CN108889066A - A kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution - Google Patents
A kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution Download PDFInfo
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- CN108889066A CN108889066A CN201811119168.9A CN201811119168A CN108889066A CN 108889066 A CN108889066 A CN 108889066A CN 201811119168 A CN201811119168 A CN 201811119168A CN 108889066 A CN108889066 A CN 108889066A
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- convex rod
- magnetic solution
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 18
- 239000012855 volatile organic compound Substances 0.000 title claims abstract description 14
- 239000002245 particle Substances 0.000 claims abstract description 41
- 239000002808 molecular sieve Substances 0.000 claims abstract description 16
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims abstract description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 12
- 230000000694 effects Effects 0.000 claims abstract description 9
- 239000003463 adsorbent Substances 0.000 claims abstract description 5
- 239000011248 coating agent Substances 0.000 claims description 12
- 238000000576 coating method Methods 0.000 claims description 12
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 10
- 241000264877 Hippospongia communis Species 0.000 claims description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 8
- 229910052802 copper Inorganic materials 0.000 claims description 8
- 239000010949 copper Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 8
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- 229910052709 silver Inorganic materials 0.000 claims description 4
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- 239000002105 nanoparticle Substances 0.000 claims description 3
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 2
- 239000010931 gold Substances 0.000 claims description 2
- 229910052737 gold Inorganic materials 0.000 claims description 2
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- 238000005516 engineering process Methods 0.000 abstract description 22
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- 238000012512 characterization method Methods 0.000 abstract description 2
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- 230000003647 oxidation Effects 0.000 description 9
- 238000007254 oxidation reaction Methods 0.000 description 9
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- 230000006872 improvement Effects 0.000 description 6
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- 238000006243 chemical reaction Methods 0.000 description 4
- 238000009841 combustion method Methods 0.000 description 4
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 4
- 230000035943 smell Effects 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 3
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000004332 deodorization Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
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- 239000003344 environmental pollutant Substances 0.000 description 3
- 235000019645 odor Nutrition 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 150000003384 small molecules Chemical class 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 239000005749 Copper compound Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000007084 catalytic combustion reaction Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 150000001880 copper compounds Chemical class 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
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- 229910021389 graphene Inorganic materials 0.000 description 2
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- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910000881 Cu alloy Inorganic materials 0.000 description 1
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
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- 239000010953 base metal Substances 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- LGFMFHLENZUZLV-UHFFFAOYSA-N benzene;methanedithione Chemical compound S=C=S.C1=CC=CC=C1 LGFMFHLENZUZLV-UHFFFAOYSA-N 0.000 description 1
- 238000011953 bioanalysis Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
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- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
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- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
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- 230000003628 erosive effect Effects 0.000 description 1
- 230000005281 excited state Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- OUUQCZGPVNCOIJ-UHFFFAOYSA-N hydroperoxyl Chemical compound O[O] OUUQCZGPVNCOIJ-UHFFFAOYSA-N 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
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- 150000007523 nucleic acids Chemical class 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D49/00—Separating dispersed particles from gases, air or vapours by other methods
-
- 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
- B01D53/04—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 with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/106—Silica or silicates
- B01D2253/11—Clays
-
- 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
-
- 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
- B01D2259/814—Magnetic fields
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Treating Waste Gases (AREA)
Abstract
The present invention discloses a kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution, the blower including processor and inside processing;The processor one side is equipped with air outlet and at least one side is equipped with air intake surface, and the air intake surface is equipped with concave convex rod molecular sieve, modified activated carbon and superparamagnetic field magnetic solution plate from outside to inside;The concave convex rod molecular sieve is equipped with three-decker, successively includes front layer fine-structure mesh, middle layer honeycomb circulation layer and rear layer fine-structure mesh, is filled with concave-convex rod particle in the honeycomb circulation layer, and have front layer fine-structure mesh and rear layer fine-structure mesh package.Exhaust processor of the invention combines the filtering of the magnetic solution of the adsorption filtration of concave convex rod adsorption plate and the adsorption plate of modified activated carbon and superparamagnetic field magnetic solution plate, waste gas purification rate is higher, concave convex rod molecular sieve is using concave convex rod as adsorbent and red pyroxene as characterization agent, it can make the hydrophobically modified technology of concave convex rod molecular sieve more easily and effect is more preferable, its selective adsorption capacity to organic compound can be improved.
