CN105056723A - Twin-tower type flue gas deep purification device through plasma coupling and sodium based absorption and method thereof - Google Patents
Twin-tower type flue gas deep purification device through plasma coupling and sodium based absorption and method thereof Download PDFInfo
- Publication number
- CN105056723A CN105056723A CN201510455550.7A CN201510455550A CN105056723A CN 105056723 A CN105056723 A CN 105056723A CN 201510455550 A CN201510455550 A CN 201510455550A CN 105056723 A CN105056723 A CN 105056723A
- Authority
- CN
- China
- Prior art keywords
- flue gas
- demist
- denitration
- desulfurization
- oxidation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Treating Waste Gases (AREA)
Abstract
The invention discloses a twin-tower type flue gas deep purification device through plasma coupling and sodium based absorption. The desulfurization tower and denitration tower in the device are separated from each other. The desulfurization tower comprises a desulfurization slurry circulating tank, a desulfurization spraying layer, a desulfurization demister, and a desulfurization flue gas outlet from bottom to top. A plasma demisting and oxidizing device comprises a demisting part and an oxidizing part, and the lower ends of the demisting part and the oxidizing part are both provided with a demisting wastewater outlet. The denitration and demercuration tower comprises a denitration and demercuration slurry circulating tank, a filling material layer, a denitration and demercuration spraying device, a denitration and demercuration demister, and a denitration and demercuration flue gas outlet from bottom to top. A desulfurization flue gas outlet is arranged between the desulfurization slurry circulating tank and the desulfurization spraying layer. The denitration and demercuration slurry circulating tank is connected to the oxidizing part. The demisting part is connected to the desulfurization flue gas outlet. The desulfurization slurry circulating tank is connected to the desulfurization spraying layer. The denitration and demercuration slurry circulating tank is connected to the denitration and demercuration spraying device. The desulfurization slurry circulating tank and the demisting wastewater outlet are both connected to the denitration and demercuration slurry circulating tank.
Description
Technical field
The present invention relates to a kind of flue gas treating reactor of coal-burning boiler, specifically a kind of double tower type plasmon coupling sodium base absorbs flue gas device for deep cleaning and method.
Background technology
China is as big coal country and coal-fired big country, and the ratio of coal in China's primary energy is up to more than 65%.Containing a large amount of atmosphere pollutions in the flue gas of Discharged form Coal Combustion, as: SO
2, NOx and Hg etc., serious harm is caused to atmospheric environment and health.The SO that current China is produced by fire coal
2with NOx discharge respectively up to 2,070 ten thousand tons (2014) and 1,643 ten thousand tons (2007), account for 90% and 70% of national total release.
SO
2and NO
xmain harm be the destruction causing acid rain and ozone layer, high risks is caused to ecological environment and health, causes economic loss to reach more than 1,000 hundred million yuan every year.To this, country has put into effect corresponding prevention and cure of pollution policy in aspect, comparatively detailed discharge standard and criterion are formulated, encourage to reduce discharge, sulfur dioxide control district and acid rain control district (being called for short " dicontrolled area ") delimited, carry out overall control and concentration control, namely on the basis of carrying out full factory prediction emission, add chimney SO
2the restriction of concentration of emission, and link up with the sulfur content of " dicontrolled area " and coal.In recent years, along with the continuous progress of smoke gas treatment technology and increasingly strict to environmental requirement, China's atmosphere pollutants emission standards is increasingly strict, has even exceeded numerous developed countries standard.Now, China's " fossil-fuel power plant atmospheric pollutant emission standard-2011 " is to the SO in coal steam-electric plant smoke
2, the maximum limit of NOx, Hg discharge quality concentration is respectively 50mg/m
3, 100mg/m
3, 0.03mg/m
3.Therefore must to the SO in flue gas
2, NOx and Hg discharge carry out the requirement that controls to make it to reach existing emission concentration standard.
Flue gas desulfurization technique mainly uses wet method limestone-gypsum method.Wet method limestone-gypsum method can arrive the desulfurization degree of about 95%, but for the concentration of emission day by day improved, the method is more and more painstaking, and the absorbent simultaneously used easily produces blockage problem; Flue gas denitration simultaneously mainly uses SCR denitration technology, but SCR method is with NH
3for reducing gases, have that transport difficult, investment and operating cost are high, catalyst easy in inactivation and catalyst after expensive, passivation easily cause secondary pollution, operating temperature range is narrow, the defect such as complex process.The domestic and international research to demercuration is less at present, mainly utilizes and improves the discharge that combustion system reduces mercury, although demercuration discharge capacity does not have strict demand, bring into schedule.
At present, wet desulphurization device has higher desulfuration efficiency, but denitration efficiency almost can be ignored.This mainly because more than 95% be NO in flue gas, is insoluble in water, very difficult absorb by absorbent.So the flue gas and desulfurizing and denitrifying integrated technique of developing the economy feasible is imperative.Although wet desulphurization can remove the mercury oxide of a part in addition, but the Elemental Mercury of the larger proportion existed in flue gas cannot effectively remove, change into so upgrading must be carried out to existing demercuration technology, make it the discharge standard adapting to more and more stricter flue gas Hg.So the desulfurization denitration demercuration integrated technique of research and development high-efficiency and economic has become the focus of attention of domestic and international many research institutions.
If NO can be oxidized to NO
2etc. absorbable high-valence state NOx, become to be easy to the bivalent mercury absorbed by elemental mercury oxidation simultaneously, so likely realize wet desulphurization denitration and demercuration, reach process equipment simple, reduce energy consumption, disposal cost low, save the effects such as space.
This experimental provision adopts sodium alkali combined desulfurization and denitration demercuration, and the product after NaOH desulfurization can be utilized just can to become the reactant of denitration demercuration, the traditional C aCO not only solved
3absorbent easily causes the problem of blocking, and the utilization rate of absorbent improves greatly.Coordinate demercuration technology can reach the out of stock demercuration of desulfurization to carry out simultaneously simultaneously, all can reach discharging standards.In addition, original wet desulphurization device can be utilized, for transformation project, there is good using value.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of structure simple double tower type plasmon coupling sodium base and absorbs flue gas device for deep cleaning and method.
In order to solve the problems of the technologies described above, the invention provides a kind of double tower type plasmon coupling sodium base and absorbing flue gas device for deep cleaning, comprising desulfurizing tower, plasma demist oxidation unit and denitration demercuration tower; Described desulfurizing tower, plasma demist oxidation unit are connected successively with denitration demercuration tower, the Double-Tower Structure that formation desulfurizing tower and denitration demercuration tower are separated from each other.
