CN106000089A - Auto-regeneration adsorber - Google Patents
Auto-regeneration adsorber Download PDFInfo
- Publication number
- CN106000089A CN106000089A CN201610466678.8A CN201610466678A CN106000089A CN 106000089 A CN106000089 A CN 106000089A CN 201610466678 A CN201610466678 A CN 201610466678A CN 106000089 A CN106000089 A CN 106000089A
- Authority
- CN
- China
- Prior art keywords
- adsorber
- autoregeneration
- supporting network
- metal supporting
- metal support
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000011069 regeneration method Methods 0.000 title abstract description 4
- 238000001179 sorption measurement Methods 0.000 claims abstract description 23
- 238000001914 filtration Methods 0.000 claims abstract description 20
- 239000002184 metal Substances 0.000 claims abstract description 19
- 229910052751 metal Inorganic materials 0.000 claims abstract description 19
- 239000010453 quartz Substances 0.000 claims abstract description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000011248 coating agent Substances 0.000 claims abstract description 11
- 238000000576 coating method Methods 0.000 claims abstract description 11
- 239000011941 photocatalyst Substances 0.000 claims abstract description 9
- 238000007789 sealing Methods 0.000 claims abstract description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- 239000011324 bead Substances 0.000 claims description 11
- 238000005276 aerator Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- 229910021536 Zeolite Inorganic materials 0.000 claims description 4
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 239000010457 zeolite Substances 0.000 claims description 4
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims 1
- 239000010931 gold Substances 0.000 claims 1
- 229910052737 gold Inorganic materials 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 3
- 230000008929 regeneration Effects 0.000 abstract description 2
- 238000010438 heat treatment Methods 0.000 abstract 2
- 239000012855 volatile organic compound Substances 0.000 abstract 1
- 238000010521 absorption reaction Methods 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 5
- 239000003344 environmental pollutant Substances 0.000 description 4
- 230000000844 anti-bacterial effect Effects 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 241000700605 Viruses Species 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000003870 refractory metal Substances 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 231100000915 pathological change Toxicity 0.000 description 1
- 230000036285 pathological change Effects 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical group [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/16—Disinfection, sterilisation or deodorisation of air using physical phenomena
- A61L9/22—Ionisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—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
- 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
- B01D53/8668—Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/80—Type of catalytic reaction
- B01D2255/802—Photocatalytic
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/708—Volatile organic compounds V.O.C.'s
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/818—Employing electrical discharges or the generation of a plasma
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—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
- B01D53/02—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 adsorption, e.g. preparative gas chromatography
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—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
- B01D53/32—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 electrical effects other than those provided for in group B01D61/00
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- General Health & Medical Sciences (AREA)
- Veterinary Medicine (AREA)
- Public Health (AREA)
- Animal Behavior & Ethology (AREA)
- Biomedical Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Epidemiology (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Catalysts (AREA)
Abstract
The invention relates to an auto-regeneration adsorber. The adsorber comprises a casing sleeve, a quartz heating tube, an air blower, baffles, a vertical wind board, a metal support screen, a filtering adsorption ring, a plasma generator, an irradiation lamp and a photocatalyst coating, wherein the casing sleeve is a hollow cylinder, and the metal support screen is arranged in the casing sleeve; the metal support screen is sleeved with the filtering adsorption ring, the quartz heating tube is inserted into one end inside the metal support screen, and the other end is connected with the air blower; a long strip-shaped opening is formed in the lower part of the casing sleeve, the baffles for sealing the long strip-shaped opening are arranged at the opening, the vertical wind board is arranged between the two baffles, the vertical wind board is fixed with the metal support screen, and the photocatalyst coating, the plasma generator and the irradiation lamp are arranged on the inner wall of the casing sleeve. The adsorber can treat VOCs in various manners and has high treatment efficiency and good effect, and rapid regeneration can be realized through the adsorber.
Description
Technical field
The present invention relates to field of Environment Protection technology, particularly relate to autoregeneration adsorber.
Background technology
Self volatilization process that volatile organic matter (VOCs) results from organic chemical industry's production process and organic products is used, right
Environment and human health are harmful to.Existing its activated carbon adsorption of waste gas treatment process VOCs, is also stored in the sky of activated carbon simultaneously
In gap, need frequently to change activated carbon guarantee adsorption effect, costly and time consuming arduously.Chinese patent CN 104028086
The open a kind of VOC exhaust treatment system of A, the UV active charcoal integrated apparatus that it includes, constantly adsorb and aoxidize desorption,
Avoided multi-pollutant to be stored in the space of activated carbon, and be not required to conventional art and the most frequently change activated carbon or increase activated carbon
The thickness of layer, has saved purification cost.But the pollutant of absorption can only be desorbed removal, this processing mode by Ultraviolet Oxidation mode
Single, disposably can not be processed by processing equipment of the prior art for different exhaust gas constituents, and the regenerating active carbon time
Long, VOCs clean-up effect is undesirable.
