CN215723204U - Diffusion type low NOx self-preheating radiant tube burner with flue gas backflow - Google Patents
Diffusion type low NOx self-preheating radiant tube burner with flue gas backflow Download PDFInfo
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- CN215723204U CN215723204U CN202121695071.XU CN202121695071U CN215723204U CN 215723204 U CN215723204 U CN 215723204U CN 202121695071 U CN202121695071 U CN 202121695071U CN 215723204 U CN215723204 U CN 215723204U
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Abstract
The utility model relates to a diffusion type low NOx self-preheating radiant tube burner with flue gas backflow, and belongs to the technical field of industrial burners. The utility model comprises a flue gas shell, an air shell, a gas spray gun, a heat exchanger, a diffusion mixed flow tube, a flow guide cylinder, a flame stabilizing mixed core, a flame guide cylinder and a radiation tube, wherein the air shell and the radiation tube are respectively arranged at two sides of the flue gas shell, the gas spray gun is arranged on the air shell, the flow guide cylinder and the flame guide cylinder are both arranged in the radiation tube, the heat exchanger and the flame stabilizing mixed core are both arranged in the flow guide cylinder, the diffusion mixed flow tube is arranged in the heat exchanger, the heat exchanger and the diffusion mixed flow tube are both connected with the flame stabilizing mixed core, and the flame stabilizing mixed core is connected with the flame guide cylinder. Still include ignition, ignition installs on flue gas casing and air casing, and ignition and the cooperation of flame stabilizing mixing core.
Description
Technical Field
The utility model relates to a diffusion type low NOx self-preheating radiant tube burner with flue gas backflow, and belongs to the technical field of industrial burners.
Background
At present, most of self-preheating radiant tube burners have columnar flame, combustion products circulate in a smoke guide tube in a radiant tube and then enter a smoke channel of a heat exchanger through a channel between the radiant tube and the smoke guide tube, so that the defects of low surface load of the radiant tube, large section temperature difference, high smoke exhaust temperature, low radiant tube efficiency and the like exist, meanwhile, the grading effect of the burners is poor, the smoke backflow amount is difficult to control, the flame is short, the NOx emission is high, the service life is short, and the popularization and the application of the burners on high-performance industrial furnaces are influenced.
In view of this, patent document No. 201120266226.8 discloses a self-preheating radiant tube gas burner which is short in service life and inconvenient to popularize and apply.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the defects in the prior art and provide the diffusion type low-NOx self-preheating radiant tube burner with the flue gas backflow function, which is reasonable in structural design.
The technical scheme adopted by the utility model for solving the problems is as follows: this take low NOx of flue gas backward flow diffusion formula self to preheat radiant tube nozzle, its structural feature lies in: including flue gas casing, air casing, gas spray gun, heat exchanger, diffusion mixed flow tube, draft tube, steady flame mixing core, leading flame tube and radiant tube, the both sides at flue gas casing are installed respectively to air casing and radiant tube, the gas spray gun is installed on air casing, draft tube and leading flame tube are all installed in the radiant tube, heat exchanger and steady flame mixing core are all installed in the draft tube, the diffusion mixed flow tube is installed in the heat exchanger, heat exchanger and diffusion mixed flow tube all are connected with steady flame mixing core, steady flame mixing core is connected with leading flame tube.
Further, still include ignition, ignition installs on flue gas casing and air casing, and ignition and flame holding mix the core cooperation.
Furthermore, one end of the heat exchanger is installed on the flue gas shell, one end of the diffusion mixed flow pipe is matched with the gas spray gun, and the other end of the heat exchanger and the other end of the diffusion mixed flow pipe are both connected with the flame stabilizing mixed core.
Further, a flue gas inner cavity and a flow guide outer cavity are arranged in the flue gas shell, and a flue gas inner cavity inlet end and a flue gas outer cavity outlet end are respectively arranged on the flue gas inner cavity.
Furthermore, a diffusion mixed flow cavity is arranged in the diffusion mixed flow pipe and communicated with the flue gas inner cavity.
