CN2675234Y - Dry method impulse corona discharge fume purifier - Google Patents
Dry method impulse corona discharge fume purifier Download PDFInfo
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- CN2675234Y CN2675234Y CN 200420032863 CN200420032863U CN2675234Y CN 2675234 Y CN2675234 Y CN 2675234Y CN 200420032863 CN200420032863 CN 200420032863 CN 200420032863 U CN200420032863 U CN 200420032863U CN 2675234 Y CN2675234 Y CN 2675234Y
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- ammonia
- corona discharge
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Abstract
The utility model relates to a dry method impulse corona discharge fume purifier. The purifier comprises a tower for humidifying and cooling fume, a device for adding gas ammonia, a nanosecond impulse high voltage power source, a plasma reactor and a by-product collector. When the dry method impulse corona discharge fume purifier is used for purifying fume, high-temperature fume is led to the tower for humidifying and cooling fume to humidify and cool the fume, the fume after being humidified and cooled enters the impulse discharge plasma reactor, the fume reacts with the gas ammonia added in the device for adding gas ammonia, and by-products are generated and collected by the by-product collector. Desulfuration and denitration can be simultaneously realized with high efficiency of desulfuration and denitration via the adoption of the dry method impulse corona discharge fume purifier, the dry method impulse corona discharge fume purifier has favorable adaptability and load tracking performance for the fume with different sulphur contents and the variation in the quantity of the fume, the fume purifier has long service life, and the impulse discharge plasma reactor and the power source in the fume purifier are matched with favorable effect.
Description
Technical field
The utility model belongs to the waste gas purification technical field.Be specifically related to the purifier of a kind of sulfur in smoke and nitrogen oxide.
Background technology
Along with the countries in the world rapid economic development, coal consumption amount as main energy sources sharply increases, and the discharge capacity of the sulfur dioxide that combustion process produced, nitrogen oxide and some other gas pollutant increases thereupon, wherein sulfur dioxide, nitrogen oxide are sour gas, with the water molecules in the atmosphere, form acid rain, bring serious economy loss and environmental pollution to the mankind.Nineteen ninety-five, China's thermoelectricity installed capacity reaches 1.6 hundred million kW, SO2 emissions are 8,300,000 tons, account for 35% of the whole nation, and nitrogen oxide emission are 4,300,000 tons, reach 2.2 hundred million kW to thermoelectricity installed capacity in 2000, SO2 emissions account for about 50% of the whole nation, and nitrogen oxide emission is 1,560 ten thousand tons, expects thermoelectricity installed capacity in 2010 and reaches 3.7 hundred million kW, SO2 emissions account for 66% of the whole nation, and nitrogen oxide emission is 2,190 ten thousand tons.
Present widely used fume desulphurization method mainly contains limestone/gypsum wet method, simple and easy wet method, rotating spraying semidry method, in-furnace calcium spraying afterbody humidification activation method, seawater neutralisation etc., wherein is most widely used with the limestone/gypsum wet method.But all there is the nitrogen oxide that can not remove in the flue gas in these methods, and the not high shortcoming of the accessory substance value that produces in the sweetening process.
The corona discharge pulse flue gas desulfurization and denitration method generally has the branch of dry method and semidry method.The collection rate of semidry method dust and drop has only 85～95%, and the collection efficiency of drop is not high, causes a large amount of ammonium salts to be discharged in the atmosphere with flue gas after being purified, and dry method reaches more than 98.5% the collection rate of dust and ammonium salt; Semidry method is compared with dry method, and needing increases bulky water circulation and water processing establishment, and energy consumption is bigger in crystallization process; The spray drying tower of semidry method is followed the tracks of flue gas load, and regulating the balance of maintenance system water and the balance of ammonium salt also is the comparison difficulty.
Summary of the invention
The purpose of this utility model is to provide a kind of coupling that can carry out desulphurization denitration simultaneously, adaptability and Steam Generator in Load Follow, the life-span that can prolong the pulse power, pulsed discharge plasma reactor and power supply preferably be arranged for the variation of sulfur-containing smoke gas and exhaust gas volumn dry type corona discharge smoke eliminator preferably.
