CN108744950A - A kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed - Google Patents
A kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed Download PDFInfo
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- CN108744950A CN108744950A CN201810765395.2A CN201810765395A CN108744950A CN 108744950 A CN108744950 A CN 108744950A CN 201810765395 A CN201810765395 A CN 201810765395A CN 108744950 A CN108744950 A CN 108744950A
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- 239000007789 gas Substances 0.000 title claims abstract description 46
- 206010070834 Sensitisation Diseases 0.000 title claims abstract description 40
- 230000008313 sensitization Effects 0.000 title claims abstract description 40
- 239000010815 organic waste Substances 0.000 title claims abstract description 10
- 239000007921 spray Substances 0.000 claims abstract description 55
- 239000000945 filler Substances 0.000 claims abstract description 32
- 238000012856 packing Methods 0.000 claims abstract description 31
- 239000000428 dust Substances 0.000 claims abstract description 26
- 238000011049 filling Methods 0.000 claims abstract description 25
- 230000015556 catabolic process Effects 0.000 claims abstract description 16
- 238000006731 degradation reaction Methods 0.000 claims abstract description 16
- 239000012452 mother liquor Substances 0.000 claims description 29
- 239000007788 liquid Substances 0.000 claims description 24
- 239000002516 radical scavenger Substances 0.000 claims description 8
- 238000001179 sorption measurement Methods 0.000 claims description 6
- 238000005507 spraying Methods 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 3
- 229920002472 Starch Polymers 0.000 claims description 3
- 238000009825 accumulation Methods 0.000 claims description 3
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 3
- 235000013305 food Nutrition 0.000 claims description 3
- 239000008103 glucose Substances 0.000 claims description 3
- 238000000465 moulding Methods 0.000 claims description 3
- 239000008107 starch Substances 0.000 claims description 3
- 235000019698 starch Nutrition 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims description 2
- 238000005259 measurement Methods 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims 1
- 230000000975 bioactive effect Effects 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 6
- 230000008929 regeneration Effects 0.000 abstract description 5
- 238000011069 regeneration method Methods 0.000 abstract description 5
- 238000001914 filtration Methods 0.000 abstract description 3
- 235000015097 nutrients Nutrition 0.000 abstract description 3
- 239000012855 volatile organic compound Substances 0.000 abstract description 3
- 230000000903 blocking effect Effects 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 238000011010 flushing procedure Methods 0.000 abstract 1
- 238000010521 absorption reaction Methods 0.000 description 5
- 238000009395 breeding Methods 0.000 description 4
- 230000001488 breeding effect Effects 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000002045 lasting effect Effects 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000010079 rubber tapping Methods 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 230000036760 body temperature Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- 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
- B01D53/84—Biological processes
-
- 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
-
- 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
- B01D53/46—Removing components of defined structure
- B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a kind of dust-laden organic waste gas treatment devices based on biochemical sensitization packed bed, are related to VOCs treatment field, can remove the dust in organic exhaust gas, and carry out biochemical degradation to organic exhaust gas and dust.The present invention includes：Babinet, packing groove, biochemical sensitization filling batch, spray system, reservoir, exhaust outlet.The device is sensitized bulky grain dust in filling batch blocking filtering organic exhaust gas by biochemistry; micronic dust is reduced because of flow velocity; the surface of biochemical sensitization filling batch is rested on, nutrient can be provided for biochemistry sensitization filler surface bioactive layer, keep the bioactivity of filling batch.Pass through cooling, flushing and circular regeneration, it is ensured that VOCs treatment effect and biochemical sensitization filler surface bioactive extend the filling batch replacement cycle, increase the service life of biochemical sensitization filling batch.
Description
Technical field
The present invention relates to VOCs treatment field more particularly to a kind of dust-laden organic wastes based on biochemical sensitization packed bed
Flash Gas Compression Skid System.
Background technology
Filler refers to the material being filled in other objects.In chemistry and environment-friendly engineering, filler refers to loaded on packed column
Interior inert solid material, effect are to increase the contact surface of solution-air, make its mutually strong mixing.In chemical products, filler
Also known as filler, refer to improve processing performance, Mechanical Properties of Products simultaneously (or) reduce the solid material of cost.At exhaust gas
Reason field is mainly used for contact oxidation technology, and micro- biochemistry can be accumulated on the surface of filler, is connect with increase and the surface of exhaust gas
It touches, degradation treatment is carried out to exhaust gas.
