CN205517253U - Accurate adsorber - Google Patents
Accurate adsorber Download PDFInfo
- Publication number
- CN205517253U CN205517253U CN201620063538.1U CN201620063538U CN205517253U CN 205517253 U CN205517253 U CN 205517253U CN 201620063538 U CN201620063538 U CN 201620063538U CN 205517253 U CN205517253 U CN 205517253U
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- CN
- China
- Prior art keywords
- adsorption tower
- tower main
- adsorber
- main part
- accurate
- 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.)
- Expired - Fee Related
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- 238000001179 sorption measurement Methods 0.000 claims abstract description 36
- 238000006303 photolysis reaction Methods 0.000 claims abstract description 12
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 10
- 230000003647 oxidation Effects 0.000 claims abstract description 9
- 238000001914 filtration Methods 0.000 claims description 7
- 238000007146 photocatalysis Methods 0.000 claims description 7
- 230000001699 photocatalysis Effects 0.000 claims description 7
- 239000002250 absorbent Substances 0.000 claims description 3
- 230000002745 absorbent Effects 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 238000000746 purification Methods 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 15
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 2
- 239000002994 raw material Substances 0.000 abstract description 2
- 238000005422 blasting Methods 0.000 abstract 1
- 238000006555 catalytic reaction Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 6
- 239000002912 waste gas Substances 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000007084 catalytic combustion reaction Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- -1 hydroxyl free radical Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 239000011941 photocatalyst Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 238000003915 air pollution Methods 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
- 230000008901 benefit Effects 0.000 description 1
- 238000011953 bioanalysis Methods 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 238000009434 installation Methods 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
- 238000006385 ozonation reaction Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 150000003738 xylenes Chemical class 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides an accurate adsorber which constitutes and includes: four landing legs of adsorption tower main part, differential pressure machine, support adsorption tower main part, adsorption tower main part inside is equipped with two feedstock channel, feedstock channel all sets up feed inlet and discharge gate, and open at both ends about the adsorption tower has air inlet and gas outlet inside active carbon adsorption device and a plurality of photodissociation oxidation module and light catalysis filter module of being equipped with of adsorption tower main part the air inlet department of adsorption tower main part installs the differential pressure gauge. The utility model discloses use the active carbon for adsorbing the material, raw material sources are convenient, the low price, and equipment structure is simple, and area is little, and simple to operate is easily capable, and the security performance is strong, can not the accident of blasting.
Description
Technical field
This utility model relates to a kind of accurate adsorber, particularly relates to a kind of accurate adsorber.
Background technology
It is inevitable for producing the waste gas containing pollutant in industrial production activities, although pollution control now can not accomplish the zero-emission of pollutant, but can control in certain scope by the discharge capacity of pollutant and concentration, i.e. qualified discharge.Along with concern and the attention of people's environmental pollution, environmental protection industry grows up the most therewith, and the Treatment process of waste gas is more and more ripe, and industrial waste gas Treatment process is also constantly improving and innovation.
Volatile organic waste gas refers to the waste gas containing VOCs such as benzene,toluene,xylenes, and the operation such as general furniture, automobile, metal and non-metallic member processing, silk-screen all can produce volatile organic waste gas.The Treatment process of organic exhaust gas has a lot, absorption process, absorption method, direct combustion method, Production by Catalytic Combustion Process, absorption+Production by Catalytic Combustion Process, bioanalysis etc..The most widely used is active carbon adsorption, and because it has, design is simple, take up an area and amass few, the low advantage such as low with operation energy consumption of investment cost.
Exhaust combustion gases refers to that fuel produces the waste gas containing pollutant such as sulfur dioxide, nitrogen oxides and carbon black pellets in combustion, and it is the most different that equipment is different, fuel difference produces exhaust emission.Compared with conventional wet, owing to need not with water when depurator works, it is greatly saved the resource of water, the secondary pollution that will not cause water, eliminates the handling of sewage, nor need to add chemical agent, simple to operate, it is novel electricity generator treating tail gas technology, but the investment of this method is of a relatively high.
The purpose of this utility model is achieved through the following technical solutions:
A kind of accurate adsorber, its composition includes: adsorption tower main body, differential pressure machine, four supporting legs of support adsorption tower main body, described adsorption tower body interior is provided with two feeding-passages, described feeding-passage is respectively provided with charging aperture and discharging opening, two ends, adsorption tower left and right have air inlet and gas outlet, it is provided with absorbent charcoal adsorber and multiple photodissociation oxidation module and photocatalysis filtering module in described adsorption tower body interior, at the air inlet of described adsorption tower main body, differential pressure gauge is installed.
Described photodissociation purification assembly is arranged on adsorption tower body interior, installs described photocatalysis filtering module before described gas outlet.
The beneficial effects of the utility model are:
1., with activated carbon for absorption material, raw material sources are convenient, cheap.
2. device structure is simple, and floor space is little, easy for installation easy, and security performance is strong, and explosion accident will not occur.
3. reflection is carried out under negative pressure, beneficially activated carbon adsorption, and exhaust treatment efficiency height is provided with feeding slag-tapping system, regular update, can make the efficiency that equipment holding is higher.
4. possessing pressure reduction display function, when pressure reduction exceedes setting value, signal is reflected control panel, autostop by electro connecting pressure gauge.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model adsorption tower main body.
Fig. 2 is the side schematic view of this utility model adsorption tower main body.
Fig. 3 is the structural representation of this utility model photodissociation cleaning equipment.