Summary of the invention
It is an object of the invention to overcome the deficiencies in the prior art, it is provided that a kind of autoregeneration adsorber, it is possible in several ways
Processing VOCs, treatment effeciency is high, effective simultaneously, and realizes the rapid regeneration of adsorber.
The present invention solves it and technical problem is that and take techniques below scheme to realize: autoregeneration adsorber, including shell body,
Quartz heating-pipe, aerator, baffle plate, vertical deep bead, metal supporting network, Filtration Adsorption circle, plasma generator, irradiation
Lamp and photocatalyst coating；Described shell body is the cylinder of hollow, and in described casing body, portion is provided with metal supporting network；Described
Metal supporting network outer cover is equipped with Filtration Adsorption circle, and internal one end has inserted quartz heating-pipe, and the other end is connected with aerator；Institute
State shell body bottom and be provided with strip opening, opening is provided with the baffle plate sealing strip opening, sets in the middle of described two baffle plates
Have vertical deep bead, described vertical deep bead and metal supporting network to fix, in described casing body wall be provided with photocatalyst coating,
Plasma generator and irradiation light.
Further, described shell body is refractory metal material, and in described casing body, wall is whiteware material.
Further, described irradiation light is blue LED lamp.
Further, described Filtration Adsorption circle is activated carbon and the fibrous reticular structure of zeolite powder compacting.
The invention have the benefit that autoregeneration adsorber can process VOCs in several ways, treatment effeciency is high；Cross
The stephanoporate framework molecular sieve structure of filter absorption circle, absorption contact area is big, and it is to organic gas high adsorption capacity；Plasma occurs
Device can make the charged scission of link of Organic substance in gas decompose reaction, carries out toxic and harmful and life virus, antibacterial etc. quickly
Degraded, thus efficiently virus killing, sterilizing, go abnormal flavour, smoke elimination, dedusting；After the absorption of Filtration Adsorption circle is saturated, start air blast simultaneously
Machine and quartz heating-pipe, escape in pollutant inherent filtration absorption circle and decompose, and the adsorption function of Filtration Adsorption circle is the most resilient, weight
Multiple use.
Accompanying drawing explanation
Fig. 1 is the structure sectional view of the present invention；
Fig. 2 is autoregeneration adsorber side cutaway view.
In figure, 1, shell body, 2, quartz heating-pipe, 3, aerator, 4, baffle plate, 5, vertical deep bead, 6, metal
Supporting network, 7, Filtration Adsorption circle, 8, plasma generator, 9, irradiation light, 10, photocatalyst coating.
Detailed description of the invention
The present invention will be further described below in conjunction with the accompanying drawings:
As shown in Figure 1-2, autoregeneration adsorber, including shell body 1, quartz heating-pipe 2, aerator 3, baffle plate 4,
Vertical deep bead 5, metal supporting network 6, Filtration Adsorption circle 7, plasma generator 8, irradiation light 9 and photocatalyst coating 10；
Described shell body 1 is the cylinder of hollow, and described shell body 1 is internal is provided with metal supporting network 6, described metal supporting network 6
Outer cover is equipped with Filtration Adsorption circle 7, and internal one end has inserted quartz heating-pipe 2, and the other end is connected with aerator 3, described shell
Body 1 bottom is provided with strip opening, is provided with the baffle plate 4 sealing strip opening, sets in the middle of described two baffle plates 4 on opening
Having vertical deep bead 5, described vertical deep bead 5 and metal supporting network 6 to fix, described shell body 1 inwall is provided with light and touches
Matchmaker's coating 10, plasma generator 8 and irradiation light 9.Described shell body 1 is refractory metal material, described shell body
1 inwall is whiteware material.Described irradiation light 9 is blue LED lamp.Described Filtration Adsorption circle 6 is activated carbon and zeolite powder
The fibrous reticular structure of compacting.
