CN205948624U - Industry flue gas dry -type low temperature is in coordination with removing dust SOx/NOx control removal of mercury integrated device - Google Patents
Industry flue gas dry -type low temperature is in coordination with removing dust SOx/NOx control removal of mercury integrated device Download PDFInfo
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- CN205948624U CN205948624U CN201620477301.8U CN201620477301U CN205948624U CN 205948624 U CN205948624 U CN 205948624U CN 201620477301 U CN201620477301 U CN 201620477301U CN 205948624 U CN205948624 U CN 205948624U
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- sack cleaner
- flue gas
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- pipeline
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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Abstract
The utility model relates to an industry flue gas dry -type low temperature is in coordination with removing dust SOx/NOx control removal of mercury integrated device. Industry flue gas many pollutant treatment equipment's integration has been realized through first, the second bag room that set up the sack cleaner. Simultaneously, the device adopts first desulfurization to remove dust and gets rid of nitrogen oxide and mercury again, but can realize low temperature SCR catalyst cyclic utilization, effectively avoids the dust to the wearing and tearing of catalyst, prevents that low temperature SCR catalyst from becoming sulfur trioxide with the sulfur dioxide oxidation. And then prevent that sulfur trioxide that the oxidation becomes and ammonia reactions formation ammonium sulfate can be less than in the flue -gas temperature and condense into the stickness material under 230 degrees centigrade of situations and influence low temperature denitration efficiency.
Description
Technical field
This utility model belongs to industrial smoke process field, is related to the Collaborative Control of industrial smoke multi-pollutant, specifically relates to
And a kind of industrial smoke dry type low temperature works in coordination with dust-removal and desulfurizing denitration removal of mercury integrated apparatus.
Background technology
With economic fast development, the economy especially based on energy resource consumption rapidly increases, and leads to plant emissions big
Amount contains particle dust, SO2（Sulfur dioxide）、NOx（Oxynitride）、Hg（Hydrargyrum）Deng the flue gas of pollutant, to atmospheric environment
Cause high risks with public health.Environmental requirement improves constantly, the GB13223-2011 that country promulgates《Coal-burning power plant's pollutant
Discharge standard》Respectively to dust and SO2Emission limit requires more strictly, and newly-increased NOxWith the emission limit of Hg, therefore, simultaneously
Control dust, SO2、NOX, Hg discharge extremely urgent.
Traditional smoke gas treatment is to carry out independent improvement according to the difference of pollutant kind.At present, main sulfur method
There are wet method, semidry method and dry method.In practical engineering application, wet desulphurization occupation rate is most, and particularly limestone-gypsum is wet
Method desulfurization technology application is the most extensive, and its removal efficiency is up to 95%, but it is also easy to produce, and gypsum rain, water consumption be high, secondary dirt
The problems such as dye, equipment are perishable, and it is unable to the NO in effective control flue gasXAnd Hg.In order to prevent NOx pollution environment, need
Denitration process.Denitration technology mainly includes SCR（SCR）And SNCR（SNCR）Two kinds, due to
Up to 850 DEG C ~ 1050 DEG C of SNCR desired reaction temperature window, and industrial furnace exit gas temperature is relatively low, so need to separately set
Heater is by flue gas so far temperature window, additionally, this out of stock system energy consumption increases and the slow efficiency of SNCR response speed
Low.Therefore, great majority are all use SCR technology with denitrating system, but with V more than traditional SCR2O5/TiO2（Vanadic anhydride/titanium dioxide
Titanium）、V2O5-WO3/TiO2（Vanadic anhydride Tungstic anhydride ./titanium dioxide）Deng for catalyst, this reaction temperature window is
250 DEG C ~ 420 DEG C, in order to reach this temperature window, for the waste-heat boiler feedwater using boiler tail flue gas, economize on coal,
And reduce flue gas loss, improve inlet temperature, improve the efficiency of boiler, it is pre- with sky that SCR device is typically placed in economizer
Between device, so make catalyst be in high dirt region and easily block.Meanwhile, in SCR catalyst, metal can be by SO2It is oxidized to SO3（Three
Sulfur oxide）With NH3（Ammonia）Reaction generates NH4HSO4（Ammonium hydrogen sulfate）Or NH4SO4（Ammonium sulfate）, these are less than 230 in flue-gas temperature
Condensing into emplastic under DEG C situation makes the heavy metal contaminants carrying in catalyst blockage or corrosion, and flue gas also can cause
Make catalyst poisoning, in turn result in catalyst life reduction, system operation cost increases（SCR catalyst expense accounts for denitrating system
40 % ~ 60 % of gross investment）It is impossible to control effectively to hydrargyrum.
