CN110513701A - A kind of novel spraying device and SNCR denitration system for waste incinerator - Google Patents
A kind of novel spraying device and SNCR denitration system for waste incinerator Download PDFInfo
- Publication number
- CN110513701A CN110513701A CN201910762149.6A CN201910762149A CN110513701A CN 110513701 A CN110513701 A CN 110513701A CN 201910762149 A CN201910762149 A CN 201910762149A CN 110513701 A CN110513701 A CN 110513701A
- Authority
- CN
- China
- Prior art keywords
- connecting tube
- nozzle
- gun
- incinerator
- barral
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2215/00—Preventing emissions
- F23J2215/10—Nitrogen; Compounds thereof
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chimneys And Flues (AREA)
- Treating Waste Gases (AREA)
- Incineration Of Waste (AREA)
Abstract
The invention discloses a kind of novel spraying devices and SNCR denitration system for waste incinerator, belong to garbage incinerating system field, including pedestal, the first barral of a gun, first jet and nozzle angle regulating mechanism；The first connecting tube is rotatably connected on pedestal, first jet is mounted in the first connecting tube, and the first connecting tube is horizontally disposed, fluid channel is equipped in pedestal, the both ends of fluid channel are connected to the end of the first barral of a gun, the first connecting tube respectively；Nozzle angle regulating mechanism is rotated for being drivingly connected pipe relative to pedestal；Second nozzle is fixed in first jet, the second connecting tube is fixed in first connecting tube, the second barral of a gun is fixed in first barral of a gun, switching part is fixed in fluid channel, second nozzle is connect with the second connecting tube, second connecting tube and switching part are rotatablely connected, and switching part is connect with the second barral of a gun.The configuration of the present invention is simple, design rationally, can adjust the spray angle of nozzle according to the smoke-gas area change in location of optimal reaction temperature.
Description
Technical field
The present invention relates to garbage incinerating system field, in particular to a kind of novel spraying device for waste incinerator and
SNCR denitration system.
Background technique
SNCR system is a kind of " selective non-catalytic reduction denitrogenation " process system, can effectively reduce garbage incinerating power plant
The nitrous oxides concentration that waste incineration generates.By spraying to smoke-gas area of the in-furnace temperature between 850 DEG C to 1050 DEG C is burned
Urea liquid or ammonium hydroxide are penetrated, urea liquid or ammonium hydroxide and reaction of nitrogen oxides generate the innocuous substances such as N2, H2O at high temperature,
To reduce the discharge amount of nitrogen oxides.
DeNOx method is known as the SNCR of reducing agent using ammonia, using urea for reducing agent is NOxOUT method；Ammonium hydroxide side
The process of case are as follows: ammonium hydroxide discharging pump-ammonium hydroxide storage tank-ammonium hydroxide supply unit-mixed allocation unit-spray gun-incinerator, meanwhile,
Soft water is transported to mixed allocation unit and mixed with ammonium hydroxide by soft water supply unit, and compressed air is connect with spray gun, will be mixed
Weak ammonia is taken out of by air-flow；The process of urea scheme are as follows: urea liquid storage tank-urea liquid supply unit-mixing point
With unit-spray gun-incinerator, mixed likewise, soft water is transported to mixed allocation unit by soft water supply unit with urea liquid,
Compressed air is connect with spray gun, and mixed urea liquid is taken out of by air-flow.
In denitration process, to burn in-furnace temperature between 850 DEG C to 1050 DEG C smoke-gas area injection urea liquid or
Person's ammonium hydroxide can obtain better denitration effect.It is general to select 900~950 DEG C of temperature region as denitration reaction efficiency
Optimal temperature window.
But in actual production, it is (warm i.e. in incinerator in variation for burning in-furnace temperature in the process of running
Degree is distributed in short transverse and is not fixed), therefore, in order to enable urea liquid or ammonium hydroxide always in optimal reaction temperature window
Injection, in the prior art, by the way of multilayer spray, in the short transverse of incinerator, (temperature is between 850 DEG C to 1050 DEG C
Smoke-gas area fluctuation range in) setting multilayer (at least two layers) spray gun, thus according in the incinerator of spray gun present position
Whether temperature devotes oneself to work to control the spray gun of respective layer closer to optimal reaction temperature window, makes urea liquid or ammonium hydroxide
The smoke-gas area closer to optimal reaction temperature window can be ejected into.
