CN201582822U - Concentric type axial rotational flow burner adopting high-temperature air combustion technology for industrial furnace - Google Patents
Concentric type axial rotational flow burner adopting high-temperature air combustion technology for industrial furnace Download PDFInfo
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- CN201582822U CN201582822U CN2009200733280U CN200920073328U CN201582822U CN 201582822 U CN201582822 U CN 201582822U CN 2009200733280 U CN2009200733280 U CN 2009200733280U CN 200920073328 U CN200920073328 U CN 200920073328U CN 201582822 U CN201582822 U CN 201582822U
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- industrial furnace
- temperature air
- layer sleeve
- concentric type
- burner
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Abstract
The utility model relates to a concentric type axial rotational flow burner adopting the high-temperature air combustion technology for an industrial furnace. The burner comprises a central circular straight pipe (1), an outer-layer sleeve (2), a rotary passage (3), and spiral fins (4), wherein the central circular straight pipe (1) is arranged in the outer-layer sleeve (2) and is coaxial with the outer-layer sleeve (2). The burner can strengthen the thorough mixing of the gaseous fuel and the high-temperature air in a furnace chamber of the industrial furnace, so as to realize the stable burning under the lower inlet air oxygen density, ensure the more uniform temperature distribution in the furnace chamber, decrease the phenomenon of high temperature at local parts, and meanwhile greatly lower the discharge of the nitrogen oxides (NOXs) and realize the goal of energy conservation and environmental protection.
Description
Technical field
The utility model belongs to the burner nozzle field, particularly relates to a kind of axial turbulent burner of concentric type of industrial furnace high-temperature air burning technology.
Background technology
Industrial furnace is very extensive in sector applications such as iron and steel, metallurgy, machinery, pottery, glass, is to carry out hot worked key equipment.In the industrial furnace of heat treatment and all kinds of hot procedures, adopt the technological approaches of the mode of fuel gas buring more and more as heating.High-temperature air burning (High temperature air combustion, HTAC) be a kind of advanced combustion technology of high preheated air under ultralow oxygen concentration condition that adopt, with natural gas or coal gas is fuel, send in the industrial furnace in the mode of jet and to burn, and by adopting the waste heat in the gas fume after burning of thermal storage ceramic material limits recovery efficiently, and be used for heating the air that enters in the burner hearth, thereby saved energy significantly.Simultaneously, because it is a high-intensity combustion under ultralow oxygen concentration, the therefore thermal NO (NO that generates in combustion process
X) concentration can be very low, has very low NO
XEmission performance, thereby its environment-friendly advantage is very remarkable.In addition, under ultralow oxygen condition, make the oxidized degree of hardware reduce, thereby improved the hot-working quality of metal to a certain extent.HTAC has obtained developing rapidly in 20 years in the past, has broad application prospects in the industrial furnace of industries such as Ferrous Metallurgy, glass, pottery, cement.
From relevant experiment,, can effectively change their mixed process in stove, to the uniformity and the NO of the smooth combustion under the ultralow oxygen condition, Temperature Distribution owing to change the condition that sprays into of gaseous fuel and preheated air
XThe influence of local growing amount very big.
At present, the burner structure of the high-temperature air burning industrial furnace of using in the engineering all is that the mode that high-temperature preheated air and gaseous fuel flow with direct projection sprays into burner hearth at a high speed usually, mixing between this several strands of jets turbulent motion in the confined space of burner hearth causing smoke backflow and fuel, air and the flue gas, guarantee characteristics such as the Temperature Distribution in the stove, local oxygen concentration distribution, thereby maintain smooth combustion and local heating power type NO under the hypoxia condition
XGeneration.Range of circulating flow and degree in the stove that the phase mutual interference of multiply direct projection stream causes are more limited.If high-temperature preheated air and fuel can be mixed in stove more fully, then will make local oxygen concentration and Temperature Distribution in the stove more reasonable, thereby make burning can under lower inlet oxygen concentration, realize burning and reduction local NO
XGrowing amount.
Eddy flow can play immixture better.In the burner nozzle structure of the present invention's design, skin is several strands of eddy flow high-temperature preheated air jets, the center is combustion gas direct projection stream, they are after entering burner hearth, the multiply swirl jet surrounds one direct jet, in the confined space of burner hearth, can realize mixing more fully, thereby be implemented in smooth combustion under the low oxygen concentration more and lower NO than direct projection stream
XDischarging.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of axial turbulent burner of concentric type of industrial furnace high-temperature air burning technology, and direct projection stream is difficult to make the more abundant mixing between furnace gas and makes more even, the NO of Temperature Distribution in the prior art to solve
XThe difficult problem that growing amount is lower.
