desorption fan, and the desorption fan is uniformly distributed in a regeneration zone through a steam nozzle for high-temperature desorption, and the adsorption efficiency of the concentrating rotating wheel is effectively improved.
Description
Technical Field
The utility model relates to a regeneration device, in particular to a deep regeneration device of a rotating wheel concentration system.
Background
The molecular sieve is an adsorbent or film substance which is provided with uniform micropores and mainly consists of silicon, aluminum, oxygen and other metal cations, the aperture of the molecular sieve is equivalent to the size of a common molecule, and the molecular sieve concentration rotating wheel for sieving various fluids according to the effective aperture of the molecular sieve is characterized in that the special aperture of the molecular sieve is utilized to have adsorption and desorption capability on organic pollutants, so that the original VOCs waste gas with lower concentration and large air quantity is converted into gas with small air quantity and high concentration through rotating wheel concentration, and the running cost of back-end terminal treatment equipment can be reduced. The device characteristics are suitable for treating waste gas with large flow, low concentration and multiple organic components. However, the concentration runner is subjected to long-time online desorption, and the problem that desorption is incomplete or desorption performance is reduced due to the fact that high-boiling-point substances generated by polymerization are accumulated in the runner.
Disclosure of Invention
The utility model aims to provide a deep regeneration device of a rotating wheel concentration system, which aims to solve the problems in the background technology.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
the utility model provides a runner concentration system degree of depth regenerating unit, including first pipeline, filter equipment, the second pipeline, the runner device, add the thermal reactor, adsorb the fan, steam conduit, the desorption fan, open the air inlet in first pipeline, the surface mounting of first pipeline is connected with filter equipment, and first pipeline and runner device pass through soft material laminating sealing contact and are connected, and the one end installation of first pipeline is connected with the adsorption fan, and the logical groove has been seted up on the surface of first pipeline, and correspond the position with logical groove and install and be connected with the second pipeline, and the second pipeline corresponds and be connected with runner device position and through soft material laminating sealing contact, the second pipeline is connected with add the thermal reactor, and logical groove has been seted up on the second pipeline surface, and logical groove corresponds the position and insert steam conduit, and the valve is installed to steam conduit corresponds the position, the one end installation of second pipeline is connected with the desorption fan.
As a further scheme of the utility model: the filter equipment includes coarse strainer, thin filter screen, dry layer, device main part, and coarse strainer, thin filter screen and dry layer are once installed to the internal surface of device main part, through the design of this structure, can filter the tiny granule of abandonment, and can carry out drying treatment to moisture through the dry layer.
As a further scheme of the utility model: the runner device includes adsorption zone, cooling zone, regeneration zone, vapor nozzle, runner main part, baffle, and the baffle has been seted up to the internal surface of runner main part, and runner main part internally mounted has the molecular sieve, and divide into adsorption zone, cooling zone and regeneration zone through the baffle, and regeneration zone corresponds the position, and the surface mounting of runner main part is connected with vapor nozzle, and vapor nozzle material model is stainless steel 304, and runner device is rotated by rotation motor control.
Compared with the prior art, the utility model has the beneficial effects that:
compared with the existing regeneration device on the market, the deep regeneration device of the rotating wheel concentration system is characterized in that a steam pipeline is arranged between a regeneration zone and a heating reactor, steam is introduced in an off-line mode regularly, the steam is conveyed to a steam nozzle of the regeneration zone, the steam nozzle is used for uniformly spraying, high-temperature desorption of the regeneration zone is achieved, the rotating wheel recovers the original adsorption capacity of the rotating wheel, the steam pipeline is introduced before the waste gas enters the regeneration zone for being sprayed in the regeneration zone in a regular off-line mode, the high-temperature desorption is carried out, and the adsorption efficiency of the concentrated rotating wheel is effectively improved.
Drawings
FIG. 1 is a schematic diagram of a deep regeneration device of a rotor concentrating system.
Fig. 2 is a schematic structural diagram of a runner apparatus in a deep regeneration apparatus of a runner concentration system.
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. 1-2, in an embodiment of the present utility model, a deep regeneration device of a rotating wheel concentration system includes a first pipeline 14, a filtering device 16, a second pipeline 15, a rotating wheel device 9, a heating reactor 10, an adsorption fan 11, a steam pipeline 12, and a desorption fan 13.
The air inlet 5 is arranged on the first pipeline 14, the filtering device 16 is connected to the surface of the first pipeline 14, the first pipeline 14 is connected with the rotating wheel device 9 through soft material fitting sealing contact, the adsorption fan 11 is arranged at one end of the first pipeline 14, the through groove is arranged on the surface of the first pipeline 14, the second pipeline 15 is connected with the rotating wheel device 9 through soft material fitting sealing contact, the second pipeline 15 is connected with the heating reactor 10, the through groove is arranged on the surface of the second pipeline 15, the steam pipeline 12 is connected to the corresponding position of the through groove, the valve is arranged at the corresponding position of the steam pipeline 12, and the desorption fan 13 is arranged at one end of the second pipeline 15.