Air inlet and air outlet, in the same side of casing body 1, are separated by vertical deep bead 5, make by air inlet and air outlet
Move in a circle when gas is by shell body 1.Filtration Adsorption circle 7 is the straw activated carbon and zeolite made for raw material with straw
The stephanoporate framework filamentary structure that powder is prepared from through distributing mixing compact technique, is pressed into cylindrical sleeve, set metal
On supporting network 6, VOCs is fine particle Organic substance in out-of-date adsorbable gas.Shell body 1 inwall is whiteware material,
And at surface spraying photocatalyst coating 10, adsorbed organic contamination composition granule is carried out by irradiation light 9 exciting light catalyst coating 10
Photocatalysis Decomposition.Plasma generator 8 forms asymmetric plasma electric field mainly by circuit high pressure, high-frequency impulse electric discharge
Produce electric discharge ionized gas, produce the high concentration gas ions such as the active substance including electronics and intermediate active material, it is achieved right
Organic matter degradation process, plasma generator ionization simultaneously produces a large amount of negative ions, and anion can make an initiative sally, find
Miniature pollution particulate matter in air, and with its conglomerate, be actively settled down to Filtration Adsorption circle 7 surface and carried out absorption point
Solve.Cation easily adsorbs antibacterial so that it is recurring structure changes and energy shifts, and causes antibacterial pathological changes and dead.By so
Various ways processes VOCs, and treatment effeciency is high.
Quartz heating-pipe 2 is arranged on the center of Filtration Adsorption circle 7, adsorb saturated after, according to job requirement, at one's leisure between,
Such as low power consumption period at night, simultaneously startup aerator 3 and quartz heating-pipe 2, device is heated and ventilation stripping processes,
Pollutant inherent filtration absorption circle 7 escape and decomposes, making saturated Filtration Adsorption circle 7 have adsorption treatment ability again, repeat to make
With, cost-effective.
Above by embodiment, the present invention is described in detail, but described content has been only presently preferred embodiments of the present invention, no
The practical range for limiting the present invention can be considered.All impartial changes made according to the present patent application scope and improvement etc., all should
Within still belonging to the patent covering scope of the present invention.
Claims (4)
1. autoregeneration adsorber, it is characterised in that: include shell body, quartz heating-pipe, aerator, baffle plate, hang down
Straight deep bead, metal supporting network, Filtration Adsorption circle, plasma generator, irradiation light and photocatalyst coating；
Described shell body is the cylinder of hollow, and in described casing body, portion is provided with metal supporting network, described metal supporting network
Outer cover is equipped with Filtration Adsorption circle, and internal one end has inserted quartz heating-pipe, and the other end is connected with aerator, described casing
Body bottom is provided with strip opening, is provided with the baffle plate sealing strip opening on opening, is provided with vertical in the middle of described two baffle plates
Deep bead, described vertical deep bead and metal supporting network fix, in described casing body wall be provided with photocatalyst coating, etc. from
Electronic generator and irradiation light.
Autoregeneration adsorber the most according to claim 1, it is characterised in that: described shell body is high temperature resistant gold
Belonging to material, in described casing body, wall is whiteware material.
Autoregeneration adsorber the most according to claim 1, it is characterised in that: described irradiation light is blue LED lamp.
Autoregeneration adsorber the most according to claim 1, it is characterised in that: described Filtration Adsorption circle is activated carbon
Fibrous reticular structure with zeolite powder compacting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610466678.8A CN106000089A (en) | 2016-06-20 | 2016-06-20 | Auto-regeneration adsorber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610466678.8A CN106000089A (en) | 2016-06-20 | 2016-06-20 | Auto-regeneration adsorber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106000089A true CN106000089A (en) | 2016-10-12 |
Family
ID=57087304
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610466678.8A Pending CN106000089A (en) | 2016-06-20 | 2016-06-20 | Auto-regeneration adsorber |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106000089A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111760455A (en) * | 2020-07-24 | 2020-10-13 | 北京市环境保护科学研究院 | Volatile organic compound adsorption regeneration coupling filter element and purification device |
| CN117085463A (en) * | 2023-10-17 | 2023-11-21 | 杭州特盈低温液化装备有限公司 | High-efficiency molecular sieve adsorber |
-
2016
- 2016-06-20 CN CN201610466678.8A patent/CN106000089A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111760455A (en) * | 2020-07-24 | 2020-10-13 | 北京市环境保护科学研究院 | Volatile organic compound adsorption regeneration coupling filter element and purification device |
| CN117085463A (en) * | 2023-10-17 | 2023-11-21 | 杭州特盈低温液化装备有限公司 | High-efficiency molecular sieve adsorber |
| CN117085463B (en) * | 2023-10-17 | 2024-01-12 | 杭州特盈低温液化装备有限公司 | High-efficiency molecular sieve adsorber |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20161012 |