CN205868577U - Bipolar lotus that is used for flue gas dust removal whirlwind separator - Google Patents
Bipolar lotus that is used for flue gas dust removal whirlwind separator Download PDFInfo
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- CN205868577U CN205868577U CN201620598745.7U CN201620598745U CN205868577U CN 205868577 U CN205868577 U CN 205868577U CN 201620598745 U CN201620598745 U CN 201620598745U CN 205868577 U CN205868577 U CN 205868577U
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- flue gas
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- lotus
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Abstract
The utility model discloses a bipolar lotus that is used for flue gas dust removal whirlwind separator through set up lotus electricity section before cyclone's entry, just makes on the granule lotus in the flue gas, the reentrant cyclone of negative electrical charge, through carrying on one's shoulder or back the coalescence of coulomb force between the electric granule reinforceing granule among the cyclone, forms great granule, makes it easy desorption to improve whirlwind separation desorption fine particle's efficiency, flue gas torrent degree can be reinforceed to the electric wire netting that sets up W shape in the lotus electricity section, improves the lotus electrical efficiency, is favorable to reinforcing coulomb coalescence effect.
Description
Technical field
The invention belongs to waste gas dedusting technical field, be particularly used for the bipolar charge-cyclonic separation of flue gas dedusting
Device.
Background technology
Along with developing rapidly of national economy, China's some areas haze takes place frequently, and arch-criminal is that airborne particulate pollutes
Thing.The aerodynamically size of diameter (da), airborne particulates can be divided into overall suspended pellet (TSPs, da <
100 μm), pellet (PM10, da < 10 μm) and lung particulate matter (PM2.5, da < 2.5 μm) can be entered.Big with thicker
Aerated particle pollutant are compared, and the particle diameter of PM2.5 is little, are adsorbed with substantial amounts of poisonous and harmful substances, can be by blood and tissue
Absorbing, and time of staying length in an atmosphere, fed distance are remote, the impact on health and atmosphere quality is bigger.Combustion
The industries such as coal power generation, Coal Chemical Industry, waste incineration, metallurgy, cement are airborne particulates by the flue gas of air flue emission
One of main source.Cyclone separator is the equipment utilizing centrifugal force to be separated from air-flow by granule, has simple in construction, separation
Efficiency is high, pressure drop is moderate, the advantage adapting to the harsh operating mode such as high temperature, high pressure, high granule density, is widely used in the preliminary of flue gas
Dedusting.Modern efficient cyclone separator can more than Ex-all 10 μm granule, granules more than 5 μm is also had preferably trapping
Ability.Along with improving constantly of flue gas emissions standard, conventional cyclone needs combined highly effective cleaner (as cloth bag removes
Dirt, electrostatic precipitation, electric bag dust) carrying out multistage dedusting could qualified discharge.But, the unit dedusting expense of high-effective dust-removing equipment
Also big, if improving the cyclone separator capture rate to the 10 following fine particles of μm, the negative of follow-up cleaner just can be reduced
Lotus, effectively reduces dedusting total cost.The most how to improve the cyclone separator capture rate to the 10 following fine particles of μm, become
For a problem demanding prompt solution in current gas-solid two phases technical research.
The method developing into exploitation strengthening cyclonic separation removing fine particle of bipolar charge-turbulent flow coagulating technique provides
New thinking, its ultimate principle is as shown in Figure 1.Bipolar charge-turbulent flow coalescence device is the pipeline of one section of rectangle, and this pipeline divides
For bipolar charge section and turbulent flow coalescence section two parts.Bipolar charge section is the parallel channels of one group of positive and negative electric field action, and granule leads to
When crossing this section, positive and negative by its passage obtains positive charge and negative charge, respectively subsequently into turbulent flow coalescence section coalescence;Turbulent flow coalescence
Turbulence columns or votex sheet (accompanying drawing 1 is to be provided with turbulence columns in vertical paper direction) are set in Duan, are used for strengthening air-flow by being somebody's turn to do
Less turbulence during section, thus increase the collision probability between charged particle, improve coalescence efficiency.Bipolar charge-turbulent flow coalescence
The Basic Mechanism of technology is conveying and the mixing that bipolar charge granule realizes space large scale under turbulent flow,
The collision of Kolmogorov yardstick, coalescence, and granule coalescence is played facilitation in short distance by Coulomb force.Intergranular coulomb
Power is the key that bipolar charge-turbulent flow coagulating technique has greater efficiency to the facilitation of turbulent flow coalescence.If cyclonic separation mistake
Journey exists turbulent flow coalescence effect, then bipolar charge device is set at cyclone inlet to bipolar electric on granule lotus
Lotus, just can utilize the intergranular Coulomb force of bipolar charge to strengthen the efficiency of cyclonic separation fine particle.The research of Hou Guangxin etc.
Show cyclone separator exists stronger turbulent flow coalescence effect.
