CN103111165B - Coal-fired flue-gas dust-removing and desulfurization one purifies technique and can implement the filter of this technique - Google Patents
Coal-fired flue-gas dust-removing and desulfurization one purifies technique and can implement the filter of this technique Download PDFInfo
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- CN103111165B CN103111165B CN201210589570.XA CN201210589570A CN103111165B CN 103111165 B CN103111165 B CN 103111165B CN 201210589570 A CN201210589570 A CN 201210589570A CN 103111165 B CN103111165 B CN 103111165B
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 239000003546 flue gas Substances 0.000 title claims abstract description 72
- 238000000034 method Methods 0.000 title claims abstract description 38
- 230000003009 desulfurizing Effects 0.000 title claims abstract description 35
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 28
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000000428 dust Substances 0.000 claims abstract description 26
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitrogen oxide Substances O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims abstract description 24
- DVARTQFDIMZBAA-UHFFFAOYSA-O Ammonium nitrate Chemical compound [NH4+].[O-][N+]([O-])=O DVARTQFDIMZBAA-UHFFFAOYSA-O 0.000 claims abstract description 22
- BFNBIHQBYMNNAN-UHFFFAOYSA-N Ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims abstract description 22
- 235000011130 ammonium sulphate Nutrition 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 20
- 239000007787 solid Substances 0.000 claims abstract description 20
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 17
- 229910052813 nitrogen oxide Inorganic materials 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 229910001868 water Inorganic materials 0.000 claims abstract description 9
- 230000000717 retained Effects 0.000 claims abstract description 6
- 239000007789 gas Substances 0.000 claims description 14
- 238000004140 cleaning Methods 0.000 claims description 13
- 238000001914 filtration Methods 0.000 claims description 13
- 239000004020 conductor Substances 0.000 claims description 11
- 235000012970 cakes Nutrition 0.000 claims description 10
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 5
- -1 titanium-aluminium Chemical compound 0.000 claims description 4
- 235000019504 cigarettes Nutrition 0.000 claims description 3
- 230000005684 electric field Effects 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- 229910000838 Al alloy Inorganic materials 0.000 claims description 2
- 210000003800 Pharynx Anatomy 0.000 claims description 2
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical class [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 claims description 2
- 108060003095 GAS2 Proteins 0.000 description 16
- 230000000694 effects Effects 0.000 description 10
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 6
- 235000011149 sulphuric acid Nutrition 0.000 description 6
- 239000001117 sulphuric acid Substances 0.000 description 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 5
- 230000005611 electricity Effects 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 210000002381 Plasma Anatomy 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000010894 electron beam technology Methods 0.000 description 3
- 230000002708 enhancing Effects 0.000 description 3
- 208000002173 Dizziness Diseases 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 210000001367 Arteries Anatomy 0.000 description 1
- 241000357209 Cordia subcordata Species 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N Potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 210000003462 Veins Anatomy 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
Abstract
The invention discloses a kind of coal-fired flue-gas dust-removing and desulfurization one that can simultaneously realize dedusting and desulfurization and purify technique.The coal-fired flue-gas dust-removing and desulfurization one of the present invention purifies technique, containing solid dust, sulfur dioxide, nitrogen oxides, water vapour and other materials existed in described flue gas, the step that this technique includes is: injects ammonia in described flue gas, and makes this flue gas move from the windward side of filter element to lee face in the filter；Before described windward side, electrion field is produced by electrion generating means；Inspired the sulfur dioxide in flue gas, nitrogen oxides by electrion field and react generation ammonium sulfate and ammoniumnitrate prill respectively with ammonia；Described ammonium sulfate and ammoniumnitrate prill are retained in together with the solid dust that in flue gas, itself is contained the side, windward side of this filter element by filter element, and other materials that can not be trapped then pass through from filter element and enter the lee face side of filter element.
Description
Technical field
The present invention relates to purifying coal-fired flue gas technology, be specifically related to coal-fired flue-gas dust-removing and desulfurization one and purify
Technique and the filter of this technique can be implemented.
