CN202494102U - Industrial burner for reducing NOx emission through gas self-circulation - Google Patents
Industrial burner for reducing NOx emission through gas self-circulation Download PDFInfo
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- CN202494102U CN202494102U CN2012201191962U CN201220119196U CN202494102U CN 202494102 U CN202494102 U CN 202494102U CN 2012201191962 U CN2012201191962 U CN 2012201191962U CN 201220119196 U CN201220119196 U CN 201220119196U CN 202494102 U CN202494102 U CN 202494102U
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- burner
- gas
- flue gas
- aditus laryngis
- throat
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Abstract
The utility model relates to an industrial burner for reducing NOx emission through gas self-circulation, and belongs to the technical field of a high-power industrial burner. The industrial burner is characterized in that the inner side face of the inner end of a refractory brick wall is fixedly connected with the outer side face of an outer throat; the space between the inner side face of the outer end of the refractory brick wall and the axis of a burner core is flared outwards at an angle beta; the inner end of a gas reflux guide ring is connected with the inner side face of the outer throat; and gas reflux passages are arranged between the outer throat and a throat and between the throat and the reflux guide ring. The industrial burner has the positive effects that the structure is simple, only simple reconstruction is required on the basis of the original burner, the gas is self-circulated through the burner, the temperature in the hearth and the oxygen concentration in gas-air mixture can be effectively reduced, and production of thermodynamic NOX and fuel type NOX is facilitated. During gas burning, the NOX concentration can be reduced by 35 percent, the NOX concentration can be reduced by 10-35 percent during oil burning, and the effect is obvious.
Description
Technical field
The present invention relates to high-power industrial technical field of burner, relate in particular to a kind of flue gas self-loopa and reduce NO
XThe industrial burner of discharging, gas fume after burning is mixed with fresh air at burner larynx place, all mixes burning with fuel again, reduces NO
XDischarging.
Background technology
Environmental protection and energy-saving and emission-reduction are eternal problems of industrial burner.Particularly current, to reducing NO
XThe requirement of discharging is strict more.Area such as Beijing, Shanghai is to gas burner NO
XNumerical value require 150mg/Nm from 2008
3, be reduced to present 100mg/Nm
3In China, the burner research and development of single-machine capacity more than 24MW also are in the imperfection stage, to NO
XReduction also lack effective method.
From mechanism, combustion gas and oil burner NO
XGeneration mainly contain two big types, one type is the heating power type, depends on temperature, i.e. temperature NO then more than 1536 degree
XThe a large amount of generation; Another kind of is fuel type, and promptly the N atom in the fuel exists with the compound state, under lower temperature, just can produce NO with combination with oxygen
XAt present, reduce NO
XThe means of discharging are mainly started with from above two aspects, and the one, reduce the flame peak temperature, relatively effective method is hierarchical segmented burning, half premixed combustion, bias combustion, flue gas recirculation, the 2nd, can carry out denitration to flue gas.
For flue gas recirculation, be divided into circulation and flue gas outer circulation in the flue gas, mainly be through dilution oxygen concentration, thereby reduce nitrogen (N
2) and the probability of nitrogen-containing group and combination with oxygen, and then reduce NO
XSo-called flue gas outer circulation promptly makes the gas fume after burning part mix mutually in the outside of burner with combustion-supporting fresh air, is forced then to send in the burner and goes, and this method is effective, but needs to increase extra attachment device and certain energy consumption; And the mechanism of vortex burner itself is promptly adopted in the interior circulation of flue gas; Make the flue gas of burner hearth afterbody directly get back to the flame kernel that burner produces automatically; This method need have higher requirement to cyclone, and swirl strength can not be too high or low excessively, otherwise tempering easily.
Summary of the invention
The objective of the invention is: based on the mechanism that circulates in the flue gas, improve the burner throat structural design, provide a kind of flue gas self-loopa to reduce NO
XFlue gas combines with combustion air to burner throat in the industrial burner of discharging, Automatic Extraction partial hearth, burns with fuel mix, thereby produces suitable, even, stable flame, produced simultaneously NO
XDischarge capacity is few.
For achieving the above object, the technical scheme of employing is: a kind of flue gas self-loopa reduces NO
XThe industrial burner of discharging; Comprise the coaxial setting of ecto-entad refractory brickwork, aditus laryngis, place the burner movement in the said aditus laryngis; It is characterized in that: the inner end medial surface of said refractory brickwork is fixedly connected with the lateral surface of outer aditus laryngis, between the outer end medial surface of said refractory brickwork and the axis of burner movement with β angle outer flare; The inner end of flue gas refluence lead ring is connected with the medial surface of outer aditus laryngis, is equipped with flue gas refluence passage between said outer aditus laryngis and the aditus laryngis and between aditus laryngis and the refluence lead ring.
Said β angle is: 45<β<90.
During work; Fuel contacts, mixes by former burner mode respectively with air; And, having 5%~15% in the flue gas of generation under the effect of jet absorption type aditus laryngis in the burner hearth internal combustion, the refractory brickwork enlarging refluxes outside aditus laryngis; It is inner to get into burner along flue gas refluence passage, and mixes mutually with combustion air.At this moment, because sneaking into of flue gas reduced the concentration and the ignition temperature of the oxygen of combustion process, prevent that localized hyperthermia from producing so suppressed NO
XGeneration.