Being inspired by the studies above, this project proposes to use bipolar charge technology before cyclone separator, makes fume duct fly ash
Bipolar charge distribution on lotus, enters back into and carries out coalescence, separation in whirlwind field, can strengthen the arresting efficiency of fine particle.
Summary of the invention
The technical problem to be solved is provide for flue gas dedusting for the above-mentioned state of the art double
The most charged-cyclone separator.The present invention solves the technical scheme that above-mentioned technical problem used: for flue gas dedusting
Bipolar charge-cyclone separator includes: positive pole entrance 2, exhaustor 3, negative pole entrance 4, cylinder 6, circular cone 7 and dust flue 8 structure
The cyclone separator become, wherein positive pole entrance 2 and negative pole entrance 4 are with the central shaft of cylinder 6 as axis of symmetry, are arranged on axisymmetrically
The top of cylinder 6, and the most through with cylinder 6;Positive pole connects with positive pole entrance 2 for charged section 1, and negative pole enters with negative pole for charged section 5
Mouth 4 connection;The structure that positive pole is charged section 1 charged with negative pole section 5 is identical, be by epipleural 1-1, lower side panel 1-3, interior plate 1-4,
The rectangular duct that outer panel 1-5 is welded, is provided with electrical network 1-2 in this rectangular duct.
As improvement, described electrical network 1-2 is to be bent into, by the steel wire of 1 piece of rectangle, the W shape that 4 pieces of rectangular wire nets are formed
Steel wire, angle in W-shaped steel silk screen is identical is 20 ~ 90 degree.
Improving further, described electrical network 1-2 and epipleural 1-1 and lower side panel 1-3 is vertical, and with epipleural 1-1 and under
The distance of side plate 1-3 is identical is 5 ~ 10 cm.
Compared with prior art, it is an advantage of the current invention that: by arranging charged section before the entrance of cyclone separator, make
On granule lotus in flue gas, positive and negative electric charge enters back into cyclone separator, strengthens whirlwind by the Coulomb force between electrically charged particle
The coalescence of granule in separator, forms larger particles, makes it easy to removing, thus improves the effect of cyclonic separation removing fine particle
Rate;The electrical network arranging W shape in charged section can strengthen flue gas turbulence degree, improves charged efficiency.
Accompanying drawing explanation
Fig. 1 is bipolar charge-turbulent flow coagulating technique principle schematic.
Fig. 2 is the schematic perspective view of the bipolar charge-cyclone separator of the present invention.
Fig. 3 is the front elevational schematic of the charged segment structure of the present invention.
Fig. 4 is the schematic top plan view of the charged segment structure of the present invention.
Wherein: 1 is charged section of positive pole, and 2 is positive pole entrance, and 3 is exhaustor, and 4 is negative pole entrance, 5 is charged section of negative pole, 6
For cylinder, 7 is circular cone, and 8 is dust flue, and 1-1 is epipleural, and 1-2 is electrical network, and 1-3 is lower side panel, and 1-4 is interior plate, outside 1-5
Side plate.
Detailed description of the invention
2, accompanying drawing 3 and accompanying drawing 4, be described in further detail the present invention by embodiment below in conjunction with the accompanying drawings.
Embodiment 1
Bipolar charge-cyclone separator for flue gas dedusting includes: positive pole entrance 2, exhaustor 3, negative pole entrance
4, the cyclone separator that cylinder 6, circular cone 7 and dust flue 8 are constituted, wherein positive pole entrance 2 and negative pole entrance 4 are with the center of cylinder 6
Axle is axis of symmetry, is arranged on the top of cylinder 6 axisymmetrically, and the most through with cylinder 6;Charged section 1 of positive pole and positive pole entrance 2
Connection, negative pole connects with negative pole entrance 4 for charged section 5.The structure that positive pole is charged section 1 charged with negative pole section 5 is identical.Charged section of positive pole
1 and charged section 5 of negative pole be the rectangular duct being welded by epipleural 1-1, lower side panel 1-3, interior plate 1-4, outer panel 1-5,
Electrical network 1-2 it is provided with in this rectangular duct.Electrical network 1-2 is to be bent into 4 pieces of rectangular wire nets by the steel wire of 1 piece of rectangle to be formed
W-shaped steel silk screen, included angle A in W-shaped steel silk screen is identical is 20 degree.Electrical network 1-2 and epipleural 1-1 and lower side panel 1-3 is vertical, and
Identical with the distance of epipleural 1-1 and lower side panel 1-3 it is 5 cm.