But according to said method coordinated desulfurization denitration dust collecting needs, such as dealkylation reaction device, cleaner unit, desulfurizing tower etc. are many
Complete equipment, many complete equipments work independently.This many complete equipments have that gross investment is big, operation energy consumption is high, floor space is big, technique is multiple
The problems such as miscellaneous, maintenance is big, does not meet the vision of energy-saving and emission-reduction and sustainable development.Therefore, how dirty R ＆ D design industrial smoke is
It is most important that dye thing works in coordination with integration removing sulfuldioxide.
Content of the invention
This utility model purpose is to provide a kind of industrial smoke dry type low temperature to work in coordination with dust-removal and desulfurizing denitration removal of mercury one to disguise
Put it is achieved that the integration of industrial smoke multi-pollutant abatement equipment, a bag-type dust will be concentrated on by flue gas multiple pollutant
Processed within device, had the advantages that gross investment is little, operation energy consumption is low, floor space is little, concise in technology, maintenance are little.
In order to realize object above, the technical solution of the utility model is：A kind of industrial smoke dry type low temperature works in coordination with dedusting
Desulphurization denitration removal of mercury integrated apparatus, including sack cleaner, described sack cleaner includes juxtaposed first, second bag
Room, sack cleaner the first pocket bottom connects quick lime cast feeder, sack cleaner the first pocket bottom pipe above-below direction
It is disposed with the first unloading valve, the first storehouse pump, described quick lime cast feeder top connects separator, and separator connects disintegrating machine,
In quick lime cast feeder bottom pipe, the first ball valve is set, UNICOM's gas approach pipeline below the first ball valve, described cigarette
Gas inlet pipeline is postponed to sack cleaner the first pocket import, the upper upper setting in ball valve UNICOM position of gas approach pipeline
First porous plate；
Sack cleaner the second pocket import of sack cleaner first pocket outlet UNICOM, this unicom pipeline arranges second
Porous plate, is provided with ammonia nozzle positioned at the bottom of the second porous plate, and ammonia nozzle is connected with weak ammonia storage tank, ammonia nozzle and weak ammonia
Compressed air reservoir is connected with the connecting pipe of storage tank, the delivery outlet of weak ammonia storage tank is provided with the first bleeder valve, compressed air
The delivery outlet of storage tank is provided with the second bleeder valve；
Sack cleaner the second pocket bottom connects catalyst cast feeder, and sack cleaner the second pocket bottom pipe is upper and lower
Direction is disposed with the second unloading valve, the second storehouse pump, and catalyst cast feeder top connects low-temperature SCR catalyst hopper, bag-type dust
Sack cleaner the first pocket outlet of device the second pocket bottom UNICOM and the unicom pipeline of sack cleaner the second pocket import, cloth
The connection position of bag dust collector the second pocket bottom unicom pipeline is located at the bottom of ammonia nozzle, and sack cleaner the second pocket bottom joins
Thread a pipe and be provided with the second ball valve；
The outlet of sack cleaner second pocket connects air-introduced machine, and air-introduced machine arranges chimney.