Background technology
Existing plasma for desulfurizing flue gas technology mainly includes that electronic beam method flue gas desulfurization technique (is called for short
And impulse electric corona method flue gas desulfurization technique (be called for short PPCP) EBA).Electronic beam method flue gas desulfurization skill
Art is the electron beam irradiation flue gas produced by electron accelerator in the reactor, utilizes generation
Sulfur dioxide in free radical activity radical oxidation flue gas and nitrogen oxides, then with the ammonia added
Reaction, generates ammonium sulfate and ammoniumnitrate prill, finally realizes pollutant removing.Pulse electricity
The desulphurization denitration mechanism of dizzy method flue gas desulfurization technique is essentially identical with electronic beam method flue gas desulfurization technique
, difference instead of the electron accelerator in electronic beam method with high-voltage pulse power source, instead with it
Answer generation high voltage narrow pulse corona field in device, thus inspire the sulfur dioxide in flue gas, nitrogen oxidation
Thing reacts generation ammonium sulfate and ammoniumnitrate prill respectively with ammonia.Although these plasmas above-mentioned
Body flue gas desulfurization technique has can the incomparable advantage of the tradition desulfurization technology such as simultaneous SO_2 and NO removal
But, ammonium sulfate, ammoniumnitrate prill and the cigarette that their reactor all can not will produce
In gas, contained solid dust itself is separated from flue gas, the most also must
Cleaner must be equipped, increase technology implementation cost.
Summary of the invention
It is desirable to provide a kind of coal-fired flue-gas dust-removing and desulfurization one that can simultaneously realize dedusting and desulfurization
Body purifies technique.
The coal-fired flue-gas dust-removing and desulfurization one of the present invention purifies technique, containing solid dust in described flue gas
, sulfur dioxide, nitrogen oxides, water vapour and other exist material, the step that this technique includes
Suddenly it is: in described flue gas, inject ammonia, and make this flue gas meeting from filter element in the filter
Wind moves towards lee face；Before described windward side, high pressure is produced by electrion generating means
Electric discharge field；Inspired by electrion field the sulfur dioxide in flue gas, nitrogen oxides respectively with ammonia
Reaction generates ammonium sulfate and ammoniumnitrate prill；By filter element by described ammonium sulfate
It is retained in this filter element together with the solid dust that in flue gas, itself is contained with ammoniumnitrate prill
Side, windward side, other materials that can not be trapped then pass through from filter element and entered
The lee face side of filtering element.
The above-mentioned coal-fired flue-gas dust-removing and desulfurization one of the present invention purifies technique by plasma for desulfurizing flue gas skill
Art and smoke filtration dedusting have carried out organic combination.In the implementation process of this technique, flue gas
In contained solid dust itself gradually can form cake layer, filter on the windward side of filter element
The duct on orifice throat ratio filter element in cake layer is less, so that reaction generates ammonium sulfate
It is difficult to pass through with ammoniumnitrate prill.Therefore, the present invention can be by chemistry and physical method simultaneously
Sulfur dioxide in flue gas, nitrogen oxides and solid dust are separated, reaches one clean
Change effect.
The present invention is described further with detailed description of the invention below in conjunction with the accompanying drawings.The present invention adds
Aspect and advantage will be
Giving out in the middle part of explained below, part will become apparent from the description below, or by this
The practice of invention is recognized.
Accompanying drawing explanation
Fig. 1 is that the dust-removal and desulfurizing one of the embodiment of the present invention 1 purifies schematic diagram.
Fig. 2 is that the dust-removal and desulfurizing one of the embodiment of the present invention 2 purifies schematic diagram.
Fig. 3 is that the dust-removal and desulfurizing one of the embodiment of the present invention 3 purifies schematic diagram.
Fig. 4 is the filtration device structure signal of the dust-removal and desulfurizing one purification technique implementing the embodiment of the present invention 3
Figure.
Detailed description of the invention
As it is shown in figure 1, the coal-fired flue-gas dust-removing and desulfurization one of the embodiment of the present invention 1 purifies technique by height
Press discharging generator 1 to produce a height before being positioned at the windward side of filter element 3 in the filter to press
Electric field, specifically, this electrion field is to be produced and through electron gun by from electron accelerator 101
102 are formed to extraradial electron beam 103.Containing solid dust 201, sulfur dioxide, nitrogen oxygen
The coal-fired flue-gas 2 of compound, water vapour and other materials with direction shown in arrow in Fig. 1 by this height
Pressing electric field, therebetween, it is extremely strong that electrion field inspires oxidisability from the water vapour of flue gas 2
Free radical activity group, thus sulfur dioxide and nitrogen oxides are oxidized to sulphuric acid and nitric acid respectively
, sulphuric acid and nitric acid react generation ammonium sulfate 202 the most respectively with the ammonia being previously implanted in flue gas 2
With ammoniumnitrate prill 203, understand due to contained solid dust 201 own in flue gas 2 and gradually filtering
Forming cake layer on the windward side of element 3, cake layer enhances filter element 3 to ammonium sulfate
202 and the rejection effect of ammoniumnitrate prill 203, so that ammonium sulfate 202 and ammoniumnitrate prill
203 are retained in meeting of this filter element 3 together with the solid dust 201 that in flue gas 2, itself is contained
Side, wind face, other materials that can not be trapped then pass through from filter element 3 and enter filtration
The lee face side of element 3.