A kind of dry type corona discharge smoke eliminator of the present utility model comprises the flue gas humidifying cooling tower that is used for the flue gas humidifying cooling, be used to add the gas ammonia throwing device of desulfurization denitrification agent, be used for the nanosecond pulse high voltage source that corona discharge pulse causes free radical and ion generation, be used for activated water steam and ammonia, the pulsed discharge plasma reactor that steam after the activation and ammonia and sulfur in smoke and nitrogen oxide react, be used to collect 5 unit of accessory substance gathering-device of accessory substance, flue gas humidifying cooling tower and pulsed discharge plasma reactor, the accessory substance gathering-device connects successively, the gas ammonia throwing device, the nanosecond pulse high voltage source is connected with the pulsed discharge plasma reactor respectively.
The structure and the course of work of each unit of dry type corona discharge smoke eliminator of the present utility model are described below.
1) flue gas humidifying cooling tower
Flue gas humidifying cooling tower comprises the smoke inlet that is arranged on cat head, be arranged on the atomized water nozzle on top in the tower, be arranged on dredge pump and plash at the bottom of the tower, be arranged on the parts such as exhanst gas outlet at tower middle part, wherein the atomized water nozzle is arranged in the form of a ring, and tower body adopts the column type housing structure.
The humidifying cooling water is sprayed by the atomized water nozzle, the atomized water nozzle atomizes water into the droplet that particle diameter is 100 μ m～150 μ m, atomized water forms following current with the flue gas that flows into from top of tower and contacts, flue gas through humidifying cooling is sent to the pulsed discharge plasma reactor, and the dust-laden effluent stream is discharged at the bottom of flue gas humidifying cooling Tata through plash and by dredge pump.The atomized water that sprays into has 85～95% heats that absorbed flue gas to vaporize, and with flue gas inflow pulsed discharge plasma reactor, 5～15% atomized water is vaporization not, the blowdown apparatus that the atomized water of big particle diameter flows at the bottom of the tower is discharged, and the small particle diameter atomized water enters the pulsed discharge plasma reactor with flue gas.
2) gas ammonia throwing device
The gas ammonia throwing device comprises liquid ammonia storage tank, liquefied ammonia compressor, liquefied ammonia evaporimeter and the gas ammonia surge tank that connects successively.
Adopt liquefied ammonia with the gas ammonia of sulfur dioxide and reaction of nitrogen oxides, the liquid ammonia storage tank liquefied ammonia compressor of flowing through enters the liquefied ammonia evaporimeter, is evaporated to gas ammonia and enters in the gas ammonia surge tank.
3) nanosecond pulse high voltage source
The nanosecond pulse high voltage source mainly by the accumulate container that is used for storing high voltage electric energy, be used for the thyratron of accumulate condenser discharge, pulse transformer that voltage that middle accumulate container is spread out of raises, the pulse shaper of the voltage waveform shaping of pulse transformer output and the magnetic switch that is used for sharpening pulse shaper output voltage waveforms formed.The nanosecond pulse high voltage source is called existing detailed description the in detail in the utility model patent of " the high-voltage pulse power source device that a kind of impulse electric corona plasma flue gas desulfurization is used " (patent No. is 01247614.5) in name.
4) pulsed discharge plasma reactor
Be disposed with airflow uniform distribution plate, steam activation device, ammonia activating apparatus, rapping apparatus, positive plate and negative electrode, pulsed electrode device in the pulsed discharge plasma reactor, be provided with ash bucket at reactor lower part at the smoke inlet place.
The airflow uniform distribution plate is used to regulate the steady air flow direction.
The steam activation device comprises quartz ampoule, porcelain axle, steam air inlet pipe, air accumulator, the sparking electrode that connects successively, and pole plate is parallel with sparking electrode.Steam enters air accumulator by the steam air inlet pipe, adds 30～90kV voltage on the steam sparking electrode, and fully after the activation, the steam that contains the OH free radical is by the ejection of sparking electrode gas outlet.
