CN203549816U - Multidirectional jet-type swirl pulverized coal burner - Google Patents
Multidirectional jet-type swirl pulverized coal burner Download PDFInfo
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- CN203549816U CN203549816U CN201320523055.1U CN201320523055U CN203549816U CN 203549816 U CN203549816 U CN 203549816U CN 201320523055 U CN201320523055 U CN 201320523055U CN 203549816 U CN203549816 U CN 203549816U
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Abstract
The utility model discloses a multidirectional jet-type swirl pulverized coal burner which is mounted in an air box on the outer side of a coal-fired boiler and connected with an opening in a water-cooled wall of a hearth. The multidirectional jet-type swirl pulverized coal burner comprises a primary air pulverized coal nozzle perpendicular to the water-cooled wall of the hearth, an annular secondary air flow nozzle is formed between the periphery of the primary air pulverized coal nozzle and the opening in the water-cooled wall of the hearth, a wall-attached air flow guide cylinder is arranged in the secondary air flow nozzle, an annular wall-attached air jet nozzle is formed between the wall-attached air flow guide cylinder and the opening in the water-cooled wall of the hearth, and the circulation area of an outlet of the wall-attached air jet nozzle accounts for 3-18% of that of an outlet of the secondary air flow nozzle. The wall-attached air flow guide cylinder is added without largely modifying the structure of a conventional swirl pulverized coal burner, part of distributed secondary air forms flowing oxidation air membranes on a water-cooled wall surface, the water-cooled wall surface of the periphery of the burner is in oxidizing atmosphere, and high-temperature corrosion and coking of the water-cooled wall of the hearth near the burner are avoided.
Description
Technical field
The utility model relates to vortex burner technical field, refers to particularly a kind of multidirectional jetting type vortex burner.
Background technology
At present, thermal power generation large-sized boiler is due to the extensive use of low nitrogen burning technology, and wall coking and the high temperature corrosion phenomenon of furnace wall cooling are day by day serious, has become gradually the key factor that threatens boiler of power plant safe and stable operation.It is all the factor that causes the coking of furnace wall cooling wall and high temperature corrosion that near smoke components ature of coal variation, tube wall temperature and furnace wall cooling changes.In order to meet the boiler low nitrogen burning requirement of power plant's environmental protection, in boiler coal-ash burning, implement oxygen debt low nitrogen burning air distribution, more easily cause near coal dust anoxycausis water-cooling wall, form high temperature and reducing atmosphere, carry out serious high temperature corrosion hidden danger to water-cooled cornice.Especially in the boiler running process of arranging in opposed firing formula, due to outside Secondary Air jet eddy flow flow and burner and water-cooling wall between there is negative pressuren zone, drive high temperature thermal flue gas back stream around to supplement, cause burner near furnace wall cooling, the adherent burning of coal dust easily to occur around, under anaerobic condition, more easily cause furnace wall cooling that serious high temperature corrosion and coking situation easily occur, the generation of this type of situation brings great hidden danger to the safe and stable operation of boiler, simultaneously a large amount of maintenance cost of annual generation.Particularly contain in recent years a large amount of eastern coals of the alkali-metal standard of sodium potassium and utilized in a large number, during boiler combustion, more easily cause serious furnace water cooling wall high-temperature corrosion and coking.Therefore, need to be a kind of in the situation that not affecting boiler combustion efficiency, prevent the adherent burning of coal dust, avoid the solution of high temperature corrosion and the coking of furnace wall cooling.
Summary of the invention
The purpose of this utility model is exactly to avoid the adherent burning of coal dust to cause the defect of near the water-cooling wall wall large area high temperature corrosion of boiler-burner and coking, and a kind of multidirectional jetting type vortex burner is provided.
For achieving the above object, the multidirectional jetting type vortex burner that the utility model is designed, be arranged in the bellows in coal-burning boiler outside, be connected with the opening on furnace wall cooling, it comprises a wind coal nozzle of installing perpendicular to furnace wall cooling, the Secondary Air air current spray nozzle of looping between opening on a described wind coal nozzle periphery and furnace wall cooling, its special character is: in described Secondary Air air current spray nozzle, be provided with adherent wind guide shell, the adherent wind jet nozzle of looping between opening on described adherent wind guide shell and furnace wall cooling, the circulation area of described adherent wind jet nozzle outlet accounts for 3～18% of Secondary Air air current spray nozzle outlet circulation area.
