CN106390715A - High temperature waste gas treatment device - Google Patents
High temperature waste gas treatment device Download PDFInfo
- Publication number
- CN106390715A CN106390715A CN201610864478.8A CN201610864478A CN106390715A CN 106390715 A CN106390715 A CN 106390715A CN 201610864478 A CN201610864478 A CN 201610864478A CN 106390715 A CN106390715 A CN 106390715A
- Authority
- CN
- China
- Prior art keywords
- waste gas
- atomization
- temperature waste
- treating apparatus
- atomizer
- 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.)
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- 239000002912 waste gas Substances 0.000 title claims abstract description 54
- 238000000746 purification Methods 0.000 claims abstract description 21
- 238000000926 separation method Methods 0.000 claims abstract description 10
- 230000005684 electric field Effects 0.000 claims abstract description 7
- 238000000889 atomisation Methods 0.000 claims description 37
- 239000007789 gas Substances 0.000 claims description 12
- 239000010453 quartz Substances 0.000 claims description 11
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 11
- 230000008676 import Effects 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 238000003780 insertion Methods 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 230000001066 destructive effect Effects 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 13
- 230000002159 abnormal effect Effects 0.000 description 6
- 239000000796 flavoring agent Substances 0.000 description 6
- 235000019634 flavors Nutrition 0.000 description 6
- 239000000779 smoke Substances 0.000 description 6
- 239000013618 particulate matter Substances 0.000 description 5
- 239000000428 dust Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 238000001727 in vivo Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000000844 anti-bacterial effect Effects 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
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002894 chemical waste Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002781 deodorant agent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- -1 ozone ion Chemical class 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 238000006303 photolysis reaction Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
-
- 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
- B01D53/26—Drying gases or vapours
- B01D53/266—Drying gases or vapours by filtration
-
- 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
- B01D53/76—Gas phase processes, e.g. by using aerosols
-
- 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
- B01D2259/804—UV light
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/818—Employing electrical discharges or the generation of a plasma
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Dispersion Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention discloses a high temperature waste gas treatment device. The device comprises a separator body and a cleaner body. Both sides of the separator body are provided with an inlet and an outlet. The inside of the cleaner body is provided with a uniform flow net, a low temperature plasma electrical field, a filter screen component, an ultraviolet lamp tube and an ultrasonic atomizer component sequentially from the inlet to the outlet. The filter screen component is levelly placed and both sides of the screen are fixed by a first flow block plate in crisscrossing arrangement. An air inlet connector and an air outlet are placed on the upper portion of one side of the separator body. The air outlet is communicated with the cleaner body. A separation block is mounted between the inner part of the separator body between the air inlet connector and the air outlet. A water storage trough is placed in the inner part of the separator body under the separation block. The water storage trough is connected with the atomizer nozzle through a high pressure pump. The atomizer nozzle is placed in the air inlet connector. The device can effectively eliminate the particles in waste gas, and carry out a destructive purification treatment to the waste gas molecules. The treatment effect is fine. The application scope is wide.
Description
Technical field
The present invention relates to field of Environment Protection is and in particular to a kind of high-temperature waste gas treating apparatus.
Background technology
Waste gas purification is primarily referred to as the industrial waste gas that produces for industrial site such as dust granules thing, flue gas flue dust, different
The work that taste gas, toxic and harmful are administered.Common waste gas purification has factory's fume and exhaust gas purifying, workshop dust to give up
Gas purification, organic waste-gas purification, the purification of waste gas abnormal flavour, acid-base waste gas purifying, purification of chemical waste gas etc..It is thus desirable to a kind of function
Emission-control equipment complete, that evolution effect is good, nowadays processing meanss are all more single, and the purification for many waste gas is generally up to
Less than Expected Results or not up to standard, it is unfavorable for environmental conservation.
Content of the invention
It is an object of the invention to the problem above overcoming prior art to exist, provide a kind of high-temperature waste gas treating apparatus,
The present invention can effectively remove the particulate matter in removing exhaust gas, and emission molecule is carried out destroy purification, and effect is good, the scope of application
Extensively.
For realizing above-mentioned technical purpose, reach above-mentioned technique effect, the present invention is achieved through the following technical solutions：
A kind of high-temperature waste gas treating apparatus, including separate body and purify body, described purification body two ends be provided with into
Mouth and outlet, described purification body interior is disposed with equal drift net, low-temperature plasma electric field, filtration along import to Way out
Screen component, quartz burner and ultrasonic atomization assembly, described screen modules are horizontally disposed with, and described screen modules both sides lead to
Cross and fix in the first choked flow fixed plate of being crisscross arranged, the described body that separates is arranged on the inlet end purifying body, described point
The side top of body is provided with inlet suction port and venthole, described venthole is connected with purifying body insertion, described air inlet
Separation body interior between joint and venthole is provided with skimming baffle, and the separation body interior below described skimming baffle sets
It is equipped with aqua storage tank, described aqua storage tank is connected with atomizer by high-pressure hydraulic pump, described atomizer is arranged in inlet suction port.