Of the present utility model have technical effect that：By this device not only can to the particle dust in low-temperature flue gas,
SO2、NOX, Hg carry out dry type and work in coordination with administering, and this device achieves the integration of industrial smoke multi-pollutant abatement equipment, that is,
Flue gas multiple pollutant is concentrated on and is processed within a tablecloth bag dust collector, have that gross investment is little, operation energy consumption is low, occupation of land face
Amass the advantages of little, concise in technology, maintenance are little.Meanwhile, this device removes denitrification and hydrargyrum again using first desulfurization and dedusting, permissible
Realize low-temperature SCR catalyst reusable edible, be prevented effectively from the abrasion to catalyst for the dust, prevent low-temperature SCR catalyst by two
Sulfur oxide is oxidized to sulfur trioxide.And then prevent the sulfur trioxide being oxidized to and ammonia react generation ammonium sulfate can be low in flue-gas temperature
Emplastic impact low-temperature denitration efficiency is condensed under 230 degrees Celsius of situations.This device can be widely applied to various industry
The smoke gas treatment of kiln, including coal-burning boiler, glass furnace, cement kiln, coke oven, sintering machine etc., its technological design economical rationality, dress
Put reliable, pollutant in flue gas can be made to reach the emission limit required by environmental protection standard（Particle dust≤30
mg/m3、SO2≤ 100 mg/m3、NOX≤ 100 mg/m3、Hg ≤ 0.03 mg/m3）.
Brief description
Fig. 1 is the structural representation of this utility model device；
In figure：1- disintegrating machine, 2- separator, 3- quick lime cast feeder, 4,20- first, second ball valve, 5- gas approach,
6th, 12- first, second porous plate, the first pocket import of 7- sack cleaner, 8- sack cleaner first pocket, 9,22- first,
Second unloading valve, 10,23- storehouse pump, 11- sack cleaner first pocket exports, 13- weak ammonia storage tank, and 14,16- first, second
Bleeder valve, 15- compressed air reservoir, 17- ammonia nozzle, 18- low-temperature SCR catalyst hopper, 19- catalyst cast feeder, 21- cloth
Bag dust collector the second pocket import, 24- sack cleaner second pocket, 25- sack cleaner second pocket exports, 26- air inducing
Machine, 27- chimney.
Specific embodiment
Referring to the drawings, a kind of industrial smoke dry type low temperature works in coordination with dust-removal and desulfurizing denitration removal of mercury integrated apparatus, including cloth bag
Cleaner unit, described sack cleaner includes juxtaposed first, second pocket 8,24, and sack cleaner the first pocket 8 bottom is even
Deliver a child Calx cast feeder 3, sack cleaner the first pocket 8 bottom pipe above-below direction is disposed with the first unloading valve 9, the first storehouse pump
10, described quick lime cast feeder 3 top connects separator 2, and separator 2 connects disintegrating machine 1, quick lime cast feeder 3 lower tube
First ball valve 4 is arranged on road, positioned at the first ball valve 4 lower section UNICOM gas approach 5 pipeline, described gas approach 5 pipeline is postponed
To sack cleaner the first pocket import 7, gas approach 5 pipeline is located at upper setting first porous plate of ball valve 4 UNICOM position
6；
Sack cleaner first pocket exports 11 UNICOM's sack cleaner the second pocket imports 24, and this unicom pipeline is arranged
Second porous plate 12, is provided with ammonia nozzle 17 positioned at the bottom of the second porous plate 12, and ammonia nozzle 17 is connected with weak ammonia storage tank 13,
It is connected with compressed air reservoir 15, the delivery outlet of weak ammonia storage tank 13 sets on ammonia nozzle 17 and the connecting pipe of weak ammonia storage tank 13
There is the first bleeder valve 14, the delivery outlet of compressed air reservoir 15 is provided with the second bleeder valve 16；
Sack cleaner the second pocket 24 bottom connects catalyst cast feeder 19, sack cleaner the second pocket 24 lower tube
Road above-below direction is disposed with the second unloading valve 22, the second storehouse pump 23, and catalyst cast feeder 19 top connects low-temperature SCR catalyst material
Groove 18, sack cleaner the second pocket 24 bottom UNICOMs sack cleaner the first pocket outlet 11 and sack cleaner second pocket
The unicom pipeline of import 21, the connection position of sack cleaner the second pocket 24 bottom unicom pipeline is located at the bottom of ammonia nozzle 17,
Sack cleaner the second pocket 21 bottom unicom pipeline is provided with the second ball valve 20；
Sack cleaner second pocket outlet 25 connection air-introduced machine 26, air-introduced machine 26 arranges chimney 27.
Further, described sack cleaner first pocket outlet 11 is arranged at the upper of sack cleaner the first pocket 8
Side, described sack cleaner the first pocket import 7 is arranged at the lower section of sack cleaner the first pocket 8.