But the spray gun that above scheme is arranged there is needs is excessive, manufacturing cost is high, and can not be according to incinerator cigarette
Gas Temperature Distribution accurately adjusts the shortcomings that spray gun investment position；Simultaneously as needing to carry out spray gun cooling drop under hot environment
Temperature, excessive spray gun setting, needs the investment of more cooling airs or coolant liquid, this causes the increase of use cost.
Meanwhile the reducing agent used can not be mixed in advance for two kinds, when needing to spray into incinerator together
When, the prior art is usually that two sets of nozzles and corresponding material conveying mechanism is arranged, this is also unfavorable for the control of cost.
Summary of the invention
For spray gun arrangement quantity is more in SNCR denitration system of the existing technology and can not be according to incinerator cigarette
Gas Temperature Distribution accurately adjust spray gun investment position and two kinds of material spray sites must scattering device the problem of, mesh of the invention
Be a kind of novel spraying device for waste incinerator is provided.
To achieve the above object, the technical solution of the present invention is as follows:
A kind of novel spraying device for waste incinerator is worn including the pedestal that is mounted on incinerator inner wall, end
Cross the first barral of a gun of incinerator inner wall and the first jet in incinerator and nozzle angle regulating mechanism；On the pedestal
It is rotatably connected to the first connecting tube, the first jet is mounted in first connecting tube, the first jet and described the
The connection of one connecting tube, first connecting tube is horizontally disposed, and fluid channel, the both ends of the fluid channel are equipped in the pedestal
It is connected to respectively with the end of first barral of a gun, first connecting tube；The nozzle angle regulating mechanism is described for driving
Connecting tube is rotated relative to the pedestal；Second nozzle is fixed in the first jet, fixation is set in first connecting tube
There is the second connecting tube, the second barral of a gun is fixed in first barral of a gun, switching part is fixed in the fluid channel, it is described
Second nozzle is connect with one end of second connecting tube, and the second nozzle is connected to second connecting tube, and described second
One end of the other end of connecting tube and the switching part is rotatablely connected, and the other end of the switching part and second barral of a gun connect
It connects.
Preferably, the nozzle angle regulating mechanism includes the slave mantle tooth being fixedly mounted in first connecting tube
Wheel, the drive shaft being rotatablely connected with the pedestal and the drive bevel gear being fixedly mounted in the drive shaft, the active
Bevel gear is meshed with the driven wheel of differential, and the other end of the drive shaft passes through the outer wall of the incinerator.
Another preferred, the nozzle angle regulating mechanism includes the tooth being fixedly mounted in first connecting tube
The rack gear take turns, being slidably connected on the pedestal and the push rod being fixedly connected with the rack gear, the gear and the rack gear
It is meshed, the other end of the push rod passes through the outer wall of the incinerator.
Preferably, the first jet is Venturi nozzle.
Preferably, the second nozzle is straight hole nozzle or taper hole nozzle.
Preferably, the second nozzle is second fluid nozzle.
The invention also discloses a kind of SNCR denitration systems, fill including the above-mentioned novel spray for waste incinerator
It sets.
Preferably, the novel spraying device for waste incinerator has several, and described several are burnt for rubbish
The novel spraying device for burning furnace is distributed on the sustained height position of incinerator inner wall.
By adopting the above technical scheme, setting due to pedestal, the first connecting tube, first jet and nozzle angle regulating mechanism
It sets, so that by the movement of nozzle angle regulating mechanism to drive the rotation of the first connecting tube, and then make to be mounted on the first connection
The pitch angle of first jet on pipe is adjusted, thus make in incinerator that flue-gas temperature is when changing, first jet
The solution containing reducing agent sprayed can still fall within the smoke-gas area of optimal reaction temperature window, be arranged from without being layered
Nozzle also reduces the dosage of cooling air-flow or water flow while reducing first jet setting quantity；It is identical, due to stream
The setting of switching part in body channel, so that the angle of second nozzle can be also adjusted in synchronism when first jet angular adjustment, from
And while realizing the synchronous transport of two kinds of materials, two kinds of objects can be realized according to the variation of flue-gas temperature in incinerator
Expect the variation of spray angle.
