CN109364676A - A kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment - Google Patents
A kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment Download PDFInfo
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- CN109364676A CN109364676A CN201811514363.1A CN201811514363A CN109364676A CN 109364676 A CN109364676 A CN 109364676A CN 201811514363 A CN201811514363 A CN 201811514363A CN 109364676 A CN109364676 A CN 109364676A
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- low temperature
- adsorbent equipment
- humidification
- porcelain insulator
- electrostatic adsorbent
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- 239000003463 adsorbent Substances 0.000 title claims abstract description 36
- 239000000428 dust Substances 0.000 title claims abstract description 30
- 238000005453 pelletization Methods 0.000 title claims abstract description 17
- 238000009827 uniform distribution Methods 0.000 claims abstract description 24
- 229910052573 porcelain Inorganic materials 0.000 claims description 40
- 239000012212 insulator Substances 0.000 claims description 39
- 238000005485 electric heating Methods 0.000 claims description 19
- 238000009413 insulation Methods 0.000 claims description 19
- 210000004907 gland Anatomy 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 13
- 238000001179 sorption measurement Methods 0.000 claims description 11
- 239000007921 spray Substances 0.000 claims description 4
- 229920001971 elastomer Polymers 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 239000012535 impurity Substances 0.000 claims description 3
- 238000005259 measurement Methods 0.000 claims description 3
- 239000004033 plastic Substances 0.000 claims description 3
- 230000001939 inductive effect Effects 0.000 claims 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 32
- 239000003546 flue gas Substances 0.000 abstract description 32
- 238000000034 method Methods 0.000 abstract description 14
- 238000005336 cracking Methods 0.000 abstract description 12
- 239000007789 gas Substances 0.000 abstract description 11
- 238000005516 engineering process Methods 0.000 abstract description 10
- 230000008569 process Effects 0.000 abstract description 7
- 238000012545 processing Methods 0.000 abstract description 7
- 239000000779 smoke Substances 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000002440 industrial waste Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 9
- 239000007788 liquid Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 4
- 238000004581 coalescence Methods 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 230000002411 adverse Effects 0.000 description 2
- 238000005352 clarification Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- 230000003009 desulfurizing effect Effects 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 206010017577 Gait disturbance Diseases 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000185 dioxinlike effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002663 nebulization Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 230000009885 systemic effect Effects 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 239000002699 waste 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
-
- 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
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention belongs to industrial waste gas purifying environmental protection and energy fields, in particular to are used for the pretreating process of low temperature electrostatic adsorbent equipment, especially a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment.Venturi wet dust removal and the ingenious combination of airflow uniform distribution plate are not only saved space, but also reduce cost by the novel pre- cleaner of humidification.Since temperature garbage cracking technology and traditional coal-burning boiler have larger difference on smoke components, the pre- cleaner of this humidification has stronger adaptability.The present invention can be used for the subsequent flue gas processing device of temperature garbage cracking technology, have many advantages, such as easily implement, it is with low investment.
Description
Technical field
The invention belongs to industrial waste gas purifying environmental protection and energy fields, in particular to for the pre- of low temperature electrostatic adsorbent equipment
Treatment process, the pre- dust pelletizing system of humidification of specifically a kind of small-sized low temperature electrostatic adsorbent equipment.
Background technique
Currently, low temperature pyrolyzer technology is the harmless treatment house refuse being widely used both at home and abroad, that reduces dioxin has
Efficacious prescriptions method wherein the most garbage harmless technique of application is burning process, but generates a large amount of dust after burning, tar and
Dioxin-like chemical forms secondary pollution.Can substantially reduce the temperature garbage cracking technology of discharge of poisonous waste increasingly by
The attention of people；But such temperature garbage cracking technology device there is a problem in that: (1) what is taken due to the technique is low
Warm cracking technology, the relative response time is long, and requires boiler internal oxygen content of smoke gas low, so subsequent flue gas treating process is not
The incinerator of the same analogy same size of energy；(2) the temperature garbage cracking technology is different from other type of furnaces, and smoke components are multiple
It is miscellaneous, contain tar, dust, oxysulfide, nitrogen oxides etc. harmful substance simultaneously, classification processing is time-consuming and laborious, so being badly in need of
A kind of equipment of efficient pollutant combined removal；(3) since such low temperature pyrolyzer technique is reacted under low-temperature condition, flue gas temperature
Degree is about at 40 DEG C ~ 60 DEG C, still in flue gas acid dew point hereinafter, so when using traditional bag filter, the powder of high humidity high viscosity
The phenomenon that dirt is easily collected on the fiber surface of bag filter, causes paste bag, substantially reduces the service life of bag filter；
(4) existing flue gas treating process is deduster+desulfurizing tower processing mode, and the device systems are complicated, must be set simultaneously outside furnace
Two-stage fume treatment auxiliary is set, desulfurizing tower exiting flue gas ingredient is low temperature supersaturation wet flue gas, meets cold dry air and easily condenses shape
At water mist, visual pollution is caused, there is energy consumption height, land occupation face in garbage cracking boiler so traditional flue gas treating process is applied
Product is big, smoke evacuation when the problems such as easily forming smog, operating cost increases and the problem of secondary pollution becomes and hinders traditional fume treatment
Technique is in field of garbage disposal stumbling-block preventing the development.