Description
Technical field
It is especially a kind of to have using concave convex rod absorption and superparamagnetic field magnetic solution the present invention relates to waste gas purification technical field
Machine exhaust processor.
Background technique
Existing VOCs treatment technology:
1. liquid absorption technology:The principle of this Treatment process is by two kinds of shapes of Physical Absorption method and chemical absorption method
Formula realizes merging for harmful components and the absorbent in organic exhaust gas, reprocesses waste water, realizes purification treatment purpose.Purifying rate<
30%, and have very secondary pollution again.
2. adsorption technology:Organic exhaust gas is adsorbed using adsorbent, suitable for handling a small amount of organic exhaust gas of low concentration.Purification
Efficiency it is lower (<45%), regeneration desorption is more difficult (inflammable), needs to constantly change (3-5 days/time), maintenance cost is higher, can inhale
" spectrum " of attached organic exhaust gas is narrow, generates solid waste.Such as:Various active carbons etc..
3. heat damage technology:Also referred to as combustion method is divided into direct combustion method and catalytic oxidation combustion method.The former directly fires
Burning method is directly to burn the organic matter in organic exhaust gas, most under the elevated temperature vessel by temperature between 650 DEG C~850 DEG C
The innocuous substance for generating other nonstaining properties of carbon dioxide, water etc. afterwards can if the content of flammable organic exhaust gas is lower
To guarantee incendivity temperature and oxygen content size in combustion process burning in the present incinerator of exhaust gas;
Production by Catalytic Combustion Process, it is under the effect of the catalyst, to accelerate organic chemical reactions speed, its improvement is very
It is good, it is currently your gold using most wide catalyst in the lower catalysis burning of temperature substantially between 90%~99%
Belong to and base metal two types.
3.1 flame combustion methods:Organic exhaust gas is sufficiently mixed with fuel gas at high temperature, realizes completely burned.Suitable for place
The imflammable gas of high concentration, small tolerance is managed, purification efficiency is high, and organic exhaust gas is decomposed by exhaustive oxidation, disadvantage:Equipment is perishable
Erosion, processing cost is high, easily formation secondary pollution;
3.2 Production by Catalytic Combustion Process:Under the effect of the catalyst, make the hydrocarbon in organic exhaust gas in the lower item of temperature
Rapid oxidation Cheng Shui and carbon dioxide, achieve the purpose that improvement under part.Disadvantage:Catalyst is easily poisoned, input cost and maintenance at
This height;
4. high energy ultraviolet photodissociation technology is to generate the light quantity of different-energy by the ultraviolet light excitation light source of specific wavelength
Son;Litter is verified the strong absorption of the light quantum, largely take can make under the bombardment of light quantum exhaust gas substance molecular dissociation and
Excitation;Oxygen and moisture and additional ozone in air can produce a large amount of nascent state under (decomposition) effect of the light quantum
Hydrogen, activity (free) oxygen and hydroxyl oxygen isoreactivity group;Because the taken positron-electron imbalance of free oxygen is so need to be with oxygen molecule knot
It closes, and then generates ozone, the organic matter after ozone decomposes ultraviolet beam irradiation has extremely strong oxidation;Portion
Substance can also be reacted with active group, and final Degradation and Transformation is the innocuous substances such as low molecular compound CO2 and H2O.
5. bioanalysis:Using microorganism life process the gaseous pollutant decomposition and inversion in exhaust gas at less or even without
Evil substance.There are various microorganisms in nature, nearly all inorganic and organic pollutant can be converted.Biology
Processing does not need regeneration and other high-level processes, compared with other methods of purification, have equipment is simple, low energy consumption, safety can
The advantages that leaning on, be without secondary pollution, but polluter cannot be recycled.