Furthermore, the diffusion flow mixing cavity is respectively provided with a contraction section, a throat section and a diffusion section from the inlet end to the outlet end.
Further, an air cavity and an air nozzle are arranged in the air shell, the air cavity is communicated with the flow guide outer cavity, and a gas spray gun outlet of the gas spray gun is arranged at the air nozzle.
Further, heat exchange fins are arranged on the heat exchanger, a heat exchanger air channel is arranged between the heat exchanger and the guide cylinder, a heat exchanger flue gas channel is arranged between the heat exchanger and the diffusion mixed flow pipe, the heat exchanger air channel is communicated with the guide outer cavity, and the heat exchanger flue gas channel is communicated with the flue gas inner cavity.
Further, the flame stabilizing mixing core comprises a hemispherical gas collecting cavity, a cylindrical nozzle, a flue gas spacer bush and a wind distribution ring, the flue gas spacer bush is fixed with the wind distribution ring, a mixed combustion chamber is arranged between the flue gas spacer bush and the guide cylinder, the heat exchanger is connected with the wind distribution ring, the diffusion mixed flow cavity is communicated with the hemispherical gas collecting cavity, the hemispherical gas collecting cavity is communicated with the cylindrical nozzle, and the cylindrical nozzle is communicated with the mixed combustion chamber.
Furthermore, the number of the columnar nozzles is m, m is more than or equal to 2 and less than or equal to 6, the included angle between the columnar nozzles and the central line of the smoke spacer sleeve is theta, and theta is more than or equal to 20 degrees and less than or equal to 60 degrees.
Furthermore, an air distribution hole and an ignition device mounting hole are formed in the air distribution ring, two ends of the air distribution hole are respectively communicated with the air channel of the heat exchanger and the mixed combustion chamber, and the ignition device penetrates through the ignition device mounting hole.
Further, a flame guide barrel inner cavity is arranged in the flame guide barrel, a flame guide barrel outer cavity is arranged between the flame guide barrel and the radiant tube, the flame guide barrel outer cavity is communicated with the mixed combustion chamber, and the flame guide barrel inner cavity is communicated with a heat exchanger flue gas channel.
Compared with the prior art, the utility model has the following advantages: the diffusion type low NOx self-preheating radiant tube burner with the flue gas backflow function is mainly used for industrial furnaces and kilns in the industries of steel, nonferrous metal, machinery, aviation, heavy machinery, heat treatment and the like; the diffusion combustion is realized by the diffusion type low NOx self-preheating radiant tube burner with the flue gas backflow, the annular flame is long, no local hot spot exists, the temperature distribution is uniform, the backflow amount is easy to control, the combustion product NOx is low, the service life is long, and the diffusion type low NOx self-preheating radiant tube burner can be popularized and applied to high-performance industrial furnaces.
Drawings
FIG. 1 is a schematic cross-sectional structure diagram of a diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to an embodiment of the utility model.
FIG. 2 is a schematic view of a partial structure of a diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to an embodiment of the utility model.
FIG. 3 is a schematic cross-sectional view of a flame-holding mixing core according to an embodiment of the utility model.
FIG. 4 is a side view of a flame holding mixing core of an embodiment of the utility model.
In the figure: a flue gas shell 1, an air shell 2, a gas spray gun 3, a heat exchanger 4, a diffusion mixed flow pipe 5, a guide shell 6, a flame stabilizing mixed core 7, a guide shell 8, a radiant tube 9, an ignition device 10,
A flue gas inner cavity 11, a flow guide outer cavity 12, a flue gas inner cavity inlet end 13, a flue gas outer cavity outlet end 14,
An air cavity 21, an air nozzle 22,
An outlet 31 of the gas spray gun,
A heat exchanger air channel 41, a heat exchanger flue gas channel 42, heat exchange fins 43,
A diffusion flow mixing cavity 51,
A hemispherical air collecting cavity 71, a columnar nozzle 72, a smoke spacer 73, an air distribution ring 74, a mixed combustion chamber 75, an air distribution hole 76, an ignition device mounting hole 77,
A flame guide outer cavity 81 and a flame guide inner cavity 82.