Further, described sack cleaner second pocket outlet 25 is arranged at the upper of sack cleaner the second pocket 24
Side, described sack cleaner the second pocket import 21 is arranged at the lower section of sack cleaner the second pocket 25.
Quick lime is put into disintegrating machine 1, crushes through disintegrating machine 1 and separator 2 screens, obtain the life of particle diameter that meets the requirements
Lime particle is simultaneously delivered to quick lime cast feeder 3 and stores for future use.Flue gas under negative pressure draft effect through gas approach 5, the
In the presence of one porous plate 6, it is uniformly introduced sack cleaner inlet pipeline, open quick lime cast feeder 3 bottom the first ball valve 4
Lentamente put a little quicklime particles to mix homogeneously with flue gas in pipeline, enter sack cleaner in the flue gas containing quick lime
First pocket 8, thus realize sack cleaner the first pocket 8 filter bag is carried out process is preliminarily sprayed.Then continuous uniform is slow
Release quick lime is mixed homogeneously with flue gas to pipeline and is fully reacted, and then removes the SO in flue gas2.Flue gas through desulfurization
Enter sack cleaner the first pocket 8, to dust intrinsic in flue gas and desuifurized filter, be concurrently deposited at filter bag surface
It is desuifurized that unreacted desulfurizing agent continuation and sulfur dioxide react generation.Then, the dust that is removed and desuifurized in cloth
Under bag dust collector pulse backblowing airflow function, it is deposited among sack cleaner the first pocket 8 ash bucket, unloads ash finally by first
Ash discharge is delivered to quick lime cast feeder 3 and recycles by valve 9 and the first storehouse pump 10.Flue gas through desulfurization and dedusting is passed through to connect
The tuber drainage of sack cleaner the first pocket 8 and sack cleaner the second pocket 24 enters to sack cleaner the second pocket flue gas
Mouth 21, carries out NO using the technology that is preliminarily sprayed to sack cleaner the second pocket 24 filter bag surfaceXLow-temperature SCR catalyst sprays in advance
Process（Low-temperature SCR catalyst cast feeder on sack cleaner the secondth pocket 24 admission line will be passed through by low-temperature SCR catalyst
Uniformly mix with flue gas in 19 input pipelines, low-temperature SCR catalyst is trapped in filter bag surface through filter bag by flue gas）, by NOXAlso
Former dose is sprayed into by reducing agent spray site on sack cleaner the second pocket 24 admission line and is uniformly mixed with flue gas among pipeline,
Reducing agent and NO under catalyst actionXFully reacted, Hg is catalytically oxidized to bivalent mercury, and then removed NO in flue gasX
With simple substance Hg.Meanwhile, completely low-temperature SCR catalyst continues to participate in reaction to be deposited on filter bag surface unreacted, and generate nitrogen,
Water, mercury oxide etc..Treated clean flue gas exports from sack cleaner and discharges, under air-introduced machine 26 effect, by chimney
Enter among air.Meanwhile, by a small amount of dust of sock filtration, unreacted catalyst and oxidized hydrargyrum in pulse backblowing gas
Under stream effect, it is deposited among sack cleaner the second pocket 24 ash bucket, by the second unloading valve 22, the second storehouse pump 23 by ash discharge
It is delivered to low-temperature SCR catalyst cast feeder 3 to recycle.
This device not only can be to the particle dust in low-temperature flue gas, SO2、NOX, Hg carry out dry type work in coordination with administer, and
This device achieves the integration of industrial smoke multi-pollutant abatement equipment, flue gas multiple pollutant will concentrate on a tablecloth bag and remove
Processed within dirt device, had the advantages that gross investment is little, operation energy consumption is low, floor space is little, concise in technology, maintenance are little.