6. lower temperature plasma technology:It is generated during dielectric barrier discharge, inside plasma living rich in high chemistry
The particle of property, such as electronics, ion, free radical and excited state molecule.Polluter in exhaust gas and these with higher-energy
Active group react, be eventually converted into the substances such as CO2 and H2O, thus achieve the purpose that purify exhaust gas.The scope of application
Extensively, purification efficiency is high, is particularly suitable for the reluctant multi-component stink gas of other methods, such as chemical industry, medicine industry.Electricity
Sub- energy is high, almost can be with all foul gas molecular actions;Operating cost is low;Reaction is fast, and equipment starting stops very
Rapidly, with with opening.Disadvantage:One-time investment is compared with high, security risk is big.
7. photochemical catalytic oxidation introduction:Photooxidation catalytic treatment technology is to be urged using extraordinary ultra-violet bands (C-band) in special type
Under the action of changing oxidant, by emission molecule is broken and a kind of further redox specially treated mode.Emission molecule is first
It is crushed organic molecule by special wave band high energy ultraviolet light wave, interrupts its strand;Meanwhile by decompose air in oxygen and
Water obtains high-concentrated ozone, and ozone further absorbs energy, forms the higher free hydroxyl of oxidation susceptibility, oxidation gaseous effluent molecule.
A variety of composite inert catalyst are configured according to different exhaust gas constituents simultaneously, greatly improve the speed and efficiency of exhaust-gas treatment, from
And achieve the purpose that exhaust gas is carried out to purify
8. ultraviolet light exhaust-gas treatment:Firstly, product irradiates foul gas using special high energy high ozone ultraviolet beam,
Cracked gas such as ammonia, trimethylamine, hydrogen sulfide, first sulphur, methyl mercaptan, methyl sulfide, methyl disulfide, carbon disulfide and carbon disulfide benzene second
Alkene, hydrogen sulfide, hydrogen sulfide, benzene, toluene, dimethylbenzene molecular chain structure make organic or inorganic high-molecular compound strand, high energy
Ultraviolet light irradiation, is degraded into low molecular weight compound such as CO2, H2O.It is decomposed using high energy high ozone ultraviolet light ultraviolet beam empty
Oxygen molecule in gas generates free oxygen, i.e., the imbalance and oxygen of the active oxygen and negative electron that are carried by the free oxygen that negative electrical charge carries
Molecule needs to combine, and then generates ozone.UV+O2 → O-+O* (active oxygen) O+O2 → O3 (ozone), it is known that ozone has strong
The smell of strong oxidation operation, gas and other penetrating odors is immediately affected by removal.Using high energy UV in molecular link
It is middle that gas bacterium sterilizes, it destroys bacterial nucleic acid (DNA), then by ozone oxidation, complete deodorization simultaneously kills bacterium.
It is high-efficient, in addition to foul smell:Volatile organic compounds (VOC), inorganic, hydrogen sulfide, ammonia, mercaptan etc. can be effectively removed
Major pollutants, and various smells, odor removal efficient 99% are much higher than the national emission standard for odor pollutants promulgated in 1993
(GB14554-93).Without adding any material:Exhaust pipe appropriate and exhaust power need to be only set, and the smell of gas is by setting
It is standby to carry out deodorization decomposing, purifying, chemical reaction is participated in without adding any substance.Adapt to high concentration, atm number, different effluviums
Body deodorization scavenging material can daily 24 continuous throughout the twenty-four hour24, stable and reliable operation.But fatal disadvantage is that treating capacity is small, needs
Constant temperature, the amount of exhaust gas input and concentration want constant, automatic inactivation, maintenance cost height easily occur.
And in the discharge of existing China's organic exhaust gas, a large amount of other pollutions are mixed, such as:Dirt, paint drop, water, biology
Exhaust gas etc., in preceding pretreatment, the technology of the exhaust-gas treatment of the prior art has:Liquid absorption technology, heat damage technology, physics mistake
Filter technology, electrostatic precipitator technology etc., wherein physical filtering technology and electrostatic precipitator technology are the mainstream skill of existing exhaust-gas treatment
Art.
