CN205119048U - Bitonic wind vortex burner - Google Patents
Bitonic wind vortex burner Download PDFInfo
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- CN205119048U CN205119048U CN201520908744.3U CN201520908744U CN205119048U CN 205119048 U CN205119048 U CN 205119048U CN 201520908744 U CN201520908744 U CN 201520908744U CN 205119048 U CN205119048 U CN 205119048U
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- air
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- air pipeline
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- wind
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Abstract
The utility model discloses a bitonic wind vortex burner, this bitonic wind vortex burner include wind tube cell way one time, and the interior overgrate air pipeline in this wind tube cell way outside is located to the cover, overlaps the outer overgrate air pipeline of locating this interior overgrate air pipeline, the wind tube cell is provided with the automatic ignition device who is used for lighting the buggy in one time being said, be provided with between interior overgrate air pipeline and the outer overgrate air pipeline and be used for adjusting the adjusting device of the amount of wind proportion of interior overgrate air and outer overgrate air. Through setting up inside and outside overgrate air pipeline, can realize the fractional combustion of buggy, guarantee promptly that pulverized coal air flow's stability is caught fire and the burning, do benefit to the production that suppresses NOx, in addition, because the proportion of inside and outside overgrate air can be adjusted, realized the diameter of buggy torch, the three -dimensional dynamic automatic adjustment of length, improved the adaptability with different furnace body combustion space.
Description
Technical field
The utility model relates to Industrial Boiler field, particularly, relates to a kind of Bi-register swirl burner.
Background technology
Technical grade pulverized-coal fired boiler has started sizable application in developed countries such as America and Europes, this technical development is the eighties in last century, ripe the nineties, domestic in beginning technology transfer in 2005, innovation, wherein pulverized coal combustion is core and the key technology of this technology.Comprise power boiler burning technology at present domestic generally to introduce, Japan, Germany, power station pulverized coal combustion that the is French and U.S. occupy prostatitis, the world.
Germany due to national conditions and its Industrial Boiler pulverized coal combustion of energy resource structure problem the most advanced and flourishing.
Domestic pulverized coal combustion is mainly divided into bias combustion, bluff body to burn and swirl flow combustion technology, and under the support of a large amount of engineering practice and correlation theory, hundred million Li Jieneng companies develop that Industrial Boiler is two adjusts the low nitrogen coal burner of wind eddy flow.
China energy resource structure determine considerable time power fuel will based on coal, ratio is about 70%.
The subject matter that current industrial boilers in China coal burner exists has:
1, the less coal in region of Germany is based on brown coal, and kind is single, and its combustion technology coal adapts to comparatively single.This technology is higher to the Lower heat value of coal, ashless dry base fugitive constituent, ash, moisture requirement.
2, burner configuration mode and quantity are reasonable not, and in running, combustion system exists slagging scorification, coking phenomenon.
3, load adjustment adaptability is lower, and coal dust burn-off rate is not ideal enough, is not suitable for current power conservation requirement.
4, burning torch characteristic regulating measure is limited, poor with therrmodynamic system matching.
5, coal dust firing is stable not, and system exists deflagration phenomenon, affects steam generator system safe operation.
6, automatic detection and control system is reasonable not, and operability is poor, cannot realize automatic operation.
7, combustion-system fuel and blowing system design not rationally, and NOx original discharge concentration is higher, reaches about 500mg/Nm3, is not suitable for current environmental requirement, and afterbody NOx control expense is higher.
Utility model content
The purpose of this utility model is to provide a kind of Bi-register swirl burner, and this Bi-register swirl burner can realize low nitrogen burning, and improves the adaptability of body of heater combustion space.
To achieve these goals, the utility model provides a kind of Bi-register swirl burner, this Bi-register swirl burner comprises primary wind and powder pipeline, be sheathed on the inner second air pipeline outside this primary wind and powder pipeline, be sheathed on the outer second air pipeline of this inner second air pipeline, being provided with the automatic ignition device for firing coal-dust in described primary wind and powder pipeline, between described inner second air pipeline and outer second air pipeline, being provided with the adjusting device of the air quantity ratio for regulating described inner second air and outer second air.
Preferably, be provided with inward eddy blade in described inner second air pipeline, this inward eddy blade is set on described primary wind and powder pipeline.
Preferably, described Bi-register swirl burner also comprises the first adjusting device of the swirl strength regulating described inner second air.
Preferably, described inward eddy blade extends from front to back gradually with reducing, described inner second air pipeline is provided with the first nut, described first adjusting device is the first screw rod, this first screw flight is tightened on described first nut, and one end of this first screw rod is fixed to the rear end of described inward eddy blade, the other end extends to outside through described outer second air pipeline.
