CN106669343A - Electric mist dust removal equipment adopting turbulent coagulation - Google Patents
Electric mist dust removal equipment adopting turbulent coagulation Download PDFInfo
- Publication number
- CN106669343A CN106669343A CN201710017477.4A CN201710017477A CN106669343A CN 106669343 A CN106669343 A CN 106669343A CN 201710017477 A CN201710017477 A CN 201710017477A CN 106669343 A CN106669343 A CN 106669343A
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- Prior art keywords
- electric
- mist
- power
- electric mist
- dust removal
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- 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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- 239000003595 mist Substances 0.000 title claims abstract description 72
- 239000000428 dust Substances 0.000 title claims abstract description 68
- 230000015271 coagulation Effects 0.000 title abstract 10
- 238000005345 coagulation Methods 0.000 title abstract 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 60
- 238000004062 sedimentation Methods 0.000 claims abstract description 25
- 238000001816 cooling Methods 0.000 claims abstract description 24
- 239000002002 slurry Substances 0.000 claims abstract description 23
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000003546 flue gas Substances 0.000 claims abstract description 12
- 238000009833 condensation Methods 0.000 claims description 45
- 230000005494 condensation Effects 0.000 claims description 45
- 230000005611 electricity Effects 0.000 claims description 22
- 239000007789 gas Substances 0.000 claims description 21
- 238000004581 coalescence Methods 0.000 claims description 18
- 239000000779 smoke Substances 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 10
- 238000000151 deposition Methods 0.000 claims description 7
- 230000008595 infiltration Effects 0.000 claims description 7
- 238000001764 infiltration Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 7
- 239000008187 granular material Substances 0.000 claims description 6
- 240000002853 Nelumbo nucifera Species 0.000 claims description 4
- 235000006508 Nelumbo nucifera Nutrition 0.000 claims description 4
- 235000006510 Nelumbo pentapetala Nutrition 0.000 claims description 4
- 239000007921 spray Substances 0.000 claims description 4
- 201000008827 tuberculosis Diseases 0.000 claims description 4
- 238000009826 distribution Methods 0.000 claims description 3
- 239000000706 filtrate Substances 0.000 claims description 3
- 229920006395 saturated elastomer Polymers 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 description 10
- 239000002245 particle Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 239000012530 fluid Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000000889 atomisation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000009297 electrocoagulation Methods 0.000 description 1
- 238000005367 electrostatic precipitation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000001869 rapid Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 230000005514 two-phase flow Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
Abstract
The invention discloses electric mist dust removal equipment adopting turbulent coagulation. The equipment comprises a power coagulation cooling dust removal pipe and an electric mist sedimentation tower, wherein the bottom of the power coagulation cooling dust removal tube is communicated with the middle of the electric mist sedimentation tower through a pipeline, a flue gas inlet pipe is arranged at the top of the power coagulation cooling dust removal pipe, a nozzle is arranged at the lower part of the power coagulation cooling dust removal pipe and communicated with a power coagulation water generator, and a power coagulation water supply pump is arranged on the power coagulation water generator and communicated with a clear water tank; an electric mist generator and an anode plate are arranged in the electric mist sedimentation tower, the anode plate is arranged above the electric mist generator, an electric mist dust removal area is arranged below the electric mist generator, a slurry collecting tank is arranged at the bottom of the electric mist dust removal area, the top of the electric mist sedimentation tower is communicated with an induced draft fan, and the electric mist generator is communicated with an electric mist dust removal water supply pump. The electric mist dust removal equipment adopting turbulent coagulation is high in dust removal efficiency, high in automation degree and low in energy consumption and particularly increases fine dust removal efficiency, and water can be recycled.
Description
Technical field
The present invention relates to turbulent flow coalescence electricity mist cleaner, belongs to environmental technology field.