As preferred version, the circulation area in described adherent wind jet nozzle exit accounts for 3～12% of Secondary Air air current spray nozzle circulation area, and the best is: 5～8%.Like this, in the situation that not affecting burning, by changing air-flow, distribute, make adherent wind jet near water-cooling wall hearth combustor, form oxidation wind film, be conducive to prevent the adherent burning of coal dust and avoid near the high temperature corrosion of burner to occur.
Further, the port of export of described adherent wind guide shell is provided with flange wind-guiding flange, and described flange wind-guiding flange and furnace wall cooling are arranged in parallel.Like this, can adjust adherent wind and enter the flow direction after burner hearth, strengthen near the high temperature heat exchange of furnace wall cooling.
Further, the position of described flange wind-guiding flange is in furnace wall cooling inner side, thereby makes adherent wind facies be parallel injection state for furnace wall cooling.
Further, the position of described flange wind-guiding flange is concordant with furnace wall cooling, thereby makes adherent wind facies for the angled spray regime of furnace wall cooling.
As preferred version, on the outer wall of described adherent wind guide shell, edge is circumferentially evenly equipped with 4～16 adherent wind deflectors.Like this, both can play tissue and guide effect to adherent wind jet, can also strengthen the intensity of adherent wind guide shell.
Further, described adherent wind deflector is arranged in parallel with respect to the outer wall bus of adherent wind guide shell.Like this, adherent wind is direct current form along adherent wind guide shell outer wall and sprays, and can fast be distributed in furnace water cooling wall surface.
Further, described adherent wind deflector is in tilted layout with respect to the outer wall bus of adherent wind guide shell.Like this, adherent wind, along the formula injection twist of adherent wind guide shell outer wall, can be strengthened adherent wind swirl strength, impels it to be evenly distributed on furnace water cooling wall surface.
As preferred version, a described wind coal nozzle periphery is provided with Secondary Air guide shell, and described adherent wind guide shell is arranged between the spout on Secondary Air guide shell and furnace wall cooling.Like this, by changing air-flow, distribute, can improve coal dust firing situation in stove, strengthen heat exchange in stove, avoid the adherent burning of coal dust.
As preferred version, the spout section of a described wind coal nozzle is two-sided battlement flow-guiding structure, it comprises the internal withdraw type flow deflector of interlaced arrangement along the circumferential direction and extends out formula flow deflector, described internal withdraw type flow deflector reduces gradually take spout section intracavity diameter D as the section radius of benchmark from root to end, the described formula flow deflector that extends out increases gradually take spout section intracavity diameter D as the section radius of benchmark from root to end, and adjacent internal withdraw type flow deflector and extending out between formula flow deflector by radial transition plate is connected.Like this, can impel coal dust fully to burn, avoid near anoxycausis furnace wall cooling, form high temperature and reducing atmosphere.
Further, the end arranged outside of described internal withdraw type flow deflector inside contracts the steady combustion of end catch, the described end arranged outside that extends out formula flow deflector extends out the steady combustion of end catch, described in inside contract end steady combustion catch and extend out the steady combustion of end catch and all perpendicular to spout section axial line, arrange.Like this, can prevent Secondary Air too early from internal withdraw type flow deflector and extend out formula flow deflector and enter in stove and mixes with coal dust, play steady fuel efficiency really.
Further, the described radial height h1 that inside contracts the steady combustion of end catch, described in extend out the radial height h2 of the steady combustion of end catch, described internal withdraw type flow deflector inwall and meet following mathematical relationship: h1=0.5～1.0H, h2=0.5～2.0H to extending out between the radial height H of formula flow deflector inwall.Like this, the parameter of can optimizing structure, guarantees steady fuel efficiency fruit.
Further, described internal withdraw type flow deflector, extend out formula flow deflector and radial transition plate is monoblock cast, forging and stamping or compression molding structure.Like this, can simplified processing process, improve nozzle-integrated intensity, increase the service life.
Further, described spout section intracavity diameter D, described internal withdraw type flow deflector or extend out the axial length L of formula flow deflector and described internal withdraw type flow deflector inwall meets and has following preferred mathematical relationship: H=0.05～0.25D, L=0.6～1.5D to extending out between the radial height H of formula flow deflector inwall.The best is: H=0.10～0.20D, L=0.9～1.3D.Like this, can optimize nozzle body each several part dimension scale, realize best steady fuel efficiency fruit.
Further, the quantity of described internal withdraw type flow deflector is 4～12, is preferably 6～8, described in to extend out the quantity of formula flow deflector corresponding one by one with internal withdraw type flow deflector.Like this, not only simple in structure, be convenient to processing, and be conducive to even water conservancy diversion.