The device of the most effective processing garbage cracking exhaust gas of current position is low temperature electrostatic adsorbent equipment, and low temperature electrostatic adsorbs
Device there are certain requirements internal circulation medium, and low temperature is saturated wet flue gas, and the currently known maximum of low temperature electrostatic adsorbent equipment
Efficiency of dust collection is 92%, so be badly in need of a kind of preconditioning technique, while flue gas is changed into low temperature saturation wet flue gas to delay into
Row pretreatment.
There are three types of the arrangement forms of low temperature electrostatic adsorbent equipment: i.e. adverse current, fair current and cross-flow.Adverse current refers to collection liquid by upper
It flows downward, and flue gas flows from bottom to top, collection liquid is contrary with flow of flue gas；Fair current refers to that collection liquid flows from top to bottom
It is dynamic, while flue gas also flows from top to bottom, collection liquid is identical as flow of flue gas direction；Cross-flow refers to that collection liquid flows from top to bottom
It is dynamic, and flue gas bottom horizontal flow sheet, collection liquid and flow of flue gas direction are staggered.
In three of the above arrangement, in the identical situation of design parameter, the treatment effect of reflux type is more excellent.But nothing
By which kind of processing mode, low temperature electrostatic adsorbent equipment generally can all be connect with insulated case, and moist flue gas conduction occurs in order to prevent
Danger, insulated case is generally disposed at low temperature electrostatic adsorbent equipment upper end, and four or two insulated cases are arranged, using cloth outside tower
Mode is set, above-mentioned arrangement takes up a large area, while the box bracket that insulate increases certain investment cost.Especially for some small
There is the phenomenon that can not installing in type place.
Summary of the invention
The present invention solves prior art deficiency and provides a kind of compact, facilitates installation, adsorption effect outstanding small-sized low
The pre- dust pelletizing system of the humidification of warm electrostatic adsorption device.
The technical solution adopted by the present invention to solve the technical problems are as follows:
A kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment, including flue, high-efficiency atomizing nozzle, airflow uniform distribution system
System, electrostatic adsorption device and air-introduced machine, it is characterised in that the flue lower section is equipped with venturi aditus laryngis section, and flue middle section is equipped with mist
Change nozzle, airflow uniform distribution pipe, electrostatic adsorption device and insulated case, flue upper section is equipped with air-introduced machine and air-flow uniform board.
The insulated case is connect with low temperature electrostatic adsorbent equipment, exhaust gas by insulated case import low temperature electrostatic adsorbent equipment into
Row purification；Insulated case includes insulation outer cylinder, porcelain insulator, porcelain insulator gland, electric heating tube and cathode sunpender, is insulated on outer cylinder
Air inlet is opened up, opens up venthole on porcelain insulator gland；Porcelain insulator is connect by insulated case support plate with insulation outer cylinder, absolutely
Cavity is formed between on the inside of edge outer cylinder and on the outside of porcelain insulator；Cavity passes through the venthole and porcelain insulator of porcelain insulator gland
Inner chambers connection.
The porcelain insulator is in cone cylinder shape, and porcelain insulator upper end connects porcelain insulator gland, and porcelain insulator gland upper end connects
Sunpender nut and cathode sunpender are connect, cathode sunpender penetrates in porcelain insulator, and cathode downrod lower end connects low temperature electrostatic adsorbent equipment.