Detailed Description
The present invention will be described in further detail below by way of examples with reference to the accompanying drawings, which are illustrative of the present invention and are not to be construed as limiting the present invention.
Examples are given.
Referring to fig. 1 to 4, it should be understood that the structures, ratios, sizes, and the like shown in the drawings attached to the present specification are only used for matching the disclosure of the present specification, so as to be understood and read by those skilled in the art, and are not used to limit the conditions that the present invention can be implemented, so that the present invention has no technical essence, and any modifications of the structures, changes of the ratio relationships, or adjustments of the sizes, should still fall within the scope of the present invention without affecting the functions and the achievable objectives of the present invention. In the present specification, the terms "upper", "lower", "left", "right", "middle" and "one" are used for clarity of description, and are not used to limit the scope of the present invention, and the relative relationship between the terms and the relative positions may be changed or adjusted without substantial technical changes.
The diffusion type low NOx self-preheating radiant tube burner with the flue gas backflow in the embodiment comprises a flue gas shell 1, an air shell 2, a gas spray gun 3, a heat exchanger 4, a diffusion mixed flow tube 5, a guide cylinder 6, a flame stabilizing mixed core 7, a flame guide cylinder 8, a radiant tube 9 and an ignition device 10.
Air casing 2 and radiant tube 9 in this embodiment install respectively in the both sides of flue gas casing 1, gas spray gun 3 is installed on air casing 2, draft tube 6 and flame guide tube 8 are all installed in radiant tube 9, heat exchanger 4 and the mixed core 7 of steady flame are all installed in draft tube 6, diffusion mixed flow tube 5 is installed in heat exchanger 4, heat exchanger 4 and diffusion mixed flow tube 5 all are connected with the mixed core 7 of steady flame, under the normal condition, the one end of heat exchanger 4 is installed on flue gas casing 1, the one end and the gas spray gun 3 cooperation of diffusion mixed flow tube 5, the other end of heat exchanger 4 and the other end of diffusion mixed flow tube 5 all are connected with the mixed core 7 of steady flame, the mixed core 7 of steady flame is connected with flame guide tube 8, ignition 10 is installed on flue gas casing 1 and air casing 2, and ignition 10 and the mixed core 7 cooperation of steady flame.
A flue gas inner cavity 11 and a flow guide outer cavity 12 are arranged in the flue gas shell 1 in the embodiment, a flue gas inner cavity inlet end 13 and a flue gas outer cavity outlet end 14 are respectively arranged on the flue gas inner cavity 11, one end of the heat exchanger 4 is connected with the flue gas inner cavity inlet end 13, one end of the diffusion mixed flow pipe 5 is located in the flue gas inner cavity 11, a diffusion mixed flow cavity 51 is arranged in the diffusion mixed flow pipe 5, and the diffusion mixed flow cavity 51 is communicated with the flue gas inner cavity 11. The diffusion flow mixing cavity 51 is respectively provided with a contraction section, a throat section and a diffusion section from the inlet end to the outlet end.
An air cavity 21 and an air nozzle 22 are arranged in the air shell 2 in the embodiment, the air cavity 21 is communicated with the flow guide outer cavity 12, a gas spray gun outlet 31 of the gas spray gun 3 is arranged at the air nozzle 22, heat exchange fins 43 are arranged on the heat exchanger 4, a heat exchanger air channel 41 is arranged between the heat exchanger 4 and the flow guide cylinder 6, a heat exchanger flue gas channel 42 is arranged between the heat exchanger 4 and the diffusion mixed flow pipe 5, the heat exchanger air channel 41 is communicated with the flow guide outer cavity 12, and the heat exchanger flue gas channel 42 is communicated with the flue gas inner cavity 11.