Traditional environmentally friendly exhaust-gas treatment industry is mainly with processing modes such as activated carbon adsorption, spray gas washing, photocatalysis, ozone
Based on, the processing for dust-laden exhaust gas needs to carry out effective dedusting before entering emission-control equipment.Filter method can be effective
The dirt of bulky grain is handled, and micronic dust can block sorbing material, spray port or covering catalysis material surface layer, use a period of time
Afterwards, exhaust-gas treatment effect is not up to standard, while the workloads such as maintenance, maintenance, replacement for causing post facility operation are larger.
Therefore, lack a kind of emission-control equipment in the prior art, short grained micronic dust can be handled, avoid micronic dust to place
The damage for managing device, prolongs the service life.
Invention content
The present invention provides a kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed, can remove organic waste
Dust in gas, and biochemical degradation is carried out to organic exhaust gas and dust.
A kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed, including：Babinet, packing groove, biochemistry are quick
Change filling batch, spray system, reservoir, exhaust outlet.
Reservoir is arranged in the bottom of box, is arranged packing groove above reservoir, the vertical section shape of packing groove be U-shaped or
V-arrangement.Biochemical sensitization filler, biochemistry sensitization filling adsorption and degradation little particle micronic dust, biochemistry sensitization filler are placed inside packing groove
Accumulation molding forms biochemical sensitization filling batch.Air-introduced machine is set among packing groove, when air-introduced machine works, on the inside of packing groove
Form negative pressure.Several holes are set outside packing groove, dust-laden organic exhaust gas enters packing groove by the hole of packing groove outer surface,
Hole diameter is less than biochemical sensitization filler.
Spray system extracts the liquid spraying filler slot in reservoir, and the nozzle of spray system is located at packing groove intermediate recess
The top of position.Liquid in reservoir is mother liquor, mother liquor degradation dust and exhaust gas.Exhaust outlet is arranged in top of the box.
Further, spray system includes circulating pump, spray apertures case, gas-liquid separator, and circulating pump connects reservoir, cycle
Pump connects spray apertures case by pipeline, and gas-liquid separator is installed on spray apertures case.The liquid in pumped reservoir is recycled, is first led to
The gas in gas-liquid separator removal liquid is crossed, then is sprayed by spray apertures case.
Further, mother liquor includes 0.1% ~ 2% strain, 1% ~ 2% pure glucose of analysis, 3% ~ 5% food starch,
Remaining is deionized water.
Further, Mu liquid Nong Du≤2 ‰, it is ensured that spraying effect；Temperature is 38 ± 2 DEG C, and for the breeding of strain, provide must
Standby condition.
Further, interior spray apertures pipe is also set up inside packing groove, interior spray apertures pipe is connected with inlet, and mother liquor passes through interior
Spray apertures pipe sprays into packing groove.
Further, scavenger fan is set below exhaust outlet, for exhaust gas to be discharged.
Further, setting temperature sensor and electric heater inside reservoir, for monitoring mother liquor temperature in real time, and
Mother liquor can be heated.
Further, scavenger fan is driven by motor, the temperature data of control module collecting temperature sensor measurement, motor
Rotating speed and electric heater are adjusted by control module.When mother liquor temperature is higher than preset temperature, control module accelerates scavenger fan to turn
It is dynamic, reduce case body temperature；When mother liquor temperature is less than preset temperature, control module control electric heater adds mother liquor
Heat.
Further, spray system single spray time≤15min.
The present invention operation principle be：
When air-introduced machine works, negative pressure is formed on the inside of packing groove, dust-laden organic exhaust gas is entered by the hole of packing groove appearance, had
Machine waste gas stream speed reduces, and bulky grain dust is trapped within biochemical sensitization packed bed outer surface；Little particle micronic dust is filled out with biochemistry sensitization
Expect the contact of surface bioactive film, because of bioactivity film tension, micronic dust is attracted to biochemical sensitization filler surface；In exhaust gas
Organic principle reacts, most with constantly contact of biochemical sensitization filler with filler surface bioactive film generation complex biochemical
It is degraded to nontoxic, odorless gas discharge eventually.
Absorption rests on the micronic dust of biochemical sensitization filler surface bioactive film surface, and organic principle is the bioactivity
The supply nutrient of strain in film maintains film surface bioactivity, and is finally degraded to common mineral matter.During use, it is
The continuous activity for ensuring biochemical sensitization filler surface bioactive film, need to maintain temperature in the dust-laden organic waste gas treatment device to exist
Between 15 DEG C ~ 50 DEG C, and supplement moisture content and nutrient.
