CN214425975U - Coal and biomass coupled combustion system and boiler - Google Patents
Coal and biomass coupled combustion system and boiler Download PDFInfo
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- CN214425975U CN214425975U CN202120450989.1U CN202120450989U CN214425975U CN 214425975 U CN214425975 U CN 214425975U CN 202120450989 U CN202120450989 U CN 202120450989U CN 214425975 U CN214425975 U CN 214425975U
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- 239000002028 Biomass Substances 0.000 title claims abstract description 109
- 239000003245 coal Substances 0.000 title claims abstract description 70
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 50
- 239000000203 mixture Substances 0.000 claims abstract description 27
- 239000000843 powder Substances 0.000 claims description 5
- 230000001105 regulatory effect Effects 0.000 claims description 5
- 239000003570 air Substances 0.000 claims description 3
- 230000008878 coupling Effects 0.000 abstract description 13
- 238000010168 coupling process Methods 0.000 abstract description 13
- 238000005859 coupling reaction Methods 0.000 abstract description 13
- 230000004048 modification Effects 0.000 abstract description 2
- 238000012986 modification Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 4
- 230000003247 decreasing effect Effects 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000004939 coking Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
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Abstract
The utility model relates to a boiler technical field discloses a coal and living beings coupling combustion system and boiler. Wherein coal and living beings coupling combustion system include primary air pipeline, the overgrate air pipeline, buggy conveyor and living beings conveyor, primary air pipeline and overgrate air pipeline homoenergetic can communicate in the furnace of boiler, outside the primary air pipeline was located to overgrate air pipeline cover, be used for to the inside whirl wind that lets in of furnace, buggy conveyor communicates in primary air pipeline, be used for to leading to wind and buggy mixture in the primary air pipeline, living beings conveyor communicates in primary air pipeline, be used for leading to wind and living beings mixture in the primary air pipeline, under this setting, can realize the coupling burning of living beings and coal, and system architecture is simple. Furthermore, the coal and biomass coupled combustion system can be applied to boilers, is low in modification cost and has better economic performance.
Description
Technical Field
The utility model relates to a boiler technical field especially relates to a coal and living beings coupling combustion system and boiler.
Background
The biomass is the fourth most energy source in the world, has the main characteristics of being renewable, low in sulfur content and capable of effectively reducing SO in flue gas2Concentration and achievement of CO2Zero emission, and is a clean low-carbon fuel. The biomass power generation has economic, ecological and social comprehensive benefits, and can relieve the increasingly prominent problems of energy shortage and environmental deterioration.
At present, biomass and a coal-fired boiler are mainly coupled and utilized in two forms, firstly, the biomass is gasified and then is sent into a hearth, and the biomass blending combustion in the form has little influence on the boiler, but the investment is high; and secondly, biomass is directly coupled with fire coal for combustion, but the combustion characteristics of the biomass and pulverized coal are greatly different, so that the air distribution form and position required for the combustion of the biomass fed into the pulverized coal furnace are different, and the problems of complex device structure, high operation control difficulty and the like exist in the coal and biomass coupled combustion power generation technology.
Therefore, a coal and biomass coupled combustion system and a boiler are urgently needed, which not only can realize the coupled combustion of biomass and coal, but also have simple system structure and low modification cost.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a coal and living beings coupling combustion system and boiler to realize the coupling burning of living beings and coal, and system's simple structure, it is with low costs to reform transform.
As the conception, the utility model adopts the technical proposal that:
a coal and biomass coupled combustion system comprising:
the primary air pipeline and the secondary air pipeline can be communicated with a hearth of the boiler, the secondary air pipeline is sleeved outside the primary air pipeline, and the secondary air pipeline is used for introducing swirling air into the hearth;
the coal powder conveying device is communicated with the primary air pipeline and is used for introducing a mixture of air and coal powder into the primary air pipeline;
and the biomass conveying device is communicated with the primary air pipeline and is used for introducing air and biomass mixture into the primary air pipeline.