Meanwhile, this device removes denitrification and hydrargyrum technique again using first desulfurization and dedusting, it is possible to achieve low-temperature SCR catalyst profit capable of circulation
With being prevented effectively from the abrasion to catalyst for the dust, preventing low-temperature SCR catalyst from oxidizing sulfur dioxide is become sulfur trioxide.And then
Prevent the sulfur trioxide being oxidized to and ammonia react generation ammonium sulfate can flue-gas temperature be less than 230 degrees Celsius of situations under condense into glutinous
Property material impact low-temperature denitration efficiency.This device can be widely applied to the smoke gas treatment of various Industrial Stoves, including coal-fired pot
Stove, glass furnace, cement kiln, coke oven, sintering machine etc., its technological design economical rationality, plant running are reliable, can make dirty in flue gas
Dye thing reaches the emission limit required by environmental protection standard（Particle dust≤30 mg/m3、SO2≤ 100 mg/m3、NOX
≤ 100 mg/m3、Hg ≤ 0.03 mg/m3）.
The processing procedure that above-mentioned industrial smoke dry type low temperature works in coordination with dust-removal and desulfurizing denitration removal of mercury integrated apparatus is such：
Using disintegrating machine 1 to quick lime（CaO）Carry out break process so as to grain graininess reaches 90% is respectively less than 30 μm,
Now separator 2 speed controlling of quick lime is between 270 ~ 280 r/min.Well-graded limestone particle is delivered to life
Standby in Calx cast feeder 3.
Under sack cleaner gas outlet air-introduced machine 26 effect, not higher than 220 DEG C of flue gas is entered by sack cleaner
QI KOU pipeline, in the presence of the first porous plate 6, is uniformly introduced sack cleaner.Open quick lime cast feeder 3 bottom first
Ball valve 4 is lentamente put a little quicklime particles and is mixed homogeneously with flue gas in pipeline, enters cloth bag in the flue gas containing quick lime
Cleaner unit the first pocket 8, thus realize sack cleaner the first pocket 8 filter bag is carried out process is preliminarily sprayed.
By well-graded limestone particle with Ca/S than for 1：3 ratio continuous uniform is slowly added in pipeline, with cigarette
Gas mix homogeneously is simultaneously fully reacted, and then removes the SO in flue gas2, through test data, desulfuration efficiency can reach 80 %
~ 90 %.This sulfur method desulfuration efficiency is higher, and desulfurizing agent is cheap, desuifurized disposable, non-secondary pollution；
Concrete chemical reaction in this step is presented herein below：
Quick lime（CaO）Dry desulfurization main chemical reactions relational expression is as follows：
CaO + SO2→ CaSO3
2CaSO3+ O2→ 2CaSO4
From above-mentioned reaction relation formula, calcium oxide and sulfur dioxide in flue gas carry out reaction and generate calcium sulfite, flue gas
In oxygen again calcium sulfite oxidation is become calcium sulfate.Finally, realize the removing of sulfur dioxide.
Enter sack cleaner the first pocket 8, now filter bag through the flue gas of desulfurization along admission line（High temperature resistant corrosion resistant
Erosion）To particle dust intrinsic in flue gas and desuifurized effectively filtered, be concurrently deposited at filter bag surface and have neither part nor lot in reaction
Desulfurizing agent continue with sulfur dioxide react generate desuifurized.When the dedusting resistance of sack cleaner the first pocket 8 reaches
During 1000 Pa, the pulse valve of sack cleaner is opened, and in gas bag, compressed gas spray into sack cleaner by injection tube, will glue
It is attached to the dust on filter bag surface and desuifurized remove and be deposited among sack cleaner the first pocket 8 ash bucket finally by
Ash discharge is delivered to quick lime cast feeder 3 and recycles by one unloading valve 9 and the first storehouse pump 10；
Flue gas through desulfurization and dedusting is passed through to connect sack cleaner the first pocket 8 and sack cleaner the second pocket 24
Tuber drainage to sack cleaner the second pocket 24 gas approach, by low-temperature SCR catalyst MnOX/AC（Mn oxide/activity
Charcoal）Add catalyst cast feeder 19, open catalyst cast feeder 19 discharge port the second ball valve 20, so that catalyst is slowly uniformly flowed into
Mix homogeneously with flue gas in pipeline, low-temperature SCR catalyst is trapped in filter bag surface through filter bag by the flue gas containing catalyst, from
And sack cleaner the second pocket 24 filter bag has been carried out process is preliminarily sprayed.