Good effect of the present invention is: burner of the present invention is simple in structure; Only need on the basis of original burner, simply transform and get final product; Special jet absorption type principle through burner; The self-loopa flue gas can effectively reduce the temperature in the burner hearth, can reduce the oxygen concentration in the flue gas-air mixture simultaneously, helps reducing heating power high temperature modification NO
XGeneration, also reduced the reaction of intermediate product nitrogen-containing group and oxygen in addition, therefore also help reducing fuel type NO
XGeneration.When burning natural gas, NO
XConcentration can reduce by 35%, NO during oil firing
XConcentration can reduce by 10%~35%, reduces NO
XThe good results are evident.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the present invention is described further.
Fig. 1 is a structural representation of the present invention;
Fig. 2 is a flue gas refluence path partially structural representation (amplification) among Fig. 1.
Among the figure, the outer aditus laryngis of 1-; 2-flue gas refluence lead ring; The 3-refractory brickwork; 4-burner movement; The 5-aditus laryngis; 6-flue gas refluence passage.
The specific embodiment
Fig. 1 is a structural representation of the present invention, and Fig. 2 is a characteristic flue gas refluence path partially structural representation of the present invention.As shown in the figure, the flue gas self-loopa reduces NO
XThe industrial burner of discharging; Comprise the coaxial setting of ecto-entad refractory brickwork 3, aditus laryngis 5, place the burner movement 4 in the said aditus laryngis 5; It is characterized in that: the inner end medial surface of said refractory brickwork 3 is fixedly connected with the lateral surface of outer aditus laryngis 1, between the outer end medial surface of said refractory brickwork 3 and the axis of burner movement with β angle outer flare; The inner end of flue gas refluence lead ring 2 is connected with the medial surface of outer aditus laryngis 1, is equipped with flue gas refluence passage 6 between said outer aditus laryngis 1 and the aditus laryngis 5 and between aditus laryngis 5 and the flue gas refluence lead ring 2.
Said β angle is: 45<β<90.
When combustion air sprays toward burner hearth in burner throat 5; With make place between said outer aditus laryngis 1 and the aditus laryngis 5 and aditus laryngis 5 and flue gas refluence lead ring 2 between flue gas refluence passage 6 interior formation negative pressure; Under the self-priming effect of this negative pressure; A part is just turned back in the flue gas that the fuel of burner and combustion air produce after the burner hearth internal combustion, arrives burner throat 5 inside through flue gas refluence passage 6, mixes mutually with combustion air and fuel; Effectively reduce the temperature in the burner hearth and reduced the oxygen concentration in the flue gas-air mixture, help reducing heating power type NO
XGeneration and help reducing fuel type NO
XGeneration, therefore reduce NO
XThe good results are evident, when burning natural gas, and NO
XConcentration can reduce by 35%, NO during oil firing
XConcentration can reduce by 10%~35%.
Claims (2)
1. a flue gas self-loopa reduces NO
XThe industrial burner of discharging; Comprise the coaxial setting of ecto-entad refractory brickwork, aditus laryngis, place the burner movement in the said aditus laryngis; It is characterized in that: the inner end medial surface of said refractory brickwork is fixedly connected with the lateral surface of outer aditus laryngis, between the outer end medial surface of said refractory brickwork and the axis of burner movement with β angle outer flare; The inner end of flue gas refluence lead ring is connected with the medial surface of outer aditus laryngis, is equipped with flue gas refluence passage between said outer aditus laryngis and the aditus laryngis and between aditus laryngis and the refluence lead ring.
2. said a kind of flue gas self-loopa reduces NO according to claim 1
XThe industrial burner of discharging, it is characterized in that: said β angle is: 45<β<90.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2012201191962U CN202494102U (en) | 2012-03-27 | 2012-03-27 | Industrial burner for reducing NOx emission through gas self-circulation |
Applications Claiming Priority (1)
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CN2012201191962U CN202494102U (en) | 2012-03-27 | 2012-03-27 | Industrial burner for reducing NOx emission through gas self-circulation |
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CN202494102U true CN202494102U (en) | 2012-10-17 |
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CN2012201191962U Expired - Lifetime CN202494102U (en) | 2012-03-27 | 2012-03-27 | Industrial burner for reducing NOx emission through gas self-circulation |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102635853A (en) * | 2012-03-27 | 2012-08-15 | 上海诺特飞博燃烧设备有限公司 | Industrial combustor for reducing NOx emission by self-circulation of smoke |
CN105358910A (en) * | 2013-07-02 | 2016-02-24 | 托普索公司 | Mixing of recycle gas with fuel gas to a burner |
CN105485897A (en) * | 2016-01-29 | 2016-04-13 | 青岛全能节能环保锅炉有限公司 | Water-tube boiler achieving internal circulation of flue gas and low-nitrogen combustion control method |
-
2012
- 2012-03-27 CN CN2012201191962U patent/CN202494102U/en not_active Expired - Lifetime
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102635853A (en) * | 2012-03-27 | 2012-08-15 | 上海诺特飞博燃烧设备有限公司 | Industrial combustor for reducing NOx emission by self-circulation of smoke |
CN105358910A (en) * | 2013-07-02 | 2016-02-24 | 托普索公司 | Mixing of recycle gas with fuel gas to a burner |
CN105358910B (en) * | 2013-07-02 | 2018-06-15 | 托普索公司 | The method of burning fuel, burner and its application in catalytic reactor |
CN105485897A (en) * | 2016-01-29 | 2016-04-13 | 青岛全能节能环保锅炉有限公司 | Water-tube boiler achieving internal circulation of flue gas and low-nitrogen combustion control method |
CN105485897B (en) * | 2016-01-29 | 2018-08-28 | 青岛全能节能环保锅炉有限公司 | Circulating water pipe boiler and low nitrogen burning control method in flue gas |
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GR01 | Patent grant | ||
CX01 | Expiry of patent term | ||
CX01 | Expiry of patent term |
Granted publication date: 20121017 |