Preferably, be provided with contour stealth blade in described outer second air pipeline, this contour stealth blade is set on described inner second air powder pipeline.
Preferably, described Bi-register swirl burner also comprises the second adjusting device of the swirl strength regulating described outer second air.
Preferably, described contour stealth blade extends from front to back gradually with reducing, described inner second air pipeline is provided with the second nut, described second adjusting device is the second screw rod, this second screw flight is tightened on described second nut, and one end of this second screw rod is fixed to the rear end of described contour stealth blade, the other end extends to outside through described inner second air pipeline and described outer second air pipeline.
Preferably, the strong rotational flow atomization device of wind powder is provided with in described primary wind and powder pipeline.
Preferably, the strong rotational flow atomization device of described wind powder is the adjustable atomising device of swirl strength.
Preferably, described automatic ignition device is the automatic ignition device of extension type.
Preferably, the outlet side of described outer second air pipeline is formed as the outer enlarging of taper, and this outer enlarging is in the outlet side axially protruding from described inner second air pipeline of described burner.
Preferably, the straight length that described primary wind and powder pipeline comprises elbow section and removably connects with this elbow section, primary wind and powder feeding system enters from the import of this elbow section.
Preferably, described burner also comprises combustion control system and the host computer PLC that is electrically connected with this combustion control system or DCS system, and this combustion control system comprises described automatic ignition system, runs stored program controlled, Image Fire check system, infrared fire check system, oxygen content fume component analysis system, outer second air air pressure air flow checkout gear.
Pass through technique scheme, in burner actual moving process, because secondary air separating is inner second air and outer second air, first the less inner second air of air quantity can mix with primary wind and powder stream, oxygen needed for coal powder ignition and initiation combustion is provided, the more outer second air of air quantity then mixes with breeze airflow gradually along range, there is provided coal dust firing to burning required oxygen further, and strengthen later stage disturbance, which forms the fractional combustion of staged air distribution and coal dust, flame range is long, and it is longer that coal dust burns the time, avoids flame peak value.Namely the fractional combustion of coal dust ensures stable ignition and the burning of breeze airflow, be beneficial to again the generation suppressing NOx, in addition, because the ratio of inside and outside Secondary Air can adjust, achieve the diameter of coal dust torch, the Three-Dimensional Dynamic of length adjusts automatically, improve the adaptability from different body of heater combustion space.
Other feature and advantage of the present utility model are described in detail in detailed description of the invention part subsequently.
Accompanying drawing explanation
Accompanying drawing is used to provide further understanding of the present utility model, and forms a part for description, is used from explanation the utility model, but does not form restriction of the present utility model with detailed description of the invention one below.In the accompanying drawings:
Fig. 1 is the structural representation of the Bi-register swirl burner that the utility model preferred embodiment provides.
Description of reference numerals
11 primary wind and powder pipeline 111 wind powder strong rotational flow atomization device 112 elbow section
113 straight length 12 inner second air pipeline 121 inward eddy blades
122 first adjusting device 123 adjusting device 13 outer second air pipelines
The outer enlarging of 131 contour stealth blade 132 second adjusting device 133
30 combustion control system 31 automatic ignition systems 32 run stored program controlled
33 Image Fire check system 34 infrared fire check system 35 oxygen content fume component analysis systems
36 outer second air air pressure air flow checkout gear 37 primary wind and powder feeding systems
38 overfire air device 39 flue gas recycled 40 afterbody cleaning flue gases
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described in detail.Should be understood that, detailed description of the invention described herein, only for instruction and explanation of the utility model, is not limited to the utility model.
In the utility model, when not doing contrary explanation, the noun of locality used such as " upper and lower, left and right " typically refers to the page of accompanying drawing, " inside and outside " refers to the interior and outer of corresponding component profile, " forward and backward " is for the flow direction of coal dust and wind, particularly, the flow direction towards coal dust and wind is front, and the flow direction deviating from coal dust and wind is rear.
As shown in Figure 1, the utility model provides a kind of Bi-register swirl burner, this Bi-register swirl burner comprises primary wind and powder pipeline 11, be sheathed on the inner second air pipeline 12 outside this primary wind and powder pipeline 11, be sheathed on the outer second air pipeline 13 of this inner second air pipeline 12, being provided with the automatic ignition device for firing coal-dust in primary wind and powder pipeline 11, between inner second air pipeline 12 and outer second air pipeline 13, being provided with the adjusting device 123 of the air quantity ratio for regulating inner second air and outer second air.