The electric heating tube is located in the cavity between on the inside of insulation outer cylinder and on the outside of porcelain insulator, and electric heating tube is ring
Shape；For the electric heating tube at least provided with 3, every electric heating tube power is 1.5kw.
The insulation outer cylinder is equipped with insulating layer, and the material of insulating layer is foamed plastic；It is set in the insulated case support plate
There is insulating layer, the material of insulating layer is rubber.
The insulation outer cylinder is equipped with power supply connect cylinder, and the power connection of electric heating tube is arranged in power supply connect cylinder；It is described exhausted
Edge outer cylinder is equipped with temperature control measuring point interface and air inlet, and thermometer passes through temperature in temperature control measuring point interface measurement insulation outer cylinder.
The airflow uniform distribution pipe is equipped with more, and the section of airflow uniform distribution pipe is round or hexagon, in circular hole or hexagon
Tangential circle diameter is 130 ~ 320mm, 2.5 ~ 6m of pipe range.
The atomizer is equipped with multiple groups, and atomizer sprays clear water and settles exhaust gas impurity.
For the airflow uniform distribution plate at least provided with two layers, the material of airflow uniform distribution plate is FRP material.
The invention has the benefit that
The effect of air-introduced machine of the present invention: the polluted gas inside furnace chamber leaks in order to prevent, so being in tiny structure inside furnace chamber
Operation, so that air-introduced machine has been row's purified gas effect.The effect of insulated case air-introduced machine: being that flue gas will be obtained after purifying and cooling
It is sent into insulated case and is internally heated circulation, then carry out the white effect that disappears that sufficiently exchanged heat with the cold flue gas of bottom.
The novel pre- dust collecting process of humidification, the device are directly arranged in low temperature electrostatic adsorbent equipment equipment, airflow uniform distribution plate
Using FRP material, flue gas enters nebulization dust section after the speed-raising of aditus laryngis section, guarantees that low temperature electrostatic is inhaled by high-efficiency atomizing nozzle
Smoke behavior is that low temperature is saturated wet flue gas, and passes through the systemic effect of airflow uniform distribution plate and high-efficiency atomizing nozzle in adsorption device,
Just flue gas is pre-processed before entering low temperature electrostatic adsorbent equipment, is guaranteeing that its smoke property is that low temperature is saturated wet flue gas
Most large dust particles and fraction little particle dust are removed simultaneously, mitigates certain burden to subsequent dust-extraction unit.
Venturi wet dust removal and the ingenious combination of airflow uniform distribution plate are both saved sky by the novel pre- cleaner of humidification
Between, and reduce cost.Since temperature garbage cracking technology and traditional coal-burning boiler have larger difference, this increasing on smoke components
Wet pre- cleaner has stronger adaptability.The present invention can be used for the subsequent flue gas processing device of temperature garbage cracking technology,
Have many advantages, such as easily implement, it is with low investment.
Detailed description of the invention
Fig. 1 is system structure diagram of the invention；
Fig. 2 is that air-flow exchanges schematic diagram；
Fig. 3 is the structural schematic diagram of insulated case；
Fig. 4 is the top view of insulated case；
Fig. 5 is the structural schematic diagram of electric heating tube；
Fig. 6 is the structural schematic diagram of porcelain insulator gland；
Fig. 7 uses schematic diagram for insulated case.
Specific embodiment
A kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment, including flue, high-efficiency atomizing nozzle, air-flow are equal
Distribution system, electrostatic adsorption device and air-introduced machine, the flue lower section are equipped with venturi aditus laryngis section 13, and flue middle section is equipped with atomization spray
Mouth 14, airflow uniform distribution pipe 15, electrostatic adsorption device 16 and insulated case 17, flue upper section are equipped with air-introduced machine 18 and air-flow uniform board
19。
The insulated case is connect with low temperature electrostatic adsorbent equipment, exhaust gas by insulated case import low temperature electrostatic adsorbent equipment into
Row purification；Insulated case includes insulation outer cylinder 5, porcelain insulator 12, porcelain insulator gland 8, electric heating tube 7 and cathode sunpender 10, absolutely
Air inlet 4 is opened up on edge outer cylinder 5, opens up venthole on porcelain insulator gland 8；Porcelain insulator 12 by insulated case support plate 1 with
The outer cylinder 5 that insulate connects, and 5 inside of insulation outer cylinder and porcelain insulator form cavity between 12 outside；Cavity passes through porcelain insulator gland
8 venthole is connected to 12 inner chambers of porcelain insulator.The porcelain insulator 12 is in cone cylinder shape, and the connection of 12 upper end of porcelain insulator is exhausted
Edge porcelain vase gland 8,8 upper end of porcelain insulator gland connection sunpender nut 9 and cathode sunpender 10, cathode sunpender 10 penetrate porcelain insulator
In 12,10 lower end of cathode sunpender connects low temperature electrostatic adsorbent equipment.