The utility model has the advantage of: conventional vortex burner structure is not being carried out under the prerequisite of larger change, by increasing adherent wind guide shell, can be conveniently for design upgrading and the plant modification of existing vortex burner; The part Secondary Air of shunting out, in the situation that not affecting secondary air combustion aid, can form mobility oxidation wind film at water-cooling wall wall, assurance burner periphery water-cooling wall wall, in oxidizing atmosphere, has effectively been avoided the high temperature corrosion of water-cooling wall and washing away of breeze airflow.As preferred version, a wind coal nozzle spout section design is two-sided battlement flow-guiding structure, in the time of can making breeze airflow spray from nozzle interior and the strong mixed heat transfer of external heat flue gas, guaranteed the combustion stability that catches fire by force of coal dust, avoid near coal dust anoxycausis water-cooling wall to form high temperature and reducing atmosphere, thereby stopped high temperature corrosion and the coking hidden danger of furnace wall cooling.
Accompanying drawing explanation
Fig. 1 is the basic structure schematic diagram of traditional vortex burner.
Fig. 2 is a kind of main sectional structure schematic diagram of multidirectional jetting type vortex burner.
Fig. 3 is the main TV structure schematic diagram of adherent wind guide shell in Fig. 2.
Fig. 4 is left TV structure schematic diagram when adherent wind deflector is arranged in parallel in Fig. 3.
Fig. 5 is left TV structure schematic diagram when adherent wind deflector is in tilted layout in Fig. 3.
Fig. 6 is the first perspective view of a wind coal nozzle in Fig. 2.
Fig. 7 is the main TV structure schematic diagram of Fig. 6.
Fig. 8 is the second perspective view of a wind coal nozzle in Fig. 2.
Fig. 9 is the main TV structure schematic diagram of Fig. 8.
Figure 10 is the main sectional structure schematic diagram of another kind of multidirectional jetting type vortex burner.
Figure 11 is the main sectional structure schematic diagram of the third multidirectional jetting type vortex burner.
In figure: a wind coal nozzle 1(wherein: internal withdraw type flow deflector 1a, extend out formula flow deflector 1b, radial transition plate 1c, inside contract the steady combustion of end catch 1d, extend out the steady combustion of end catch 1e); Secondary Air guide shell 2; Adherent wind guide shell 3; Bracing or strutting arrangement 4; Flange wind-guiding flange 5; Furnace wall cooling 6; Bellows 7; Adherent wind deflector 8; Secondary Air air current spray nozzle Q; Adherent wind jet nozzle T; A wind breeze airflow A; Secondary Air air-flow B; Adherent wind jet C.
The specific embodiment
In order to explain better the utility model, below in conjunction with the drawings and specific embodiments, further illustrate main contents of the present utility model, but content of the present utility model is not only confined to following examples.
As shown in Figure 1, tradition vortex burner is arranged on the opening part of furnace wall cooling 6, its basic structure comprises that 1, wind coal nozzle 1 of a wind coal nozzle installs perpendicular to furnace wall cooling 6, forms annular Secondary Air air current spray nozzle Q between its periphery and furnace wall cooling 6 openings.
Embodiment 1:
As shown in Figure 2, the multidirectional jetting type vortex burner of one of the present utility model, be arranged in the bellows 7 in coal-burning boiler outside, be connected with the opening on furnace wall cooling 6, it comprises a wind coal nozzle 1 of installing perpendicular to furnace wall cooling 6, the Secondary Air air current spray nozzle Q of looping between opening on wind coal nozzle 1 periphery and furnace wall cooling 6, in Secondary Air air current spray nozzle Q, be provided with adherent wind guide shell 3, the adherent wind jet nozzle T of looping between opening on adherent wind guide shell 3 and furnace wall cooling 6, the circulation area of adherent wind jet nozzle T outlet accounts for 3～18% of Secondary Air air current spray nozzle Q outlet circulation area, during optimal design, the circulation area of adherent wind jet nozzle T outlet accounts for 3～12% of Secondary Air air current spray nozzle Q outlet circulation area, and optimal proportion is: 5～8%.
Adherent wind guide shell 3 is rigidly connected by bracing or strutting arrangement 4 and wind coal nozzle 1 outer wall, and bracing or strutting arrangement 4 can adopt round steel support, steel flat support, shape steel bracket or their sectional shelf-unit; The port of export of adherent wind guide shell 3 is provided with flange wind-guiding flange 5, and flange wind-guiding flange 5 is arranged in parallel in furnace wall cooling 6 inner sides with furnace wall cooling 6, thereby makes adherent wind facies be parallel injection state for furnace wall cooling 6.