The ammonia activating apparatus comprises quartz ampoule, porcelain axle, ammonia air inlet pipe, air accumulator, the sparking electrode that connects successively, and pole plate is parallel with sparking electrode.Ammonia enters air accumulator by the ammonia air inlet pipe, adds 30～90kV voltage on the ammonia sparking electrode, fully after the activation, produces NH, NH
2Free radical, the ammonia after the activation is by the ejection of sparking electrode gas outlet.
Steam and ammonia enter air accumulator and can regulate by three-way device, and three-way device can guarantee that steam is activated earlier or guarantees that ammonia is activated earlier or steam and ammonia are activated simultaneously, regulates the flow of steam or ammonia.
Air accumulator is used to lay in steam or ammonia or steam and the ammonia that will be activated.
Quartz ampoule and porcelain axle play insulating effect.
The sparking electrode of steam activation device and ammonia activating apparatus all adopts pin-plank frame, and the needle tube type sparking electrode is made of the person in charge and needle tubing, and the homonymy pin is adjacent, and the both sides pin is staggered, and all pins are in same plane, and parallel with pole plate.
Rapping apparatus mainly is made up of rapping electrode, cathode rapping and anode rapping etc., collects the part byproduct of reaction by cathode rapping and anode rapping.
According to exhaust gas volumn one or more electric fields are set in reactor.
Positive plate and negative electrode are used to collect accessory substance.
The pulsed electrode device comprises line style sparking electrode, low pressure plate electrode and pulsed high voltage generator.Sparking electrode adopts little cylinder molded lines or the star-like line of radius of curvature, and the low pressure plate electrode adopts the metallic plate of plate or Z type, and the proportionate relationship of distance is 0.6-1 between distance between the discharge lines and the line plate.The rise time that pulsed high voltage generator requires to produce voltage waveform, pulse width was less than 1 μ s less than 100ns, and frequency can be regulated according to obtaining removal effect.
Flue gas again by steam activation device or ammonia activating apparatus or steam activation device and ammonia activating apparatus, again by the pulsed electrode device, produces OH, HO earlier by behind the airflow uniform distribution plate
2, NH, NH
2, N
2 +Isoreactivity free radical and ion, the SO in the oxidation flue gas
2And NO
xMolecular reaction generates SO
3NO with high price
x, finally generating accessory substances such as sulphur ammonium and ammonium nitrate, accessory substance is collected by positive plate and negative electrode again, again by after cathode rapping and the anode rapping, collects the part accessory substance by ash bucket.
5) accessory substance gathering-device
The accessory substance gathering-device mainly comprises housing, crossbeam, positive plate, negative electrode, cathode rapping and anode rapping, airflow-distribution board, air inlet, gas outlet, storage hopper etc., also contains brush dust system and heat-insulation layer.The accessory substance gathering-device is called existing detailed description the in detail in the utility model patent document of " electron beam irradiation flue gas desulfurization and denitrification accessory substance gathering-device " (patent No. 01213936.X) in name.
Flue gas enters in the humidifying cooling tower after the electrostatic precipitator of power plant is handled, flue gas behind the humidifying cooling enters the pulsed discharge plasma reactor, apply high pressure, and add ammonia by the gas ammonia throwing device, corona discharge takes place, produce the strong oxidizing property free radical, free radical causes sulfur dioxide in flue gas and reaction of nitrogen oxides, final ammonium sulfate and the ammonium nitrate particulate of generating, particulate is collected by the accessory substance gatherer.