Further, described screen modules are rearranged successively from top to bottom by some active carbon layers.
Further, it is additionally provided with stop net between described skimming baffle and import, described stop net bottom face is provided with
Guiding gutter.
Further, described atomizer is arranged on the center of inlet suction port, described atomizer direction and waste gas
Airintake direction is oppositely arranged.
Further, described ultrasonic atomization equipment includes being atomized casing, and in described atomization box body, side bottom is provided with mist
Change plate, the atomization casing above described pulverizer plate is provided with deflector, described deflector is towards the atomization casing of adjacent side
Side wall, is reserved with passage and forms inlet air diversion space, institute with atomization box body between described deflector and this atomization wall box
State and be provided with blower fan on the external side roof part of the corresponding atomization box of inlet air diversion space, described atomization casing top is further opened with
Fog outlet.
Further, it is additionally provided with the second choked flow fixed plate, institute between described quartz burner and ultrasonic atomization assembly
State the second choked flow fixed plate to be crisscross arranged with the first adjacent choked flow fixed plate.
The invention has the beneficial effects as follows:
1st, this device first by the way of spraying by the particulate matter retention in waste gas, so it can be avoided that substantial amounts of solid
It is internal that grain entrance purifies this, it is to avoid is attached on the intrinsic purification assembly of purification, leads to produce the problems such as clean-up effect is poor, and
And the clean-up effect of low-temperature plasma electric field and quartz burner after removing these particulate matters, can be effectively improved, improve and purify
Quality.
2nd, pass through to stop the setting netted, the moisture content in the waste gas passing through can be retained, and flow back to along its surface guiding gutter
In aqua storage tank, it is to avoid excessive steam enters and purifies this in vivo, effectively reduce steam net on the damage of intraware and impact
Change quality.
3rd, waste gas produces high energy electron saboteur's structure, such as polymerization state, and in the air through low-temperature plasma high pressure
Oxygen, hydrone etc. through high energy region, be provoked into that to participate in deep oxidation for Strong oxdiative group ozone ion, hydroxyl etc. anti-
Should, UV ultraviolet bispectrum fluorescent tube is irradiated to emission molecule key, cracks big π key in phenyl ring in molecular link etc.；Produce simultaneously
Ozone oxidation pollutant.
4th, the position setting of screen modules and the first choked flow fixed plate of two sides are crisscross arranged position, by waste gas
Unawakened hydrone, aqueous vapor and some micro impurity are all adsorbed, and setting takes up room little, and ensure that and makes to give up
It is good that gas passes fully through screen modules using effect.
5th, ultrasonic atomization assembly can further purify waste gas, and front-end-of-line cannot be processed clean abnormal flavour completely
Or trace impurity by after atomizing the liquid into again with process after waste gas be combined, effective guarantee purification quality.
Described above is only the general introduction of technical solution of the present invention, in order to better understand the technological means of the present invention,
And can be practiced according to the content of description, below with presently preferred embodiments of the present invention and coordinate accompanying drawing describe in detail as after.
The specific embodiment of the present invention is shown in detail in by following examples and its accompanying drawing.
Brief description
In order to be illustrated more clearly that the technical scheme in embodiment of the present invention technology, below will be in the description of embodiment technology
The accompanying drawing of required use be briefly described it should be apparent that, drawings in the following description be only the present invention some are real
Apply example, for those of ordinary skill in the art, on the premise of not paying creative work, can also be according to these accompanying drawings
Obtain other accompanying drawings.
Fig. 1 is the overall structure diagram of the present invention.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation description is it is clear that described embodiment is only a part of embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of not making creative work
Embodiment, broadly falls into the scope of protection of the invention.
With reference to shown in Fig. 1, a kind of high-temperature waste gas treating apparatus, including separation body 2 and purification body 1, purification body two
End is provided with import 3 and outlet 4, purifies body interior and is disposed with equal drift net 5, low-temperature plasma along import to Way out
Electric field 6, screen modules 7, quartz burner 8 and ultrasonic atomization assembly 9, screen modules are horizontally disposed with, screen modules
Both sides are passed through to fix in the first choked flow fixed plate 10 being crisscross arranged, and separate body and are arranged on the inlet end purifying body, point
The side top of body is provided with inlet suction port 11 and venthole 12, venthole is connected with purifying body insertion, inlet suction port
Separation body interior and venthole between is provided with skimming baffle 13, and the separation body interior below skimming baffle is provided with storage
Tank 14, aqua storage tank is connected with atomizer 16 by high-pressure hydraulic pump 15, and atomizer is arranged in inlet suction port.During use,
Waste gas is accessed from the inlet suction port separating body, and the liquid in aqua storage tank is sprayed by atomizer with mist-like form, herein
Liquid can be the medicinal liquid of water or debugging, and after waste gas is contacted with water smoke, the granule within waste gas can be with the water in water smoke
Pearl contacts and is trapped, and after then striking skimming baffle, the globule can flow in aqua storage tank along it, and waste gas then bypasses and separates gear
Plate enters and purifies this in vivo, is arranged by equal drift net, waste gas uniformly enters purification body interior, is sufficiently full of in low temperature etc.