As shown in Fig. 3～5, during optimal design, on the outer wall of adherent wind guide shell 3, along being circumferentially evenly equipped with 4～16 adherent wind deflectors 8, it can be with respect to the outer wall bus of adherent wind guide shell 3 be arranged in parallel (as Fig. 4); Also can be with respect to the outer wall bus of adherent wind guide shell 3 be in tilted layout (as Fig. 5); Adherent wind deflector 8, except playing the effect of organizing and leading adherent wind jet, also can be strengthened the intensity of flange wind-guiding flange 5.
As shown in Fig. 6～7, the wind coal nozzle 1 of one adopting for embodiment 1, its spout section is two-sided battlement flow-guiding structure, it comprises the internal withdraw type flow deflector 1a of interlaced arrangement along the circumferential direction and extends out formula flow deflector 1b, internal withdraw type flow deflector 1a reduces gradually take spout section intracavity diameter D as the section radius of benchmark from root to end, extending out formula flow deflector 1b increases gradually take spout section intracavity diameter D as the section radius of benchmark from root to end, adjacent internal withdraw type flow deflector 1a and extend out the radial transition plate 1c by triangular structure between formula flow deflector 1b and be connected as a single entity.The quantity of internal withdraw type flow deflector 1a is generally designed to 4～12, and the best is 6～8, in the present embodiment, is 8, and the quantity that extends out formula flow deflector 1b is corresponding one by one with internal withdraw type flow deflector 1a, staggered being evenly arranged.Specifically add man-hour, internal withdraw type flow deflector 1a, extend out formula flow deflector 1b and radial transition plate 1c selects heat resisting steel, monoblock cast, forging and stamping or compression molding structure.
Spout section intracavity diameter D, the internal withdraw type flow deflector 1a of an above-mentioned wind coal nozzle 1 or extend out the axial length L of formula flow deflector 1b and internal withdraw type flow deflector 1a inwall preferably meets following mathematical relationship: H=0.05～0.25D to extending out between the radial height H of formula flow deflector 1b inwall, L=0.6～1.5D, best parameter ratio is H=0.10～0.20D, L=0.9～1.3D.H=0.10D in the present embodiment, L=0.95D.
As shown in Fig. 8～9, the wind coal nozzle 1 of another kind adopting for embodiment 1, a wind coal nozzle 1 shown in its general structure and Fig. 6～7 is basic identical, just outside, the end of internal withdraw type flow deflector 1a is welded with and inside contracts the steady combustion of end catch 1d, the outside, end that extends out formula flow deflector 1b is welded with and extends out the steady combustion of end catch 1e, inside contracts the steady combustion of end catch 1d and extend out the steady combustion of end catch 1e all perpendicular to the spout section axial line of a wind coal nozzle 1, to arrange.During optimal design, the above-mentioned radial height h1 of the steady combustion of end catch 1d, the radial height h2 that extends out the steady combustion of end catch 1e, the internal withdraw type flow deflector 1a inwall of inside contracting meets following mathematical relationship: h1=0.5～1.0H, h2=0.5～2.0H to extending out between the radial height H of formula flow deflector 1b inwall.In the present embodiment, h1=0.8H, h2=0.9H.This inside contracts the steady combustion of end catch 1d and extends out the steady combustion of end catch 1e and can effectively stop Secondary Air air-flow B to enter into prematurely wind breeze airflow A one time, thereby avoids the coal powder density dilution at coal powder ignition initial stage, further strengthens the combustion stability that catches fire of coal dust.
During the utility model work, coal dust and a wind breeze airflow A of a wind composition are sprayed in stove by a wind coal nozzle 1; The wind entering in bellows 7 is divided into two strands: one is blown in stove as Secondary Air air-flow B, mixes with a wind breeze airflow A, and coal dust is fully burnt, and plays combustion-supporting effect.Another strand enters in stove from adherent wind jet nozzle T as adherent wind jet C, along furnace wall cooling 6, flow, at furnace wall cooling 6 walls, form oxidisability wind film, avoid imperfect combustion high temperature coal dust airflow scouring wall, thereby efficiently solve the phenomenon of near furnace wall cooling 6 high temperature corrosions of boiler-burner and coking.