The utility model purifies sulfur in smoke and nitrogen oxide adopts the flue gas following current way of contact, flue gas contacts with the water droplet that part is not vaporized, improved the efficiency of dust collection of flue gas humidifying cooling tower, improved the quality of accessory substance, in near the sewage that forms in the humidifying cooling tower accumulates at the bottom of the tower the plash, this sewage main component is coal-fired dust, sulfate radical and sulfite ion, be acid, can be used for the modified etc. of alkaline waste water, also this sewage can be entered the detritus tank of power plant, be used for the replenishing of the modified and water yield of detritus tank alkaline waste water, also can be used for the cooling of coal-fired moisturizing and dried slag, can not cause secondary pollution; The gas ammonia surge tank is arranged on certain the force value work in 0.2MPa～0.8MPa scope, makes that gas ammonia pressure has stability preferably in surge tank and the defeated ammonia pipeline, guaranteed to add ammonia amount in the reactor accurately and stable; The nanosecond pulse high voltage source can provide up to a hundred kilovolts of steep-front nanosecond pulse voltages, and average output power is big, efficient is high, the life-span is long; By the flue gas after steam activation device, ammonia activating apparatus and the activation of pulsed electrode device, desulphurization denitration rate height, desulfurization degree can reach more than 80%; Accessory substance gatherer efficiency of dust collection height, accessory substance collection efficiency height.
The utlity model has desulphurization denitration simultaneously, change for the flue gas of different sulfur content and exhaust gas volumn adaptability and Steam Generator in Load Follow are preferably arranged, the long service life of the pulse power, the matching effect of pulsed discharge plasma reactor and power supply is good.
Description of drawings
The utility model will be further described below in conjunction with the drawings and specific embodiments.
Fig. 1 is the pulsed discharge plasma structure of reactor schematic diagram of the utility model dry method corona discharge pulse smoke eliminator embodiment
Fig. 2 is steam and the ammonia activation apparatus structure schematic diagram of the utility model dry method corona discharge pulse smoke eliminator embodiment
Fig. 3 is the discharge electrode structure schematic diagram of the utility model dry method corona discharge pulse smoke eliminator embodiment
Fig. 4 is the process chart of gas cleaning process of the present utility model
Among the figure: 1 airflow uniform distribution plate I, 2 airflow uniform distribution plate II 3 steam activation devices, 4 ammonia activating apparatus 5 rapping apparatus, 6 positive plates and negative electrode 7 pulsed electrode devices 8 ash buckets 9 pole plates 10 sparking electrodes 11 air accumulators 12 three-way devices 13 air inlet pipe 14 porcelain axles 15 quartz ampoules 16 supervisors 17 needle tubings 18 flue gas humidifying cooling towers 19 plashes 20 dredge pumps 21 liquid ammonia storage tanks 22 liquefied ammonia compressors 23 liquid ammonia evaporators 24 gas ammonia surge tanks 25 pulsed discharge plasma reactors 26 accessory substance collectors 27 air-introduced machines 28 chimneys
The specific embodiment
A kind of dry method corona discharge pulse smoke eliminator, comprise the flue gas humidifying cooling tower 18 that is used for the flue gas humidifying cooling, be used to add the gas ammonia throwing device of desulfurization denitrification agent, be used for corona discharge pulse and cause the nanosecond pulse high voltage source that free radical and ion produce, be used for the pulsed discharge plasma reactor 25 that steam after activated water steam and ammonia, the activation and ammonia and sulfur in smoke and nitrogen oxide react, the accessory substance gathering-device 26 that is used to collect accessory substance; Flue gas humidifying cooling tower 18 is connected successively with pulsed discharge plasma reactor 25, accessory substance gathering-device 26, and gas ammonia throwing device, nanosecond pulse high voltage source are connected with pulsed discharge plasma reactor 25 respectively.
Adopt dry method corona discharge pulse smoke eliminator of the present utility model, at first high-temperature flue gas is introduced the humidifying cooling tower and carried out humidifying cooling, temperature is reduced to 50～80 ℃, and the content of water is 5～15%; Flue gas behind the humidifying cooling enters the pulsed discharge plasma reactor, apply high pressure, pulse power power is 50～100kW, and adds ammonia by the gas ammonia throwing device, the metering of ammonia sulfur chemistry is than being 0.8: 1～1: 1, and reaction generates accessory substance ammonium sulfate and ammonium nitrate; The accessory substance gatherer is collected ammonium sulfate and the ammonium nitrate that generates, and the flue gas after being cleaned is introduced chimney by air-introduced machine and entered atmosphere.