Background technology
What rapids rushed that coalescence utilizes is foamed cleaning technology, except that it creatively make use of hydromechanical correlation
Theory, using brand-new, more simple and reliable method more stable effective froth bed is produced.Its operation principle is：
1st, using foamed cleaning technology, using foam surface layer greatly, gas-liquid interface renewal speed be exceedingly fast the characteristics of, enter
The efficient mass-and heat-transfer process of row.
2nd, in biphase gas and liquid flow kinety system, the flow pattern of fluid depends on the relative mass flow rates of gas-liquid two-phase, certain
Under the conditions of can form stable froth bed.
3rd, froth bed is that gas-liquid two-phase interacts to be formed in intersection, and the position of its interface depends on gas-liquid two-phase
Momentum balance relation.Under conditions of momentum balance, interface will stabilise at a position, and work as the generation of gas-liquid relative momentum
During change, the fluid flow direction movement that interface can increase to momentum, until reaching new balance.
The height of wet purification device efficiency depends on the consumption of its energy, because turbulent flow coalescence scrubber is in running
In both make use of the energy of air-flow, also dexterously make use of the energy of liquid stream.Water mist dust-removing is that one kind is extensive in produce reality
Using and simple and practical dedusting method, by humid control of the spraying to material, play important to reducing dust yield
Effect, but it is relatively low to the control efficiency of fine dust to spray, and particularly floats the subparticle in air, with the collision of water smoke grain
Contact probability is low, and most of dust bypasses droplet and suspends in atmosphere.In order to improve the control effect to dust, strengthen droplet
With the collision probability of powder dust particle, by water smoke particle diameter in corona field action lower band electric charge, under electrostatic force, strengthen dust
Mutually collide with droplet, reach the purpose of trapping dust.
Charged water spray dedusting technology is that the water of atomization is charged, is combined with dust by effects such as electrostatic attractions, makes dust
Grain cohesion becomes big and removes.Motion in cleaner unit is dynamic for dilute gas-solid two-phase flow, and in operation stress mainly has powder dust particle
Electrostatic force, viscous resistance and particle weight power.Charged water spray dedusting is the combination of electrostatic precipitation and wet dust removal, overcomes spraying to remove
The dirt problem low to fine dust capture rate.
The purpose of water fog charge is that the droplet for forming spraying obtains higher electric charge, increases water smoke and dust collider
Meeting, so as to improve arresting efficiency of the water smoke to dust.Water fog charge mode is divided into corona charging and injection charged two in this equipment
Kind.
Corona electricity makes inductance loop (i.e. positive plate) using tinsel, and plus high-pressure electricity, releases inductance loop on inductance loop
Electrostatic discharge lotus, nozzle is located at inductance loop center, when water smoke passes through inductance loop, under electric field action, is allowed to take and sensing
The electric charge (negative electricity) of ring opposite polarity.
The method is a kind of effectively charged mode, makes water smoke obtain higher electric charge (water smoke charge-mass ratio).Water fog charge
Afterwards, increase collision, diffusion, the retention probability with powder dust particle, improve the dust removing effects that fine dirt is particularly to dust.
The content of the invention
In view of this, the invention provides turbulent flow coalescence electricity mist cleaner, efficiency of dust collection height, in particular improve fine
The removal efficiency of dirt, high degree of automation, energy consumption is low, water reusable edible.
The present invention solves above-mentioned technical problem by following technological means：
The turbulent flow coalescence electricity mist cleaner of the present invention, it includes turbulent flow coalescence electricity mist cleaner, and it includes that power coagulates
And lower the temperature dust removing tube and electric mist sedimentation tower, the bottom of the power condensation cooling dust removing tube is with the middle part of electric mist sedimentation tower by pipe
Road is connected, and flue gas inlet pipe is provided with the top of the power condensation cooling dust removing tube, and the bottom of power condensation cooling dust removing tube sets
Nozzle is equipped with, the nozzle is connected with power condensation water generator, power condensation feedwater is provided with power condensation water generator
Pump, the power condensation feed pump is connected with clear water reserviors, and in the electric mist sedimentation tower electric fog generator and positive plate, institute are provided with
The top that positive plate is arranged on electric fog generator is stated, the lower section of electric fog generator is electric mist dedusting area, the bottom of electric mist dedusting area
Slurry collecting groove is provided with, the top of the electric mist sedimentation tower connects with air-introduced machine, electric fog generator and electric mist depositing dust feed pump
Connection, electric mist depositing dust feed pump is connected with clear water reserviors, and slurry collecting groove is connected with slurry feeding pump, is set on the slurry feeding pump
Filter is equipped with, the power condensation water generator, electric fog generator and positive plate provide electric energy by HVDC power distribution cabinet.