As in figure 2 it is shown, the embodiment of the present invention 2 coal-fired flue-gas dust-removing and desulfurization one purify technique yet by
Electrion generating means 1 produces a high pressure before being positioned at the windward side of filter element 3 in the filter
Electric discharge field, specifically, this electrion field is by for conductor and double as electrion and fill
Before the filter element 3 of putting electrode, the windward side being positioned at this filter element 3 and and filter element 3 be spaced
The electrode wires 105 of certain distance and electrically connecting with described filter element 3 and electrode wires 105 respectively
Produced by high voltage power supply 104, corona 106 is formed.Containing solid dust 201, sulfur dioxide, nitrogen
The coal-fired flue-gas 2 of oxide, water vapour and other materials passes through with direction shown in arrow in Fig. 2 should
Electrion field, therebetween, it is extremely strong that electrion field inspires oxidisability from the water vapour of flue gas 2
Free radical activity group, thus sulfur dioxide and nitrogen oxides are oxidized to sulphuric acid and nitre respectively
Acid, sulphuric acid and nitric acid react generation ammonium sulfate 2 the most respectively with the ammonia being previously implanted in flue gas 2
02 and ammoniumnitrate prill 203, owing to the solid dust 201 that in flue gas 2, itself is contained can be gradually in mistake
Forming cake layer on the windward side of filtering element 3, cake layer enhances filter element 3 to ammonium sulfate
Grain 202 and the rejection effect of ammoniumnitrate prill 203, so that ammonium sulfate 202 and ammonium nitrate
Grain 203 is retained in this filter element 3 together with the solid dust 201 that in flue gas 2, itself is contained
Side, windward side, other materials that can not be trapped then pass through from filter element 3 and entered
The lee face side of filtering element 3.
Obviously, the electrion generating means of the embodiment of the present invention 1 used for reference existing electronic beam method flue gas take off
Sulfur technology is formed electricity
The correlation technique of son bundle.The electrion generating means of the embodiment of the present invention 2 then existing pulse electricity
Dizzy method flue gas desulfurization technique is formed the correlation technique of corona field.For the embodiment of the present invention 2, high
Voltage source 104 is preferably with high-voltage pulse power source, so, will form arteries and veins before filter element 3
Impulse electricity field, reaches the desulfurization off sulfide effect similar with existing impulse electric corona method flue gas desulfurization technique
.It addition, the embodiment of the present invention 2 is preferably with the filter element 3 of tabular.
As it is shown on figure 3, the embodiment of the present invention 3 coal-fired flue-gas dust-removing and desulfurization one purify technique yet by
Electrion generating means 1 produces a high pressure before being positioned at the windward side of filter element 3 in the filter
Electric discharge field, specifically, described electrion generating means includes the first tabular filter element 3a
, the second tabular filter element 3b and respectively with the first tabular filter element 3a and the second tabular mistake
Filtering element 3b electrical connection high voltage power supply 107, the windward side of described first tabular filter element 3a with
The windward side of the second tabular filter element 3b is oppositely arranged and forms electrion field betwixt.Contain
There is the coal-fired flue-gas of solid dust 201, sulfur dioxide, nitrogen oxides, water vapour and other materials
2 with direction shown in arrow in Fig. 3 by this electrion field, therebetween, electrion field is from flue gas
The water vapour of 2 inspires the free radical activity group that oxidisability is extremely strong, thus by sulfur dioxide and
Nitrogen oxides be oxidized to respectively sulphuric acid and nitric acid, sulphuric acid and nitric acid the most respectively be previously implanted into flue gas
Ammonia reaction in 2 generates ammonium sulfate 202 and ammoniumnitrate prill 203, due to own in flue gas 2
Contained solid dust 201 can be gradually at the first tabular filter element 3a and the second tabular filter element
On the windward side of 3b formed cake layer, cake layer enhance the first tabular filter element 3a, second
Tabular filter element 3b to ammonium sulfate 202 and the rejection effect of ammoniumnitrate prill 203, thus
Make ammonium sulfate 202 and ammoniumnitrate prill 203 and itself contained solid dust 201 in flue gas 2
It is retained in together between this first tabular filter element 3a and the second tabular filter element 3b, and
Other materials that can not be trapped filter from the first tabular filter element 3a and the second tabular the most respectively
In element 3b filter element 3 by and enter the first tabular filter element 3a and the second tabular crosses filtering element
The lee face side of part 3b.