The flame stabilizing mixing core 7 in the embodiment comprises a hemispherical gas collecting cavity 71, a columnar nozzle 72, a flue gas spacer 73 and an air distribution ring 74, wherein the flue gas spacer 73 is fixed with the air distribution ring 74, a mixed combustion chamber 75 is arranged between the flue gas spacer 73 and the guide cylinder 6, the heat exchanger 4 is connected with the air distribution ring 74, the diffusion mixed flow cavity 51 is communicated with the hemispherical gas collecting cavity 71, the hemispherical gas collecting cavity 71 is communicated with the columnar nozzle 72, and the columnar nozzle 72 is communicated with the mixed combustion chamber 75; the number of the columnar nozzles 72 is m, m is more than or equal to 2 and less than or equal to 6, the included angle between the columnar nozzles 72 and the central line of the flue gas spacer bush 73 is theta, and theta is more than or equal to 20 degrees and less than or equal to 60 degrees.
The air distribution ring 74 in this embodiment is provided with an air distribution hole 76 and an ignition device mounting hole 77, both ends of the air distribution hole 76 are respectively communicated with the heat exchanger air passage 41 and the mixed combustion chamber 75, and the ignition device 10 penetrates through the ignition device mounting hole 77.
In the embodiment, a flame guide tube inner cavity 82 is arranged in the flame guide tube 8, a flame guide tube outer cavity 81 is arranged between the flame guide tube 8 and the radiant tube 9, the flame guide tube outer cavity 81 is communicated with the mixed combustion chamber 75, and the flame guide tube inner cavity 82 is communicated with the heat exchanger flue gas channel 42.
The working method of the diffusion type low NOx self-preheating radiant tube burner with flue gas backflow in the embodiment comprises the following steps:
the gas is sprayed out from the gas spray gun outlet 31 through the gas spray gun 3 and mixed with a small part of combustion-supporting air sprayed out from the air nozzle 22, enters the diffusion mixed flow cavity 51, and then enters the mixed combustion chamber 75 through the semi-spherical gas collection cavity 71 and the columnar nozzle 72;
most combustion-supporting air enters the diversion outer cavity 12 of the flue gas shell 1 through the air cavity 21, enters the mixed combustion chamber 75 from the air distribution holes 76 on the air distribution ring 74 through the air channel 41 of the heat exchanger to be mixed with the mixed air, and is ignited by the ignition device 10 to realize diffusion combustion in the annular channel;
the combustion products enter the inner cavity 82 of the flame guide cylinder through the outer cavity 81 of the flame guide cylinder, enter the flue gas channel 42 of the heat exchanger through the flue gas spacer 73 and then pass through the inner cavity 11 of the flue gas, a small part of the combustion products are sucked into the diffusion mixed flow cavity 51 through the mixed gas sprayed from the outlet 31 of the gas spray gun and the air nozzle 22, and most of the combustion products are discharged from the outlet 14 of the outer cavity of the flue gas.
Specifically, the air shell 2 is fixed at one end of the smoke shell 1, and a smoke inner cavity 11 and a flow guide outer cavity 12 are arranged in the smoke shell 1; an air cavity 21 is arranged in the air shell 2, and the air cavity 21 on the air shell 2 is communicated with the flow guide outer cavity 12 on the smoke shell 1; the air casing 2 is provided with air jets 22.
One end of the heat exchanger 4 is fixed at the other end of the flue gas shell 1 through a flange, the other end of the heat exchanger 4 is matched with the flame stabilizing mixing core 7, the inlet end of the heat exchanger 4 is matched with the flue gas inner cavity inlet end 13 of the flue gas shell 1, heat exchange fins 43 are arranged on the inner wall and the outer wall of the heat exchanger 4, the heat exchanger 4 is arranged in the guide cylinder 6 and is concentric with the guide cylinder 6, and a heat exchanger air channel 41 is formed between the heat exchanger 4 and the guide cylinder 6.
One end of the diffusion mixed flow pipe 5 is matched with the flame stabilizing mixed core 7; the diffusion mixed flow pipe 5 is arranged in the heat exchanger 4 and is concentric with the heat exchanger 4, a diffusion mixed flow cavity 51 is arranged in the diffusion mixed flow pipe 5, and the inlet end to the outlet end of the diffusion mixed flow cavity 51 are distributed in a typical Venturi tube-shaped contraction section, a typical Venturi tube section and a typical diffusion section structure.