But the granular size of the physical filtering technical filter of the prior art also stop be desirably also in PM2.5 rank, it is right
In PM2.5 particle below, especially partial size in 100nm nonpolar little particulate below, still " helpless ".And in order to
Reach good filter effect, need that multistage filtering is arranged, leads to physical filtering apparatus structure complexity, the installation fiber crops of the prior art
It is tired;And service life is shorter, and maintenance cost is higher, needs to re-replace.
And electrostatic precipitator technology can not also handle PM2.5 particle below, especially partial size in 100nm nonpolarity below
Little particulate needs to access the high-pressure electrostatic of up to upper kilovolt, power consumption is excessive, Er Qiehui to reach good filter effect
High-pressure electrostatic is generated, the life security of people is jeopardized.
It is below quickly to smash pm2.5 using high-intensitive superparamagnetic field for superparamagnetic field nano magnetic solution technology, this technology
The particle of various exhaust gas allows the partial size of its particle in 100nm hereinafter, when particle is below nanoscale, particle peripheral electron, no
It is circular motion but forms spasmodic motion (movement of on-circular formula), generates superparamagnetism, under the action of externally-applied magnetic field, institute
Some particles close Key by the change that set magnetic field line of force direction strikes off small molecule, are oxidized to C0 after " magnetic solution "2、H20、02、N2Etc. inorganic
Small molecule can thoroughly handle part PM2.5 particle, PM1.0 particle and partial size in 100nm nonpolar little particulate below.
Summary of the invention
In order to overcome the disadvantages mentioned above of the prior art, higher, power consumption that the object of the present invention is to provide a kind of waste gas purification rates
Amount is less, the higher VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution of security performance.
The technical solution adopted by the present invention to solve the technical problems is:
A kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution, wherein:Including processor and set
Blower inside processing;The processor one side is equipped with air outlet and at least one side is equipped with air intake surface, the air inlet
Face is equipped with concave convex rod molecular sieve, modified activated carbon and superparamagnetic field magnetic solution plate from outside to inside;
The concave convex rod molecular sieve is equipped with three-decker, successively includes front layer fine-structure mesh, the double honeycomb circulation layers in middle layer and rear layer
Fine-structure mesh, the interstitial spaces between the double honeycombs circulation layers are 4mm-6mm, and the thickness 10mm to 2mm of each honeycomb circulation layer is described
It is filled with concave-convex rod particle filled with concave-convex rod particle or in which one layer in double layer cell circulation layer, another layer is filled with modification
Activated carbon and adsorbent, and wrapped up by front layer fine-structure mesh and rear layer fine-structure mesh;
The superparamagnetic field magnetic solution plate, which is connected by outer framework with magnetic solution Intranet, to be formed, and is coated with nanometer on the net in the magnetic solution
Grade metal coating.
As a further improvement of the present invention:The superparamagnetic field magnetic solution plate is connected with electrostatic generator, the electrostatic hair
Raw device includes at least one:With 18kV-25kV electrostatic pressure output strong electrostatic generator or have 12V-36V electrostatic
Press the weak electrostatic generator of output.
As a further improvement of the present invention:The magnetic solution Intranet is more made of tweezer, copper alloy or basalt materials
Hole reticular structure or the foaming irregular empty pocket structure of sample.
As a further improvement of the present invention:The nano metal coating is by nanosized copper particle or nanometer-level silver particle
It sprays.
As a further improvement of the present invention:The nano metal coating with a thickness of 2-10 μm, the nanoparticle or
The granularity of nano silver particles is 2-4nm size.
Compared with prior art, the beneficial effects of the invention are as follows:
Exhaust processor of the invention filters the magnetic solution of the adsorption filtration of concave convex rod adsorption plate and superparamagnetic field magnetic solution plate
It combines, waste gas purification rate is higher, and waste gas purification rate is up to 99.99% or more.
Concave convex rod molecular sieve is used as characterization agent as adsorbent and red pyroxene using concave convex rod, on the one hand can make concave convex rod
The hydrophobically modified technology of molecular sieve is easier and effect is more preferable, its selective adsorption capacity to organic compound can be improved;
On the other hand, relative to concave convex rod, the price of red pyroxene is cheaper, can save cost of material.