Further, the coal and biomass coupled combustion system further comprises a switching device, the pulverized coal conveying device and the biomass conveying device are both communicated with the primary air pipeline through the switching device, and the switching device is configured to enable the primary air pipeline to enable air and pulverized coal mixture or air and biomass mixture to flow into the hearth.
Further, the biomass conveying device is used for introducing a mixture of wind and biomass at the temperature of 50-100 ℃ into the primary air pipeline when the wind speed at the nozzle end of the primary air pipeline is 30-45 m/s and the wind speed at the nozzle end of the secondary air pipeline is 10-20 m/s.
Further, the biomass conveying device comprises an air blower, a biomass bin, a discharge pipeline and a hot air pipeline, wherein one end of the discharge pipeline is communicated with the biomass bin, the other end of the discharge pipeline is communicated with the primary air pipeline, the air blower is configured to enable biomass in the biomass bin to enter the primary air pipeline through the discharge pipeline, and the hot air pipeline is configured to increase the temperature of the biomass leaving the biomass bin.
Furthermore, one end of the hot air pipeline is communicated with the discharge pipeline, and the other end of the hot air pipeline can be communicated with the secondary air box.
Furthermore, one end of the hot air pipeline is communicated with the primary air pipeline, and the other end of the hot air pipeline can be communicated with the secondary air box.
Furthermore, a flow regulating valve is arranged on the hot air pipeline.
Further, biomass conveying device still includes the cold air duct, the air-blower pass through the cold air duct communicate in the biomass storehouse.
Further, one end, extending into the hearth, of the secondary air pipeline is provided with a frustum-shaped pipe, the small-diameter end of the frustum-shaped pipe is connected to the secondary air pipeline, and the included angle between the extending direction of the conical wall of the frustum-shaped pipe and the axial direction of the secondary air pipeline is 25-35 degrees.
Further, still provide a boiler, including boiler furnace, secondary bellows and as above any one the coal and biomass coupled combustion system, the secondary bellows is equipped with a plurality ofly, and is a plurality of the secondary bellows encircles along furnace circumference and arranges at least one deck, and at least one the secondary bellows intercommunication at least one coal and biomass coupled combustion system.
The utility model has the advantages that:
the utility model provides a coal and living beings coupling combustion system, including once wind pipeline, overgrate air pipeline, buggy conveyor and living beings conveyor. Primary air pipeline and overgrate air pipeline homoenergetic can feed through in the furnace of boiler, and outside the primary air pipeline was located to overgrate air pipeline cover, the overgrate air pipeline was used for letting in the whirl wind to furnace inside, and buggy conveyor feeds through in primary air pipeline for to leading to wind and buggy mixture in the primary air pipeline, living beings conveyor feeds through in primary air pipeline for to leading to wind and living beings mixture in the primary air pipeline. The coal powder conveying device and the biomass conveying device which are respectively arranged can realize the coupled combustion of coal and biomass in the working process of the boiler, and the system is simple in structure.
The utility model also provides a boiler, including foretell coal and living beings coupling combustion system, can realize the coupling burning of coal and living beings, reform transform with low costs moreover, have more economic performance.
Drawings
Fig. 1 is a schematic structural diagram of a coal and biomass coupled combustion system provided in an embodiment of the present invention;
fig. 2 is a schematic structural diagram of a coal and biomass coupled combustion system provided by the second embodiment of the present invention.
In the figure:
1. a primary air duct;
2. a secondary air duct; 21. a swirl vane; 22. a frustum-shaped tube;
3. a biomass conveying device; 31. a cold air duct; 32. a biomass bin; 33. a discharge pipeline; 34. a hot air duct; 341. a flow regulating valve;
4. a pulverized coal conveying device;
5. a switching device;
6. a secondary air box;
7. and (4) a hearth.
Detailed Description
In order to make the technical problem solved by the present invention, the technical solution adopted by the present invention and the technical effect achieved by the present invention clearer, the technical solution of the present invention will be further explained by combining the drawings and by means of the specific implementation manner. It is to be understood that the specific embodiments described herein are merely illustrative of the invention and are not limiting of the invention. It should be further noted that, for the convenience of description, only some but not all of the elements related to the present invention are shown in the drawings.