Open compressed air reservoir 15 second bleeder valve 16, make compressed air inject sack cleaner through ammonia nozzle 17
Inside two pocket 24 inlet pipeline, subsequently, open weak ammonia storage tank 13 first bleeder valve 14, ammonia mass fraction is 18.3 more than %
Weak ammonia mix with compressed air under compressed air induction, and inject in pipeline by ammonia nozzle 17, last and process
What the second porous plate 12 was uniformly processed uniformly mixes flowing flue gas.
Flue gas containing weak ammonia is through catalyst cast feeder 19 and low-temperature SCR catalyst MnOX/ AC uniformly mixes, low
Warm SCR catalyst MnOXThe lower NH of/AC effect3By NOXIt is reduced into nitrogen gas and water.Due to MnOXOxidizing to Elemental Mercury, activated carbon
AC can adsorb mercury vapour and bivalent mercury, and the simple substance Hg therefore in flue gas is catalytically oxidized to bivalent mercury and is adsorbed by activated carbon AC,
And then simple substance Hg in removing flue gas.Meanwhile, it is deposited on filter bag surface unreacted completely low-temperature SCR catalyst MnOX/ AC continues
Participate in reaction, and will be the NO being reduced in flue gasXIt is reduced into nitrogen gas and water, simple substance Hg is catalytically oxidized to bivalent mercury and is lived
Property charcoal absorption.The method is in NH3/NOXMol ratio is 0.85 ~ 1, and NH3Leakage rate is less than 3 ml/m3When, denitration efficiency is more than
90%；Mercury removal efficiency is more than 70%；
Concrete chemical reaction in this step is presented herein below：
Low-temperature SCR selective reduction denitration main chemical reactions formula is as follows：
4NO + 4NH3+ O2→ 4N2+ 6H2O
6NO + 4NH3→ 5N2+ 6H2O
6NO2+ 8NH3→ 3N2+ 6H2O
2NO2+ 4NH3+ O2→ 3N2+ 6H2O
Elemental Mercury catalytic oxidation formula is as follows：
2Hg + O2→ 2HgO
There is above-mentioned chemical equation to understand, under catalyst action, in the flue gas of about 80～180 DEG C of temperature, spray into ammonia,
By NOXIt is reduced into N2And H2O.Its primary response is aforementioned four reaction equation.Meanwhile, simple substance Hg is catalytically oxidized to bivalent mercury
It is tightly held by activated carbon.Because in flue gas, dust and sulfur dioxide are processed in sack cleaner the first pocket 8, so
SO2/SO3Conversion ratio low, a large amount of (NH will not be produced4)2SO4Or NH4HSO4, enter without to sack cleaner the second pocket 24
Cloth bag causes to paste bag phenomenon, and can reduce catalyst and react with sulfur, and then can improve catalyst recycling number of times.
Treated clean flue gas exports from sack cleaner and discharges, and under air-introduced machine 26 effect, is entered by chimney
Among air.When the dedusting resistance of sack cleaner the second pocket 24 reaches 1000 Pa, the pulse valve of sack cleaner leaves
Open, in gas bag, compressed gas spray into sack cleaner by injection tube, by a small amount of dust of sock filtration, unreacted catalyst
And oxidized hydrargyrum removing, and it is deposited among sack cleaner the second pocket 24 ash bucket, by the second unloading valve 22, the second storehouse
Ash discharge is delivered to low-temperature SCR catalyst cast feeder 19 and recycles by pump 23.The method can ensure that efficiency of dust collection is more than
99.98%.