In burner actual moving process, because secondary air separating is inner second air and outer second air, first the less inner second air of air quantity can mix with primary wind and powder stream, oxygen needed for coal powder ignition and initiation combustion is provided, the more outer second air of air quantity then mixes with breeze airflow gradually along range, there is provided coal dust firing to burning required oxygen further, and strengthen later stage disturbance, which forms the fractional combustion of staged air distribution and coal dust, flame range is long, it is longer that coal dust burns the time, avoids flame peak value.The fractional combustion of coal dust had both ensured stable ignition and the burning of breeze airflow, be beneficial to again the generation suppressing NOx, in addition, because the ratio of inside and outside Secondary Air can adjust, achieve the diameter of coal dust torch, the Three-Dimensional Dynamic of length adjusts automatically, improve the adaptability from different body of heater combustion space.
In preferred embodiment of the present utility model, regulate the air quantity scale of inside and outside Secondary Air for convenience, adjusting device 123 specifically comprises the baffle plate be separately positioned on inner second air pipeline 12, and controls the adjusting screw(rod) of aperture of two baffle plates respectively.
For improving the burn-off rate of fuel further, and increase burning torch characteristic regulating measure, strengthen and therrmodynamic system matching, be provided with inward eddy blade 121 in inner second air pipeline 12, this inward eddy blade 121 is set on primary wind and powder pipeline 11.Like this, by changing the blade angle of inward eddy blade, can to change in inner second air pipeline 12 by the swirl strength of inner second air.
Preferably, for convenience of the swirl strength regulating inner second air, Bi-register swirl burner also comprises the first adjusting device 122 of the swirl strength regulating inner second air.
Particularly, inward eddy blade 121 extends from front to back gradually with reducing, inner second air pipeline 12 is provided with the first nut, first adjusting device 122 is the first screw rod, this first screw flight is tightened on the first nut, and one end of this first screw rod is fixed to the rear end of inward eddy blade 121, the other end extends to outside through outer second air pipeline 13.Like this, when needing the swirl strength strengthening inner second air, the first screw rod can be rotated, first screw rod is moved backward relative to the first nut, thus pull inward eddy blade 121 to move backward, therefore there is more air quantity to flow through from the gap of inward eddy blade 121 and inner second air pipeline 12, and do not participate in swirling motion.
For improving again the burn-off rate of fuel further, and increase burning torch characteristic regulating measure further, strengthen and therrmodynamic system matching, be provided with contour stealth blade 131 in outer second air pipeline 13, this contour stealth blade 131 is set on inner second air powder pipeline 12.Like this, by changing the blade angle of contour stealth blade, the swirl strength of the outer second air passed through in outer second air pipeline 13 can be changed.
Bi-register swirl burner also comprises the second adjusting device 132 of the swirl strength regulating outer second air.
Contour stealth blade 131 extends from front to back gradually with reducing, inner second air pipeline 12 is provided with the second nut, second adjusting device 132 is the second screw rod, this second screw flight is tightened on the second nut, and one end of this second screw rod is fixed to the rear end of contour stealth blade 131, the other end extends to outside through inner second air pipeline 12 and outer second air pipeline 13.
Like this, when needing the swirl strength strengthening outer second air, the second screw rod can be rotated, second screw rod is moved backward relative to the second nut, thus pull contour stealth blade 131 to move backward, therefore there is more air quantity to flow through from the gap of contour stealth blade 131 and outer second air pipeline 13, and do not participate in swirling motion.
In addition, such as, the rational ratio of interior outer second air and appropriate flow velocity can be controlled, 0.9 is about at the excess air coefficient in primary zone, be in reproducibility combustion atmosphere, rational control combustion process reduces ignition temperature, and core space ignition temperature controls at 1350 DEG C, effectively can reduce the generation of heating power type and fuel type NOx.
For improving the burn-off rate of fuel, realizing the rationally efficient atomization fully of coal dust, in primary wind and powder pipeline 11, being provided with the strong rotational flow atomization device 111 of wind powder.Like this, when the primary wind and powder of direct current is by after the strong rotational flow atomization device 111 of wind powder, the turbulent flow atomization of primary wind and powder can be realized, mix, make sufficient combustion.
In addition, can the ratio of reasonable disposition First air and pulverized-coal concentration, realize lighting in time and tiny-oil ignition of fuel torch, effectively can reduce the pressure head of primary air fan, flow and power, save energy consumption.