In the description of the present invention, unless expressly stated or limited otherwise, the terms "connected," "connected," and "fixed" are to be construed broadly, e.g., as meaning permanently connected, detachably connected, or integral to one another; can be mechanically or electrically connected; either directly or indirectly through intervening media, either internally or in any other relationship. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
In the present disclosure, unless expressly stated or limited otherwise, the first feature "on" or "under" the second feature may comprise direct contact between the first and second features, or may comprise contact between the first and second features not directly. Also, the first feature being "on," "above" and "over" the second feature includes the first feature being directly on and obliquely above the second feature, or merely indicating that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature includes the first feature being directly under and obliquely below the second feature, or simply meaning that the first feature is at a lesser elevation than the second feature.
In the description of the present embodiment, the terms "upper", "lower", "left", "right", and the like are used in the orientation or positional relationship shown in the drawings only for convenience of description and simplicity of operation, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed in a specific orientation, and be operated, and thus should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used only for descriptive purposes and are not intended to have a special meaning.
The technical solution of the present invention is further explained by the following embodiments with reference to the accompanying drawings.
Example one
As shown in fig. 1, the embodiment provides a coal and biomass coupled combustion system, which includes a primary air duct 1, a secondary air duct 2, a pulverized coal conveying device 4, and a biomass conveying device 3. Wherein the primary air pipeline 1 and the secondary air pipeline 2 all can communicate in the furnace 7 of boiler, the secondary air pipeline 2 cover is located outside the primary air pipeline 1, the secondary air pipeline 2 is used for letting in whirl wind to the furnace 7 inside, buggy conveyor 4 communicates in the primary air pipeline 1 for lead to wind and buggy mixture in the primary air pipeline 1, living beings conveyor 3 communicates in the primary air pipeline 1 for lead to wind and living beings mixture in the primary air pipeline 1. Under this setting, can realize the coupling burning of coal and living beings in the boiler working process, system simple structure moreover reforms transform with low costsly.
Further, the coal and biomass coupled combustion system further comprises a switching device 5, the pulverized coal conveying device 4 and the biomass conveying device 3 are both communicated with the primary air pipeline 1 through the switching device 5, and the switching device 5 is configured to enable the primary air pipeline 1 to enable air and pulverized coal mixture or air and biomass mixture to flow into the hearth 7. In this embodiment, the switching device 5 is preferably a three-phase valve, and is simple in structure, and the switching of the conveying device communicated with the primary air pipeline 1 can be realized by adjusting the on-off direction of the three-phase valve, so that the co-combustion of pulverized coal and biomass in different proportions is completed, and the operation flexibility of the coal and biomass coupled combustion system is effectively enhanced.
Specifically, when the mixture of air and pulverized coal is introduced into the hearth 7 from the primary air duct 1, the air speed at the nozzle end of the primary air duct 1 is 16-24 m/s, the air speed at the nozzle end of the secondary air duct 2 is 36-50 m/s, and the secondary air duct 2 is arranged on the outer layer of the primary air duct 1, so that an air-coated pulverized coal flow field can be formed at the nozzle of the burner, and pulverized coal ignition is effectively promoted.
When the mixture of the air and the biomass is introduced into the hearth 7 from the primary air pipeline 1, the air speed at the nozzle end of the primary air pipeline 1 is obviously higher than that at the nozzle end of the primary air pipeline 1 under the conventional coal-fired working condition, because the biomass has the characteristic of easy ignition and burnout, the ignition distance of the biomass is increased by the high primary air speed, and the temperature near the nozzle of the combustor is reduced. In addition, the air speed of the nozzle end of the secondary air pipeline 2 is lower than that of the nozzle end of the secondary air pipeline 2 under the conventional coal burning working condition, so that the secondary air with strong swirling flow and low speed can form an expanded air film and an oxidizing atmosphere on the wall surface of the hearth 7, and the coking phenomenon of the nozzle of the combustor under the working condition of biomass burning is effectively prevented. Specifically, the biomass conveying device 3 is used for introducing a mixture of wind and biomass at a temperature of 50-100 ℃ into the primary air pipeline 1 when the wind speed at the nozzle end of the primary air pipeline 1 is 30-45 m/s and the wind speed at the nozzle end of the secondary air pipeline 2 is 10-20 m/s.