The diffusion mixed flow pipe 5 is arranged in the heat exchanger 4 and is concentric with the heat exchanger 4, and a heat exchanger flue gas channel 42 is formed between the diffusion mixed flow pipe 5 and the heat exchanger 4; the heat exchanger flue gas channel 42 is communicated with the flue gas inner cavity 11 of the flue gas shell 1, and the heat exchanger air channel 41 is communicated with the flow guide outer cavity 12 of the flue gas shell 1.
The flame guide cylinder 8 is arranged in the radiant tube 9, one end of the flame guide cylinder 8 is matched with the flame stabilizing mixed core 7, and a support frame is arranged on the flame guide cylinder 8; the flame guide cylinder 8 is concentric with the radiant tube 9, a flame guide cylinder outer cavity 81 is formed between the flame guide cylinder 8 and the radiant tube 9, the flame guide cylinder outer cavity 81 is a flame channel, a flame guide cylinder inner cavity 82 is arranged in the flame guide cylinder 8, and the flame guide cylinder inner cavity 82 is a flue gas channel; the muffle chamber 82 is divergent.
The gas lance 3 is arranged on the air housing 2, and the gas lance outlet 31 is arranged in the air nozzle 22.
The flame stabilizing mixing core 7 is arranged in the guide shell 6, the flame stabilizing mixing core 7 is a flue gas spacer 73 with an air distribution ring 74 at one end, a mixed combustion chamber 75 is arranged between the flue gas spacer 73 and the guide shell 6, a hemispherical air collecting cavity 71 is also arranged at one end of the flame stabilizing mixing core 7, and the hemispherical air collecting cavity 71 is connected with the flue gas spacer 73 through a columnar nozzle 72; air distribution holes 76 and ignition device mounting holes 77 are circumferentially distributed on the air distribution ring 74.
One end of the ignition device 10 is provided on the air casing 2, and the other end of the ignition device 10 is disposed at the ignition device mounting hole 77 of the flame-stabilizing mixing core 7.
In addition, it should be noted that the specific embodiments described in the present specification may be different in the components, the shapes of the components, the names of the components, and the like, and the above description is only an illustration of the structure of the present invention. Equivalent or simple changes in the structure, characteristics and principles of the utility model are included in the protection scope of the patent. Various modifications, additions and substitutions for the specific embodiments described may be made by those skilled in the art without departing from the scope of the utility model as defined in the accompanying claims.
Claims (10)
1. The utility model provides a take low NOx of flue gas backward flow diffusion formula self-preheating radiant tube nozzle which characterized in that: including flue gas casing (1), air casing (2), gas spray gun (3), heat exchanger (4), diffusion mixed flow tube (5), draft tube (6), steady flame mix core (7), lead flame tube (8) and radiant tube (9), install the both sides in flue gas casing (1) respectively air casing (2) and radiant tube (9), install on air casing (2) gas spray gun (3), all install in radiant tube (9) draft tube (6) and lead flame tube (8), heat exchanger (4) and steady flame mix core (7) and all install in draft tube (6), diffusion mixed flow tube (5) are installed in heat exchanger (4), heat exchanger (4) and diffusion mixed flow tube (5) all are connected with steady flame mix core (7), steady flame mixes core (7) and is connected with lead flame tube (8).
2. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to claim 1, wherein: still include ignition (10), ignition (10) are installed on flue gas casing (1) and air casing (2), and ignition (10) and flame holding mix core (7) cooperation.
3. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to claim 1, wherein: one end of the heat exchanger (4) is installed on the flue gas shell (1), one end of the diffusion mixed flow pipe (5) is matched with the gas spray gun (3), and the other end of the heat exchanger (4) and the other end of the diffusion mixed flow pipe (5) are both connected with the flame stabilizing mixed core (7).
4. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to claim 1, wherein: the flue gas shell (1) is internally provided with a flue gas inner cavity (11) and a flow guide outer cavity (12), and the flue gas inner cavity (11) is respectively provided with a flue gas inner cavity inlet end (13) and a flue gas outer cavity outlet end (14).
5. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to claim 1, wherein: a diffusion mixed flow cavity (51) is arranged in the diffusion mixed flow pipe (5), and the diffusion mixed flow cavity (51) is communicated with the flue gas inner cavity (11); and/or; the diffusion mixed flow cavity (51) is respectively provided with a contraction section, a throat section and a diffusion section from the inlet end to the outlet end.
6. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to claim 1, wherein: an air cavity (21) and an air nozzle (22) are arranged in the air shell (2), the air cavity (21) is communicated with the flow guide outer cavity (12), and a gas spray gun outlet (31) of the gas spray gun (3) is arranged at the air nozzle (22).
7. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to claim 1, wherein: the heat exchanger is characterized in that heat exchange fins (43) are arranged on the heat exchanger (4), a heat exchanger air channel (41) is arranged between the heat exchanger (4) and the guide cylinder (6), a heat exchanger flue gas channel (42) is arranged between the heat exchanger (4) and the diffusion mixed flow pipe (5), the heat exchanger air channel (41) is communicated with the guide outer cavity (12), and the heat exchanger flue gas channel (42) is communicated with the flue gas inner cavity (11).
8. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to claim 1, wherein: the flame stabilizing mixing core (7) comprises a hemispherical gas collecting cavity (71), a cylindrical nozzle (72), a flue gas spacer bush (73) and a wind distribution ring (74), the flue gas spacer bush (73) is fixed with the wind distribution ring (74), a mixing combustion chamber (75) is arranged between the flue gas spacer bush (73) and the guide cylinder (6), the heat exchanger (4) is connected with the wind distribution ring (74), the diffusion mixed flow cavity (51) is communicated with the hemispherical gas collecting cavity (71), the hemispherical gas collecting cavity (71) is communicated with the cylindrical nozzle (72), and the cylindrical nozzle (72) is communicated with the mixing combustion chamber (75); and/or; the number of the columnar nozzles (72) is m, m is more than or equal to 2 and less than or equal to 6, the included angle between the columnar nozzles (72) and the central line of the flue gas spacer bush (73) is theta, and theta is more than or equal to 20 degrees and less than or equal to 60 degrees.
9. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation of claim 8, wherein: the air distribution ring (74) is provided with an air distribution hole (76) and an ignition device mounting hole (77), two ends of the air distribution hole (76) are respectively communicated with the heat exchanger air channel (41) and the mixed combustion chamber (75), and the ignition device (10) penetrates through the ignition device mounting hole (77).
10. The diffusion type low NOx self-preheating radiant tube burner with flue gas recirculation according to claim 1, wherein: a flame guide barrel inner cavity (82) is arranged in the flame guide barrel (8), a flame guide barrel outer cavity (81) is arranged between the flame guide barrel (8) and the radiant tube (9), the flame guide barrel outer cavity (81) is communicated with the mixed combustion chamber (75), and the flame guide barrel inner cavity (82) is communicated with the heat exchanger flue gas channel (42).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121695071.XU CN215723204U (en) | 2021-07-23 | 2021-07-23 | Diffusion type low NOx self-preheating radiant tube burner with flue gas backflow |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121695071.XU CN215723204U (en) | 2021-07-23 | 2021-07-23 | Diffusion type low NOx self-preheating radiant tube burner with flue gas backflow |
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| CN215723204U true CN215723204U (en) | 2022-02-01 |
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| CN202121695071.XU Active CN215723204U (en) | 2021-07-23 | 2021-07-23 | Diffusion type low NOx self-preheating radiant tube burner with flue gas backflow |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113531528A (en) * | 2021-07-23 | 2021-10-22 | 杭州中景科技有限公司 | Diffusion type low-NOx self-preheating radiant tube burner with flue gas backflow and method |
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2021
- 2021-07-23 CN CN202121695071.XU patent/CN215723204U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113531528A (en) * | 2021-07-23 | 2021-10-22 | 杭州中景科技有限公司 | Diffusion type low-NOx self-preheating radiant tube burner with flue gas backflow and method |
| CN113531528B (en) * | 2021-07-23 | 2024-04-12 | 杭州中景科技有限公司 | Low-NOx self-preheating radiant tube burner with smoke backflow diffusion and method |
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