Further, the strong rotational flow atomization device of wind powder 111 is the adjustable atomising device of swirl strength.Like this, can the ratio of based on fuel characteristic changing backflow flue gas and recirculation zone in real time, ensure lighting in time and surely firing of fuel, enhance the broadness that fuel is suitable for.That is, for different coals, different swirl strengths can be adopted, when burning inferior coal, then adopt stronger swirl strength, to form larger smoke backflow amount, to ensure catching fire and burning of coal dust; And when using inflammable coal, then can weaken swirl strength, to form little smoke backflow amount, namely can ensure that coal dust stably catches fire and burning.
For protection burner, automatic ignition device is the automatic ignition device of extension type.Like this, when after firing coal-dust, particularly, the igniting of automatic ignition device is robbed and is retreated backward, to prevent from being burned, increases the service life.
Delay and coal dust mixing participation burning relative to inner second air for realizing outer second air, the outlet side of outer second air pipeline 13 is formed as the outer enlarging 133 of taper, and this outer enlarging 133 is in the outlet side axially protruding from inner second air pipeline 12 of burner.Like this, can realize when overfire air device 38 sends into Secondary Air from secondary air inlet simultaneously, inside and outside secondary wind energy participates in burning with the different moment.
For ease of installing, the straight length 113 that primary wind and powder pipeline 11 comprises elbow section 112 and removably connects with this elbow section 112, primary wind and powder feeding system 37 enters from the import of this elbow section 112.
Burner also comprises combustion control system 30 and the host computer PLC that is electrically connected with this combustion control system 30 or DCS system, and this combustion control system 30 comprises automatic ignition system 31, runs stored program controlled 32, Image Fire check system 33, infrared fire check system 34, oxygen content fume component analysis system 35, outer second air air pressure air flow checkout gear 36.Therefore; the function such as can realize system start and stop stove self-inspection purging, program automatic ignition by host computer PLC or DCS system, program auto extinguishing is protected automatically, load PID adjusts automatically; and run stored program controlled and achieve burning torch and automatically pass in and out, automatically carry out coal-air ratio adjustment, the monitoring of burner malfunctions and recovery; run interlock protection with boiler plant, the demand of high-efficiency pulverized coal Automatic Control of Boiler can be met.
In addition, flue gas recycled 39 can be equipped with, such as, afterbody cleaning flue gases 40 is sent in overfire air device 38, and then enters inside and outside secondary air system, reduce primary zone oxygen concentration first, second primary zone ignition temperature is lowered, the auxiliary generation reducing heating power type and fuel type NOx.
In addition, can also arrange three burnout degree on boiler body, the hydrocarbon that activation primary zone generates makes it further Thorough combustion, ensures more than burn-off rate >=99.6% of fuel, realizes energy-conservation target.
Like this, by arranging one or two tertiary airs of rational proportion, ensure that the lighting in time of fuel, flame mechanism is controlled, rapid after-flame, achieves the burning of clean and effective.Improve efficiency of combustion, effectively reduce ash content carbon 2 ~ 3 percentage points.
Below preferred embodiment of the present utility model is described by reference to the accompanying drawings in detail; but; the utility model is not limited to the detail in above-mentioned embodiment; within the scope of technical conceive of the present utility model; can carry out multiple simple variant to the technical solution of the utility model, these simple variant all belong to protection domain of the present utility model.
It should be noted that in addition, each concrete technical characteristic described in above-mentioned detailed description of the invention, in reconcilable situation, can be combined by any suitable mode, in order to avoid unnecessary repetition, the utility model illustrates no longer separately to various possible combination.
In addition, also can be combined between various different embodiment of the present utility model, as long as it is without prejudice to thought of the present utility model, it should be considered as content disclosed in the utility model equally.
Claims (13)
1. a Bi-register swirl burner, it is characterized in that, comprise primary wind and powder pipeline (11), be sheathed on the inner second air pipeline (12) in this primary wind and powder pipeline (11) outside, be sheathed on the outer second air pipeline (13) of this inner second air pipeline (12), the automatic ignition device for firing coal-dust is provided with in described primary wind and powder pipeline (11), the adjusting device (123) of the air quantity ratio for regulating described inner second air and outer second air is provided with between described inner second air pipeline (12) and outer second air pipeline (13).
2. Bi-register swirl burner according to claim 1, it is characterized in that, be provided with inward eddy blade (121) in described inner second air pipeline (12), this inward eddy blade (121) is set on described primary wind and powder pipeline (11).
3. Bi-register swirl burner according to claim 2, is characterized in that, described Bi-register swirl burner also comprises first adjusting device (122) of the swirl strength regulating described inner second air.