In ion electric field, high energy electron is produced and destroyed molecular structure by low-temperature plasma electric field high pressure, then pass through drainage screen
Some unnecessary moisture content, impurity absorption are filtered by assembly, are then irradiated by quartz burner and purify waste gas, final discharge.This dress
Put the waste gas use that can be suitable for most of species, the good speed of effect is fast.And ultrasonic atomization assembly can flexibly ensure
The standard of whole waste gas discharge, when the purification waste gas that test is discharged is exceeded, can be used by ultrasonic atomization assembly, by mist
Change liquid to evolve again waste gas, reach reinforcement clean-up effect.
Wherein, screen modules are rearranged successively from top to bottom by some active carbon layers, its surface by with both sides
In the same direction, waste gas plays good filtration effect through out-of-date it becomes possible to contact with surface completely to first choked flow fixed plate setting direction
Really, multilamellar active carbon layer can make full use of inner space and play multiple filtration effect, active adsorption granule, steam and abnormal flavour.
It is additionally provided with stop net 17 between skimming baffle and import, stop and be provided with guiding gutter, due to fog on net bottom face
It is kept completely separate before import cannot being entered back into after being combined with waste gas, therefore pass through to stop the setting netted, the globule in fog can be made
Striking stop net, thus being retained down, then aqua storage tank being flowed back to by guiding gutter.
Atomizer is arranged on the center of inlet suction port, and the water smoke of ejection uniform four can be scattered to whole air inlet connecting
In head, thus ensureing the contact surface of water smoke and waste gas, atomizer towards being oppositely arranged with gas inlet direction, such water smoke and
Waste gas formed convection current impact, the particulate matter in waste gas can because with water smoke in the globule clash into and be fused, finally because gravity realize
Effect detached with waste gas.Particulate matter in waste gas is trapped, it is to avoid purify this internal pile up, cause performance decline and
The shortening in life-span.
Ultrasonic atomization equipment includes being atomized casing 18, and in atomization box body, side bottom is provided with pulverizer plate 19, on pulverizer plate
It is provided with deflector 20, deflector is towards the atomization wall box of adjacent side, deflector and this atomization on the atomization casing of side
It is reserved with passage between wall box and form inlet air diversion space 21, the corresponding atomization of inlet air diversion space with atomization box body
Blower fan 22 is provided with casing outside top, atomization casing top is further opened with fog outlet.Ultrasonic atomization equipment passes through mist
Change liquid case feed flow, liquid is atomized by pulverizer plate, then the cooperation of blower fan and deflector by the liquid being atomized in atomization box body
Portion blows out, and last atomized liquid and waste gas fully merge, and so that waste gas is purified, and preamble can be purified by ultrasonic atomization equipment
In completely filter " clean " exhaust gas strengthen purify, such as in waste gas, abnormal flavour cannot be when UV photodissociation lamp tube removes completely, then
Deodorant liquid can be added, atomized liquid physical ability and waste gas fully merge so that in waste gas abnormal flavour up to standard.When in waste gas abnormal flavour up to standard and
When particulate matter noxious substance etc. is up to standard, sterilizing liquid etc. can be added, substantial amounts of by discharging during ultrasonic atomization
Anion and sterilizing liquid, the smog that in the air is floated, dust etc. produce electrostatic reaction so as to precipitation, can also have simultaneously
Effect removes formaldehyde, carbon monoxide, the harmful substance such as antibacterial, so that air is purified it is ensured that depuration quality.
It is additionally provided with the second choked flow fixed plate 23, the second choked flow fixed plate between quartz burner and ultrasonic atomization assembly
It is crisscross arranged with the first adjacent choked flow fixed plate, by setting of the second choked flow fixed plate and the first adjacent choked flow fixed plate
Put, waste gas cannot directly from stop mouth go out directly through, as shown in figure 1, waste gas from top enter quartz burner at, Ran Houhui
Stopped by the second choked flow fixed plate, then descending, then flow out below the second choked flow fixed plate, do not increasing quartz burner water
In the case of length square upwards, effectively improve the time of staying at quartz burner for the waste gas.