Detailed description of the invention
Fig. 1 is a kind of schematic top plan view of the novel spraying device for waste incinerator in the embodiment of the present invention one；
Fig. 2 is a kind of left view schematic diagram of the novel spraying device for waste incinerator in the embodiment of the present invention one；
Fig. 3 is a kind of schematic side view of the novel spraying device for waste incinerator in the embodiment of the present invention two.
In figure: 1- pedestal, 2- barral of a gun, 3- nozzle, 4- connecting tube, 5- driven wheel of differential, 6- drive shaft, 7- active conical tooth
Wheel, 8- gear, 9- rack gear, 10- push rod, 11- fluid channel, 12- ontology, 13- connector, 14- bolt, 15- handle, 16- are burnt
Burn furnace, 17- connector, 18- switching part, the second barral of a gun of 21-, 31- second nozzle, the second connecting tube of 41-.
Specific embodiment
Specific embodiments of the present invention will be further explained with reference to the accompanying drawing.It should be noted that for
The explanation of these embodiments is used to help understand the present invention, but and does not constitute a limitation of the invention.In addition, disclosed below
The each embodiment of the present invention involved in technical characteristic can be combined with each other as long as they do not conflict with each other.
Embodiment one
As shown in Figures 1 and 2, a kind of novel spraying device for waste incinerator, including be mounted in incinerator 16
Pedestal 1, end on wall pass through the first barral of a gun 2 of 16 inner wall of incinerator and the first jet 3 in incinerator 16 and spray
Mouth angle adjusting mechanism；
Pedestal 1 is usually connected on the inner wall of incinerator 16 by bolt 14, and the first connecting tube is rotatably connected on pedestal 1
4, first jet 3 is mounted in the first connecting tube 4, the jet stream emission direction through slot of first jet 3 perpendicular to the first connecting tube 4,
First jet 3 is connected to the first connecting tube 4, and the first connecting tube 4 is horizontally disposed, and fluid channel 11, fluid channel are equipped in pedestal 1
11 both ends are connected to the end of the first barral of a gun 2, the first connecting tube 4 respectively；Nozzle angle regulating mechanism is for being drivingly connected pipe 4
It is rotated relative to pedestal 1.
In the present embodiment, it is fixed with second nozzle 31 in first jet 3, is fixed with second in the first connecting tube 4
Connecting tube 41 is fixed with the second barral of a gun 21 in first barral of a gun 2, is fixed with switching part 18, second nozzle in fluid channel 11
31 connect with one end of the second connecting tube 41, the connection of second nozzle 31 and the second connecting tube 41, the second connecting tube 41 it is another
End and one end of switching part 18 are rotatablely connected, and the other end of switching part 18 is connect with the second barral of a gun 21.
In general, the first barral of a gun 2 is coaxially arranged with the second barral of a gun 21, first jet 3 is coaxially arranged with second nozzle 31,
First connecting tube 4 is coaxially arranged with the second connecting tube 41；Between first gun body 2 and the second gun body 21, first jet 3 and second
It is fixedly connected by connector 17 between nozzle 31 and between switching part 18 and fluid channel 11, connector 17 is preferably bar
Shape is latticed, thus enable material normal through.
In actual use, since the first gun body 2, the second gun body 21 are usually all to pass perpendicularly through incinerator, and connect with first
Adapter tube 4, the second connecting tube 41 are vertical, therefore switching part 18 should be arranged to carrying out material into 90 ° of directions foldings of flow direction progress
Curved shape, such as 90 ° of bend pipes.
In general, the first connecting tube 4 is rotatably connected on fluid channel 11, sealing ring is set between the two and is sealed, sealing
The material of circle is preferably metal or plastic products resistant to high temperature.Correspondingly, also being set between the second connecting tube 41 and switching part 18
Sealing ring sealing is set, the material of the sealing ring is preferably also metal or plastic products resistant to high temperature.
