CN201108798Y - Volatile organic contaminant removing apparatus - Google Patents
Volatile organic contaminant removing apparatus Download PDFInfo
- Publication number
- CN201108798Y CN201108798Y CNU2007201901922U CN200720190192U CN201108798Y CN 201108798 Y CN201108798 Y CN 201108798Y CN U2007201901922 U CNU2007201901922 U CN U2007201901922U CN 200720190192 U CN200720190192 U CN 200720190192U CN 201108798 Y CN201108798 Y CN 201108798Y
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- Prior art keywords
- reactor
- filler
- volatile organic
- pollutant removal
- field intensity
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- 239000000356 contaminant Substances 0.000 title claims description 10
- 239000000463 material Substances 0.000 claims abstract description 23
- 239000000945 filler Substances 0.000 claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 230000008676 import Effects 0.000 claims description 4
- 230000005684 electric field Effects 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 13
- 239000003344 environmental pollutant Substances 0.000 abstract description 10
- 231100000719 pollutant Toxicity 0.000 abstract description 10
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- 230000008569 process Effects 0.000 abstract description 4
- 230000002269 spontaneous effect Effects 0.000 abstract description 2
- 239000002957 persistent organic pollutant Substances 0.000 abstract 2
- 238000004804 winding Methods 0.000 abstract 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 21
- 239000012855 volatile organic compound Substances 0.000 description 14
- 239000007789 gas Substances 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 6
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 5
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 4
- 229910002113 barium titanate Inorganic materials 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
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- 150000008282 halocarbons Chemical class 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
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- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Treating Waste Gases (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a volatile organic pollutant removal device, which belongs to gaseous pollutant process technique field. The device comprises a gas inlet (1), a reactor (2), a power supply (3) and a gas vent (4), and is characterized in that the device also comprises insulating concrete discs (5) on the two ends of the reactor (2), an inner electrode (6) in the center of the reactor, an external electrode (7) winding on the external pipe of the reactor, a filler (8) in the reactor; the filler is a rasching ring coated with ferroelectric material; the holes in the two sides of the rasching ring are towards the outlet hole and the inlet hole of the reactor, and are placed evenly in the reactor. When the electric field intensity reaches to certain value, the filler has spontaneous polarization. The volatile organic pollutant removal device can cause the reactor to reduce the energy consumption under the precondition of keeping the pollutant removal rate, and is simple in structure and strong in applicability.
Description
Technical field
The utility model belongs to the gas pollutant processing technology field.
Background technology
Volatile organic matter (volatile organic compounds is called for short VOCs) is the general designation of a class organic compound, and their evaporation rate is big at normal temperatures, and is volatile.It is meant that saturated vapour pressure under the room temperature surpasses 70.91Pa or boiling point less than 260 ℃ organic matter, is the modal pollutant of industries dischargings such as oil, chemical industry, pharmacy, printing, building materials, spraying.The harm of VOCs mainly contains the following aspects: (1) most of VOCs have peculiar smell and poisonous, that many materials among the VOCs have is carcinogenic, teratogenesis, mutagenicity, these materials disturb the human endocrine system, have genetoxic and cause the serious consequence of " feminizing ", environmentally safe and human survival procreation constitutes a threat to; (2) under the irradiation of light, many VOCs are easy to and some oxidant generation photochemical reactions, generate photochemical fog, are detrimental to health, and influence crop growth; (3) some halogenated hydrocarbons may cause the destruction of ozone layer, as chlorofluorocarbons (CFCs) and CFC; (4) a lot of VOCs belong to inflammable, explosive compounds, produce to enterprise and cause big hidden danger.