Improvement as absorbing flue gas device for deep cleaning to double tower type plasmon coupling sodium base of the present invention: described desulfurizing tower comprises desulfurization slurry circulatory pool, desulfurization spraying layer, mist separator of desulfurization and the desulfurization fume outlet set gradually from bottom to top; Described plasma demist oxidation unit comprises the demist part, the oxidized portion that are interconnected, and the lower end of described demist part, oxidized portion arranges demist wastewater outlet; Described denitration demercuration tower comprise arrange from bottom to top successively denitration demercuration serum recycle pond, packing layer, denitration demercuration spray equipment, denitration demercuration demister and denitration demercuration exhanst gas outlet; Sidewall between described desulfurization slurry circulatory pool, desulfurization spraying layer is provided with desulfurization fume import; Sidewall between described denitration demercuration serum recycle pond and packing layer is provided with the import of denitration demercuration tower flue gas; Described demist part upper end arranges plasma demist oxidation unit gas approach and exports with desulfurization fume and be connected; Described oxidized portion upper end arranges plasma demist oxidation unit exhanst gas outlet and is connected with the import of denitration demercuration tower flue gas; Described desulfurization slurry circulatory pool is connected by being with the pipeline of pump with desulfurization spraying layer; Described denitration demercuration serum recycle pond is connected by being with the pipeline of pump with denitration demercuration spray equipment; Lower end, the demist wastewater outlet of described desulfurization slurry circulatory pool are all connected with denitration grout circulatory pool by pipeline.
Further improvement as absorbing flue gas device for deep cleaning to double tower type plasmon coupling sodium base of the present invention: the external slurry pool of described desulfurization slurry circulatory pool; Fresh sodium base absorbing liquid is provided with in this slurry pool; Described plasma demist oxidation unit exhanst gas outlet is provided with H
2the additive injection devices such as S.
Further improvement as absorbing flue gas device for deep cleaning to double tower type plasmon coupling sodium base of the present invention: described demist part forms passage by demist electrode and demist pole plate; Described demist electrode is disc type electrode; Disk is uniformly distributed from top to bottom along a polar curve; Described disk diameter 10mm, thickness 1 ~ 2mm, be spaced apart 10mm between arbitrary neighborhood disk; The spacing of disk electrode and demist pole plate is 300 ~ 400mm; Described oxidized portion forms passage by oxidizing electrode and oxidation pole plate; Described oxidizing electrode is needle electrode, is arranged symmetrically with and forms one group, be uniformly distributed from top to bottom along a polar curve by 4,6 or 8 pin same planes; The length 5mm of described every root pin; Tip diameter is less than 0.5mm, and described often group is spaced apart 10mm between needle electrode; Described two adjacent groups pin uniform crossover is arranged, during 4,6 or 8 pins, the angle between upper and lower pin is respectively 45 °, 30 ° and 22.5 °; Spacing between needle electrode and oxidation pole plate is 150 ~ 200mm.
Further improvement as absorbing flue gas device for deep cleaning to double tower type plasmon coupling sodium base of the present invention: the air duct that described demist part and oxidized portion lower end arrange level is interconnected; The lower end connected entrance of described oxidized portion arranges flue gas air guide.
A kind of double tower type plasmon coupling sodium base absorbs flue gas deep-purifying method, carries out desulfurization, plasma demist oxidation, the sulfuration of Hg and denitration demercuration process successively.
Improvement as absorbing flue gas deep-purifying method to double tower type plasmon coupling sodium base of the present invention: 1) described sweetening process comprises the steps: 1.1) original pending flue gas sprayed from top to bottom by sodium base absorbing liquid after carrying out dust removal process, makes the SO in flue gas
2contact with sodium base absorbing liquid is reverse, neutralization reaction occurs, completes desulphurization reaction; 1.2) flue gas completing desulfurization in above-mentioned steps is carried out preliminary demist by demister, enter plasma demist oxidation unit afterwards and carry out plasma demist oxidation step; 2) the plasma demist oxidizing process following steps described in: 2.1) by the flue gas after desulfurization through demist electrode electrion, negative electrical charge on water smoke lotus, moves to pole plate subsequently, then makes liquid flow from top to bottom; 2.2) the flue gas level after demist enters plasma oxidation section, then flows from bottom to top, through the electrion of oxidizing electrode, produces a large amount of oxidative free radical, NO and Hg is oxidized to NO respectively
2, HNO
2, HNO
3with HgO; 2.3) flue gas after oxidation is discharged from the outlet of plasma demist oxidator, enters the sulfidation of Hg afterwards; 3) sulfidation of the mercury described in comprises the steps: 3.1) pass through H
2s jetting device sprays into H to the flue gas after oxidation
2s gas, changes into HgS by HgO; H
2the addition of S is as follows: H
2s:Hg=1.5:1 ~ 2:1, the H after adding
2s and HgO reaction generates HgS; 4) the denitration demercuration process described in comprises the steps: 4.1) by above step 1.2) in the desulfurizing byproduct that produces and step 2.1) liquid solution of collecting sprays from top to bottom as the absorbing liquid of denitration and demercuration, and flue gas after sulfuration by packing layer time, fully contact with the solution of spray, there is redox reaction, finally complete NO_x Reduction by Effective; And by step 1.2) with the sulfuration of non-complete reaction sodium base absorbing liquid after smoke contacts, there is neutralization reaction, complete partial denitrification; And the H of this sodium base absorbing liquid and non-complete reaction
2there is neutralization reaction in S, generates Na
2s, completes H
2s removes; And Na
2s and NO
2there is redox reaction, promote that NOx removes.
While described denitration, the HgS in flue gas is washed in packing layer, completes finally removing of Hg;
4.2) accessory substance after denitration demercuration is regularly discharged to aerator and is oxidized, and is converted into Na completely
2sO
4, NaHSO
4and NaNO
3after enter wastewater treatment equipment again;
4.3) flue gas after denitration demercuration process is directly discharged after simple demist.
SO in a kind of flue gas
2, NOx and Hg deep removal method, comprise the steps:
(1) desulfurization
Flue gas after high-effective dust-removing is introduced desulfurizing tower, with NaOH absorbing liquid spray, the SO in flue gas
2there is quick neutralization reaction with NaOH, complete high-efficiency desulfurization, control the addition of fresh NaOH absorbing liquid simultaneously, generate Na
2sO
3/ NaHSO
3mixed liquor, for removing of follow-up NOx;
(2) demist, oxidation
First efficient demist is carried out: flue gas moves from top to bottom from desulfurizing tower flue gas out, negative electrical charge on drop lotus, pole plate is moved to afterwards under electrostatic force, then the bottom of plasma demist oxidation unit is flow to from top to bottom, finally discharged by wastewater outlet, enter the denitration grout circulatory pool of denitration demercuration tower; Flue gas bottom horizontal flow sheet after demist is to the bottom of oxidized portion, then flow from bottom to top in oxidized portion, realizing the oxidation of NO and Hg: create a large amount of oxidative free radicals in discharge process, there is oxidation reaction in NO and Hg in described free radical and flue gas, generates the NO being easy to absorb
2, HNO
2, HNO
3and HgO; Flue gas is from bottom to top through oxidized portion, and the flue gas finally after oxidation is discharged from its top;
(3) sulfuration of Hg
First flue gas after oxidation carries out sulfuration in flue, sprays into H at the smoke outlet of oxidized portion (23)
2s gas, makes HgO be converted into HgS;
(4) the denitration removal of mercury
The accessory substance Na produced in sweetening process
2sO
3/ NaHSO
3blend absorbent introduces the recycle slurry liquid pool of denitration demercuration tower as the absorbing liquid of denitration demercuration, is sprayed to packing layer from top to bottom; Flue gas after sulfuration passes through packing layer, reverse contact Na
2sO
3/ NaHSO
3blend absorbent, on the one hand Na
2sO
3/ NaHSO
3and NO
2by redox reaction, HgS absorbed liquid is washed on the other hand, completes the denitration removal of mercury; Simultaneously in denitration removal of mercury process, the H of non-complete reaction
2s is absorbed by NaOH, and the product Na after absorbing
2s also participates in denitration, and last flue gas enters air by accessing chimney after demister.