Negative charge is sent in the power condensation water generator, power condensation water band after power condensation water generator is negative
The power condensation area phase of electric charge bottom-up ejection from nozzle, electronegative water and flue gas in power condensation cooling dust removing tube
Meet, a part of little particle is directly landed by electrostatic attraction in flue gas, the volume increase after water smoke infiltration of another part granule,
Automatic sedimentation gets off.
The quality and volume is more fine or dust of the not charged sedimentation of airflow fluctuation in power condensation cooling dust removing tube, with
Air-flow is entered behind electric mist dedusting area, and charged mist will be blended further with dust infiltration so as to charged, and reach electric mist dedusting area
To vapo(u)rous state, fine dust may act as tuberculosis in vapo(u)rous state, the saturated vapor sent with electric fog generator
Sedimentation is formed, is dropped in slurry collecting groove.
The positive plate is inductance loop made by tinsel, and plus high-pressure electricity, makes inductance loop release electrostatic lotus on inductance loop,
Tail gas after electric mist dedusting area electricity mist is processed carries a large amount of negative charges, and tail gas when positive plate, condense by the electric discharge on positive plate,
Remove the steam of tail gas.
Filtering material is provided with the filter, the slurry in slurry collecting groove returns clear through filtering material, filtrate
Pond, arranges outside filtering residue.
The invention has the beneficial effects as follows：
1st, the purification efficiency of turbulent flow coalescence electricity mist cleaner is far above the legacy equipments such as void tower, packed tower, especially to de-
Except subparticle more effectively.
2nd, device structure is simple, and convenient operating maintenance, gas passage is unblocked, simple structure, and reliability is very high to be difficult
Damage, Operation and Maintenance is simple, and service cycle is long, equipment low-profile, reduces investment outlay and takes up an area, intensity and sealing problem are easy to solution
Certainly, number of devices and floor space are all few than traditional process, and device configuration is flexibly, applied widely, almost can be used for appointing
What gas purification process, good cooling effect can be used to process various high-temperature gases, be not easily blocked, and the dustiness in gas is almost
Without limiting, the permission solid content in circulation fluid is high.
3rd, energy consumption is low, water reusable edible, after slurries filtration, clear water reusable edible, and while efficiency is improved, energy consumption is more
It is low.
Description of the drawings
With reference to the accompanying drawings and examples the invention will be further described.
Fig. 1 is the structural representation of the present invention.
Specific embodiment
Below with reference to accompanying drawing, the present invention is described in detail, as shown in Figure 1：The turbulent flow coalescence electricity mist of the present embodiment is removed
Dirt equipment, it includes power condensation cooling dust removing tube 1 and electric mist sedimentation tower 2, the bottom of the power condensation cooling dust removing tube 1 with
The middle part of electric mist sedimentation tower 2 is provided with flue gas inlet pipe 3, is moved by pipeline communication, the top of the power condensation cooling dust removing tube 1
The bottom of power coalescence cooling dust removing tube 1 is provided with nozzle 4, and the nozzle 4 is connected with power condensation water generator 5, power condensation
Power condensation feed pump 6 is provided with water generator 5, the power condensation feed pump 6 is connected with clear water reserviors 7, the electric mist sinks
Electric fog generator 8 and positive plate 9 are provided with drop tower 2, the positive plate 9 is arranged on the top of electric fog generator 8, and electric mist occurs
The lower section of device 8 is electric mist dedusting area 10, and the bottom of electric mist dedusting area 10 is provided with slurry collecting groove 11, the electric mist sedimentation tower 2
Top connect with air-introduced machine 12, electric fog generator 8 is connected with electric mist depositing dust feed pump 13, electric mist depositing dust feed pump 13 and clear water
Pond 7 connects, and slurry collecting groove 11 is connected with slurry feeding pump 14, and filter 15 is provided with the slurry feeding pump 14, described
Power condensation water generator 5, electric fog generator 8 and positive plate 9 provide electric energy by HVDC power distribution cabinet 16.