As shown in fig. 1, the biomass transportation device 3 includes a blower, a biomass bin 32, a discharge pipe 33 and a hot air pipe 34, wherein one end of the discharge pipe 33 is connected to the biomass bin 32, and the other end is connected to the primary air pipe 1, the blower is configured to enable biomass in the biomass bin 32 to enter the primary air pipe 1 through the discharge pipe 33, and the hot air pipe 34 is configured to increase the temperature of the biomass leaving the biomass bin 32. Specifically, what the air-blower (not shown in the figure) let in the biomass bin 32 is gas under the room temperature state, because the biomass needs to adopt cold air to carry to effectively postpone the ignition point of the biomass, thereby avoid the biomass to take place spontaneous combustion in the transportation process, and the hot-blast pipeline 34 is the ignition heat that is needed when guaranteeing the biomass to get into the burning of furnace 7, but finally, the cold air that the air-blower lets in and the hot-blast pipeline 34 let in will mix in the primary air pipeline 1, in order to guarantee that the temperature of the wind in the primary air pipeline 1 and the biomass mixture is in 50 ~ 100 ℃.
In addition, as can be understood, for a conventional coal-fired boiler, the temperature of gas provided by the secondary air box 6 equipped in the conventional coal-fired boiler is high, generally 280-350 ℃, so that the secondary air box 6 can be directly used as a hot air source. Therefore, in the present embodiment, one end of the hot air duct 34 is connected to the discharging duct 33, and the other end of the hot air duct 34 can be connected to the secondary air box 6, which not only simplifies the system structure, but also is more convenient and energy-saving.
In another embodiment, because the temperature variation range of hot air in the secondary air box 6 is small, if the wide mixture ratio of hot air and cold air is ensured, one end of the hot air pipeline 34 communicated with the secondary air box 6 can also be communicated with other hot air sources with adjustable temperature, and only the range of the hot air temperature is required to be suitable for the biomass conveying device 3.
Furthermore, in order to conveniently regulate and control the temperature in the primary air pipe 1 when the biomass is conveyed, a flow regulating valve 341 is disposed on the hot air pipe 34, and the flow regulating valve 341 can regulate the flow of the hot air entering the primary air pipe 1. It can be understood that when the temperature of the hot air in the secondary air box 6 cannot be changed, the adjustment of the temperature of the mixture of the air and the biomass in the primary air pipeline 1 can be realized by adjusting the flow rate of the hot air introduced into the discharge pipeline 33. Specifically, the flow rate of the hot air passing through the flow rate adjustment valve 341 may be increased if the temperature in the primary air duct 1 is to be raised, and the flow rate of the hot air passing through the flow rate adjustment valve 341 may be decreased if the temperature in the primary air duct 1 is to be lowered.
In addition to changing the flow rate of the hot air in the hot air duct 34 to adjust the temperature in the primary air duct 1, the temperature can also be adjusted by changing the flow rate of the cold air introduced into the primary air duct 1. Specifically, the power of the blower can be changed to change the amount of cold air introduced, thereby adjusting the temperature of the mixed cold air and hot air in the primary air duct 1. The adjusting method is similar to changing the flow rate of the hot air in the hot air duct 34, that is, when the flow rate of the hot air in the hot air duct 34 is not changed, if the temperature in the primary air duct 1 is to be decreased, the flow rate of the cold air can be correspondingly increased, and if the temperature in the primary air duct 1 is to be increased, the flow rate of the cold air can be correspondingly decreased.
Preferably, in this embodiment, the particle diameter of the biomass stored in the biomass bin 32 is less than 2mm, that is, it is ensured that the biomass can be wrapped into the discharge pipeline 33 by the cold air flowing out from the blower, so as to enter the primary air pipeline 1, and therefore, the power of the blower needs to be adjusted and controlled in consideration of a proper biomass conveying amount.