The filter device 16 comprises a coarse screen 6, a fine screen 7, a drying layer 8 and a device main body 17, wherein the coarse screen 6, the fine screen 7 and the drying layer 8 are arranged on the inner surface of the device main body 17 at one time, and through the design of the structure, waste fine particles can be filtered, and moisture can be dried through the drying layer 8.
The runner device 9 includes adsorption zone 1, cooling zone 2, regeneration zone 3, vapor nozzle 4, runner main part 18, baffle 19, and baffle 19 has been seted up to the internal surface of runner main part 18, and runner main part 18 internally mounted has the molecular sieve, and is divided into adsorption zone 1, cooling zone 2 and regeneration zone 3 through baffle 19, and regeneration zone 3 corresponds the position, and the surface mounting of runner main part 18 is connected with vapor nozzle 4, and vapor nozzle 4 material model is stainless steel 304, and runner device 9 is rotated by rotation motor control.
The working principle of the utility model is as follows: organic waste gas gets into inside first pipeline 14 through air inlet 5, firstly get rid of the tiny granule of waste gas through coarse strainer 6 and thin filter screen 7, make organic waste gas satisfy runner device 9 absorptive cleanliness requirement, dry layer 8 carries out the drying to the moisture in the organic waste gas, through the effect of adsorption fan 11, the organic waste gas that will be through preliminary treatment passes through the adsorption zone 1 of concentrated runner, after the organic matter molecule is adsorbed the treatment, the gas that adsorbs up to standard directly is discharged into the chimney, after a period of adsorption, adsorption zone 1 can adsorb saturation, then the runner is transferred to regeneration zone 3, at this moment, the cooling wind through second pipeline 15 through cooling zone 2 is passed through and is heated the ware 10 and let in regeneration zone 3, desorb the part that adsorbs saturation, high concentration waste gas after the desorption is introduced into subsequent processing apparatus through regeneration fan 13, because runner device 9 carries out high temperature desorption for a long time on line, can exist and lead to the desorption to the condition of not thoroughly because of containing polymer or high boiling point material, lead to the adsorption performance to the fact to be reduced to some extent, need regularly introduce steam pipe 12, carry steam to regeneration zone 3's vapor shower nozzle 4, make full use of the high-temperature, the steam separation, the high-cycle system is realized at this moment, the high temperature, the recovery of the adsorption system is realized, the recovery of the steam, the system is recovered, the recovery of the steam, the system is recovered, and the system is recovered.
Although the present utility model has been described with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described, or equivalents may be substituted for elements thereof, and any modifications, equivalents, improvements and changes may be made without departing from the spirit and principles of the present utility model.
Claims (3)
1. The utility model provides a runner concentration system degree of depth regenerating unit, including first pipeline (14), filter equipment (16), second pipeline (15), runner device (9), heating reactor (10), adsorption fan (11), steam pipe (12), desorption fan (13), a serial communication port, first pipeline (14) are opened there is air inlet (5), the surface mounting of first pipeline (14) is connected with filter equipment (16), and first pipeline (14) are connected through soft material laminating sealing contact with runner device (9), and the one end installation of first pipeline (14) is connected with adsorption fan (11), and logical groove has been seted up on the surface of first pipeline (14), and be connected with second pipeline (15) with logical groove corresponding position installation, and second pipeline (15) correspond and through soft material laminating sealing contact connection with runner device (9), second pipeline (15) are connected with heater (10), and the logical groove has been seted up on second pipeline (15) surface, and logical groove corresponding position inserts steam pipe (12), and steam pipe (12) correspond the position installation valve, the one end of second pipeline (15) is connected with desorption fan (13).
2. A rotor concentrating system deep regeneration apparatus according to claim 1, wherein the filtering means (16) comprises a coarse screen (6), a fine screen (7), a drying layer (8), and an apparatus body (17), and the inner surface of the apparatus body (17) is provided with the coarse screen (6), the fine screen (7) and the drying layer (8) at one time.
3. The rotating wheel concentration system deep regeneration device according to claim 1, wherein the rotating wheel device (9) comprises an adsorption zone (1), a cooling zone (2), a regeneration zone (3), a steam spray head (4), a rotating wheel main body (18) and a partition plate (19), the partition plate (19) is arranged on the inner surface of the rotating wheel main body (18), the rotating wheel main body (18) is internally provided with a molecular sieve, the rotating wheel main body is divided into the adsorption zone (1), the cooling zone (2) and the regeneration zone (3) through the partition plate (19), the regeneration zone (3) corresponds to the position, the steam spray head (4) is connected to the surface of the rotating wheel main body (18), the steam spray head (4) is made of stainless steel 304, and the rotating wheel device (9) is controlled to rotate by a rotating motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321991910.1U CN220609755U (en) | 2023-07-27 | 2023-07-27 | Runner concentration system degree of depth regenerating unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321991910.1U CN220609755U (en) | 2023-07-27 | 2023-07-27 | Runner concentration system degree of depth regenerating unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220609755U true CN220609755U (en) | 2024-03-19 |
Family
ID=90233091
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321991910.1U Active CN220609755U (en) | 2023-07-27 | 2023-07-27 | Runner concentration system degree of depth regenerating unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220609755U (en) |
-
2023
- 2023-07-27 CN CN202321991910.1U patent/CN220609755U/en active Active
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