As to SO in flue gas of the present invention
2, NOx and Hg deep removal further improvements in methods: Na in described step
2sO
3/ NaHSO
3the generation step of mixed liquor is as follows:
2NaOH+SO
2＝Na
2SO
3+H
2O
Na
2SO
3+SO
2+H
2O＝2NaHSO
3；
In described step (2), the generation step of free radical is as follows:
O
2+e＝O+O+e
H
2O+e＝OH+H+e
O+O
2＝O
3；
In described step (2), the oxidation step of NO and Hg is as follows:
NO+O＝NO
2
NO+O
3＝NO
2+O
2
NO+OH＝HNO
2
NO
2+OH＝HNO
3
Hg+O＝HgO
Hg+O
3＝HgO+O
2；
In described step (3), vulcanization reaction step is as follows:
HgO+H
2S＝HgS+H
2O；
In described step (4), denitrification step is as follows:
2NaOH+NO
2+NO＝2NaNO
2+H
2O
2NaOH+2NO
2＝NaNO
2+NaNO
3+H
2O
2NaOH+H
2S＝Na
2S+2H
2O
4Na
2SO
3+2NO
2＝4Na
2SO
4+N
2
Na
2SO
3+2NO
2+H
2O＝Na
2SO
4+2HNO
2
4NaHSO
3+2NO
2＝4NaHSO
4+N
2
NaHSO
3+2NO
2+H
2O＝NaHSO
4+2HNO
2
Na
2S+2NO
2＝Na
2SO
4+N
2。
As to SO in flue gas of the present invention
2, NOx and Hg deep removal further improvements in methods: regularly bottom the denitration grout circulatory pool of denitration demercuration tower, discharge waste water, after carrying out pressure air oxidation, by the Na of high concentration
2sO
4, NaHSO
4, HgS is discharged to wastewater treatment equipment.
Double tower type plasmon coupling sodium base of the present invention absorbs flue gas device for deep cleaning compared with the prior art, has following beneficial effect:
(1) adopt wet desulphurization denitration demercuration, efficiency is high, and accessory substance easily processes.
(2) adopt sodium base absorbant, absorption rate is fast, effective and absorbent and absorption product are solubility.Product Na after desulfurization simultaneously
2sO
3and NaHSO
3can be used as the absorbent of denitration demercuration, the traditional C aCO not only solved
3absorbent easily causes the problem of blocking, and the utilization rate of absorbent improves greatly.
(3) using plasma forced oxidation and two sections of absorptions, the SO in efficient removal flue gas
2, NOx and Hg, SO in tail gas
2, NOx and Hg concentration can control at 30mg/Nm respectively
3, 50mg/Nm
3and 0.01mg/Nm
3below, SO
2, NOx emission concentration can reach combustion gas standard.
(4) plasma reactor adopts two-piece design, and according to the particular/special requirement of demist and oxidative function, namely except fog effect depends on more electronics, and oxidation effectiveness depends on higher electron energy.Demist and oxidation are separately carried out and carried out different designs to discharging structure, avoids a large amount of drop absorption high energy electrons after wet desulphurization, greatly can improve the oxidation efficiency of NO and Hg.
(5) because HgO instability is easily reduced, after plasma reactor, a small amount of H is sprayed into
2s, makes the HgO after oxidation react in time, generates stable product HgS, avoid Hg
2+back reaction occurs and regenerates HgO, the removal efficiency of full mercury can reach more than 80%.
(6) Na
2sO
3and NaHSO
3with NO
2have good reaction effect, adopt packed tower simultaneously, the reaction time increases greatly, contributes to sodium sulfite and sodium hydrogensulfite and NO
2redox reaction, denitration can reach more than 80%, realizes NO_x Reduction by Effective.
(7) adopt spray column and packed tower two-part to arrange, carry out the plasma forced oxidation of NO and HgO after desulfurization, avoid SO
2competitive reaction, the oxidation effectiveness of NO and HgO is good, substantially increases denitration and the demercuration effect of follow-up packed tower.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the specific embodiment of the present invention is described in further detail.
Fig. 1 is primary structure schematic diagram of the present invention;
Fig. 2 is the primary structure schematic diagram of demist part 22 in Fig. 1;
Fig. 3 is the primary structure schematic diagram of oxidized portion 23 in Fig. 1.
Detailed description of the invention
Embodiment 1, Fig. 1 provide a kind of double tower type plasmon coupling sodium base and absorb flue gas device for deep cleaning and method, comprise desulfurizing tower 1, plasma demist oxidation unit 2 and denitration demercuration tower 3.
The setting that the present invention adopts desulfurizing tower 1 and denitration demercuration tower 3 to be separated from each other; First this mode arranged that is separated reduces vying each other of desulfurization and denitration, improves desulfurized effect; Secondly after desulfurization, carrying out the oxidation of NOx and Hg out, contributing to improving oxidation efficiency; Finally can according to SO
2, NOx and Hg chemical characteristic, carry out the targeted design on absorption tower.
Desulfurizing tower 1 comprise set gradually from bottom to top desulfurization slurry circulatory pool 11, desulfurization fume import 12, desulfurization spraying layer 13, mist separator of desulfurization 14 and desulfurization fume outlet 15.
The bottom of desulfurization slurry circulatory pool 11 is provided with Na
2sO
3and NaHSO
3mixture export 10.Mixture export 10 bottom desulfurization slurry circulatory pool 11 is connected by the mixed liquor import 36 of slush pump 4 with the serum recycle pond 31 of denitration demercuration tower 3; Desulfurization slurry circulatory pool 11 sidewall opening is provided with desulfurization slurry pump inlet 16, and the desulfurization spraying layer 13 that slurries (slurries in desulfurization slurry circulatory pool 11) squeeze into desulfurizing tower 1 top is connected (solution in desulfurization slurry circulatory pool 11 being squeezed into desulfurization spraying layer 13 by desulfurization slurry circulating pump I 17) by desulfurization slurry circulating pump I 17 by this desulfurization slurry pump inlet 16; Desulfurizing tower 1 sidewall (position between desulfurization spraying layer 13 and the desulfurization slurry circulatory pool 11) upper shed of desulfurization slurry circulatory pool more than 11 is provided with desulfurization fume import 12, and this desulfurization fume import 12 connects dust arrester 5; Desulfurizing tower 1 sidewall upper shed below desulfurization fume import 12 is provided with fresh NaOH entrance 18, and desulfurization slurry circulatory pool 11 connects NaOH slurry pool 6 by NaOH entrance 18.
Desulfurizing tower 1 is according to hollow-spraying-tower design, and spray column can provide the absorbing liquid coverage rate of 200 ~ 300%, efficient absorption SO
2, the removal efficiency of more than 98% can be reached when NaOH absorbing liquid sprays, meet the current SO improved constantly
2discharge standard.
Accessory substance Na after NaOH absorbs
2sO
3and NaHSO
3as the absorbing liquid of denitration, Na
2sO
3and NaHSO
3to NO
2assimilation effect be better than NaOH far away, not only reach the object that absorbent makes full use of, and reach the efficient absorption of NOx.