Embodiment 2:
As shown in figure 10, the multidirectional jetting type vortex burner of another kind of the present utility model, its general structure is substantially the same manner as Example 1, just flange wind-guiding flange 5 is arranged on the position concordant with furnace wall cooling 6, can make so adherent wind facies spurt in stove for furnace wall cooling 6 is angled.
Embodiment 3:
As shown in figure 11, the third multidirectional jetting type vortex burner of the present utility model, its general structure is substantially the same manner as Example 1, just wind coal nozzle 1 periphery is provided with Secondary Air guide shell 2, adherent wind guide shell 3 is arranged between the spout on Secondary Air guide shell 2 and furnace wall cooling 6, and it is rigidly connected by bracing or strutting arrangement 4 and Secondary Air guide shell 2 outer walls.
During its work, coal dust and a wind breeze airflow A of a wind composition are sprayed in stove by a wind coal nozzle 1; The wind entering in bellows 7 is divided into two strands: one is as Secondary Air air-flow B, and this Secondary Air air-flow B divides two-way to be blown in stove inside and outside the barrel of Secondary Air guide shell 2, mixes with a wind breeze airflow A, and coal dust is fully burnt, and plays combustion-supporting effect.Another strand is as adherent wind jet C, from adherent wind jet nozzle T, enter in stove, along furnace wall cooling 6, flow, at furnace wall cooling 6 walls, form oxidisability wind film, avoid imperfect combustion high temperature coal dust airflow scouring wall, thereby efficiently solve the phenomenon of near furnace wall cooling 6 high temperature corrosions of boiler-burner and coking.
The utility model is through on-the-spot boiler renovation test, operation result shows: in two 660MW unit pulverized coal firing boilers, adopt opposed firing mode to arrange multidirectional jetting type vortex burner of the present utility model, it can either be solved over well in the water screen tube generation high temperature corrosion of run duration burner near zone and the problem such as be subject to that breeze airflow washes away, effectively ensured the safety of water screen tube, can solve over again poor the and problems such as the boiler extinguishment that causes of combustion stability of burning during underrun simultaneously, improve the efficiency of combustion of boiler, and be suitable for using meager coal, anthracite, ub-bituminous coal, one or more mixed coals in bituminous coal.
Claims (18)
1. a multidirectional jetting type vortex burner, be arranged in the bellows (7) in coal-burning boiler outside, be connected with the opening on furnace wall cooling (6), it comprises a wind coal nozzle (1) of installing perpendicular to furnace wall cooling (6), the Secondary Air air current spray nozzle (Q) of looping between opening on described wind coal nozzle (1) periphery and furnace wall cooling (6), it is characterized in that: in described Secondary Air air current spray nozzle (Q), be provided with adherent wind guide shell (3), the adherent wind jet nozzle (T) of looping between opening on described adherent wind guide shell (3) and furnace wall cooling (6), the circulation area of described adherent wind jet nozzle (T) outlet accounts for 3～18% of Secondary Air air current spray nozzle (Q) outlet circulation area.
2. multidirectional jetting type vortex burner according to claim 1, is characterized in that: the circulation area in described adherent wind jet nozzle (T) exit accounts for 3～12% of Secondary Air air current spray nozzle (Q) circulation area.
3. multidirectional jetting type vortex burner according to claim 1, is characterized in that: the circulation area in described adherent wind jet nozzle (T) exit accounts for 5～8% of Secondary Air air current spray nozzle (Q) circulation area.
4. multidirectional jetting type vortex burner according to claim 1, is characterized in that: the port of export of described adherent wind guide shell (3) is provided with flange wind-guiding flange (5), and described flange wind-guiding flange (5) is arranged in parallel with furnace wall cooling (6).
5. multidirectional jetting type vortex burner according to claim 4, is characterized in that: the position of described flange wind-guiding flange (5) is in furnace wall cooling (6) inner side, thereby makes adherent wind facies be parallel injection state for furnace wall cooling (6).
6. multidirectional jetting type vortex burner according to claim 4, is characterized in that: the position of described flange wind-guiding flange (5) is concordant with furnace wall cooling (6), thereby makes adherent wind facies be angle spray regime for furnace wall cooling (6).
7. multidirectional jetting type vortex burner according to claim 1, is characterized in that: on the outer wall of described adherent wind guide shell (3), edge is circumferentially evenly equipped with 4～16 adherent wind deflectors (8).
8. multidirectional jetting type vortex burner according to claim 7, is characterized in that: described adherent wind deflector (8) is arranged in parallel with respect to the outer wall bus of adherent wind guide shell (3).