Fig. 1 is the pulsed discharge plasma structure of reactor schematic diagram of the utility model dry method corona discharge pulse smoke eliminator embodiment, airflow uniform distribution plate I1, airflow uniform distribution plate II2, steam activation device 3, ammonia activating apparatus 4, rapping apparatus 5, positive plate and the negative electrode 6, the pulsed electrode device 7 that are disposed with in the pulsed discharge plasma reactor at the smoke inlet place are provided with ash bucket 8 at reactor lower part.
Fig. 2 is steam and the ammonia activation apparatus structure schematic diagram of the utility model dry method corona discharge pulse smoke eliminator embodiment, activating apparatus comprises successively the quartz ampoule 15, the porcelain axle 14 that connect, be used for air inlet pipe 13, air accumulator 11, sparking electrode 10 that steam or ammonia enter, pole plate 9 is parallel with sparking electrode 10, also comprises three-way device 12.
Fig. 3 is the discharge electrode structure schematic diagram of the utility model dry method corona discharge pulse smoke eliminator embodiment, sparking electrode 10 is made of the person in charge 16 and needle tubing 17, and the homonymy pin is adjacent, and the both sides pin is staggered, all pins are in same plane, and parallel with pole plate 9.
Fig. 4 is the process chart of gas cleaning process of the present utility model, flue gas humidifying cooling tower 18 is connected successively with pulsed discharge plasma reactor 25, accessory substance gathering-device 26, and gas ammonia throwing device, nanosecond pulse high voltage source are connected with pulsed discharge plasma reactor 25 respectively.Flue gas humidifying cooling tower 18 comprises plash 19 and dredge pump 20, and the gas ammonia throwing device comprises liquid ammonia storage tank 21, liquefied ammonia compressor 22, liquefied ammonia evaporimeter 23 and the gas ammonia surge tank 24 that connects successively.Also comprise air-introduced machine 27 and chimney 28.
The course of work of the present utility model is described below.
SO with factory's boiler generation
2Concentration is 2, the flue gas of 500ppm, and with 20,000Nm
3The flow of/h is handled by device of the present utility model.The humidifying cooling water adopts pressurization by the atomized water nozzle ejection of arranging in the form of a ring, the atomized water nozzle atomizes water into the droplet that particle diameter is 100 μ m～150 μ m, atomized water forms following current with the flue gas that flows into humidifying cooling tower 18 from top of tower and contacts, make flue-gas temperature reduce to 60～80 ℃, the content of water increases to about 10% in the flue gas, flue gas through humidifying cooling is sent to pulsed discharge plasma reactor 25, and the dust-laden effluent stream is discharged at the bottom of flue gas humidifying cooling tower 18 towers through plash 19 and by dredge pump 20.The atomized water that sprays into has 85%～95% heat that has absorbed flue gas to vaporize, and with flue gas inflow pulsed discharge plasma reactor 25,5%～15% atomized water is vaporization not, the blowdown apparatus that the atomized water of big particle diameter flows at the bottom of the tower is discharged, and the small particle diameter atomized water enters pulsed discharge plasma reactor 25 with flue gas.Gas ammonia is obtained to liquefied ammonia evaporimeter 23 evaporation by the liquid ammonia storage tank 21 liquefied ammonia compressor 22 of flowing through by liquefied ammonia again, and gas ammonia sprays into pulsed discharge plasma reactor 25 inlets by gas ammonia surge tank 24 with certain force value in 0.2MPa～0.8MPa scope again., mix by behind airflow uniform distribution plate I1 and the air-flow uniform board II2 through the flue gas behind the humidifying cooling with steam or ammonia after activated.Steam or ammonia are by the steam or the ammonia air inlet pipe 13 of steam activation device 3 or ammonia activating apparatus 4 or steam activation device 3 and ammonia activating apparatus 4, air inflow by three-way device 12 adjusting steam or ammonia, and, have OH, HO through the corona activation generation by air accumulator 11 storages
2The steam of isoreactivity free radical or have NH, NH
2, N
2 +The ammonia of isoreactivity free radical and ion, the person in charge 16 and needle tubing 17 ejections by sparking electrode 10 again by pulsed electrode device 7, continue activated water steam or ammonia, and the SO in the flue gas