In the embodiment of the present invention 3, high voltage power supply 104 is preferably with high-voltage pulse power source.The present invention implements
The electrion field produced in example 3 had both been different from embodiment 1 electron beam 103 produced, also different
In implementing the corona 106 that produces in 2, embodiment 3 use the first tabular filter element 3a, second
High voltage is applied thus by interpolar gas medium disruptive discharge between tabular filter element 3b.This
The something in common of bright embodiment 3 and embodiment 2 with, their filter element 3 for conductor and doubles as
The electrode of electrion generating means.Due to electrion field can make in flue gas 2 to be clean miscellaneous
Matter is charged, and filter element 3 itself is as the electrode of electrion generating means, therefore, and mistake
Filtering element 3 can in flue gas 2 charged impurity produce absorption or repulsive interaction, make these impurity without
Method is passed through from filter element 3, improves gas cleaning effect further.The embodiment of the present invention 3 with
The filter element 3 of embodiment 2 can be made up of inorganic porous conductor material, such as rustless steel porous material
Material, nickel porous material etc., it is preferred that many by titanium-aluminium alloy porous conductor material, ferroaluminium
A kind of composition in hole conductor material, nickel alumin(i)um alloy porous conductor material, to enable the invention to
Adapt to high temperature filtration condition.
Fig. 4 is the filter that a kind of dust-removal and desulfurizing one implementing the embodiment of the present invention 3 purifies technique
Structural representation.This filter 4 includes air inlet 401, air vent 404 and slag-drip opening 405, mistake
It is provided with in the shell of filter 4 and described air inlet
Inlet plenum 402 that 401 communicate and the dust storage chamber 406 communicated with slag-drip opening 405, described inlet plenum
For gas cleaning district between 402 and dust storage chamber 406, in gas cleaning district, windward side is installed relative
The the first tabular filter element 3a arranged and the second tabular filter element 3b, described first tabular mistake
Filtering element 3a, the second tabular filter element 3b electrically connect with high voltage power supply 107 respectively, thus
Formed between windward side and the windward side of the second tabular filter element 3b of one tabular filter element 3a
Electrion field；Being positioned at the periphery in described gas cleaning district in the shell of filter 4, to be provided with one only
Vertical annular air-purifying chamber 403, this annular air-purifying chamber 403 and described air vent 404 and be positioned at first
Clean gas after the lee face of tabular filter element 3a and the lee face of the second tabular filter element 3b
Exhaust passage connects.It addition, for convenience of ammonia is injected in coal-fired flue-gas 2 to be clean, described in enter
Spray ammonia pipe 5 it is provided with at QI KOU 401.Can install according to same way in described gas cleaning district
Polylith the first tabular filter element 3a and the second tabular filter element 3b, to improve treatment quantity
。
The work process of above-mentioned filter is: flue gas 2 enters filter 4 from air inlet 401, therebetween,
In flue gas 2, ammonia is injected by spray ammonia pipe 5；Hereafter, the flue gas 2 containing ammonia from inlet plenum 402 to
Between windward side and the windward side of the second tabular filter element 3b of the first tabular filter element 3a
Passage moves, then inspires the sulfur dioxide in flue gas 2, nitrogen oxygen by described electrion field
Compound reacts generation ammonium sulfate and ammoniumnitrate prill respectively with ammonia；Filtered by the first tabular
Element 3a and the second tabular filter element 3b is by described ammonium sulfate and ammoniumnitrate prill and cigarette
In gas, contained solid dust itself retains in described passage together, and falls by gravity into dust
Room 406, thus be deposited at the slag-drip opening 405 of dust storage chamber 406, and other things that can not be trapped
Matter is then passed through and by being positioned at from the first tabular filter element 3a and the second tabular filter element 3b
After the lee face of the first tabular filter element 3a and the lee face of the second tabular filter element 3b
Clean gas exhaust passage enters annular air-purifying chamber 403, discharges from air vent 404 the most again.