Detailed description of the invention
A kind of accurate adsorber, its composition includes: adsorption tower main body 4, differential pressure machine 7, four supporting legs 8 of support adsorption tower main body, it is characterized in that: adsorption tower main body 4 is internal is provided with two feeding-passages 12, described feeding-passage is respectively provided with charging aperture 2 and discharging opening 5, adsorption tower main body about 4 two ends have air inlet 1 and gas outlet 3, inside described adsorption tower main body 4, it is provided with absorbent charcoal adsorber 6 and multiple photodissociation oxidation module 10 and photocatalysis filtering module 11, at the air inlet 1 of described adsorption tower main body 4, differential pressure gauge 7 is installed.
Described photodissociation oxidation module is arranged on adsorption tower body interior, installs described photocatalysis filtering module before described gas outlet.
Being provided with control system in described adsorption tower main body 4, this control system possesses pressure reduction display function, and when pressure reduction exceedes setting value, signal is reflected control panel, autostop by electro connecting pressure gauge；Air inlet 1 and the air outlet 3 of adsorption tower main body 4 respectively install air gauge, are shown by pressure, when pressure reaches setting value, report to the police, and can accurately know that activated carbon is the most saturated, enable users to change in time activated carbon, it is ensured that clean-up effect.
Photodissociation oxidation module 10 produces high energy ultraviolet Line beam by ultraviolet lamp tube 13, decompose the oxygen molecule in air produce free oxygen and then produce the ozone of high concentration, Pre-Ozonation on Organic Matter has extremely strong Oxidation, foul gas and other zest abnormal flavour there is obviously elimination effect, photodissociation oxidation module 10 utilizes high energy ultraviolet Line beam and high-concentrated ozone that foul gas carries out collaborative decomposition oxidation reaction, make foul gas mass degradation change into low molecular compound, water and carbon dioxide, then discharged by air outlet.
Photocatalysis filtering module 11 is under the C-band ultraviolet irradiation that photodissociation oxidation module produces, activated nano photocatalyst, generate electron-hole pair, photocatalyst is made to react with the hydrone of surrounding, generate hydroxyl free radical OH-, by hydroxyl free radical OH-decomposing harmful substances molecular configuration, bacteria growing inhibiting and the activity of virus, thus reach sterilization, air cleaning, deodorization, the purpose of elimination air pollution.
Dusty gas is provided power by blower fan, negative pressure enters activated carbon adsorption tower body, owing to there is lack of equilibrium and unsaturated molecular attraction or valence bond power on activated charcoal solid surface, therefore when this surface of solids contacts with gas, just can attract gas molecule so that it is dense coalescence is maintained at the surface of solids, polluter thus adsorbed, waste gas, after filter, purifies gas high-altitude qualified discharge.
Above example is only in order to illustrate this utility model and and technical scheme described by unrestricted this utility model；Therefore, although this specification has been carried out detailed description with reference to each above-mentioned embodiment to this utility model, but, it will be understood by those within the art that, still this utility model can be modified or equivalent；And all are without departing from the technical scheme of spirit and scope of the present utility model and improvement thereof, it all should be contained in right of the present utility model.
Claims (3)
1. an accurate adsorber, its composition includes: adsorption tower main body, differential pressure machine, support four supporting legs of adsorption tower main body, UV photodissociation cleaning equipment, it is characterized in that: adsorption tower body interior is provided with two feeding-passages, described feeding-passage is respectively provided with charging aperture and discharging opening, two ends, adsorption tower left and right have air inlet and gas outlet, inside described adsorption tower, it is provided with absorbent charcoal adsorber and multiple photodissociation oxidation module and photocatalysis filtering module, at the air inlet of described adsorption tower, differential pressure gauge is installed.
A kind of accurate adsorber the most according to claim 1, it is characterised in that: described photodissociation purification assembly is arranged on adsorption tower body interior, installs described photocatalysis filtering module before described gas outlet.
A kind of accurate adsorber the most according to claim 1, it is characterised in that: in described adsorption tower main body, control system is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620063538.1U CN205517253U (en) | 2016-01-23 | 2016-01-23 | Accurate adsorber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620063538.1U CN205517253U (en) | 2016-01-23 | 2016-01-23 | Accurate adsorber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205517253U true CN205517253U (en) | 2016-08-31 |
Family
ID=56767569
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620063538.1U Expired - Fee Related CN205517253U (en) | 2016-01-23 | 2016-01-23 | Accurate adsorber |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205517253U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107126839A (en) * | 2017-07-01 | 2017-09-05 | 成都国化环保科技有限公司 | A kind of denitrating tower for denitration device line |
| CN107138042A (en) * | 2017-07-01 | 2017-09-08 | 成都国化环保科技有限公司 | A kind of flue gas denitrification equipment line |
| CN107138043A (en) * | 2017-07-01 | 2017-09-08 | 成都国化环保科技有限公司 | A kind of flue gas conditioning component for denitration device line |
| CN108716718A (en) * | 2018-06-07 | 2018-10-30 | 苏州赛易特环保科技有限公司 | A kind of laminar flow hood of automatic replacement activated carbon |
-
2016
- 2016-01-23 CN CN201620063538.1U patent/CN205517253U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107126839A (en) * | 2017-07-01 | 2017-09-05 | 成都国化环保科技有限公司 | A kind of denitrating tower for denitration device line |
| CN107138042A (en) * | 2017-07-01 | 2017-09-08 | 成都国化环保科技有限公司 | A kind of flue gas denitrification equipment line |
| CN107138043A (en) * | 2017-07-01 | 2017-09-08 | 成都国化环保科技有限公司 | A kind of flue gas conditioning component for denitration device line |
| CN108716718A (en) * | 2018-06-07 | 2018-10-30 | 苏州赛易特环保科技有限公司 | A kind of laminar flow hood of automatic replacement activated carbon |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20220123 |