The electric heating tube 7 is located in the cavity between 12 outside of 5 inside of insulation outer cylinder and porcelain insulator, electric heating tube 7
For annular；The electric heating tube 7 is equipped with 3, and every 7 power of electric heating tube is 1.5kw.The insulation outer cylinder 5 is equipped with heat preservation
Layer 6, the material of insulating layer 6 are foamed plastic；The insulated case support plate 1 is equipped with insulating layer 3, and the material of insulating layer 3 is rubber
Glue.The insulation outer cylinder 5 is equipped with power supply connect cylinder 2, and the power connection of electric heating tube 7 is arranged in power supply connect cylinder 2；The insulation
Outer cylinder 5 is equipped with temperature control measuring point interface 11 and air inlet 4, and thermometer passes through temperature in the measurement insulation outer cylinder 5 of temperature control measuring point interface 11
Degree.
The airflow uniform distribution pipe 15 is equipped with more, and the section of airflow uniform distribution pipe 15 is round or hexagon, circular hole or six sides
Shape inscribed circle diameter is 130 ~ 320mm, 2.5 ~ 6m of pipe range.The atomizer 14 is equipped with multiple groups, and atomizer 14 sprays clear water
Settle exhaust gas impurity.The airflow uniform distribution plate 19 is equipped with two layers, and the material of airflow uniform distribution plate is FRP material.Thickness < 200mm,
Every layer of < 150pa of resistance, defogging effect 80% ~ 93%.
The flue gas come out from temperature garbage cracking boiler initially enters venturi aditus laryngis section, in efficient mist after aditus laryngis speed-raising
Under the action of changing nozzle, dust and droplet collision coalescence form bulky grain and are removed, and subsequent flue gas enters diffuser.After reduction of speed
Upper layer and lower layer velocity of flue gas is significantly different, and lower layer's flue gas collides upper layer flue gas, and little particle dust continues and droplet coalescence, is formed big
It is removed under gravity after particle.Subsequent flue gas enters airflow uniform distribution plate, forms one under the uniformly distributed effect of uniform board
A stable flow field enters subsequent low temperature electrostatic adsorbent equipment.After venturi aditus laryngis section is inversely contacted with high-efficient atomizing particle water
Mutually collision coalescence forms bulky grain, falls under gravity into lower part water tank, completes dust removing effects.Treated, and flue gas is logical
It crosses after airflow uniform distribution plate is evenly distributed with and enters low temperature electrostatic adsorption system, remove the substances such as drop, aerosol, micronic dust and heavy metal Hg,
Fine defogging is carried out subsequently into two-stage plate demister system, is finally discharged from exhanst gas outlet；Low temperature electrostatic adsorbent equipment captures
The substance to get off falls into the water tank of device bottom together with dedusting product, and flusher is arranged in water tank, and flushing liquor is collected recyclable
It uses.Insulated case is arranged in low temperature electrostatic adsorption system, for hanging cathode wire frame, and bears whole cathode lines and frame
Full payload.Insulated case keeps internally dry using hot wind, in case moist occur short circuit.The liquid that the device passes through themselves capture
Or outer water receiving keeps the cleaning of electrode surface, it is easy to operate.The section of airflow uniform distribution pipe 15 is that round or hexagon being capable of pole
The big resistance for reducing demister, pressure drop are generally 100 ~ 150Pa.
The low temperature electrostatic adsorbent equipment, cooperation venturi water film dust pelletizing system and two-stage plate demister system, the present invention can
Current temperature garbage cracking technology common problem is effectively solved, not only reduces secondary pollution, but also reduce costs.Separately
Outside, the present apparatus cleans electrode surface by the liquid or outer water receiving of themselves capture, and easy to operate, operating cost is low.