Spray system is for adjusting and regenerating biochemical sensitization filler surface bioactive film.Regeneration spray can be by packing groove table
Face and biochemical sensitization filler surface dirt are rinsed into device in the reservoir of lower layer, and reservoir is provided with temperature sensor, control
Reservoir processed is in 38 ± 2 DEG C of constant temperature, and necessary requirement is provided for the breeding of strain.
Dust-laden organic exhaust gas, after being sensitized filling batch processing by biochemistry, organic exhaust gas is given birth on biochemistry sensitization filler surface
Redox reaction occurs for object active membrane, and gas with foreign flavor and micronic dust are substantially degraded in discharge gas；It is tieed up by circular regeneration
The bioactivity for holding biochemical sensitization filler surface bioactive film, to further improve the stabilization of bioactive layer attachment
Property, extend the replacement cycle of filler, reduces maintenance, use cost.
The beneficial effects of the invention are as follows：
Organic exhaust gas is sensitized filling batch by biochemistry, and the gas with foreign flavor and micronic dust in discharge gas are sensitized filling adsorption by biochemistry
Or degradation；Spray system draws the mother liquor in reservoir, and cycle hydro-peening biochemistry is sensitized filling batch, adjusts and regeneration is biochemical quick
Change filler surface bioactive film, more Xinshenghua is sensitized absorption and the degradation capability of filling batch；The temperature of mother liquor is supervised in real time
It surveys, mother liquor temperature is adjusted by fan or electric heater, ensures the breeding of strain in mother liquor；By the degradation of cycle, spray,
Renewal process, the absorption degradation dust and exhaust gas, filtering exhaust gases that the present invention can be lasting, avoids damage of the micronic dust to tapping equipment
Evil, prolongs the service life.
Description of the drawings
It to describe the technical solutions in the embodiments of the present invention more clearly, below will be to needed in the embodiment
Attached drawing is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the invention, for ability
For the those of ordinary skill of domain, without creative efforts, it can also be obtained according to these attached drawings other attached
Figure.
Fig. 1 is the structural schematic diagram of the present invention；
Fig. 2 is spray apertures pipe schematic diagram.
Wherein, 1- water discharging valves, 2- liquid outlets, 3- circulating pumps, 4- inlets, 5- biochemistry sensitization filling batch, spray in 6-
Drench hole pipe, 7- spray apertures pipe, 8- gas-liquid separators, 9- exhaust outlets, 10- scavenger fans, 11- motors, 12- babinets, 13- air inlets
Mouth, 14- reservoirs, 15- temperature sensors, 16- electric heaters, 71- branches spray apertures pipe, 72- spray apertures pipes main pipe, 73- gas
Liquid/gas separator supports plate.
Specific implementation mode
To make those skilled in the art more fully understand technical scheme of the present invention, With reference to embodiment to this
Invention is described in further detail.
The embodiment of the present invention provides a kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed, such as Fig. 1 institutes
Show, including：Babinet 18, packing groove 17, biochemical sensitization filling batch 5, spray system, reservoir 14, exhaust outlet 9.
Reservoir 14 is arranged in 12 bottom of babinet, and packing groove 17, the vertical section shape of packing groove 17 is arranged in 14 top of reservoir
Shape is U-shaped or V-arrangement, and liquid outlet 2 is arranged in 14 bottom of reservoir.
Biochemical sensitization filler, biochemistry sensitization filling adsorption and degradation little particle micronic dust are placed in 17 inside of packing groove, biochemical quick
Change filler accumulation molding, forms biochemical sensitization filling batch 5.Air-introduced machine, 17 outside setting of packing groove are set among packing groove 17
Several holes, hole diameter are less than biochemical sensitization filler.
Spray system includes：Liquid outlet 2, circulating pump 3, inlet 4, spray apertures case 7, gas-liquid separator 8.Reservoir 14 passes through
Liquid outlet 2 is crossed, circulating pump 3 is connected by pipeline, circulating pump 3 connects spray apertures case 7 by pipeline by inlet 4.