4. Bi-register swirl burner according to claim 3, it is characterized in that, described inward eddy blade (121) extends from front to back gradually with reducing, described inner second air pipeline (12) is provided with the first nut, described first adjusting device (122) is the first screw rod, this first screw flight is tightened on described first nut, and one end of this first screw rod is fixed to the rear end of described inward eddy blade (121), the other end extends to outside through described outer second air pipeline (13).
5. Bi-register swirl burner according to any one of claim 1 to 4, it is characterized in that, be provided with contour stealth blade (131) in described outer second air pipeline (13), this contour stealth blade (131) is set on described inner second air powder pipeline (12).
6. Bi-register swirl burner according to claim 5, is characterized in that, described Bi-register swirl burner also comprises second adjusting device (132) of the swirl strength regulating described outer second air.
7. Bi-register swirl burner according to claim 6, it is characterized in that, described contour stealth blade (131) extends from front to back gradually with reducing, described inner second air pipeline (12) is provided with the second nut, described second adjusting device (132) is the second screw rod, this second screw flight is tightened on described second nut, and one end of this second screw rod is fixed to the rear end of described contour stealth blade (131), the other end extends to outside through described inner second air pipeline (12) and described outer second air pipeline (13).
8. Bi-register swirl burner according to claim 1, is characterized in that, is provided with the strong rotational flow atomization device of wind powder (111) in described primary wind and powder pipeline (11).
9. Bi-register swirl burner according to claim 8, is characterized in that, the strong rotational flow atomization device of described wind powder (111) is the adjustable atomising device of swirl strength.
10. Bi-register swirl burner according to claim 1, is characterized in that, described automatic ignition device is the automatic ignition device of extension type.
11. Bi-register swirl burners according to claim 1, it is characterized in that, the outlet side of described outer second air pipeline (13) is formed as the outer enlarging (133) of taper, and this outer enlarging (133) is in the outlet side axially protruding from described inner second air pipeline (12) of described burner.
12. Bi-register swirl burners according to claim 1, it is characterized in that, the straight length (113) that described primary wind and powder pipeline (11) comprises elbow section (112) and removably connects with this elbow section (112), primary wind and powder feeding system (37) enters from the import of this elbow section (112).
13. Bi-register swirl burners according to claim 1, it is characterized in that, described burner also comprises combustion control system (30) and the host computer PLC that is electrically connected with this combustion control system (30) or DCS system, and this combustion control system (30) comprises described automatic ignition system (31), runs stored program controlled (32), Image Fire check system (33), infrared fire check system (34), oxygen content fume component analysis system (35), outer second air air pressure air flow checkout gear (36).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520908744.3U CN205119048U (en) | 2015-11-11 | 2015-11-11 | Bitonic wind vortex burner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520908744.3U CN205119048U (en) | 2015-11-11 | 2015-11-11 | Bitonic wind vortex burner |
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| Publication Number | Publication Date |
|---|---|
| CN205119048U true CN205119048U (en) | 2016-03-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520908744.3U Expired - Fee Related CN205119048U (en) | 2015-11-11 | 2015-11-11 | Bitonic wind vortex burner |
Country Status (1)
| Country | Link |
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| CN (1) | CN205119048U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106196041A (en) * | 2016-07-05 | 2016-12-07 | 哈尔滨锅炉厂有限责任公司 | Multiple stage separation annular return formula axial rotational flow burner |
| CN112443833A (en) * | 2019-09-05 | 2021-03-05 | 中国科学院工程热物理研究所 | Pulverized coal fired boiler with bottom burner and control method thereof |
| CN114562723A (en) * | 2022-03-04 | 2022-05-31 | 四川科达节能技术有限公司 | Steel rolling heating furnace blowback nozzle |
-
2015
- 2015-11-11 CN CN201520908744.3U patent/CN205119048U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106196041A (en) * | 2016-07-05 | 2016-12-07 | 哈尔滨锅炉厂有限责任公司 | Multiple stage separation annular return formula axial rotational flow burner |
| CN112443833A (en) * | 2019-09-05 | 2021-03-05 | 中国科学院工程热物理研究所 | Pulverized coal fired boiler with bottom burner and control method thereof |
| CN112443833B (en) * | 2019-09-05 | 2023-01-06 | 中国科学院工程热物理研究所 | Pulverized coal fired boiler with bottom-mounted burner and control method thereof |
| CN114562723A (en) * | 2022-03-04 | 2022-05-31 | 四川科达节能技术有限公司 | Steel rolling heating furnace blowback nozzle |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160330 Termination date: 20211111 |
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| CF01 | Termination of patent right due to non-payment of annual fee |