The technical scheme that its technical problem that solves the utility model adopts is: the axial turbulent burner of concentric type that a kind of industrial furnace high-temperature air burning technology is provided, by the central circular straight pipe, outer layer sleeve, rotating channel, spiral fin is formed, and described central circular straight pipe is positioned at the inner coaxial position of outer layer sleeve.
The high temperature air import of described rotating channel and the anglec of rotation of outlet are 90 to spend to 360 degree and change.
Described rotating channel is spent to 360 degree spiral angle and 1～3 zero dimension spiral spread length R (R=l/h by 90 vertically by 2-4 bar spiral fin, l is the axial length of spiral fin, and h is the spiral fin height) rotation be arranged between central circular straight pipe and the outer layer sleeve.
Beneficial effect
The utility model can be strengthened gaseous fuel and the abundant mixing of high temperature air in the industrial furnace burner hearth, thereby guaranteed under lower inlet air oxygen concentration, to realize stable burning, Temperature Distribution in the burner hearth of chamber is more even, reduces localized hyperthermia, has greatly reduced nitrogen oxide (NO simultaneously
X) discharging, realize energy-conservation and target environmental protection.
Description of drawings
Fig. 1 is the axial turbulent burner front view of concentric type;
Fig. 2 is the axial turbulent burner air inlet of a concentric type schematic diagram;
Fig. 3 is an axial screw rib structure schematic diagram.
The specific embodiment
Below in conjunction with specific embodiment, further set forth the utility model.Should be understood that these embodiment only to be used to the utility model is described and be not used in the restriction scope of the present utility model.Should be understood that in addition those skilled in the art can make various changes or modifications the utility model after the content of having read the utility model instruction, these equivalent form of values fall within the application's appended claims institute restricted portion equally.
A kind of axial turbulent burner of concentric type of industrial furnace high-temperature air burning technology, by central circular straight pipe 1, outer layer sleeve 2, rotating channel 3, spiral fin 4 is formed, and central circular straight pipe 1 is positioned at outer layer sleeve 2 inner coaxial positions.The high temperature air import of rotating channel 3 and the anglec of rotation of outlet are 90 to spend to 360 degree and change.Rotating channel 3 is spent to 360 degree spiral angle and 1～3 zero dimension spiral spread length R (R=l/h by 90 vertically by 2-4 bar spiral fin 4, l is the axial length of spiral fin, and h is the spiral fin height) rotation be arranged between central circular straight pipe 1 and the outer layer sleeve 2.
When air rotating channel eddy flow angle was 0 ° (direct projection stream), intake condition is respectively: fuel was city gas, center circle pipe jet speed 29.5m/s; Air rotating channel effluxvelocity 35.6m/s.Preheated air 1273K, excess air coefficient 1.2, oxygen concentration 8% in the air, and the burner hearth bottom heat radiation is constant heat flux, and size is 28580W/m
2
After the industrial furnace high-temperature air burning, the combustion chamber mean temperature is: 1556K, final NO
XConcentration of emission is 38.2ppm, average CO, O in the combustion chamber
2Concentration is respectively: 80.6ppm and 1.98%.
When air rotating channel eddy flow angle was 180 °, intake condition was respectively: fuel is city gas, center circle pipe jet speed 29.5m/s; Air rotating channel effluxvelocity 35.6m/s.Preheated air 1273K, excess air coefficient 1.2, oxygen concentration 8% in the air, and the burner hearth bottom heat radiation is constant heat flux, and size is 28580W/m
2
After the industrial furnace high-temperature air burning, the combustion chamber mean temperature is: 1577K, final NO
XConcentration of emission is 34.3ppm, average CO, O in the combustion chamber
2Concentration is respectively: 30.4ppm and 1.31%.
When air rotating channel eddy flow angle was 210 °, intake condition was respectively: fuel is city gas, center circle pipe jet speed 29.5m/s; Air rotating channel effluxvelocity 35.6m/s.Preheated air 1273K, excess air coefficient 1.2, oxygen concentration 8% in the air, and the burner hearth bottom heat radiation is constant heat flux, and size is 28580W/m
2
After the industrial furnace high-temperature air burning, the combustion chamber mean temperature is: 1584K, final NO
XConcentration of emission is 34.1ppm, average CO, O in the combustion chamber
2Concentration is respectively: 28.6ppm and 1.29%.