Negative charge, power condensation water band after power condensation water generator 5 are sent in the power condensation water generator 5
Negative charge bottom-up ejection from nozzle 4, electronegative water and flue gas are in the power condensation area of power condensation cooling dust removing tube 1
Meet, a part of little particle is directly landed by electrostatic attraction in flue gas, another part granule volume after water smoke infiltration increases
Greatly, automatic sedimentation gets off.
The quality and volume is more fine or dust of the not charged sedimentation of airflow fluctuation in power condensation cooling dust removing tube 1,
Enter behind electric mist dedusting area 10 with air-flow, charged mist will be blended further with dust infiltration so as to charged, and make electric mist dedusting
Area 10 reaches vapo(u)rous state, and fine dust may act as tuberculosis in vapo(u)rous state, full with what electric fog generator 8 sent
Formed with steam and settled, dropped in slurry collecting groove 11.
The positive plate 9 is inductance loop made by tinsel, and plus high-pressure electricity, makes inductance loop release electrostatic on inductance loop
Lotus, the tail gas after the electric mist in electric mist dedusting area 10 is processed carries a large amount of negative charges, and tail gas is put when positive plate 9 on positive plate 9
Electrocoagulation, removes the steam of tail gas.
Filtering material is provided with the filter 15, the slurry in slurry collecting groove 11 is returned through filtering material, filtrate
Clear water reserviors 7 are returned, is arranged outside filtering residue.
Air-liquid (charged) with certain flow and flow velocity relation in flue gas inlet pipe 3 is biphase in power condensation cooling dedusting
Meet in pipe 1, on the one hand the result that both interact sets up a froth bed, using froth bed gas in gas passage
The characteristics of liquid contact surface area is very big, renewal speed is exceedingly fast, here carries out efficient mass-and heat-transfer process；On the other hand, utilize
Momentum balance principle makes froth bed swim in power condensation cooling dust removing tube 1, and interior in pipe with the change of gas-liquid relative momentum
Fluctuate, make the sufficiently charged coalescence of tiny dust in gas granule and settle.
Water is by negatively charged ejection bottom-up from nozzle 4, electronegative water and gas after power condensation water generator 5
Meet in power condensation area, a part of little particle is directly landed by electrostatic attraction in flue gas；Another part granule passes through water smoke
Volume increase after infiltration, automatic sedimentation gets off.
For in turbulent flow coalescence area because quality and volume are more fine or the dust of the not charged sedimentation of airflow fluctuation, with air-flow
Into after electric mist dedusting area 10, charged mist further will infiltrate blending with it so as to charged, and make the electric atmosphere of mist dedusting area 10
Reach vapo(u)rous state.Fine dust may act as tuberculosis in vapo(u)rous state, and with saturated vapor " rainfall " is formed, and reach
Depositing dust purpose.Because the tail gas Jing after electric mist is processed carries a large amount of electric charges (negative electricity), therefore sun is set on the electric top of mist dedusting area 10
Pole plate 9, makes charged gas and vapor discharge on positive plate 9 cohesion (positive and negative attracting), can effectively remove the steam of tail gas.