Liquid in reservoir 14 is mother liquor, and mother liquor can degrade dust and exhaust gas, and circulating pump 3 extracts mother liquor.Spray apertures case 7
Support plate 73 that gas-liquid separator 8 is installed by gas-liquid separator, spray apertures case 7 includes branch's spray apertures pipe 71 and spray apertures pipe
Main pipe 72, as shown in Fig. 2, branch's spray apertures pipe 71 connects spray apertures pipe main pipe 72, mother liquor is introduced into spray apertures pipe main pipe 72, female
Liquid is sprayed by branch's spray apertures pipe 71 again.Branch's spray apertures pipe 71 is located at the top of 17 intermediate recess position of packing groove, can be to the greatest extent
Measure large-scale spraying filler slot 17.Interior spray apertures pipe 6 is also set up inside packing groove 17, interior spray apertures pipe 6 connects inlet 4,
For mother liquor by interior spray apertures pipe 6 from internal spraying filler slot 17, spraying effect is more preferable.
Mother liquor includes：2% strain, the 2% pure glucose of analysis, 5% food starch, remaining is deionized water.Mother liquor is dense
Du≤2 ‰, temperature are 38 ± 2 DEG C.
Air inlet 13 is arranged in 12 left side of babinet, for entering air.Exhaust outlet 9,9 lower section of exhaust outlet is arranged in 12 top of babinet
Scavenger fan 10 is set.Scavenger fan 10 controls rotating speed by motor 11.14 inside setting temperature sensor 15 of reservoir and electricity add
Hot device 16.The temperature signal that control module collecting temperature sensor 15 is tested, when the temperature is excessively high, control module control motor 11
Rotating speed is improved, accelerates air flowing, reduces mother liquor temperature；When the temperature is too low, control module control electric heater 16 heats, and carries
High mother liquor temperature.
The beneficial effects of the invention are as follows：
Organic exhaust gas is sensitized filling batch by biochemistry, and the gas with foreign flavor and micronic dust in discharge gas are sensitized filling adsorption by biochemistry
Or degradation；Spray system draws the mother liquor in reservoir, and cycle hydro-peening biochemistry is sensitized filling batch, adjusts and regeneration is biochemical quick
Change filler surface bioactive film, more Xinshenghua is sensitized absorption and the degradation capability of filling batch；The temperature of mother liquor is supervised in real time
It surveys, mother liquor temperature is adjusted by fan or electric heater, ensures the breeding of strain in mother liquor；By the degradation of cycle, spray,
Renewal process, the absorption degradation dust and exhaust gas, filtering exhaust gases that the present invention can be lasting, avoids damage of the micronic dust to tapping equipment
Evil, prolongs the service life.
The above description is merely a specific embodiment, but scope of protection of the present invention is not limited thereto, any
Those familiar with the art in the technical scope disclosed by the present invention, all answer by the change or replacement that can be readily occurred in
It is included within the scope of the present invention.Therefore, protection scope of the present invention should be subject to the protection scope in claims.
Claims (9)
1. a kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed, which is characterized in that including：Babinet（18）,
Packing groove（17）, biochemical sensitization filling batch（5）, spray system, reservoir（14）, exhaust outlet（9）,
Babinet（12）Reservoir is arranged in bottom（14）, reservoir（14）Packing groove is arranged in top（17）, packing groove（17）It is vertical
Cross sectional shape is U-shaped or V-arrangement；
Packing groove（17）Biochemical sensitization filler, the biochemical sensitization filling adsorption and degradation little particle micronic dust are placed in inside, described
Biochemistry sensitization filler accumulation molding forms biochemical sensitization filling batch（5）；
Packing groove（17）Centre setting air-introduced machine, packing groove（17）Several holes are arranged in outside, and described hole diameter is less than described
Biochemistry sensitization filler；
The spray system extracts reservoir（14）Interior liquid spraying filler slot（17）, the nozzle of the spray system, which is located at, to be filled out
Hopper（17）The top of intermediate recess position；
Reservoir（14）Interior liquid is mother liquor, the mother liquor degradation dust and exhaust gas；
Babinet（12）Exhaust outlet is arranged in top（9）.
2. the apparatus according to claim 1, which is characterized in that the spray system includes circulating pump（3）, spray apertures case
（7）, gas-liquid separator（8）, circulating pump（3）Connect reservoir（14）, circulating pump（3）Spray apertures case is connected by pipeline（7）, spray
Drench hole case（7）Upper installation gas-liquid separator（8）.