In the present embodiment, nozzle angle regulating mechanism include the driven wheel of differential 5 being fixedly mounted in the first connecting tube 4,
The drive shaft 6 being rotatablely connected with pedestal 1 and the drive bevel gear 7 that is fixedly mounted in drive shaft 6, drive bevel gear 7 with from
Dynamic bevel gear 5 is meshed, and the other end of drive shaft 6 passes through the outer wall of incinerator for external staff's operation.In general, drive shaft 6
The other end for burning furnace outer wall is provided with handle 15 or is connected with motor (not shown).
In the present embodiment, axis hole compatible with drive shaft 6 is provided on pedestal 1, which is stepped hole for preventing
Drive shaft 6 moves axially；In the present embodiment, pedestal 1 includes an ontology 12, and above-mentioned fluid channel 11 is arranged in ontology 12
Interior, which is equipped with connector 13, is used to connect bolt 14 on connector 13, while drive shaft 6 is also rotatably connected on the company
On junctor 13；In order to keep stable, ontology 12 is provided with the connector 13 of at least two faces.
In the present embodiment, first jet 3 is Venturi nozzle, for spraying powder material；Second nozzle 31 is straight hole
Nozzle or taper hole nozzle, for spraying liquid material；In general, either powder material or liquid material, be by means of
Compressed air sprinkling, therefore first jet 3 and second nozzle 31 are two-fluid spray nozzle.
In use, the ammonium hydroxide or urea liquid after dilution pass sequentially through the second barral of a gun 2, switching part together with compressed air
18, the second connecting tube 41, second nozzle 31 spray into incinerator；Powder material is connected by the first barral of a gun 2, pedestal 1, first
Pipe 4, first jet 3 spray into incinerator, when flue-gas temperature changes in incinerator, operator in operation handle or
Motor drives the rotation of drive shaft 6 (or rotating by temperature change chain control drive shaft 6), and drive bevel gear 7 drives from mantle
Gear 5 rotates, and driven wheel of differential 5 drives the rotation of the first connecting tube 4, and the pitch angle of such first jet 3 changes, and makes the
One nozzle 3 is directed toward the smoke-gas area of optimal reaction temperature window always；Correspondingly, drive of the second nozzle 31 in first jet 3
Lower passive rotation, because the second connecting tube 41 and switching part 18 are rotation connections, the rotation of second nozzle 31 is not by shadow
It rings.
Embodiment two
It is from the difference of embodiment one: nozzle angle regulating mechanism is different with embodiment one, in the present embodiment, such as schemes
Shown in 3, nozzle angle regulating mechanism includes the gear 8 (roller gear) being fixedly mounted in the first connecting tube 4, is slidably connected at
Rack gear 9 on pedestal 1 and the push rod 10 being fixedly connected with rack gear 9, gear 8 are meshed with rack gear 9, and the other end of push rod 10 is worn
Cross the outer wall of incinerator.In general, one end that push rod 10 passes through burning furnace outer wall is connected with handle or straight line driving mechanism, straight line
Driving mechanism is electronic screw rod, hydraulic cylinder or cylinder.
In the present embodiment, sliding rail or sliding slot are set on ontology 12, sliding block, above-mentioned company are installed on rack gear 9
Junctor 13 is equipped with perforation compatible with push rod 10.
The invention also discloses a kind of SNCR denitration systems, and as the prior art, SNCR denitration system generally includes to store
The holding vessel of urea liquid or ammonium hydroxide, powder material storage tank, the pump of transferring raw material or blower, for diluting raw material
Water tank, for preparing or the container of hybrid reaction material (mixer or blender), the sky for generating compressed air
Press or air accumulator and corresponding pipeline and valve etc. also typically include control said pump, the control system of valve, In
This, the present invention repeat no more SNCR denitration process flow and detailed relevant device.
A kind of SNCR denitration system of the present invention further includes the above-mentioned novel spraying device for waste incinerator, and first
Barral of a gun 2 connects compressed air and powdered reagents material, and the second barral of a gun 21 connects compressed air and liquid material, empty by compression
The flowing of gas drive corresponding material spray (as needed selection spray liquid, it is powdered or simultaneously using both)；Wherein,
Novel spraying device in SNCR denitration system of the invention for waste incinerator has several (such as 3,4,5 etc.