Traditional VOCs processing method has: firing method, absorption process, condensation method, absorption method etc.All there is certain defective technically, economically in these methods: or initial outlay and operating cost height, or treatment effect is undesirable, or subsequent treatment is improper to cause secondary pollution.Especially the waste gas of low concentration, atm number does not find cost-effective improvement method as yet.In numerous environmental pollution improvement's new technologies, lower temperature plasma technology is handled poisonous and hard-degraded substance as a kind of high efficiency, low energy consumption, the scope of application is wide, treating capacity is big, simple to operate environment protection novel, is the focus of Recent study.Patent 200410014135.X discloses a kind of lower temperature plasma technology of handling volatile organic matter, realizes the removal of pollutant by the method for electrion, but needs to consume certain energy, and its structure chart is by shown in Figure 1.Patent 200410014131.1 discloses a kind of lower temperature plasma technology of handling microorgranic contaminant, utilizes the method for electrion that microorgranic contaminant is removed equally.Patent 200410014133.0 discloses H in the lower-temperature plasma industrial waste gas treatment
2S and C
2The method of S under pulse power effect, forms the low temperature plasma field in plasma reactor, make H
2S and C
2S is converted into the SO of odorless low toxicity
2Above-mentioned patent all is pollutant to be realized removing under the high voltage source effect, consumes certain energy in actual moving process.
The utility model content
The purpose of this utility model is to provide a kind of low temperature plasma VOCs treating apparatus of novel, efficient, low energy consumption.
The utility model is the reactor that corona discharge and dielectric barrier discharge combine to be produced plasma come degradation organic waste gas.In reactor, be added with ferroelectric material, utilize these materials to issue the characteristics of sending out polarization of being conigenous, apply energy or under the condition of certain energy, effectively improve pollutants removal rate effective reduction the on the basis that guarantees contaminant removal efficiency in high electric-field intensity.When additional power source is applied on the dielectric layer, dielectric filler will polarize, near each filler, will form very strong electric field, thereby generation shelf depreciation, when the alternating voltage that applies has surpassed corona generation initial voltage, will be full of a large amount of high energy electrons in the reactor, these electronics and contaminant molecule collide mutually, thereby improve the treatment effeciency of pollutant.Electric field is different to the influence of the dielectric constant of different medium.Polarization intensity for linear dielectric materials is directly proportional with electric-field intensity, and dielectric constant and electric-field intensity relation are very little.To nonlinear material, its polarization intensity becomes nonlinear relation with electric-field intensity, and the dielectric constant of material also becomes non-linear relation with electric-field intensity, and the ferroelectric material of selecting for use in the utility model belongs to nonlinear material.Accompanying drawing 2 is the relation curve of ferroelectric dielectric constant and electric-field intensity, as can be seen from the figure, the dielectric constant of ferroelectric material and the relation of electric-field intensity are non-linear relation, under certain electric-field intensity, the sudden turn of events can take place in the dielectric constant of ferroelectric material, the reactor electric field is sharply increased, thereby can realize degraded effectively for VOCs.
The reactor assembly structure as shown in Figure 3, comprise gas feed 1, reactor 2, power supply 3, gas vent 4, it is characterized in that, also comprise the insulating trip 5 at reactor two ends, the interior electrode 6 of reactor center, the external electrode 7 that the reactor outer tube is tied with, filler 8 in the reactor, filler is the Raschig ring that scribbles ferroelectric material, and the import of the hole orientating reaction device of Raschig ring both sides and outlet evenly are positioned in the reactor.
The ferroelectric material that reactor is selected for use in the utility model comprises order-disorder type ferroelectric natrium nitrosum material and displacement ferroelectric barium-titanate material.These materials are flour, select for use ceramic raschig rings as host material in the utility model, the ferroelectric pulverulent material is coated in the ceramic raschig rings surface, these ceramic raschig rings evenly are positioned in the reactor, can effectively utilize space reactor on the one hand, on the other hand, the import of the hole orientating reaction device of Raschig ring both sides and outlet can reduce the air-flow running resistance to reduce the pressure drop of reactor.
Volatile organic contaminant removal device provided by the utility model is compared difference with existing apparatus and is: be added with the ferroelectric filler in reactor, after electric-field intensity reaches certain value, filler generation spontaneous polarization can make reactor cut down the consumption of energy under the prerequisite that keeps pollutants removal rate.The natrium nitrosum filler of selecting for use simultaneously is easy to industrial applications owing to low cost.This reactor can effectively reduce the specific energy consumption of reactor for treatment pollutant, and simple in structure, and applicability is strong.