9. multidirectional jetting type vortex burner according to claim 7, is characterized in that: described adherent wind deflector (8) is in tilted layout with respect to the outer wall bus of adherent wind guide shell (3).
10. multidirectional jetting type vortex burner according to claim 1, it is characterized in that: a described wind coal nozzle (1) periphery is provided with Secondary Air guide shell (2), described adherent wind guide shell (3) is arranged between the spout on Secondary Air guide shell (2) and furnace wall cooling (6).
11. according to the multidirectional jetting type vortex burner described in any one in claim 1～10, it is characterized in that: the spout section of a described wind coal nozzle (1) is two-sided battlement flow-guiding structure, it comprises the internal withdraw type flow deflector (1a) of interlaced arrangement along the circumferential direction and extends out formula flow deflector (1b), described internal withdraw type flow deflector (1a) reduces gradually take spout section intracavity diameter D as the section radius of benchmark from root to end, the described formula flow deflector (1b) that extends out increases gradually take spout section intracavity diameter D as the section radius of benchmark from root to end, adjacent internal withdraw type flow deflector (1a) and extending out between formula flow deflector (1b) by radial transition plate (1c) is connected.
12. multidirectional jetting type vortex burners according to claim 11, it is characterized in that: the end arranged outside of described internal withdraw type flow deflector (1a) inside contracts end steady combustion catch (1d), the described end arranged outside that extends out formula flow deflector (1b) extends out end steady combustion catch (1e), described in inside contract end steady combustion catch (1d) and extend out end and surely fire catch (1e) and all perpendicular to spout section axial line, arrange.
13. multidirectional jetting type vortex burners according to claim 12, it is characterized in that: described in inside contract end steady combustion catch (1d) radial height h1, described in extend out end steady combustion catch (1e) radial height h2, described internal withdraw type flow deflector (1a) inwall to extending out between the radial height H of formula flow deflector (1b) inwall, meet following mathematical relationship: h1=0.5～1.0H, h2=0.5～2.0H.
14. multidirectional jetting type vortex burners according to claim 11, is characterized in that: described internal withdraw type flow deflector (1a), extend out formula flow deflector (1b) and radial transition plate (1c) for monoblock cast, forging and stamping or compression molding structure.
15. multidirectional jetting type vortex burners according to claim 11, it is characterized in that: described spout section intracavity diameter D, described internal withdraw type flow deflector (1a) or extend out the axial length L of formula flow deflector (1b) and described internal withdraw type flow deflector (1a) inwall meets following mathematical relationship: H=0.05～0.25D, L=0.6～1.5D to extending out between the radial height H of formula flow deflector (1b) inwall.
16. multidirectional jetting type vortex burners according to claim 15, it is characterized in that: described spout section intracavity diameter D, described internal withdraw type flow deflector (1a) or extend out the axial length L of formula flow deflector (1b) and described internal withdraw type flow deflector (1a) inwall meets following mathematical relationship: H=0.10～0.20D, L=0.9～1.3D to extending out between the radial height H of formula flow deflector (1b) inwall.
17. multidirectional jetting type vortex burners according to claim 11, is characterized in that: the quantity of described internal withdraw type flow deflector (1a) is 4～12, described in to extend out the quantity of formula flow deflector (1b) corresponding one by one with internal withdraw type flow deflector (1a).
18. multidirectional jetting type vortex burners according to claim 17, is characterized in that: the quantity of described internal withdraw type flow deflector (1a) is 6～8, described in to extend out the quantity of formula flow deflector (1b) corresponding one by one with internal withdraw type flow deflector (1a).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320523055.1U CN203549816U (en) | 2013-08-26 | 2013-08-26 | Multidirectional jet-type swirl pulverized coal burner |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320523055.1U CN203549816U (en) | 2013-08-26 | 2013-08-26 | Multidirectional jet-type swirl pulverized coal burner |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103411215A (en) * | 2013-08-26 | 2013-11-27 | 中节环立为（武汉）能源技术有限公司 | Multi-directional jet-type cyclone pulverized coal burner |
-
2013
- 2013-08-26 CN CN201320523055.1U patent/CN203549816U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103411215A (en) * | 2013-08-26 | 2013-11-27 | 中节环立为（武汉）能源技术有限公司 | Multi-directional jet-type cyclone pulverized coal burner |
| CN103411215B (en) * | 2013-08-26 | 2016-01-27 | 中节环立为（武汉）能源技术有限公司 | Multidirectional jetting type vortex burner |
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