Plasma demist oxidation unit 2 comprises plasma demist oxidation unit gas approach 21, demist part 22, oxidized portion 23, plasma demist oxidation unit exhanst gas outlet 24, wastewater outlet 25.Plasma demist oxidation unit gas approach 21 is set after the upper end open of demist part 22; The side of this demist part 22 arranges oxidized portion 23, and the upper end open of this oxidized portion 23 arranges plasma demist oxidation unit exhanst gas outlet 24; Demist part 22 and oxidized portion 23 arrange the liquid collection trough of funnel type by lower end, and the lower end of this liquid collection trough is provided with wastewater outlet 25, and wastewater disposal basin upper end then forms the air duct 27 that level is communicated with demist part 22 and oxidized portion 23.
Above-described demist part 22 is made up of multichannel demist electrode and demist pole plate, and flue gas flows from top to bottom; Oxidized portion 23 is made up of multichannel oxidizing electrode and oxidation pole plate, and flue gas flows from bottom to top; Plasma demist oxidation unit exhanst gas outlet 24 place arranges H
2s injection device 26, is preferably multiple nozzle and is evenly arranged in flue.
Plasma demist oxidation unit gas approach 21 connects the desulfurization fume outlet 15 of desulfurizing tower 1; Plasma demist oxidation unit exhanst gas outlet 24 connects the denitration demercuration tower flue gas import 37 of denitration demercuration tower 3; Wastewater outlet 25 is for the discharge of liquid after demist, and wastewater outlet 25 directly connects the mixed liquor import 36 of denitration demercuration tower 3, enters the denitration grout circulatory pool 31 of denitration demercuration tower 3.
Because after wet desulphurization, cigarette temperature drops to about 70 DEG C from 150 DEG C, a large amount of heats is only absorbed by the water, produce a large amount of steam, although be stripped of the steam drop of a part through demister 14, a large amount of fine drop is still had to exist, if be directly oxidized the flue gas after desulfurization, so plasma discharge processes will be subject to the impact of steam, cause the too large discharge voltage of humidity to reduce on the one hand, the oxidative free radical of generation will greatly reduce, and affect oxidation effectiveness; The high energy electron that electric discharge produces on the other hand mainly participates in demist process, instead of O
2or H
2the ionization of O, oxidation effectiveness will reduce further.So drop is first removed by the present invention before the oxidation, according to the different designs requirement of demist and oxidation, special design is carried out to electrode, not only improved except fog effect, and greatly can improve the oxygenation efficiency of NO and Hg.
Denitration demercuration tower 3 comprise arrange from bottom to top successively denitration grout circulatory pool 31, denitration demercuration tower flue gas import 37, packing layer 32, denitration demercuration spray equipment 33, denitration demercuration demister 34 and denitration demercuration exhanst gas outlet 35.Side sidewall opening above denitration grout circulatory pool 31 arranges Na
2sO
3and NaHSO
3mixed liquor import 36; After the sidewall opening of denitration grout circulatory pool 31 other side, denitration grout pump inlet 38 is set, this denitration grout pump inlet 38 connects denitration demercuration spray equipment 33 by denitration grout circulating pump II 39, by denitration grout circulating pump II 39, slurries is squeezed into denitration demercuration spray equipment 33; The bottom of denitration grout circulatory pool 31 is provided with sewage draining exit, discharges HgS and high concentration Na
2sO
4and NaHSO
4, and the solution of discharging the most at last introducing wastewater treatment equipment processes; The top in serum recycle pond 31 arranges denitration demercuration tower flue gas import 37 (the sidewall upper shed between denitration demercuration spray equipment 33 and serum recycle pond 31 arranges denitration demercuration tower flue gas import 37), and this denitration demercuration tower flue gas import 37 connects the plasma demist oxidation unit exhanst gas outlet 24 of plasma demist oxidation unit 2.
Flue gas through packing layer 32 NO_x removal and HgS, then removes water smoke through denitration demercuration demister 34, and the flue gas after last deep purifying is discharged by denitration demercuration exhanst gas outlet 35 (denitration demercuration exhanst gas outlet 35 is herein set to chimney).The main purpose of denitration demercuration tower 3 be by oxidation after NOx and Na
2sO
3/ NaHSO
3react, thus realize the object of denitration, in addition the HgS after sulfuration is washed, realize demercuration.Denitration demercuration tower 3 is designed to packed tower form, can increases the time of staying of gas at packing layer 32, strengthening gas-liquid contact, contributes to NO
2efficient absorption, and a small amount of HgS can not cause the blocking of packing layer 32, is also applicable to demercuration simultaneously.
Above-described because packing layer 32, demister 14 etc. are all conventional settings, adopt prior art.
Plasmon coupling sodium base absorbs double tower type coal-fired flue-gas multiple pollutant deep removal method, comprises sweetening process, plasma demist oxidation, the sulfuration of Hg and denitration demercuration process: its step is as follows:
1, sweetening process comprises the steps:
1.1, pass between desulfurization slurry circulatory pool 11 and desulfurization spraying layer 13 by the desulfurization fume import 12 of desulfurizing tower 1 after coal-burning boiler flue gas out carries out high-effective dust-removing (being completed by dust arrester 5);
1.2, use desulfurization slurry circulating pump I 17 that sodium base absorbing liquid is squeezed into desulfurization spraying layer 13 from desulfurization slurry circulatory pool 11, spray a large amount of sodium base absorbing liquids by desulfurization spraying layer 13;
1.3, the SO in flue gas
2contact with sodium base absorbing liquid is reverse, neutralization reaction occurs, completes high-efficiency desulfurization;
1.4, the flue gas after desulfurization first carries out preliminary demist through mist separator of desulfurization 14; Then export 15 by desulfurization fume to discharge, and enter the reaction that plasma demist oxidation unit 2 carries out next step;
1.5, the accessory substance Na produced in this step (step 1.4)
2sO
3/ NaHSO
3part squeezes into the absorbing liquid of denitration demercuration serum recycle pond 31 as denitration demercuration.
2, plasma demist oxidizing process following steps:
2.1, the flue gas (step 1.4 derives) after desulfurization is passed into plasma demist oxidation unit gas approach 21;
2.2, flue gas enters demist part 22 first from top to bottom, through the electrion of demist electrode, and negative electrical charge on water smoke lotus, move to pole plate subsequently, then flow into bottom liquid feeder, be finally expelled to the serum recycle pond 31 of denitration demercuration tower 3 from wastewater outlet 25, complete whole defrosting function;
Plasma demist is best defogging method known at present, effectively can remove the droplet in flue gas, obviously improves the problem that wet desulphurization afterbody emits white cigarette; Flow from top to bottom at demist part 22 flue gas, effectively can strengthen the flowing of drop on pole plate, reach better droplet removal efficiency.
2.3, the flue gas after demist enters plasma oxidation part 23 by horizontally disposed air duct 27 level, then flows from bottom to top; Through the electrion of oxidizing electrode, produce a large amount of oxidative free radical, NO and Hg is oxidized to NO respectively
2, HNO
2, HNO
3with HgO;
When level enters oxidized portion 23, in order to ensure that flue gas is uniformly distributed in the plasma channel of oxidized portion 23, flue gas air guide can be increased according to flow field simulation calculation result bottom oxidation panel.