Specifically, the biomass conveying device 3 further includes a cold air duct 31, and the air blower is communicated with the biomass bin 32 through the cold air duct 31. It can be understood, cold air duct 31 and discharge duct 33 set up respectively on living beings storehouse 32, the air-blower provides the cold wind of certain speed, through cold air duct 31 and get into living beings storehouse 32, so that the living beings in living beings storehouse 32 can be driven by the air current and get into discharge duct 33, but except that cold wind speed can influence the velocity of flow of wind and living beings mixture in discharge duct 33, the relative position that cold air duct 31 and discharge duct 33 set up on living beings storehouse 32, also with very big influence living beings the degree of difficulty that living beings leave living beings storehouse 32, therefore, when actual setting, can be according to the operating mode needs, change cold air duct 31 or cold air duct 31 and the concrete position that discharge duct 33 set up on living beings storehouse 32, in order to guarantee suitable wind and living beings mix proportion in discharge duct 33.
Finally, it should be noted that one end of the secondary air duct 2 extending into the furnace 7 is provided with a frustum-shaped tube 22, a small-diameter end of the frustum-shaped tube 22 is connected to the secondary air duct 2, and an included angle between an extending direction of a conical wall of the frustum-shaped tube 22 and an axial direction of the secondary air duct 2 is 25-35 °. The secondary air pipe nozzle end is designed to be in a taper shape, so that the ignition point can be effectively adjusted, air distribution backward moves, air classification is strengthened, the temperature at the nozzle is reduced, and the generation amount of nitrogen oxides at the initial stage of coal combustion can be effectively reduced.
In addition, in order to ensure the strong swirling effect of the secondary air, the swirling vanes 21 are arranged in the secondary air pipeline 2, and in the embodiment, the angle of the swirling vanes 21 is preferably 45-70 degrees.
The embodiment also provides a boiler, which comprises a boiler furnace 7, a secondary air box 6 and the coal and biomass coupled combustion system, wherein the secondary air box 6 is provided with a plurality of secondary air boxes 6, the plurality of secondary air boxes 6 are arranged in at least one layer in a surrounding mode along the circumferential direction of the furnace 7, and at least one secondary air box 6 is communicated with at least one coal and biomass coupled combustion system. Specifically, one or more layers of secondary air boxes 6 can be arranged on the wall of a hearth 7 of the boiler, and one or more secondary air boxes 6 can be arranged on each layer, so that when biomass is required to be co-combusted, at least one secondary air box 6 can be selected to be communicated with the coal and biomass coupled combustion system according to actual working condition requirements.
Example two
The embodiment discloses a coal and biomass coupled combustion system, and the difference between the coal and biomass coupled combustion system in the embodiment and the coal and biomass coupled combustion system in the embodiment one lies in that: as shown in fig. 2, one end of the hot air duct 34 is connected to the primary air duct 1, and the other end of the hot air duct 34 can be connected to the secondary air box 6. The purpose of setting up hot-blast pipeline 34 is in order to guarantee the ignition heat of living beings, consequently, with hot-blast pipeline 34 intercommunication in primary air pipeline 1 or ejection of compact pipeline 33, to the last burning of living beings and ignition point do not have great influence, can set up according to actual assembly demand.
In addition, the rest of the structure of the coal and biomass coupled combustion system provided in this embodiment is the same as that of the coal and biomass coupled combustion system in the embodiment, and details are not repeated herein.
This embodiment still provides a boiler, including boiler furnace 7, secondary bellows 6 and foretell coal and living beings coupling combustion system, secondary bellows 6 are equipped with a plurality ofly, and a plurality of secondary bellows 6 encircle to arrange along 7 circumference of furnace to at least one deck, and at least one secondary bellows 6 intercommunication at least one coal and living beings coupling combustion system, can realize the coupling burning of coal and living beings, avoid boiler burner spout loss of burning, coking, simple structure moreover, it is convenient to reform transform, has higher economic performance.