Finally illustrate, above example is only unrestricted to illustrate technical scheme, although with reference to compared with
Good embodiment has been described in detail to the present invention, it will be understood by those within the art that, can be to the skill of the present invention
Art scheme is modified or equivalent, and without deviating from the objective and scope of technical solution of the present invention, it all should cover at this
In the middle of the right of invention.
Claims (5)
1. turbulent flow coalescence electricity mist cleaner, it is characterised in that：Including power condensation cooling dust removing tube (1) and electric mist sedimentation tower
(2), the bottom of power condensation cooling dust removing tube (1) passes through pipeline communication, the power with the middle part of electric mist sedimentation tower (2)
Flue gas inlet pipe (3) is provided with the top of coalescence cooling dust removing tube (1), the bottom of power condensation cooling dust removing tube (1) is provided with spray
Mouth (4), the nozzle (4) connects with power condensation water generator (5), arranges dynamic solidifying on power condensation water generator (5)
And feed pump (6), the power condensation feed pump (6) connects with clear water reserviors (7), and in the electric mist sedimentation tower (2) electricity is provided with
Fog generator (8) and positive plate (9), the positive plate (9) is arranged on the top of electric fog generator (8), electric fog generator (8)
Lower section is electric mist dedusting area (10), and the bottom of electric mist dedusting area (10) is provided with slurry collecting groove (11), the electric mist sedimentation tower
(2) top connects with air-introduced machine (12), and electric fog generator (8) connects with electric mist depositing dust feed pump (13), electric mist depositing dust feedwater
Pump (13) is connected with clear water reserviors (7), and slurry collecting groove (11) is connected with slurry feeding pump (14), on the slurry feeding pump (14)
Filter (15) is provided with, the power condensation water generator (5), electric fog generator (8) and positive plate (9) are by HVDC
Power distribution cabinet (16) provides electric energy.
2. turbulent flow coalescence according to claim 1 electricity mist cleaner, it is characterised in that：The power condensation water generator
(5) send negative charge in, power condensation water after power condensation water generator (5) it is negatively charged from from nozzle (4) from it is lower to
Upper ejection, electronegative water and flue gas meet in the power condensation area of power condensation cooling dust removing tube (1), a part of little in flue gas
Granule is directly landed by electrostatic attraction, and another part granule volume increase after water smoke infiltration, automatic sedimentation gets off.
3. turbulent flow coalescence according to claim 2 electricity mist cleaner, it is characterised in that：In power condensation cooling dust removing tube
(1) interior quality and volume be more fine or dust of the not charged sedimentation of airflow fluctuation, enters after electric mist dedusting area (10) with air-flow,
Charged mist will be blended further with dust infiltration so as to charged, and make electric mist dedusting area (10) reach vapo(u)rous state, micro-
Fine dust may act as tuberculosis in vapo(u)rous state, and with the saturated vapor that electric fog generator (8) sends sedimentation is formed, and drop to
In slurry collecting groove (11).
4. turbulent flow coalescence according to claim 3 electricity mist cleaner, it is characterised in that：The positive plate (9) is metal
Inductance loop made by silk, plus high-pressure electricity on inductance loop, after processing inductance loop release electrostatic lotus, electric mist dedusting area (10) electricity mist
Tail gas carry a large amount of negative charges, tail gas when positive plate (9), on positive plate (9) electric discharge cohesion, remove tail gas water
Vapour.