Comparative example 1 and 2,3 as can be known, when adopting vortex burner, under identical condition, mean temperature in the combustion chamber increases, the final discharge capacity of NOX reduces, and the degree that burns of fuel (concentration with CO characterizes) improves, and the result shows that vortex burner can make and adopt the performance of HTAC industrial furnace to significantly improve.
Claims (3)
1. the axial turbulent burner of concentric type of an industrial furnace high-temperature air burning technology, by central circular straight pipe (1), outer layer sleeve (2), rotating channel (3), spiral fin (4) is formed, and it is characterized in that: described central circular straight pipe (1) is positioned at the inner coaxial position of outer layer sleeve (2).
2. the axial turbulent burner of concentric type of a kind of industrial furnace high-temperature air burning technology according to claim 1 is characterized in that: the high temperature air import of described rotating channel (3) and the anglec of rotation of outlet are 90 to spend to 360 degree and change.
3. the axial turbulent burner of concentric type of a kind of industrial furnace high-temperature air burning technology according to claim 1 and 2, it is characterized in that: described rotating channel (3) is spent to 360 degree spiral angle and 1～3 zero dimension spiral spread length R by 90 vertically by 2-4 bar spiral fin (4), R=l/h, l is the axial length of spiral fin, h is the spiral fin height, and rotating channel (3) rotation is arranged between central circular straight pipe (1) and the outer layer sleeve (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200733280U CN201582822U (en) | 2009-06-03 | 2009-06-03 | Concentric type axial rotational flow burner adopting high-temperature air combustion technology for industrial furnace |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200733280U CN201582822U (en) | 2009-06-03 | 2009-06-03 | Concentric type axial rotational flow burner adopting high-temperature air combustion technology for industrial furnace |
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|---|---|
| CN201582822U true CN201582822U (en) | 2010-09-15 |
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|---|---|---|---|
| CN2009200733280U Expired - Fee Related CN201582822U (en) | 2009-06-03 | 2009-06-03 | Concentric type axial rotational flow burner adopting high-temperature air combustion technology for industrial furnace |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101852434A (en) * | 2010-06-23 | 2010-10-06 | 东华大学 | Cyclone burner for high-temperature air burning industrial furnace |
| CN102537958A (en) * | 2012-02-20 | 2012-07-04 | 北京交通大学 | Cone rotor type gas burner |
| CN104235849A (en) * | 2014-10-09 | 2014-12-24 | 中冶南方(武汉)威仕工业炉有限公司 | Grading oxygen-enriched flameless combustion gas burner and control method thereof |
| CN104266190A (en) * | 2014-10-09 | 2015-01-07 | 中冶南方(武汉)威仕工业炉有限公司 | Oxygen-enriched and flameless gas burner and control method thereof |
| CN105021075A (en) * | 2015-05-26 | 2015-11-04 | 北京恩吉节能科技有限公司 | Dual-preheating rotation type heat-storage heat exchanger and combustion system |
-
2009
- 2009-06-03 CN CN2009200733280U patent/CN201582822U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101852434A (en) * | 2010-06-23 | 2010-10-06 | 东华大学 | Cyclone burner for high-temperature air burning industrial furnace |
| CN102537958A (en) * | 2012-02-20 | 2012-07-04 | 北京交通大学 | Cone rotor type gas burner |
| CN102537958B (en) * | 2012-02-20 | 2014-08-13 | 北京交通大学 | Cone rotor type gas burner |
| CN104235849A (en) * | 2014-10-09 | 2014-12-24 | 中冶南方(武汉)威仕工业炉有限公司 | Grading oxygen-enriched flameless combustion gas burner and control method thereof |
| CN104266190A (en) * | 2014-10-09 | 2015-01-07 | 中冶南方(武汉)威仕工业炉有限公司 | Oxygen-enriched and flameless gas burner and control method thereof |
| CN104235849B (en) * | 2014-10-09 | 2017-02-01 | 中冶南方(武汉)威仕工业炉有限公司 | Grading oxygen-enriched flameless combustion gas burner and control method thereof |
| CN105021075A (en) * | 2015-05-26 | 2015-11-04 | 北京恩吉节能科技有限公司 | Dual-preheating rotation type heat-storage heat exchanger and combustion system |
| CN105021075B (en) * | 2015-05-26 | 2018-12-07 | 北京恩吉节能科技有限公司 | It is double to preheat rotary regenerative heat exchanger and combustion system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100915 Termination date: 20130603 |