2.4, the flue gas after oxidation is discharged from plasma demist oxidation unit exhanst gas outlet 24, afterwards first through the sulfuration of mercury, finally enters denitration demercuration tower 3.
The sulfidation of 3, described mercury comprises the steps:
3.1, H is set at plasma demist oxidation unit exhanst gas outlet 24
2s jetting device 26, sprays into appropriate H
2s gas;
3 ~ 5 H are evenly set in flue
2s nozzle; HgO is changed into HgS by the sulfuration of mercury, thus avoids HgO to be again reduced into Hg, improves demercuration effect.
3.2, H
2the addition of S is: H
2s:Hg (total mercury)=1.5:1 ~ 2:1, the H after adding
2s and HgO reaction generates HgS; Because flue gas mixes uneven in flue, so H
2the addition of S is higher than the content of Hg in flue gas, strengthens cure efficiency with this.The H of non-complete reaction
2s will react with NaOH and generate Na in denitration demercuration tower 3
2s is removed.Na
2s is also that a kind of NOx preferably removes agent, about removing have certain promotion to NOx.
3.3, the flue gas after sulfuration enters denitration demercuration tower 3, and final HgS is removed by the washing of packed tower.
4, described denitration demercuration process comprises the steps:
The 4.1 accessory substance Na produced by sweetening process
2sO
3/ NaHSO
3denitration demercuration serum recycle pond 31 is directly squeezed into from desulfurization slurry circulatory pool 11, as the absorbing liquid of denitration and demercuration by slush pump 4; NaOH also containing a small amount of non-complete reaction in this mixed liquor.
4.2, the flue gas after over cure enters packing layer 32 from denitration demercuration tower 3 gas approach 12, with the Na of spray
2sO
3/ NaHSO
3absorbing liquid fully contacts, Na
2sO
3/ NaHSO
3and NO
2there is redox reaction, finally complete NO_x Reduction by Effective; NaOH and HNO of non-complete reaction in addition
2, HNO
3there is neutralization reaction, also can complete partial denitrification; In addition, the H of NaOH and non-complete reaction
2there is neutralization reaction in S, generates Na
2s, completes H
2s removes, in order to avoid cause secondary pollution.And Na
2s also can and NO
2there is redox reaction, thus the certain facilitation of generation is removed to NOx.While denitration, the HgS in flue gas is also washed down in packing layer, completes finally removing of Hg.
4.3, the accessory substance in denitration demercuration rear slurry pond is regularly discharged to aerator from bottom blow-down mouth and is oxidized, and is converted into Na completely
2sO
4, NaHSO
4and NaNO
3after enter wastewater treatment equipment again;
4.4, owing to entering the cigarette temperature of denitration demercuration tower 3 at 60 ~ 70 DEG C, so the water smoke produced in denitration demercuration process is very little and not containing other impurity, after simple demist, flue gas directly enters chimney, finally realizes the deep removal of various pollutants in fume.
Above-described demist part 22 is made up of multichannel demist electrode and demist pole plate; Described demist electrode is disc type electrode; Demist electrode is disc type electrode, exactly multiple disc-shaped component is evenly together in series from top to bottom along a polar curve, disk diameter 10mm, thickness 1 ~ 2mm, is spaced apart 10mm between arbitrary neighborhood disk; Disk electrode be 300 ~ 400mm with the spacing of pole plate.The corona that disc type electrode produces covers whole discharge space, and flue gas is in the flowing direction without any blind area.In order to prevent corona zone screen effect each other, the interval of disk is preferably 10mm.Be not easy under wide die opening in addition to produce spark discharge, make electric discharge more steady, contribute to the charged of droplet and migration, promote removing, so the die opening of demist section is preferably 300 ~ 400mm in the present invention of droplet.
Above-described oxidized portion 23 is made up of multichannel oxidizing electrode and oxidation pole plate; Oxidizing electrode is needle electrode, is arranged symmetrically with exactly and forms one group, be uniformly distributed from top to bottom along a polar curve by 4,6 or 8 pin same planes, and many group pins are welded on a polar curve at regular intervals.The length 5mm of every root pin; Tip diameter is less than 0.5mm, and described often group is spaced apart 10mm between needle electrode; Two adjacent groups pin uniform crossover is arranged, during 4,6 or 8 pins, the angle between upper and lower pin is respectively 45 °, 30 ° and 22.5 °; Spacing between needle electrode and pole plate is 150 ~ 200mm.Needle electrode electric discharge radius of curvature is little, is more prone to produce spark discharge, thus improves electron energy, strengthens, with the collision of gas molecule, producing more oxidative free radical.Also be that the interval often organizing needle electrode is preferably 10mm in order to prevent corona zone screen effect each other simultaneously.In addition in order to region of discharge can better cover discharging gap, the layout of upper and lower two groups of pin electrodes adopts interleaved mode, and be namely certain angle between upper and lower two groups of pins, angle corresponding respectively during 4,6 or 8 pins is 45 °, 30 ° and 22.5 °.Finally, narrower discharging gap can be more prone to produce spark discharge, the generation of oxidation free love base, thus promotes the oxidation effectiveness of NO and Hg, and in the present invention, the die opening of oxidation panel is preferably 150 ~ 200mm.
In the above step, with NaOH absorbing liquid for sodium base absorbing liquid carries out the explanation of specific implementation step:
(1) desulfurization
Flue gas after high-effective dust-removing is introduced desulfurizing tower 1, with NaOH absorbing liquid spray, the SO in flue gas
2there is quick neutralization reaction with NaOH, complete high-efficiency desulfurization, control the addition of fresh NaOH absorbing liquid simultaneously, generate Na
2sO
3/ NaHSO
3mixed liquor, for removing of follow-up NOx;
2NaOH+SO
2＝Na
2SO
3+H
2O
Na
2SO
3+SO
2+H
2O＝2NaHSO
3；
(2) demist, oxidation
First efficient demist is carried out through demist section: flue gas moves from top to bottom from desulfurizing tower 1 flue gas out, negative electrical charge on drop lotus, pole plate is moved to afterwards under electrostatic force, then the bottom of plasma demist oxidation reactor is flow to from top to bottom, finally discharged by the wastewater outlet of bottom, enter denitration demercuration tower 3 recycle slurry liquid pool.
Flue gas bottom horizontal flow sheet after demist is to oxidation panel, then flow from bottom to top at oxidation panel, realizing the efficient oxidation of NO and Hg: create a large amount of oxidative free radicals in discharge process, there is oxidation reaction in NO and Hg in these free radicals and flue gas, generates the NO being easy to absorb
2, HNO
2, HNO
3with materials such as HgO.Flue gas is from bottom to top through oxidation panel, and the flue gas finally after oxidation is discharged from reactor head.
The generation of free radical:
O
2+e＝O+O+e
H
2O+e＝OH+H+e
O+O
2＝O
3；
The oxidation of NO and Hg:
NO+O＝NO
2
NO+O
3＝NO
2+O
2
NO+OH＝HNO
2
NO
2+OH＝HNO
3
Hg+O＝HgO
Hg+O
3＝HgO+O
2；
(3) sulfuration of Hg
First flue gas after oxidation carries out sulfuration in flue, in the flue of demist oxidator exhanst gas outlet 15, spray into suitable H
2s gas, mainly makes HgO be converted into the more stable HgS of chemical property, to avoid back reaction and regenerate Elemental Mercury, finally removed by washing in the packing layer of follow-up denitration demercuration tower 3.