Processor of the invention uses superparamagnetic field magnetic solution technology, mainly for PM2.5 particle below, especially partial size
Pm2.5 various exhaust gas below are quickly smashed using high-intensitive superparamagnetic field in 100nm nonpolar little particulate below
Particle allows the partial size of its particle in 100nm hereinafter, when particle is below nanoscale, and the chemical combination for cracking organic molecule is built, and generates
C02、H20、02、N2Equal inorganic molecules;Substantially it is analogous to composition of air.
Processor of the invention uses superparamagnetic field magnetic solution technology, relative to existing physical filtering technology, without in short-term
Between replace, maintenance cost is lower, and theoretically service life can reach 20 years or more.In addition to this, the also simple, installation with structure
Convenient advantage is suitble to large-scale promotion to use.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is the structural schematic diagram of air intake surface.
Fig. 3 is the structural schematic diagram of concave convex rod molecular sieve.
Specific embodiment
Now in conjunction with Detailed description of the invention, the present invention is further described with embodiment:
With reference to Fig. 1-3, a kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution, including processor
1 and set on processing inside blower;1 one side of processor is equipped with air outlet 11 and at least one side is equipped with air intake surface 2,
The air intake surface is equipped with concave convex rod molecular sieve 21, modified activated carbon 22 and superparamagnetic field magnetic solution plate 23 from outside to inside;
The concave convex rod molecular sieve is equipped with three-decker, successively includes front layer fine-structure mesh 211, middle layer honeycomb circulation 212 and of layer
Layer fine-structure mesh 213 afterwards is filled with concave-convex rod particle in honeycomb circulation layer, and is wrapped up by front layer fine-structure mesh and rear layer fine-structure mesh;
The concave convex rod molecule particles be by the way that natural concave convex rod is crushed, be mixed with beating in blender with pure water and
Centrifuge separation carries out decontamination, and homogenate, is added red pyroxene and graphene is characterized, and is ground using formula nanometer water grinder is stood
False reunion is formed at powder at 40-80nm nanometer particle, then with high-temperature spray crushed machine, 3X2X2mm is made in dual-purpose pelletizer
Particle.The specific surface area of the concave convex rod molecule particles reaches 2000-3000m2/g。
The superparamagnetic field magnetic solution plate is connected with magnetic solution Intranet by the outer framework to insulate and is formed, and is sprayed on the net in the magnetic solution
There is nano level metal coating.
The superparamagnetic field magnetic solution plate is connected with electrostatic generator, and the electrostatic generator includes at least one:Band
The strong electrostatic generator for thering is 18kV-25kV electrostatic pressure to export or the weak electrostatic generator with the output of 12V-36V electrostatic pressure.
The magnetic solution Intranet is the porous network structure made of the alloys such as tweezer, copper, silver or basalt materials.
The nano metal coating is sprayed by nanosized copper particle or nanometer-level silver particle.
The nano metal coating with a thickness of 2-10 μm, the sizes of the nanoparticle or nano silver particles is 2-4nm.
The preparation method of the superparamagnetic field magnetic solution plate:(1) 20-22nm scale is produced by means of nano silver stamped method
Nano silver lattice;(2) graphene of partial size 2nm copper magnetic powder and 1nm is poured into nano silver lattice using fluid jet, obtains nanometer
Copper compound material;(3) Nanometer Copper compound material is sprayed on to the surface of magnetic solution Intranet, obtains the magnetic solution for being coated with nanometer copper coating
Intranet;(4) the magnetic solution Intranet for being coated with nanometer copper coating is mounted in outer framework to get superparamagnetic field magnetic solution plate.
The principle of the present invention:Under the driving of blower, exhaust gas enters inside processor from air intake surface, successively passes through concave convex rod
Molecular sieve adsorption filtration,:Nanoscale concave convex rod molecular sieve is such as most absolutely for obstructing, adsorbing the biggish particle of its in air
PM10 and part PM2.5 particle make it handle load and reduce, be more advantageous to part mainly for the protection of superparamagnetic field magnetic solution plate
PM2.5 particle and PM1.0 particle (especially partial size is in 100nm nonpolar little particulate below) are thoroughly handled.