), several are distributed in the sustained height position of incinerator inner wall for the novel spraying device of waste incinerator,
Such as cylindrical incinerator, several novel spraying devices for being used for waste incinerator are evenly spaced in same circumference
On；So set, make incinerator the smoke-gas area of optimal reaction temperature window can obtain everywhere first jet 3 and/
Or the spray of second nozzle 31.
In conjunction with attached drawing, the embodiments of the present invention are described in detail above, but the present invention is not limited to described implementations
Mode.For a person skilled in the art, in the case where not departing from the principle of the invention and spirit, to these embodiments
A variety of change, modification, replacement and modification are carried out, are still fallen in protection scope of the present invention.
Claims (8)
1. a kind of novel spraying device for waste incinerator, it is characterised in that: including the seat being mounted on incinerator inner wall
The first barral of a gun and first jet and nozzle angle regulating mechanism in incinerator that body, end pass through incinerator inner wall；
The first connecting tube is rotatably connected on the pedestal, the first jet is mounted in first connecting tube, first spray
Mouth is connected to first connecting tube, and first connecting tube is horizontally disposed, and fluid channel, the fluid are equipped in the pedestal
The both ends in channel are connected to the end of first barral of a gun, first connecting tube respectively；The nozzle angle regulating mechanism is used
It is rotated in the driving connecting tube relative to the pedestal；Second nozzle, first connection are fixed in the first jet
It is fixed with the second connecting tube in pipe, the second barral of a gun is fixed in first barral of a gun, is fixed in the fluid channel
Switching part, the second nozzle are connect with one end of second connecting tube, and the second nozzle and second connecting tube connect
Logical, the other end of second connecting tube and one end of the switching part are rotatablely connected, the other end of the switching part with it is described
The connection of second barral of a gun.
2. the novel spraying device according to claim 1 for waste incinerator, it is characterised in that: the nozzle angle
Regulating mechanism includes the driven wheel of differential being fixedly mounted in first connecting tube, the drive shaft with pedestal rotation connection
And it is fixedly mounted on the drive bevel gear in the drive shaft, the drive bevel gear is meshed with the driven wheel of differential,
The other end of the drive shaft passes through the outer wall of the incinerator.
3. the novel spraying device according to claim 1 for waste incinerator, it is characterised in that: the nozzle angle
Regulating mechanism include the gear being fixedly mounted in first connecting tube, the rack gear being slidably connected on the pedestal and with
The push rod that the rack gear is fixedly connected, the gear are meshed with the rack gear, and the other end of the push rod passes through the burning
The outer wall of furnace.
4. the novel spraying device according to claim 1 for waste incinerator, it is characterised in that: the first jet
For Venturi nozzle.
5. the novel spraying device according to claim 4 for waste incinerator, it is characterised in that: the second nozzle
For straight hole nozzle or taper hole nozzle.
6. the novel spraying device according to claim 5 for waste incinerator, it is characterised in that: the second nozzle
For second fluid nozzle.
7. a kind of SNCR denitration system, it is characterised in that: be used for waste incinerator including as claimed in any one of claims 1 to 6
Novel spraying device.