This system can be equipped with cyclic water tank as needed, in cyclic water tank unemployed slurries can be sent back to clarifying basin into
Row clarification, the supernatant after clarification carry out reuse, sediment timing cleaning outward transport processing as the rinse water of device.
Claims (9)
1. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment, including flue, high-efficiency atomizing nozzle, airflow uniform distribution
System, electrostatic adsorption device and air-introduced machine, it is characterised in that the flue lower section is equipped with venturi aditus laryngis section (13), flue middle section
Equipped with atomizer (14), airflow uniform distribution pipe (15), electrostatic adsorption device (16) and insulated case (17), flue upper section is equipped with air inducing
Machine (18) and air-flow uniform board (19).
2. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment according to claim 1, it is characterised in that institute
It states insulated case to connect with low temperature electrostatic adsorbent equipment, exhaust gas imports low temperature electrostatic adsorbent equipment by insulated case and purified；Absolutely
Edge case includes insulation outer cylinder (5), porcelain insulator (12), porcelain insulator gland (8), electric heating tube (7) and cathode sunpender (10), absolutely
It is opened up on edge outer cylinder (5) air inlet (4), porcelain insulator gland opens up venthole on (8)；Porcelain insulator (12) passes through insulated case branch
Fagging (1) is connect with insulation outer cylinder (5), forms cavity between porcelain insulator (12) outside on the inside of insulation outer cylinder (5)；Cavity
It is connected to by the venthole of porcelain insulator gland (8) with porcelain insulator (12) inner chambers.
3. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment according to claim 1, it is characterised in that institute
Porcelain insulator (12) are stated in cone cylinder shape, porcelain insulator (12) upper end connects porcelain insulator gland (8), on porcelain insulator gland (8)
End connection sunpender nut (9) and cathode sunpender (10), cathode sunpender (10) penetrates in porcelain insulator (12), under cathode sunpender (10)
End connection low temperature electrostatic adsorbent equipment.
4. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment according to claim 1, it is characterised in that institute
It states in the cavity that electric heating tube (7) is located between on the inside of insulation outer cylinder (5) and on the outside of porcelain insulator (12), electric heating tube (7) is
Annular；For the electric heating tube (7) at least provided with 3, every electric heating tube (7) power is 1.5kw.
5. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment according to claim 1, it is characterised in that institute
It states insulation outer cylinder (5) and is equipped with insulating layer (6), the material of insulating layer (6) is foamed plastic；On the insulated case support plate (1)
Equipped with insulating layer (3), the material of insulating layer (3) is rubber.
6. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment according to claim 1, it is characterised in that institute
It states insulation outer cylinder (5) and is equipped with power supply connect cylinder (2), the power connection setting of electric heating tube (7) is in power supply connect cylinder (2)；It is described
Outer cylinder (5) are insulated equipped with temperature control measuring point interface (11) and air inlet (4), and thermometer is exhausted by temperature control measuring point interface (11) measurement
Edge outer cylinder (5) interior temperature.
7. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment according to claim 1, it is characterised in that institute
Airflow uniform distribution pipe (15) are stated equipped with more, the section of airflow uniform distribution pipe (15) is round or hexagon, circular hole or hexagon inscribe
Circular diameter is 130 ~ 320mm, 2.5 ~ 6m of pipe range.
8. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment according to claim 1, it is characterised in that institute
Atomizer (14) are stated equipped with multiple groups, atomizer (14) sprays clear water and settles exhaust gas impurity.
9. a kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment according to claim 1, it is characterised in that institute
Airflow uniform distribution plate (19) is stated at least provided with two layers, the material of airflow uniform distribution plate is FRP material.
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| CN201811514363.1A CN109364676A (en) | 2018-12-12 | 2018-12-12 | A kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment |
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| CN201811514363.1A CN109364676A (en) | 2018-12-12 | 2018-12-12 | A kind of pre- dust pelletizing system of humidification of small-sized low temperature electrostatic adsorbent equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110420759A (en) * | 2019-08-21 | 2019-11-08 | 中冶焦耐(大连)工程技术有限公司 | A kind of electrical tar precipitator unidirectional osmosis membrane type insulated case |
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