Claims (3)
1. a kind of industrial smoke dry type low temperature works in coordination with dust-removal and desulfurizing denitration removal of mercury integrated apparatus, and including sack cleaner, it is special
Levy and be：Described sack cleaner includes juxtaposed first, second pocket, sack cleaner first pocket（8）Bottom connects
Quick lime cast feeder（3）, sack cleaner first pocket（8）Bottom pipe above-below direction is disposed with the first unloading valve（9）, first
Storehouse pump（10）, described quick lime cast feeder（3）Top connects separator（2）, separator（2）Connect disintegrating machine（1）, quick lime
Cast feeder（3）First ball valve is arranged on bottom pipe（4）, positioned at the first ball valve（4）Lower section UNICOM gas approach（5）Pipeline, institute
The gas approach stated（5）Pipeline is postponed to sack cleaner the first pocket import（7）, gas approach（5）Ball valve is located on pipeline
（4）Upper setting first porous plate of UNICOM position（6）；
Sack cleaner first pocket exports（11）The the second pocket import of UNICOM's sack cleaner, this unicom pipeline arranges second
Porous plate（12）, positioned at the second porous plate（12）Bottom be provided with ammonia nozzle（17）, ammonia nozzle（17）With weak ammonia storage tank
（13）Connect, ammonia nozzle（17）With weak ammonia storage tank（13）Connecting pipe on be connected with compressed air reservoir（15）, weak ammonia
Storage tank（13）Delivery outlet be provided with the first bleeder valve（14）, compressed air reservoir（15）Delivery outlet be provided with the second bleeder valve
（16）；
Sack cleaner second pocket（24）Bottom connects catalyst cast feeder（19）, sack cleaner second pocket（24）Bottom
Pipeline above-below direction is disposed with the second unloading valve（22）, the second storehouse pump（23）, catalyst cast feeder（19）Top connects low-temperature SCR
Catalyst hopper（18）, sack cleaner second pocket（24）Sack cleaner the first pocket outlet of bottom UNICOM（11）With cloth bag
Cleaner unit the second pocket import（21）Unicom pipeline, sack cleaner second pocket（24）The connection of bottom unicom pipeline is located at
Ammonia nozzle（17）Bottom, sack cleaner the second pocket bottom unicom pipeline is provided with the second ball valve（20）；
Sack cleaner second pocket exports（25）Connect air-introduced machine（26）, air-introduced machine（26）Upper setting chimney（27）.
2. industrial smoke dry type low temperature according to claim 1 works in coordination with dust-removal and desulfurizing denitration removal of mercury integrated apparatus, and it is special
Levy and be：Described sack cleaner first pocket outlet（11）It is arranged at sack cleaner first pocket（8）Top, described
Sack cleaner the first pocket import（7）It is arranged at sack cleaner first pocket（8）Lower section.
3. industrial smoke dry type low temperature according to claim 1 works in coordination with dust-removal and desulfurizing denitration removal of mercury integrated apparatus, and it is special
Levy and be：Described sack cleaner second pocket outlet（25）It is arranged at sack cleaner second pocket（24）Top, institute
Sack cleaner the second pocket import stated（21）It is arranged at the lower section of sack cleaner second pocket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620477301.8U CN205948624U (en) | 2016-05-24 | 2016-05-24 | Industry flue gas dry -type low temperature is in coordination with removing dust SOx/NOx control removal of mercury integrated device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620477301.8U CN205948624U (en) | 2016-05-24 | 2016-05-24 | Industry flue gas dry -type low temperature is in coordination with removing dust SOx/NOx control removal of mercury integrated device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205948624U true CN205948624U (en) | 2017-02-15 |
Family
ID=57968080
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620477301.8U Withdrawn - After Issue CN205948624U (en) | 2016-05-24 | 2016-05-24 | Industry flue gas dry -type low temperature is in coordination with removing dust SOx/NOx control removal of mercury integrated device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105833692A (en) * | 2016-05-24 | 2016-08-10 | 安徽威达环保科技股份有限公司 | Industrial fume dry type low-temperature synergic dedusting desulfurization and denitrification mercury removal integrated device and process |
| CN109061033A (en) * | 2018-07-10 | 2018-12-21 | 华电电力科学研究院有限公司 | SCR denitration demercuration integration catalyst integrated experiment device and test method |
-
2016
- 2016-05-24 CN CN201620477301.8U patent/CN205948624U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105833692A (en) * | 2016-05-24 | 2016-08-10 | 安徽威达环保科技股份有限公司 | Industrial fume dry type low-temperature synergic dedusting desulfurization and denitrification mercury removal integrated device and process |
| CN109061033A (en) * | 2018-07-10 | 2018-12-21 | 华电电力科学研究院有限公司 | SCR denitration demercuration integration catalyst integrated experiment device and test method |
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