2And NO
xThe final accessory substances such as sulphur ammonium and ammonium nitrate that generate, after small part ammonium sulfate and ammonium nitrate particulate are collected by positive plate and negative electrode 6, again by rapping apparatus 5 rapping positive plates and negative electrode 6, this part ammonium sulfate and ammonium nitrate particulate fall into ash bucket 8, and be collected, the flue gas that has most of ammonium sulfate and ammonium nitrate particulate enters the process pipe of pulsed discharge plasma reactor outlet, is admitted to accessory substance gatherer 26 at last.The metering of ammonia sulfur chemistry is than being 0.8: 1～1: 1, and pulse power power is 80kW, and pole plate 9 is parallel with sparking electrode 10,15 insulating effects of porcelain axle 14 and quartz ampoule.The flue gas that has accessory substance after being cleaned enters in the accessory substance gatherer 26, at first be the flow direction and the flow velocity of regulating flue gas by the airflow uniform distribution plate, enter a plurality of high-voltage electrostatic fields again, collect ammonium sulfate and ammonium nitrate particulate, after multistage rapping, ammonium sulfate and ammonium nitrate particulate fall into ash bucket, collect accessory substance by scraping apparatus for ash again, when every a few hours excessively of the accessory substance on pole plate and the polar curve or accessory substance adhesion are thicker, by brush dust device brush dust, accessory substance in flue gas accessory substance fall into ash bucket, flue gas after being purified is introduced chimney by air-introduced machine, enters in the atmosphere.Exhaust gas dust concentration is after testing less than 200mg/Nm
3, SO
2Concentration is after testing about 400ppm.
Claims (11)
1, a kind of dry method corona discharge pulse smoke eliminator, it is characterized in that: comprise the flue gas humidifying cooling tower (18) that is used for the flue gas humidifying cooling, be used to add the gas ammonia throwing device of desulfurization denitrification agent, be used for corona discharge pulse and cause the nanosecond pulse high voltage source that free radical and ion produce, be used for the pulsed discharge plasma reactor (25) that steam after activated water steam and ammonia, the activation and ammonia and sulfur in smoke and nitrogen oxide react, the accessory substance gathering-device (26) that is used to collect accessory substance; Flue gas humidifying cooling tower (18) is connected successively with pulsed discharge plasma reactor (25), accessory substance gathering-device (26), and gas ammonia throwing device, nanosecond pulse high voltage source are connected with pulsed discharge plasma reactor (25) respectively.
2, a kind of dry method corona discharge pulse smoke eliminator according to claim 1 is characterized in that: described flue gas humidifying cooling tower (18) comprises the smoke inlet that is arranged on cat head, be arranged on the ring-shaped distributed atomized water nozzle in top in the tower, be arranged on dredge pump (19) and plash (20) at the bottom of the tower, be arranged on the exhanst gas outlet in the middle part of the tower.
3, a kind of dry method corona discharge pulse smoke eliminator according to claim 1 is characterized in that: described gas ammonia throwing device comprises liquid ammonia storage tank (21), liquefied ammonia compressor (22), liquefied ammonia evaporimeter (23) and the gas ammonia surge tank (24) that connects successively.
4, a kind of dry method corona discharge pulse smoke eliminator according to claim 1, it is characterized in that: be disposed with in the described pulsed discharge plasma reactor (25) at the airflow uniform distribution plate (1) at smoke inlet place and (2), steam activation device (3), ammonia activating apparatus (4), rapping apparatus (5), positive plate and negative electrode (6), pulsed electrode device (7), be provided with ash bucket (8) in pulsed discharge plasma reactor (25) bottom.
5, a kind of dry method corona discharge pulse smoke eliminator according to claim 4, it is characterized in that: described steam activation device (3) comprises quartz ampoule (15), porcelain axle (14), steam air inlet pipe (13), air accumulator (11), the sparking electrode (10) that connects successively, and pole plate (9) is parallel with sparking electrode (10).