The magnetic solution of superparamagnetic field magnetic solution plate filters:The electrostatic electricity of 18kV-25kV or 12V-36V is provided by electrostatic generator
Pressure, nanosized copper particle coating generate superparamagnetic field after accessing electrostatic, using high-intensitive superparamagnetic field, quickly smash pm2.5
The particle of various exhaust gas below allows the partial size of its particle, hereinafter, when particle is below nanoscale, to crack organic in 100nm
The chemical combination of molecule is built, and C0 is generated2、H20、02、N2Equal inorganic molecules.
Organic exhaust gas is after the magnetic solution of the absorption of concave convex rod molecular sieve and modified activated carbon and superparamagnetic field, by air draft
Mouth discharge, while superparamagnetic field cracks the chemical bond for the various types organic exhaust gas that active carbon and concave convex rod adsorb, cracking has
The chemical combination of machine molecule is built, and the inorganic molecules such as C02, H20,02, N2, hydrogen are generated;Substantially it is analogous to composition of air, is discharged, no
Generate secondary pollution.
In conclusion after those skilled in the art read file of the present invention, according to the technique and scheme of the present invention with
Technical concept is not necessarily to creative mental labour and makes other various corresponding conversion schemes, belongs to the model that the present invention is protected
It encloses.
Claims (5)
1. a kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution, it is characterised in that:Including processor
And the blower inside processing;The processor one side is equipped with air outlet and at least one side is equipped with air intake surface, described
Air intake surface is equipped with concave convex rod molecular sieve, modified activated carbon and superparamagnetic field magnetic solution plate from outside to inside;
The concave convex rod molecular sieve is equipped with three-decker, successively includes front layer fine-structure mesh, the double honeycombs circulation layers in middle layer and rear layer fine-structure mesh,
Interstitial spaces between double honeycomb circulation layers are 4mm-6mm, the thickness 10mm to 2mm of each honeycomb circulation layer, the bilayer
It is filled with concave-convex rod particle filled with concave-convex rod particle or in which one layer in honeycomb circulation layer, another layer is filled with modified activity
Carbon and adsorbent, and wrapped up by front layer fine-structure mesh and rear layer fine-structure mesh;
The superparamagnetic field magnetic solution plate, which is connected by outer framework with magnetic solution Intranet, to be formed, and is coated with nanometer grade gold on the net in the magnetic solution
Belong to coating.
2. a kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution according to claim 1,
It is characterized in that:The superparamagnetic field magnetic solution plate is connected with electrostatic generator, and the electrostatic generator includes at least one:Band
Strong electrostatic generator, the weak electrostatic generator with the output of 12V-36V electrostatic pressure for thering is 18kV-25kV electrostatic pressure to export.
3. a kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution according to claim 1,
It is characterized in that:The magnetic solution Intranet is the porous network structure made of peptide alloy or basalt materials.
4. a kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution stated according to claim 1, special
Sign is:The nano metal coating is sprayed by nanosized copper particle or nanometer-level silver particle.
5. a kind of VOCs treatment device using concave convex rod absorption and superparamagnetic field magnetic solution according to claim 4, feature
It is:The nano metal coating with a thickness of 1-10 μm, the sizes of the nanoparticle or nano silver particles is 2-4nm.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112275039A (en) * | 2020-10-16 | 2021-01-29 | 安徽职业技术学院 | Purifying filter element and purifier comprising same |
CN114225627A (en) * | 2021-12-08 | 2022-03-25 | 上海绿强新材料有限公司 | Combined molecular sieve adsorbent for concentrating and purifying VOCs (volatile organic compounds), method and device |
-
2018
- 2018-09-25 CN CN201811119168.9A patent/CN108889066A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112275039A (en) * | 2020-10-16 | 2021-01-29 | 安徽职业技术学院 | Purifying filter element and purifier comprising same |
CN114225627A (en) * | 2021-12-08 | 2022-03-25 | 上海绿强新材料有限公司 | Combined molecular sieve adsorbent for concentrating and purifying VOCs (volatile organic compounds), method and device |
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