8. SNCR denitration system according to claim 7, it is characterised in that: the novel spray for waste incinerator
Device has several, several described novel spraying devices for being used for waste incinerator are distributed in the same of incinerator inner wall
On height and position.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910762149.6A CN110513701B (en) | 2019-08-19 | 2019-08-19 | A novel spray set and SNCR deNOx systems for waste incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910762149.6A CN110513701B (en) | 2019-08-19 | 2019-08-19 | A novel spray set and SNCR deNOx systems for waste incinerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110513701A true CN110513701A (en) | 2019-11-29 |
| CN110513701B CN110513701B (en) | 2021-04-16 |
Family
ID=68626558
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910762149.6A Active CN110513701B (en) | 2019-08-19 | 2019-08-19 | A novel spray set and SNCR deNOx systems for waste incinerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110513701B (en) |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5053210A (en) * | 1986-02-11 | 1991-10-01 | Uhde Gmbh | Method for the purification of flue gases |
| CN101371969A (en) * | 2008-10-09 | 2009-02-25 | 江苏中科节能环保技术有限公司 | Reducing reagent nozzle for denitration by SNCR method |
| JP2009208078A (en) * | 2009-06-16 | 2009-09-17 | Mitsubishi Heavy Ind Ltd | Method for treating mercury in tail gas, and treatment system for tail gas |
| CN101745306A (en) * | 2010-01-29 | 2010-06-23 | 东南大学 | Method and device for removing sulfur dioxide and nitric oxide by combining dual-shaft clash smoke gas |
| CN103611411A (en) * | 2013-12-04 | 2014-03-05 | 无锡雪浪环境科技股份有限公司 | Dry denitration processing device in furnace |
| CN103857460A (en) * | 2011-06-09 | 2014-06-11 | 梅尔道&斯坦法斯环境科技有限公司 | Process and apparatus for reducing the content of nitrogen oxides |
| CN104214788A (en) * | 2014-09-28 | 2014-12-17 | 临沂市巨亚环保节能锅炉研究所 | Reducing agent linear spray denitration boiler |
| CN204051973U (en) * | 2014-07-29 | 2014-12-31 | 北京洛卡环保技术有限公司 | A kind of injector for SNCR denitration system |
| CN104624422A (en) * | 2015-02-12 | 2015-05-20 | 西安近代化学研究所 | Novel three-fluid sprayer and spraying method thereof |
| CN105148435A (en) * | 2015-08-31 | 2015-12-16 | 福建新偌环境科技有限公司 | Multifunctional fire protection coaxial nozzle device |
| CN205495328U (en) * | 2016-04-20 | 2016-08-24 | 周建南 | Spray gun for SNCR flue gas denitration |
| CN206082164U (en) * | 2016-08-23 | 2017-04-12 | 中电投远达环保工程有限公司 | Sled formula fast -assembling flue gas denitration device |
| CN206168207U (en) * | 2016-11-09 | 2017-05-17 | 山西华仁通电力科技有限公司 | High -efficient SNCR deNOx systems's of W flame furnace spray gun arrangement structure |
| CN108722144A (en) * | 2018-07-23 | 2018-11-02 | 易善莉 | Dry denitration and selective non-catalytic reduction denitrating system and its working method |
| CN109731465A (en) * | 2019-01-16 | 2019-05-10 | 北京清新环境技术股份有限公司 | A kind of alumina rotary kiln calcining flue gas denitrification system |
| CN110038421A (en) * | 2019-05-21 | 2019-07-23 | 辽宁远景产学研环保技术有限公司 | A kind of Dual-Phrase Distribution of Gas olid can thermometric pressurization solid particle spray gun |
-
2019
- 2019-08-19 CN CN201910762149.6A patent/CN110513701B/en active Active
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5053210A (en) * | 1986-02-11 | 1991-10-01 | Uhde Gmbh | Method for the purification of flue gases |
| CN101371969A (en) * | 2008-10-09 | 2009-02-25 | 江苏中科节能环保技术有限公司 | Reducing reagent nozzle for denitration by SNCR method |
| JP2009208078A (en) * | 2009-06-16 | 2009-09-17 | Mitsubishi Heavy Ind Ltd | Method for treating mercury in tail gas, and treatment system for tail gas |
| CN101745306A (en) * | 2010-01-29 | 2010-06-23 | 东南大学 | Method and device for removing sulfur dioxide and nitric oxide by combining dual-shaft clash smoke gas |
| CN103857460A (en) * | 2011-06-09 | 2014-06-11 | 梅尔道&斯坦法斯环境科技有限公司 | Process and apparatus for reducing the content of nitrogen oxides |
| CN103611411A (en) * | 2013-12-04 | 2014-03-05 | 无锡雪浪环境科技股份有限公司 | Dry denitration processing device in furnace |