Embodiment 2
Bipolar charge-cyclone separator for flue gas dedusting includes: positive pole entrance 2, exhaustor 3, negative pole entrance
4, the cyclone separator that cylinder 6, circular cone 7 and dust flue 8 are constituted, wherein positive pole entrance 2 and negative pole entrance 4 are with the center of cylinder 6
Axle is axis of symmetry, is arranged on the top of cylinder 6 axisymmetrically, and the most through with cylinder 6;Charged section 1 of positive pole and positive pole entrance 2
Connection, negative pole connects with negative pole entrance 4 for charged section 5.The structure that positive pole is charged section 1 charged with negative pole section 5 is identical.Charged section of positive pole
1 and charged section 5 of negative pole be the rectangular duct being welded by epipleural 1-1, lower side panel 1-3, interior plate 1-4, outer panel 1-5,
Electrical network 1-2 it is provided with in this rectangular duct.Electrical network 1-2 is to be bent into 4 pieces of rectangular wire nets by the steel wire of 1 piece of rectangle to be formed
W-shaped steel silk screen, included angle A in W-shaped steel silk screen is identical is 90 degree.Electrical network 1-2 and epipleural 1-1 and lower side panel 1-3 is vertical, and
Identical with the distance of epipleural 1-1 and lower side panel 1-3 it is 10 cm.
Embodiment 3
Bipolar charge-cyclone separator for flue gas dedusting includes: positive pole entrance 2, exhaustor 3, negative pole entrance
4, the cyclone separator that cylinder 6, circular cone 7 and dust flue 8 are constituted, wherein positive pole entrance 2 and negative pole entrance 4 are with the center of cylinder 6
Axle is axis of symmetry, is arranged on the top of cylinder 6 axisymmetrically, and the most through with cylinder 6;Charged section 1 of positive pole and positive pole entrance 2
Connection, negative pole connects with negative pole entrance 4 for charged section 5.The structure that positive pole is charged section 1 charged with negative pole section 5 is identical.Charged section of positive pole
1 and charged section 5 of negative pole be the rectangular duct being welded by epipleural 1-1, lower side panel 1-3, interior plate 1-4, outer panel 1-5,
Electrical network 1-2 it is provided with in this rectangular duct.Electrical network 1-2 is to be bent into 4 pieces of rectangular wire nets by the steel wire of 1 piece of rectangle to be formed
W-shaped steel silk screen, included angle A in W-shaped steel silk screen is identical is 60 degree.Electrical network 1-2 and epipleural 1-1 and lower side panel 1-3 is vertical, and
Identical with the distance of epipleural 1-1 and lower side panel 1-3 it is 7 cm.
Claims (3)
1. for the bipolar charge-cyclone separator of flue gas dedusting, it is characterised in that described device includes: positive pole enters
The cyclone separator that mouth, exhaustor, negative pole entrance, cylinder, circular cone and dust flue are constituted, wherein positive pole entrance and negative pole entrance with
The central shaft of cylinder is axis of symmetry, is arranged on the top of cylinder axisymmetrically, and the most through with cylinder;Charged section of positive pole with just
Pole entrance connection, charged section of negative pole connects with negative pole entrance;The structure that charged section of positive pole is charged with negative pole section is identical, is by upside
The rectangular duct that plate, lower side panel, interior plate, outer panel are welded, is provided with electrical network in this rectangular duct.
Device the most according to claim 1, it is characterised in that: described electrical network is to be bent into 4 by the steel wire of 1 piece of rectangle
The W-shaped steel silk screen that block rectangular wire net is formed, angle in W-shaped steel silk screen is identical is 20 ~ 90 degree.
Device the most according to claim 1, it is characterised in that: described electrical network is vertical with epipleural and lower side panel, and with
Epipleural is identical with the distance of lower side panel is 5 ~ 10 cm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620598745.7U CN205868577U (en) | 2016-06-20 | 2016-06-20 | Bipolar lotus that is used for flue gas dust removal whirlwind separator |
Applications Claiming Priority (1)
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CN201620598745.7U CN205868577U (en) | 2016-06-20 | 2016-06-20 | Bipolar lotus that is used for flue gas dust removal whirlwind separator |
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CN201620598745.7U Withdrawn - After Issue CN205868577U (en) | 2016-06-20 | 2016-06-20 | Bipolar lotus that is used for flue gas dust removal whirlwind separator |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106362880A (en) * | 2016-06-20 | 2017-02-01 | 宁波工程学院 | Bipolar charging-cyclone separation apparatus and technology used for flue gas dedusting |
CN108716992A (en) * | 2018-06-18 | 2018-10-30 | 宁波工程学院 | A kind of bipolar charge-cyclone dust removal experimental provision |
-
2016
- 2016-06-20 CN CN201620598745.7U patent/CN205868577U/en not_active Withdrawn - After Issue
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106362880A (en) * | 2016-06-20 | 2017-02-01 | 宁波工程学院 | Bipolar charging-cyclone separation apparatus and technology used for flue gas dedusting |
CN106362880B (en) * | 2016-06-20 | 2019-01-15 | 宁波工程学院 | Bipolar charge-cyclone separator and technique for flue gas dedusting |
CN108716992A (en) * | 2018-06-18 | 2018-10-30 | 宁波工程学院 | A kind of bipolar charge-cyclone dust removal experimental provision |
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GR01 | Patent grant | ||
AV01 | Patent right actively abandoned | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20170111 Effective date of abandoning: 20190111 |
|
AV01 | Patent right actively abandoned | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20170111 Effective date of abandoning: 20190115 |