Vulcanization reaction is:
HgO+H
2S＝HgS+H
2O；
(4) the denitration removal of mercury
The accessory substance Na produced in sweetening process
2sO
3/ NaHSO
3blend absorbent introduces the absorbing liquid of recycle slurry liquid pool as denitration demercuration of denitration demercuration tower 3.Flue gas after sulfuration enters the packing layer of denitration demercuration tower 3, reverse contact Na
2sO
3/ NaHSO
3blend absorbent, on the one hand Na
2sO
3/ NaHSO
3and NO
2by redox reaction, HgS can absorbed liquid wash on the other hand, completes the efficient denitration removal of mercury.Also there is the H of non-complete reaction in denitration removal of mercury process simultaneously
2s is absorbed by NaOH, and the product Na after absorbing
2s also can participate in denitration.Last flue gas enters air by access chimney after demister 14.
Denitration reaction is:
2NaOH+NO
2+NO＝2NaNO
2+H
2O
2NaOH+2NO
2＝NaNO
2+NaNO
3+H
2O
2NaOH+H
2S＝Na
2S+2H
2O
4Na
2SO
3+2NO
2＝4Na
2SO
4+N
2
Na
2SO
3+2NO
2+H
2O＝Na
2SO
4+2HNO
2
4NaHSO
3+2NO
2＝4NaHSO
4+N
2
NaHSO
3+2NO
2+H
2O＝NaHSO
4+2HNO
2
Na
2S+2NO
2＝Na
2SO
4+N
2。
In addition, regularly bottom the serum recycle pond 31 of denitration demercuration tower 3, discharge waste water, after carrying out pressure air oxidation, by the Na of high concentration
2sO
4, NaHSO
4, HgS etc. is discharged to wastewater treatment equipment.
Finally, it is also to be noted that what enumerate above is only a specific embodiment of the present invention.Obviously, the invention is not restricted to above embodiment, many distortion can also be had.All distortion that those of ordinary skill in the art can directly derive from content disclosed by the invention or associate, all should think protection scope of the present invention.
Claims (10)
1. double tower type plasmon coupling sodium base absorbs a flue gas device for deep cleaning, comprises desulfurizing tower (1), plasma demist oxidation unit (2) and denitration demercuration tower (3); It is characterized in that: described desulfurizing tower (1), plasma demist oxidation unit (2) are connected successively with denitration demercuration tower (3), the Double-Tower Structure that formation desulfurizing tower (1) and denitration demercuration tower (3) are separated from each other.
2. double tower type plasmon coupling sodium base according to claim 1 absorbs flue gas device for deep cleaning, it is characterized in that: described desulfurizing tower (1) comprises desulfurization slurry circulatory pool (11), desulfurization spraying layer (13), mist separator of desulfurization (14) and the desulfurization fume outlet (15) that set gradually from bottom to top;
Described plasma demist oxidation unit (2) comprises the demist part (22), the oxidized portion (23) that are interconnected, and the lower end of described demist part (22), oxidized portion (23) arranges demist wastewater outlet (25);
Described denitration demercuration tower (3) comprise arrange from bottom to top successively denitration demercuration serum recycle pond (31), packing layer (32), denitration demercuration spray equipment (33), denitration demercuration demister (34) and denitration demercuration exhanst gas outlet (35);
Sidewall between described desulfurization slurry circulatory pool (11), desulfurization spraying layer (13) is provided with desulfurization fume import (12);
Sidewall between described denitration demercuration serum recycle pond (31) and packing layer (32) is provided with denitration demercuration tower flue gas import (37);
Described demist part (22) upper end arranges plasma demist oxidation unit gas approach (21) and exports (15) with desulfurization fume and be connected; Described oxidized portion (23) upper end arranges plasma demist oxidation unit exhanst gas outlet (24) and is connected with denitration demercuration tower flue gas import (37);
Described desulfurization slurry circulatory pool (11) is connected by being with the pipeline of pump with desulfurization spraying layer (13);
Described denitration demercuration serum recycle pond (31) is connected by being with the pipeline of pump with denitration demercuration spray equipment (33);
Lower end, the demist wastewater outlet (25) of described desulfurization slurry circulatory pool (11) are all connected with denitration grout circulatory pool (31) by pipeline.
3. double tower type plasmon coupling sodium base according to claim 2 absorbs flue gas device for deep cleaning, it is characterized in that: the external slurry pool of described desulfurization slurry circulatory pool (11) (6);
Fresh sodium base absorbing liquid is provided with in this slurry pool (6);
Described plasma demist oxidation unit exhanst gas outlet (24) is provided with H
2the additive injection devices (26) such as S.
4. double tower type plasmon coupling sodium base according to claim 3 absorbs flue gas device for deep cleaning, it is characterized in that: described demist part (22) forms passage by demist electrode and demist pole plate;
Described demist electrode is disc type electrode; Disk is uniformly distributed from top to bottom along a polar curve;
Described disk diameter 10mm, thickness 1 ~ 2mm, be spaced apart 10mm between arbitrary neighborhood disk;
The spacing of disk electrode and demist pole plate is 300 ~ 400mm;
Described oxidized portion (23) forms passage by oxidizing electrode and oxidation pole plate;
Described oxidizing electrode is needle electrode, is arranged symmetrically with and forms one group, be uniformly distributed from top to bottom along a polar curve by 4,6 or 8 pin same planes;
The length 5mm of described every root pin; Tip diameter is less than 0.5mm, and described often group is spaced apart 10mm between needle electrode;
Described two adjacent groups pin uniform crossover is arranged, during 4,6 or 8 pins, the angle between upper and lower pin is respectively 45 °, 30 ° and 22.5 °;
Spacing between needle electrode and oxidation pole plate is 150 ~ 200mm.
5. double tower type plasmon coupling sodium base according to claim 4 absorbs flue gas device for deep cleaning, it is characterized in that: the air duct (27) that described demist part (22) and oxidized portion (23) lower end arrange level is interconnected;
The lower end connected entrance of described oxidized portion (23) arranges flue gas air guide.
6. double tower type plasmon coupling sodium base absorbs a flue gas deep-purifying method, it is characterized in that: carry out desulfurization, plasma demist oxidation, the sulfuration of Hg and denitration demercuration process successively.