The above embodiments have been described only the basic principles and features of the present invention, and the present invention is not limited by the above embodiments, and is not departing from the spirit and scope of the present invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (10)
1. A coal and biomass coupled combustion system, comprising:
the primary air pipeline (1) and the secondary air pipeline (2) can be communicated with a hearth (7) of the boiler, the secondary air pipeline (2) is sleeved outside the primary air pipeline (1), and the secondary air pipeline (2) is used for introducing swirling air into the hearth (7);
the coal powder conveying device (4) is communicated with the primary air pipeline (1) and is used for introducing a mixture of air and coal powder into the primary air pipeline (1);
and the biomass conveying device (3) is communicated with the primary air pipeline (1) and is used for introducing air and biomass mixture into the primary air pipeline (1).
2. The coal and biomass coupled combustion system according to claim 1, further comprising a switching device (5), wherein the pulverized coal conveying device (4) and the biomass conveying device (3) are both communicated with the primary air duct (1) through the switching device (5), and the switching device (5) is configured to enable the primary air duct (1) to introduce air and pulverized coal mixture or air and biomass mixture into the hearth (7).
3. The coal and biomass coupled combustion system according to claim 1, wherein the biomass conveying device (3) is used for introducing a mixture of wind and biomass with the temperature of 50-100 ℃ into the primary air pipeline (1) when the wind speed at the nozzle end of the primary air pipeline (1) is 30-45 m/s and the wind speed at the nozzle end of the secondary air pipeline (2) is 10-20 m/s.
4. The coal and biomass coupled combustion system according to claim 1, wherein the biomass conveying device (3) comprises a blower, a biomass bin (32), a discharge pipe (33) and a hot air pipe (34), one end of the discharge pipe (33) is communicated with the biomass bin (32), the other end of the discharge pipe is communicated with the primary air pipe (1), the blower is configured to enable biomass in the biomass bin (32) to enter the primary air pipe (1) through the discharge pipe (33), and the hot air pipe (34) is configured to increase the temperature of the biomass leaving the biomass bin (32).
5. The coal and biomass coupled combustion system according to claim 4, wherein one end of the hot air duct (34) is communicated with the discharge duct (33), and the other end of the hot air duct (34) can be communicated with the secondary wind box (6).
6. The coal and biomass coupled combustion system according to claim 4, wherein one end of the hot air duct (34) is communicated with the primary air duct (1), and the other end of the hot air duct (34) can be communicated with the secondary air box (6).
7. The coal and biomass coupled combustion system according to any one of claims 5 to 6, wherein a flow regulating valve (341) is arranged on the hot air duct (34).
8. The coal and biomass coupled combustion system according to claim 7, wherein the biomass conveying device (3) further comprises a cold air duct (31), and the air blower is communicated with the biomass bin (32) through the cold air duct (31).
9. The coal and biomass coupled combustion system according to claim 1, wherein one end of the secondary air duct (2) extending into the furnace (7) is provided with a frustum-shaped pipe (22), the small-diameter end of the frustum-shaped pipe (22) is connected to the secondary air duct (2), and the extending direction of the conical wall of the frustum-shaped pipe (22) forms an included angle of 25-35 ° with the axial direction of the secondary air duct (2).
10. A boiler, characterized by comprising a boiler furnace (7), a plurality of secondary windboxes (6) and the coal and biomass coupled combustion system of any one of claims 1 to 9, wherein the secondary windboxes (6) are provided, the plurality of secondary windboxes (6) are circumferentially arranged in at least one layer along the circumference of the furnace (7), and at least one secondary windbox (6) is communicated with at least one coal and biomass coupled combustion system.
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| CN202120450989.1U CN214425975U (en) | 2021-03-02 | 2021-03-02 | Coal and biomass coupled combustion system and boiler |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112815303A (en) * | 2021-03-02 | 2021-05-18 | 烟台龙源电力技术股份有限公司 | Coal and biomass coupled combustion system and boiler |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112815303A (en) * | 2021-03-02 | 2021-05-18 | 烟台龙源电力技术股份有限公司 | Coal and biomass coupled combustion system and boiler |
| CN112815303B (en) * | 2021-03-02 | 2024-09-27 | 烟台龙源电力技术股份有限公司 | Coal and biomass coupled combustion system and boiler |
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