5. turbulent flow coalescence according to claim 4 electricity mist cleaner, it is characterised in that：Arrange in the filter (15)
There is filtering material, the slurry in slurry collecting groove (11) returns clear water reserviors (7), arranges outside filtering residue through filtering material, filtrate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710017477.4A CN106669343A (en) | 2017-01-11 | 2017-01-11 | Electric mist dust removal equipment adopting turbulent coagulation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710017477.4A CN106669343A (en) | 2017-01-11 | 2017-01-11 | Electric mist dust removal equipment adopting turbulent coagulation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106669343A true CN106669343A (en) | 2017-05-17 |
Family
ID=58850361
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710017477.4A Pending CN106669343A (en) | 2017-01-11 | 2017-01-11 | Electric mist dust removal equipment adopting turbulent coagulation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106669343A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109468990A (en) * | 2018-11-07 | 2019-03-15 | 山东港基建设集团有限公司 | A kind of building cooling dust-extraction unit |
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|---|---|---|---|---|
| DE2533690A1 (en) * | 1974-07-26 | 1976-02-05 | Michael Joseph Pilat | ELECTROSTATIC WET LAUNDRY AND COLLECTOR ARRANGEMENT |
| US20060204407A1 (en) * | 2005-03-09 | 2006-09-14 | Mcwhorter Edward M | Coal flue gas scrubber |
| WO2009113269A1 (en) * | 2008-03-11 | 2009-09-17 | ダイキン工業株式会社 | Air processor |
| CN102145316A (en) * | 2010-02-04 | 2011-08-10 | 山东大学 | Synergistic spray charging and electrostatic dust collecting method and device |
| CN103056030A (en) * | 2012-12-04 | 2013-04-24 | 武汉科技大学 | Wet-type vibrating-wire bipolar electrostatic coagulation deduster |
| CN204469472U (en) * | 2014-12-20 | 2015-07-15 | 艾尼科环保技术(安徽)有限公司 | Pre electrified coalescence sack cleaner |
| CN105797524A (en) * | 2016-05-06 | 2016-07-27 | 江苏大学 | Heteropolar electric charge fogdrop coalescence dust-removing device and method thereof |
| CN206688436U (en) * | 2017-01-11 | 2017-12-01 | 兰州凯特环境技术工程有限公司 | Turbulent flow coalescence electricity mist cleaner |
-
2017
- 2017-01-11 CN CN201710017477.4A patent/CN106669343A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2533690A1 (en) * | 1974-07-26 | 1976-02-05 | Michael Joseph Pilat | ELECTROSTATIC WET LAUNDRY AND COLLECTOR ARRANGEMENT |
| US20060204407A1 (en) * | 2005-03-09 | 2006-09-14 | Mcwhorter Edward M | Coal flue gas scrubber |
| WO2009113269A1 (en) * | 2008-03-11 | 2009-09-17 | ダイキン工業株式会社 | Air processor |
| CN102145316A (en) * | 2010-02-04 | 2011-08-10 | 山东大学 | Synergistic spray charging and electrostatic dust collecting method and device |
| CN103056030A (en) * | 2012-12-04 | 2013-04-24 | 武汉科技大学 | Wet-type vibrating-wire bipolar electrostatic coagulation deduster |
| CN204469472U (en) * | 2014-12-20 | 2015-07-15 | 艾尼科环保技术(安徽)有限公司 | Pre electrified coalescence sack cleaner |
| CN105797524A (en) * | 2016-05-06 | 2016-07-27 | 江苏大学 | Heteropolar electric charge fogdrop coalescence dust-removing device and method thereof |
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| Title |
|---|
| 中国环境保护产业协会编著, 中国环境科学出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109468990A (en) * | 2018-11-07 | 2019-03-15 | 山东港基建设集团有限公司 | A kind of building cooling dust-extraction unit |
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| PB01 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information |
Inventor after: Li Zhongguo Inventor after: Kuang Yuping Inventor after: Wu Jinzhe Inventor after: Kang Yigun Inventor after: Yang Xiaoming Inventor before: Li Zhongguo |
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| CB03 | Change of inventor or designer information | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20171228 Address after: 730030 old road, Chengguan District, Lanzhou, Gansu Province, No. 346 Applicant after: LANZHOU KAITE ENVIRONMENTAL TECHNOLOGY ENGINEERING CO.,LTD. Address before: 730030 No. 222 Tianshui South Road, Chengguan District, Gansu, Lanzhou Applicant before: Lanzhou University |
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| TA01 | Transfer of patent application right | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170517 |
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| RJ01 | Rejection of invention patent application after publication |