6, a kind of dry method corona discharge pulse smoke eliminator according to claim 5, it is characterized in that: the sparking electrode of described steam activation device (3) adopts pin---plank frame, needle tube type sparking electrode (10) constitutes by being responsible for (16) and needle tubing (17), the homonymy pin is adjacent, the both sides pin is staggered, all pins are in same plane, and parallel with pole plate (9).
7, a kind of dry method corona discharge pulse smoke eliminator according to claim 4, it is characterized in that: described ammonia activating apparatus (4) comprises quartz ampoule (15), porcelain axle (14), ammonia air inlet pipe (13), air accumulator (11), the sparking electrode (10) that connects successively, and pole plate (9) is parallel with sparking electrode (10).
8, a kind of dry method corona discharge pulse smoke eliminator according to claim 7, it is characterized in that: the sparking electrode of described ammonia activating apparatus (4) adopts pin---plank frame, needle tube type sparking electrode (10) constitutes by being responsible for (16) and needle tubing (17), the homonymy pin is adjacent, the both sides pin is staggered, all pins are in same plane, and parallel with pole plate (9).
9, a kind of dry method corona discharge pulse smoke eliminator according to claim 4, it is characterized in that: described pulsed electrode device (7) comprises sparking electrode (10), low pressure plate electrode and pulsed high voltage generator, sparking electrode (10) adopts the little line style sparking electrode of radius of curvature, the low pressure plate electrode adopts the metallic plate of plate or Z type, and the proportionate relationship of distance is 0.6～1 between distance between the discharge lines and the line plate.
10, a kind of dry method corona discharge pulse smoke eliminator according to claim 4, it is characterized in that: described rapping apparatus (5) comprises rapping electrode, cathode rapping and anode rapping.
11, a kind of dry method corona discharge pulse smoke eliminator according to claim 4 is characterized in that: the electric field that is provided with in the described pulsed discharge plasma reactor (25) is one or more.
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|---|---|---|---|
| CN 200420032863 CN2675234Y (en) | 2004-02-14 | 2004-02-14 | Dry method impulse corona discharge fume purifier |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420032863 CN2675234Y (en) | 2004-02-14 | 2004-02-14 | Dry method impulse corona discharge fume purifier |
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| CN2675234Y true CN2675234Y (en) | 2005-02-02 |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101171070B (en) * | 2005-05-06 | 2012-10-17 | 国立大学法人岐阜大学 | Dry simultaneous desulfurization/denitrification apparatus for exhaust gas |
| CN103736376A (en) * | 2013-12-25 | 2014-04-23 | 河南金土地煤气工程有限公司 | Low-temperature desulfurization and denitrification device and method |
| CN104437040A (en) * | 2014-12-16 | 2015-03-25 | 江苏淞瀚新能源有限公司 | Nitric oxide removing device and method based on delectric barrier discharge reactor |
| CN106422704A (en) * | 2016-11-04 | 2017-02-22 | 浙江大学 | Integrated system for deeply removing various pollutants |
| CN106989407A (en) * | 2016-01-20 | 2017-07-28 | 杭州中兵环保股份有限公司 | NOx cancellation elements and method in a kind of flue gas |
-
2004
- 2004-02-14 CN CN 200420032863 patent/CN2675234Y/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101171070B (en) * | 2005-05-06 | 2012-10-17 | 国立大学法人岐阜大学 | Dry simultaneous desulfurization/denitrification apparatus for exhaust gas |
| CN103736376A (en) * | 2013-12-25 | 2014-04-23 | 河南金土地煤气工程有限公司 | Low-temperature desulfurization and denitrification device and method |
| CN104437040A (en) * | 2014-12-16 | 2015-03-25 | 江苏淞瀚新能源有限公司 | Nitric oxide removing device and method based on delectric barrier discharge reactor |
| CN106989407A (en) * | 2016-01-20 | 2017-07-28 | 杭州中兵环保股份有限公司 | NOx cancellation elements and method in a kind of flue gas |
| CN106422704A (en) * | 2016-11-04 | 2017-02-22 | 浙江大学 | Integrated system for deeply removing various pollutants |
| CN106422704B (en) * | 2016-11-04 | 2022-10-14 | 浙江大学 | Integrated deep removal system for multiple pollutants |
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