Description of drawings
Fig. 1 is the disclosed VOCs treating apparatus of a patent 200410014135.X structure chart, and gas feed 1, reactor 2, power supply 3, gas vent 4 are wherein arranged.
Fig. 2 is the relation curve of ferroelectric material dielectric constant and effective field intensity.
Fig. 3 is the VOCs treating apparatus structure chart that the utility model provides, and the insulating trip 5 at gas feed 1, reactor 2, power supply 3, gas vent 4, reactor two ends, the interior electrode 6 of reactor center, the external electrode 7 that the reactor outer tube is tied with, the filler 8 in the reactor are wherein arranged.
Fig. 4 is that the VOCs treating apparatus that provides of the utility model is for toluene clearance design sketch.
The specific embodiment
Reactor material is a quartz glass tube, and wall thickness 2.4mm, internal diameter are 17.9mm, and external diameter is 20.3mm.Adopt the teflon insulation sheet that reactor is sealed at the reactor two ends, the circular hole of respectively opening one φ=4mm at two ends is as handling gas feed and outlet, in the reactor center position is interior electrode, material is φ=1.62mm tungsten filament, and the quartz glass tube outer wall is wrapped with an iron net as external electrode and do ground connection and handle.Reactor Raschig ring filler size is internal diameter 5.6mm, external diameter 9.2mm, and length is 10.5mm, is coated with ferroelectric material on Raschig ring matrix, coating thickness is 0.5mm.Between internal and external electrode, connect high voltage source providing of reactor energy is provided, in discharge process, reach filling surface in the reactor and produced a large amount of high energy electrons and active group, VOC enters reactor by import 1, in reactor and active group and high energy electron generation series of physical chemical reaction, make the nontoxic gas molecule of the final formation of contaminant molecule, discharge by gas outlet 4 at last.Fig. 3 is for being the result that target contaminant experimentizes with volatile organic matter representative toluene, experiment condition be power supply to apply voltage be 10kV, the toluene inlet flow rate is about 2400mg/m
3Its reflection be under the different electrical power frequency condition, to be added with the barium titanate filler, the removal efficient of toluene under natrium nitrosum filler and the no filler, when supply frequency is 35KHz, do not add the reactor of filler, the reactor that is added with the reactor of natrium nitrosum filler and is added with the barium titanate filler is respectively 68.7% for the clearance of toluene, 76.8% and 89.6%, the reactor that is added with barium titanate and natrium nitrosum filler all is higher than no packed column reactor for the clearance of toluene, in other words, under the prerequisite that keeps the toluene clearance, the reactor that is added with filler is lower than the energy that no packed column reactor needs.
Claims (1)
1, a kind of volatile organic contaminant removal device, comprise gas feed (1), reactor (2), power supply (3), gas vent (4), it is characterized in that, also comprise the insulating trip (5) at reactor (2) two ends, the interior electrode (6) of reactor center, the external electrode (7) that the reactor outer tube is tied with, filler in the reactor (8), described filler is the Raschig ring that scribbles ferroelectric material, and the import of the hole orientating reaction device of Raschig ring both sides and outlet evenly are positioned in the reactor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201901922U CN201108798Y (en) | 2007-11-16 | 2007-11-16 | Volatile organic contaminant removing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201901922U CN201108798Y (en) | 2007-11-16 | 2007-11-16 | Volatile organic contaminant removing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201108798Y true CN201108798Y (en) | 2008-09-03 |
Family
ID=39893314
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201901922U Expired - Lifetime CN201108798Y (en) | 2007-11-16 | 2007-11-16 | Volatile organic contaminant removing apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201108798Y (en) |
-
2007
- 2007-11-16 CN CNU2007201901922U patent/CN201108798Y/en not_active Expired - Lifetime
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20080903 |