3. the apparatus according to claim 1, which is characterized in that the mother liquor includes：0.1% ~ 2% strain, 1% ~ 2% point
Pure glucose is analysed, 3% ~ 5% food starch, remaining is deionized water.
4. device according to claim 3, which is characterized in that the Mu liquid Nong Du≤2 ‰, temperature are 38 ± 2 DEG C.
5. the apparatus according to claim 1, which is characterized in that packing groove（17）Inside also sets up interior spray apertures pipe（6）, interior
Spray apertures pipe（6）And inlet（4）Connection.
6. the apparatus according to claim 1, which is characterized in that exhaust outlet（9）Scavenger fan is arranged in lower section（10）.
7. the apparatus according to claim 1, which is characterized in that reservoir（14）Inside setting temperature sensor（15）And electricity
Heater（16）.
8. device according to claim 7, which is characterized in that scavenger fan（10）By motor（11）Driving, control module
Collecting temperature sensor（15）The temperature data of measurement, motor（11）Rotating speed and electric heater（16）By the control module tune
Section.
9. the apparatus according to claim 1, which is characterized in that spray system single spray time≤15min.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201810765395.2A CN108744950A (en) | 2018-07-12 | 2018-07-12 | A kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed |
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| CN201810765395.2A CN108744950A (en) | 2018-07-12 | 2018-07-12 | A kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115337870A (en) * | 2022-08-30 | 2022-11-15 | 陕西氢易能源科技有限公司 | Conical rotary packed bed dehydrogenation reactor suitable for organic liquid hydrogen storage |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06226033A (en) * | 1993-02-02 | 1994-08-16 | Ngk Insulators Ltd | Biological deodorizing method |
| EP1174172A2 (en) * | 2000-07-19 | 2002-01-23 | Emil A.J. D.I. Wieser-Linhart | Process and installation for gas purification |
| WO2008019687A1 (en) * | 2006-08-16 | 2008-02-21 | Turbovent Environment A/S | A system for decomposing smelling substances in air and use of the residual product of the decomposition |
| CN101549255A (en) * | 2009-05-05 | 2009-10-07 | 浙江省环境保护科学设计研究院 | Method for treating organic exhaust-gas generated in waste plastic granulation process |
| KR101139793B1 (en) * | 2011-12-29 | 2012-05-03 | 코오롱아로마트릭스(주) | Deodorizing apparatus with media multilayer type |
| CN103111184A (en) * | 2012-12-20 | 2013-05-22 | 华南理工大学 | Device for removing NOx (Nitrogen Oxide), SO2 (Sulfur Dioxide) and PM2.5 (Particulate Matter 2.5) simultaneously |
| CN103623693A (en) * | 2013-12-13 | 2014-03-12 | 北京伊普国际水务有限公司 | Efficient biological deodorization equipment |
| KR20150055684A (en) * | 2013-11-13 | 2015-05-22 | 신도이앤씨 (주) | Apparatus and method for treating hardly degradable malodorous gas |
| CN204395770U (en) * | 2014-12-05 | 2015-06-17 | 安徽华盛科技控股股份有限公司 | CIT biofiltration process emission-control equipment |
| CN205627618U (en) * | 2016-05-12 | 2016-10-12 | 南京林业大学 | Use a tower three mould integrated processing system s of bamboo charcoal for packing |
| CN209287036U (en) * | 2018-07-12 | 2019-08-23 | 江苏俊镕环保设备有限公司 | A kind of dust-laden organic waste gas treatment device based on biochemical sensitization packed bed |
-
2018
- 2018-07-12 CN CN201810765395.2A patent/CN108744950A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06226033A (en) * | 1993-02-02 | 1994-08-16 | Ngk Insulators Ltd | Biological deodorizing method |
| EP1174172A2 (en) * | 2000-07-19 | 2002-01-23 | Emil A.J. D.I. Wieser-Linhart | Process and installation for gas purification |
| WO2008019687A1 (en) * | 2006-08-16 | 2008-02-21 | Turbovent Environment A/S | A system for decomposing smelling substances in air and use of the residual product of the decomposition |
| CN101549255A (en) * | 2009-05-05 | 2009-10-07 | 浙江省环境保护科学设计研究院 | Method for treating organic exhaust-gas generated in waste plastic granulation process |
| KR101139793B1 (en) * | 2011-12-29 | 2012-05-03 | 코오롱아로마트릭스(주) | Deodorizing apparatus with media multilayer type |
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