7. double tower type plasmon coupling sodium base according to claim 6 absorbs flue gas deep-purifying method, it is characterized in that:
1) described sweetening process comprises the steps:
1.1) sprayed from top to bottom by sodium base absorbing liquid after original pending flue gas carries out dust removal process, make the SO in flue gas
2contact with sodium base absorbing liquid is reverse, neutralization reaction occurs, completes desulphurization reaction;
1.2) flue gas completing desulfurization in above-mentioned steps is carried out preliminary demist by demister, enter plasma demist oxidation unit afterwards and carry out plasma demist oxidation step;
2) the plasma demist oxidizing process following steps described in:
2.1) by the flue gas after desulfurization through demist electrode electrion, negative electrical charge on water smoke lotus, moves to pole plate subsequently, then makes liquid flow from top to bottom;
2.2) the flue gas level after demist enters plasma oxidation section, then flows from bottom to top, through the electrion of oxidizing electrode, produces a large amount of oxidative free radical, NO and Hg is oxidized to NO respectively
2, HNO
2, HNO
3with HgO;
2.3) flue gas after oxidation is discharged from the outlet of plasma demist oxidator, enters the sulfidation of Hg afterwards;
3) sulfidation of the mercury described in comprises the steps:
3.1) H is passed through
2s jetting device sprays into H to the flue gas after oxidation
2s gas, changes into HgS by HgO;
H
2the addition of S is as follows:
H
2s:Hg=1.5:1 ~ 2:1, the H after adding
2s and HgO reaction generates HgS;
4) the denitration demercuration process described in comprises the steps:
4.1) by above step 1.2) in the desulfurizing byproduct that produces and step 2.1) liquid solution of collecting sprays from top to bottom as the absorbing liquid of denitration and demercuration, and flue gas after sulfuration by packing layer time, fully contact with the solution of spray, there is redox reaction, finally complete NO_x Reduction by Effective;
And by step 1.2) with the sulfuration of non-complete reaction sodium base absorbing liquid after smoke contacts, there is neutralization reaction, complete partial denitrification; And the H of this sodium base absorbing liquid and non-complete reaction
2there is neutralization reaction in S, generates Na
2s, completes H
2s removes; And Na
2s and NO
2there is redox reaction, promote that NOx removes;
While described denitration, the HgS in flue gas is washed in packing layer, completes finally removing of Hg;
4.2) accessory substance after denitration demercuration is regularly discharged to aerator and is oxidized, and is converted into Na completely
2sO
4, NaHSO
4and NaNO
3after enter wastewater treatment equipment again;
4.3) flue gas after denitration demercuration process is directly discharged after simple demist.
8. SO in a flue gas
2, NOx and Hg deep removal method, it is characterized in that, comprise the steps:
(1) desulfurization
Flue gas after high-effective dust-removing is introduced desulfurizing tower (1), with NaOH absorbing liquid spray, the SO in flue gas
2there is quick neutralization reaction with NaOH, complete high-efficiency desulfurization, control the addition of fresh NaOH absorbing liquid simultaneously, generate Na
2sO
3/ NaHSO
3mixed liquor, for removing of follow-up NOx;
(2) demist, oxidation
First efficient demist is carried out from desulfurizing tower (1) flue gas out:
Flue gas moves from top to bottom, negative electrical charge on drop lotus, pole plate is moved to afterwards under electrostatic force, then the bottom of plasma demist oxidation unit (2) is flow to from top to bottom, finally discharged by wastewater outlet (25), enter the denitration grout circulatory pool (31) of denitration demercuration tower (3);
Flue gas bottom horizontal flow sheet after demist, to the bottom of oxidized portion (23), then flows from bottom to top in oxidized portion (23), realizes the oxidation of NO and Hg:
Creating a large amount of oxidative free radicals in discharge process, there is oxidation reaction in NO and Hg in described free radical and flue gas, generates the NO being easy to absorb
2, HNO
2, HNO
3and HgO;
Flue gas is from bottom to top through oxidized portion (23), and the flue gas finally after oxidation is discharged from its top;
(3) sulfuration of Hg
First flue gas after oxidation carries out sulfuration in flue, sprays into H at the smoke outlet of oxidized portion (23)
2s gas, makes HgO be converted into HgS;
(4) the denitration removal of mercury
The accessory substance Na produced in sweetening process
2sO
3/ NaHSO
3blend absorbent introduces the recycle slurry liquid pool of denitration demercuration tower as the absorbing liquid of denitration demercuration, is sprayed to packing layer (32) from top to bottom;
Flue gas after sulfuration passes through packing layer (32), reverse contact Na
2sO
3/ NaHSO
3blend absorbent, on the one hand Na
2sO
3/ NaHSO
3and NO
2by redox reaction, HgS absorbed liquid is washed on the other hand, completes the denitration removal of mercury; Simultaneously in denitration removal of mercury process, the H of non-complete reaction
2s is absorbed by NaOH, and the product Na after absorbing
2s also participates in denitration, and last flue gas enters air by accessing chimney after demister.
9. SO in flue gas according to claim 8
2, NOx and Hg deep removal method, it is characterized in that: Na in described step (1)
2sO
3/ NaHSO
3the generation step of mixed liquor is as follows:
2NaOH+SO
2＝Na
2SO
3+H
2O
Na
2SO
3+SO
2+H
2O＝2NaHSO
3；
In described step (2), the generation step of free radical is as follows:
O
2+e＝O+O+e
H
2O+e＝OH+H+e
O+O
2＝O
3；
In described step (2), the oxidation step of NO and Hg is as follows:
NO+O＝NO
2
NO+O
3＝NO
2+O
2
NO+OH＝HNO
2
NO
2+OH＝HNO
3
Hg+O＝HgO
Hg+O
3＝HgO+O
2；
In described step (3), vulcanization reaction step is as follows:
HgO+H
2S＝HgS+H
2O；
In described step (4), denitrification step is as follows:
2NaOH+NO
2+NO＝2NaNO
2+H
2O
2NaOH+2NO
2＝NaNO
2+NaNO
3+H
2O
2NaOH+H
2S＝Na
2S+2H
2O
4Na
2SO
3+2NO
2＝4Na
2SO
4+N
2
Na
2SO
3+2NO
2+H
2O＝Na
2SO
4+2HNO
2
4NaHSO
3+2NO
2＝4NaHSO
4+N
2
NaHSO
3+2NO
2+H
2O＝NaHSO
4+2HNO
2
Na
2S+2NO
2＝Na
2SO
4+N
2。
10. SO in flue gas according to claim 8
2, NOx and Hg deep removal method, it is characterized in that:
Regularly discharge waste water, after carrying out pressure air oxidation, by the Na of high concentration from denitration grout circulatory pool (31) bottom of denitration demercuration tower (3)
2sO
4, NaHSO
4, HgS is discharged to wastewater treatment equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510455550.7A CN105056723B (en) | 2015-07-29 | 2015-07-29 | Twin-tower type flue gas deep purification device through plasma coupling and sodium based absorption and method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510455550.7A CN105056723B (en) | 2015-07-29 | 2015-07-29 | Twin-tower type flue gas deep purification device through plasma coupling and sodium based absorption and method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105056723A true CN105056723A (en) | 2015-11-18 |
| CN105056723B CN105056723B (en) | 2017-04-12 |
Family
ID=54486363