Claims (5)
1. coal-fired flue-gas dust-removing and desulfurization one purify technique, in described flue gas containing solid dust, sulfur dioxide, nitrogen oxides,
Water vapour, the step that this technique includes is: injects ammonia in described flue gas, and makes this flue gas in the filter from filter element (3)
Windward side to lee face move；Before described windward side, electrion field is produced by electrion generating means (1)；Pass through
Electrion field inspires the sulfur dioxide in flue gas, nitrogen oxides and reacts generation ammonium sulfate and ammoniumnitrate prill respectively with ammonia；
By filter element (3), described ammonium sulfate and ammoniumnitrate prill are retained in together with the solid dust that in flue gas, itself is contained
The side, windward side of this filter element (3), other materials that can not be trapped then pass through from filter element (3) and enter
The lee face side of filter element (3)；In the implementation process of this technique, in flue gas, contained solid dust itself can gradually exist
Forming cake layer on the windward side of filter element, the duct on orifice throat ratio filter element on cake layer is less, so that reaction is raw
Ammonium sulfate and ammoniumnitrate prill is become to be difficult to pass through；Described filter element (3) is conductor and doubles as electrion generating means
Electrode, this electrion generating means includes the first tabular filter element (3a), the second tabular filter element (3b) and difference
The high voltage power supply electrically connected with the first tabular filter element (3a) and the second tabular filter element (3b), described first tabular mistake
The windward side of filtering element (3a) is oppositely arranged with the windward side of the second tabular filter element (3b) and forms electrion betwixt
?；Described filter element (3) is made up of inorganic porous conductor material.
2. coal-fired flue-gas dust-removing and desulfurization one as claimed in claim 1 purifies technique, it is characterised in that: described filter element (3)
It is made up of the one in titanium-aluminium alloy porous conductor material, ferroaluminium porous conductor material, nickel alumin(i)um alloy porous conductor material.
3. coal-fired flue-gas dust-removing and desulfurization one as claimed in claim 1 purifies technique, it is characterised in that: described high voltage power supply is
High-voltage pulse power source.
4. coal-fired flue-gas dust-removing and desulfurization one as claimed in claim 1 or 2 purifies technique, it is characterised in that: described height presses
Electric field is Pulsed Corona.
5. can implement coal-fired flue-gas dust-removing and desulfurization one described in claim 1 and purify the filter of technique, including air inlet, aerofluxus
Mouth and slag-drip opening, be provided with the inlet plenum communicated with described air inlet and the dust storage chamber communicated with slag-drip opening in the shell of filter,
For gas cleaning district between described inlet plenum and dust storage chamber, it is characterised in that: in gas cleaning district, windward side is installed and is oppositely arranged
The first tabular filter element (3a) and the second tabular filter element (3b), described first tabular filter element (3a), second
Tabular filter element (3b) electrically connects with high voltage power supply (107) respectively, thus at the first tabular filter element (3a) windward
Electrion field is formed between the windward side of face and the second tabular filter element (3b)；Described cigarette it is positioned in the shell of filter
The periphery of gas purifying area is provided with an independent annular air-purifying chamber (403), this annular air-purifying chamber (403) and described air vent and position
Clean gas aerofluxus after the lee face of the first tabular filter element (3a) and the lee face of the second tabular filter element (3b) is led to
Road connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210589570.XA CN103111165B (en) | 2012-12-29 | Coal-fired flue-gas dust-removing and desulfurization one purifies technique and can implement the filter of this technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210589570.XA CN103111165B (en) | 2012-12-29 | Coal-fired flue-gas dust-removing and desulfurization one purifies technique and can implement the filter of this technique |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103111165A CN103111165A (en) | 2013-05-22 |
| CN103111165B true CN103111165B (en) | 2016-11-30 |
Family
ID=
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1559651A (en) * | 2004-02-14 | 2005-01-05 | 中国工程物理研究院环保工程研究中心 | Exbaust gas purification method and device by pulse corona dicharging method |
| CN1562445A (en) * | 2004-03-29 | 2005-01-12 | 广东杰特科技发展有限公司 | Method of synchronous cleansing air pollutant by smoke of plasma discharge caused by spreading light |
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1559651A (en) * | 2004-02-14 | 2005-01-05 | 中国工程物理研究院环保工程研究中心 | Exbaust gas purification method and device by pulse corona dicharging method |
| CN1562445A (en) * | 2004-03-29 | 2005-01-12 | 广东杰特科技发展有限公司 | Method of synchronous cleansing air pollutant by smoke of plasma discharge caused by spreading light |
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