Described above to the disclosed embodiments, makes professional and technical personnel in the field be capable of or uses the present invention.
Multiple modifications to these embodiments will be apparent from for those skilled in the art, as defined herein
General Principle can be realized without departing from the spirit or scope of the present invention in other embodiments.Therefore, the present invention
It is not intended to be limited to the embodiments shown herein, and be to fit to and principles disclosed herein and features of novelty phase one
The scope the widest causing.
Claims (6)
1. a kind of high-temperature waste gas treating apparatus it is characterised in that：Including separation body and purification body, described purification body two ends
It is provided with inlet and outlet, described purification body interior is disposed with equal drift net, low-temperature plasma along import to Way out
Electric field, screen modules, quartz burner and ultrasonic atomization assembly, described screen modules are horizontally disposed with, described drainage screen
The first choked flow fixed plate that assembly both sides are passed through in being crisscross arranged is fixed, and the described body that separates is arranged on the import one purifying body
End, the described side top separating body is provided with inlet suction port and venthole, and described venthole is connected with purifying body insertion,
Separation body interior between described inlet suction port and venthole is provided with skimming baffle, and the separation below described skimming baffle is originally
Body is internally provided with aqua storage tank, and described aqua storage tank is connected with atomizer by high-pressure hydraulic pump, described atomizer be arranged on into
In gas joint.
2. a kind of high-temperature waste gas treating apparatus according to claim 1 it is characterised in that：Described screen modules are by some
Active carbon layer rearranges successively from top to bottom.
3. a kind of high-temperature waste gas treating apparatus according to claim 1 it is characterised in that：Described skimming baffle and import it
Between be additionally provided with stop net, described stop net bottom face is provided with guiding gutter.
4. a kind of high-temperature waste gas treating apparatus according to claim 1 it is characterised in that：Described atomizer be arranged on into
The center of gas joint, described atomizer direction is oppositely arranged with gas inlet direction.
5. a kind of high-temperature waste gas treating apparatus according to claim 1 it is characterised in that：Described ultrasonic atomization equipment bag
Include atomization casing, in described atomization box body, side bottom is provided with pulverizer plate, the atomization casing above described pulverizer plate is provided with
Deflector, described deflector is towards the atomization wall box of adjacent side, pre- between described deflector and this atomization wall box
Leave passage and form inlet air diversion space, the corresponding external side roof part of atomization box of described inlet air diversion space with atomization box body
On be provided with blower fan, described atomization casing top is further opened with fog outlet.
6. a kind of high-temperature waste gas treating apparatus according to claim 1 it is characterised in that：Described quartz burner and ultrasonic
It is additionally provided with the second choked flow fixed plate, described second choked flow fixed plate and the first adjacent choked flow fixed plate between ripple atomizing component
It is crisscross arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610864478.8A CN106390715A (en) | 2016-09-28 | 2016-09-28 | High temperature waste gas treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610864478.8A CN106390715A (en) | 2016-09-28 | 2016-09-28 | High temperature waste gas treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106390715A true CN106390715A (en) | 2017-02-15 |
Family
ID=59227966
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610864478.8A Withdrawn CN106390715A (en) | 2016-09-28 | 2016-09-28 | High temperature waste gas treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106390715A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108176671A (en) * | 2017-12-28 | 2018-06-19 | 徐工集团工程机械有限公司 | Salt bath cleaning equipment |
| CN110449263A (en) * | 2019-08-19 | 2019-11-15 | 中国科学院过程工程研究所 | A kind of electrical dust collector device and its processing method with groove profile filter assemblies |
| CN111097240A (en) * | 2019-12-30 | 2020-05-05 | 江苏腾龙生物药业有限公司 | Waste gas purification process |
| CN112023594A (en) * | 2020-09-15 | 2020-12-04 | 李佳佳 | Heat accumulating type organic waste gas purification device |
-
2016
- 2016-09-28 CN CN201610864478.8A patent/CN106390715A/en not_active Withdrawn
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108176671A (en) * | 2017-12-28 | 2018-06-19 | 徐工集团工程机械有限公司 | Salt bath cleaning equipment |
| CN110449263A (en) * | 2019-08-19 | 2019-11-15 | 中国科学院过程工程研究所 | A kind of electrical dust collector device and its processing method with groove profile filter assemblies |
| CN111097240A (en) * | 2019-12-30 | 2020-05-05 | 江苏腾龙生物药业有限公司 | Waste gas purification process |
| CN112023594A (en) * | 2020-09-15 | 2020-12-04 | 李佳佳 | Heat accumulating type organic waste gas purification device |
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| C06 | Publication | ||
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Application publication date: 20170215 |