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510455550.7A Active CN105056723B (en) | 2015-07-29 | 2015-07-29 | Twin-tower type flue gas deep purification device through plasma coupling and sodium based absorption and method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105056723B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105311946A (en) * | 2015-12-09 | 2016-02-10 | 深圳广昌达环境科学有限公司 | Flue gas denitration and desulfuration washing system and denitration and desulfuration method |
| CN106215653A (en) * | 2016-09-09 | 2016-12-14 | 北京交通大学 | The device of plasma for desulfurizing flue gas denitration |
| CN109589766A (en) * | 2018-12-17 | 2019-04-09 | 湖北蔚天环保科技有限公司 | Ultra-low temperature denitration device combined with dual-alkali desulfurization process |
| CN112275079A (en) * | 2020-11-20 | 2021-01-29 | 浙江富春江环保热电股份有限公司 | SO in flue gas after wet desulphurization3Device of high-efficient desorption |
| CN113117474A (en) * | 2019-12-31 | 2021-07-16 | 中晶环境科技股份有限公司 | Integrated method for dry flue gas desulfurization and denitrification |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5285978A (en) * | 1976-01-12 | 1977-07-16 | Toshiba Corp | Removal of mercury in waste gas |
| JPH05161821A (en) * | 1991-12-16 | 1993-06-29 | Senichi Masuda | Treatment of exhaust gas |
| CN101310834A (en) * | 2008-02-25 | 2008-11-26 | 北京博奇电力科技有限公司 | Desulfurization, denitration, demercuration technique using gas-liquid contact step oxidation process |
| CN101716451A (en) * | 2009-12-29 | 2010-06-02 | 北京航空航天大学 | Method for removing various pollutants in fume by combining discharge plasmas and absorption |
| CN201543380U (en) * | 2009-11-02 | 2010-08-11 | 河南蓝森环保科技有限公司 | Efficient wet-type flue gas desulfurization device employing dual-alkali method for industrial coal-fired boiler |
| CN101862587A (en) * | 2010-05-10 | 2010-10-20 | 上海电气石川岛电站环保工程有限公司 | Wet flue-gas desulfurization tower based on baffle air distribution |
| CN204952620U (en) * | 2015-07-29 | 2016-01-13 | 浙江富春江环保热电股份有限公司 | Double tower type plasma coupling sodium base absorbs flue gas deep purification device |
-
2015
- 2015-07-29 CN CN201510455550.7A patent/CN105056723B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5285978A (en) * | 1976-01-12 | 1977-07-16 | Toshiba Corp | Removal of mercury in waste gas |
| JPH05161821A (en) * | 1991-12-16 | 1993-06-29 | Senichi Masuda | Treatment of exhaust gas |
| CN101310834A (en) * | 2008-02-25 | 2008-11-26 | 北京博奇电力科技有限公司 | Desulfurization, denitration, demercuration technique using gas-liquid contact step oxidation process |
| CN201543380U (en) * | 2009-11-02 | 2010-08-11 | 河南蓝森环保科技有限公司 | Efficient wet-type flue gas desulfurization device employing dual-alkali method for industrial coal-fired boiler |
| CN101716451A (en) * | 2009-12-29 | 2010-06-02 | 北京航空航天大学 | Method for removing various pollutants in fume by combining discharge plasmas and absorption |
| CN101862587A (en) * | 2010-05-10 | 2010-10-20 | 上海电气石川岛电站环保工程有限公司 | Wet flue-gas desulfurization tower based on baffle air distribution |
| CN204952620U (en) * | 2015-07-29 | 2016-01-13 | 浙江富春江环保热电股份有限公司 | Double tower type plasma coupling sodium base absorbs flue gas deep purification device |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105311946A (en) * | 2015-12-09 | 2016-02-10 | 深圳广昌达环境科学有限公司 | Flue gas denitration and desulfuration washing system and denitration and desulfuration method |
| WO2017096692A1 (en) * | 2015-12-09 | 2017-06-15 | 深圳广昌达环境科学有限公司 | Fuel gas denitration and desulfurization washing system and denitration and desulfurization method |
| CN106215653A (en) * | 2016-09-09 | 2016-12-14 | 北京交通大学 | The device of plasma for desulfurizing flue gas denitration |
| CN109589766A (en) * | 2018-12-17 | 2019-04-09 | 湖北蔚天环保科技有限公司 | Ultra-low temperature denitration device combined with dual-alkali desulfurization process |
| CN113117474A (en) * | 2019-12-31 | 2021-07-16 | 中晶环境科技股份有限公司 | Integrated method for dry flue gas desulfurization and denitrification |
| CN112275079A (en) * | 2020-11-20 | 2021-01-29 | 浙江富春江环保热电股份有限公司 | SO in flue gas after wet desulphurization3Device of high-efficient desorption |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105056723B (en) | 2017-04-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP6171096B2 (en) | Semi-dry simultaneous desulfurization / denitration / demercury equipment and method using circulating fluidized bed | |
| CN102059050B (en) | Low-temperature plasma smoke compound pollutant control method | |
| CN105561776B (en) | A kind of industry coal-boiler flue gas multiple pollutant minimum discharge cooperation-removal system | |
| CN105056723A (en) | Twin-tower type flue gas deep purification device through plasma coupling and sodium based absorption and method thereof | |
| CN105879621A (en) | Two-section type dual-circulation desulfurization and denitrification device and method for realizing near zero emission | |
| CN106237814A (en) | A kind of flue gas ultra-clean discharge desulphurization denitration dust removal integrated plant and technique thereof | |
| CN103506002B (en) | Two-period form Two-way Cycle spraying filler composite absorption tower | |
| CN106524205B (en) | Ultra-low emission purification equipment for flue gas of coal-fired industrial furnace | |
| CN205517261U (en) | Minimum discharge of many pollutants of industry coal fired boiler flue gas is desorption system in coordination | |
| CN105797562A (en) | Two-section type double-ammonia-process integrated desulfurization and denitration system for coking flue gas | |
| CN104437046A (en) | Catalytic cracking flue gas desulfurization and dust removal process and desulfurization and dust removal device | |
| CN104524935A (en) | Single-tower type double-circulation sprinkling composite absorption device and method | |
| CN105148698A (en) | Boiler flue gas desulfurization and denitrification system | |
| CN113304591A (en) | Method and system for purifying flue gas of carbon roasting furnace | |
| CN101342455B (en) | Rotational flow and spray combined desulfurizing device | |
| CN102423593A (en) | Method for simultaneously dedusting, desulphurizing and denitrating boiler flue gas in coal-fired industry | |
| CN206008413U (en) | A kind of removing acid gas in flue gas the system for aiding in desulphurization denitration | |
| CN204952620U (en) | Double tower type plasma coupling sodium base absorbs flue gas deep purification device | |
| CN204619713U (en) | A kind of system and boiler removing various pollutants in fume | |
| CN205055777U (en) | Boiler flue gas desulfurization deNOx systems | |
| CN205182493U (en) | A absorption tower device for SOx/NOx control | |
| CN207822775U (en) | A kind of efficient flue gas desulfurization and denitrification device | |
| CN106390701A (en) | Multilevel plasma ultralow intensified smoke emission control system and multilevel plasma ultralow intensified smoke emission control method | |
| CN107020005A (en) | A kind of minimum discharge system for desulfuration and denitration | |
| CN201300034Y (en) | Vortex-sprinkling combined desulphurizing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230425 Address after: No. 99, Tengfei Road, Licheng Town, Liyang City, Changzhou City, Jiangsu Province 213399 Patentee after: Jiangsu Fuchunjiang environmental protection Thermal Power Co.,Ltd. Address before: No. 188, Chunyong Road, Lingqiao Town, Fuyang City, Hangzhou City, Zhejiang Province, 311418 Patentee before: ZHEJIANG FUCHUNJIANG ENVIRONMENTAL PROTECTION THERMOELECTRICITY Co.,Ltd. Patentee before: ZHEJIANG GONGSHANG University |
|
| TR01 | Transfer of patent right |