| CN204051973U (en) * | 2014-07-29 | 2014-12-31 | 北京洛卡环保技术有限公司 | A kind of injector for SNCR denitration system |
| CN104214788A (en) * | 2014-09-28 | 2014-12-17 | 临沂市巨亚环保节能锅炉研究所 | Reducing agent linear spray denitration boiler |
| CN104624422A (en) * | 2015-02-12 | 2015-05-20 | 西安近代化学研究所 | Novel three-fluid sprayer and spraying method thereof |
| CN105148435A (en) * | 2015-08-31 | 2015-12-16 | 福建新偌环境科技有限公司 | Multifunctional fire protection coaxial nozzle device |
| CN205495328U (en) * | 2016-04-20 | 2016-08-24 | 周建南 | Spray gun for SNCR flue gas denitration |
| CN206082164U (en) * | 2016-08-23 | 2017-04-12 | 中电投远达环保工程有限公司 | Sled formula fast -assembling flue gas denitration device |
| CN206168207U (en) * | 2016-11-09 | 2017-05-17 | 山西华仁通电力科技有限公司 | High -efficient SNCR deNOx systems's of W flame furnace spray gun arrangement structure |
| CN108722144A (en) * | 2018-07-23 | 2018-11-02 | 易善莉 | Dry denitration and selective non-catalytic reduction denitrating system and its working method |
| CN109731465A (en) * | 2019-01-16 | 2019-05-10 | 北京清新环境技术股份有限公司 | A kind of alumina rotary kiln calcining flue gas denitrification system |
| CN110038421A (en) * | 2019-05-21 | 2019-07-23 | 辽宁远景产学研环保技术有限公司 | A kind of Dual-Phrase Distribution of Gas olid can thermometric pressurization solid particle spray gun |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110513701B (en) | 2021-04-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102921284B (en) | Method and device for controlling NOx concentration in smoke gas of cement kiln | |
| CN102274687B (en) | SNCR (Selective Non-Catalytic Reduction) flue gas denitration device taking urea as reducting agent | |
| CN102658022A (en) | SNCR (Selective non-catalytic reaction) denitration system | |
| CN110513702A (en) | A kind of waste incinerator denitration adjustable spray equipment and SNCR denitration system | |
| CN102179171A (en) | Multi-stage themolysis coupled denitration method using front flow field uniformizing device and device thereof | |
| CN104383808A (en) | Process and device for carrying out flue gas denitrification by utilizing solid organic denitrifying agent | |
| CN108561893B (en) | Industrial boiler flue gas multi-pollutant cooperative control device and process flow thereof | |
| CN106807206A (en) | A kind of SNCR flue gas denitrification systems for domestic waste incineration | |
| CN102806003A (en) | SNCR (selective non-catalytic reduction) denitration device and method for rotary cement kiln | |
| CN201031196Y (en) | Fine material conveying and blowing device used for float glass kiln | |
| CN110513701A (en) | A kind of novel spraying device and SNCR denitration system for waste incinerator | |
| CN209076420U (en) | A kind of MPR equipment for denitrifying flue gas | |
| CN202237748U (en) | SNCR (selective non catalytic reduction) flue gas denitration device taking carbamide as reducing agent | |
| CN209229785U (en) | It is capable of handling the rocket engine burner and power drive unit of complex component | |
| CN206262345U (en) | A kind of SNCR denitration system for garbage power | |
| CN213801933U (en) | Denitration material conveying equipment for coal-fired boiler | |
| CN215196238U (en) | Denitration device for cement production | |
| CN112915760B (en) | Solid waste pyrolysis flue gas cooperative treatment system | |
| CN212068303U (en) | Polymer selectivity deNOx systems that feed is accurate | |
| CN210356669U (en) | Desulfurization and denitrification tower for waste gas treatment of thermal power plant | |
| CN207462971U (en) | A kind of rotary kiln flue gas denitrification system | |
| CN103301737A (en) | Urea hydrolyzed SNCR (selective non-catalytic reduction) flue gas denitrification device for fluidized bed boiler | |
| CN219362598U (en) | Dry denitration distribution conveying system | |
| CN208574451U (en) | A kind of limekiln combined denitration system | |
| CN218131055U (en) | Novel denitration agent sprays device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |