CN111536511A - A pulverized coal swirl burner - Google Patents
A pulverized coal swirl burner Download PDFInfo
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- CN111536511A CN111536511A CN202010461383.8A CN202010461383A CN111536511A CN 111536511 A CN111536511 A CN 111536511A CN 202010461383 A CN202010461383 A CN 202010461383A CN 111536511 A CN111536511 A CN 111536511A
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- 239000003245 coal Substances 0.000 title claims abstract description 65
- 238000002485 combustion reaction Methods 0.000 claims abstract description 25
- 230000000087 stabilizing effect Effects 0.000 claims description 8
- 230000009467 reduction Effects 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 5
- 239000000843 powder Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000003034 coal gas Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000013598 vector Substances 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D1/00—Burners for combustion of pulverulent fuel
- F23D1/02—Vortex burners, e.g. for cyclone-type combustion apparatus
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2201/00—Burners adapted for particulate solid or pulverulent fuels
- F23D2201/20—Fuel flow guiding devices
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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Abstract
本发明公开了一种煤粉旋流燃烧器,包括:沿径向从内向外依次布置的一次风通道、内二次风通道和外二次风通道,一次风通道的出风口设置有喷嘴,还包括调风器。调风器包括外二次风套筒挡板和外二次风套筒挡板调节部、外二次风旋流叶片和外二次风旋流叶片调节部;外二次风套筒挡板调节部可驱动外二次风套筒挡板移动以调节外二次风通道的进风口的开度。外二次风旋流叶片调节部可驱动外二次风旋流叶片移动。本申请的煤粉旋流燃烧器无中心风设计,在燃烧器喷口形成更大的还原性区域,进入炉膛的煤粉能够快速着火和快速升温,在有限的时间内,可释放出煤种中更多CH基团,用以来还原燃烧器主燃区所生成的NOx,实现火焰内还原降低NOx。
The invention discloses a pulverized coal swirl burner, comprising: a primary air channel, an inner secondary air channel and an outer secondary air channel arranged in sequence from the inside to the outside along the radial direction, the air outlet of the primary air channel is provided with a nozzle, Also includes air regulator. The air regulator includes outer secondary air sleeve baffle and outer secondary air sleeve baffle adjustment part, outer secondary air swirl blade and outer secondary air swirl blade adjustment part; outer secondary air sleeve baffle The adjusting part can drive the outer secondary air sleeve baffle plate to move to adjust the opening of the air inlet of the outer secondary air passage. The outer secondary air swirl blade adjusting part can drive the outer secondary air swirl blade to move. The pulverized coal swirl burner of the present application has no central air design, and a larger reducing area is formed at the burner nozzle. The pulverized coal entering the furnace can quickly ignite and heat up quickly, and can be released into the coal within a limited time. More CH groups are used to reduce the NOx generated in the main combustion zone of the burner to achieve reduction in the flame and reduce NOx.
Description
技术领域technical field
本发明涉及煤粉燃烧技术领域,尤其涉及一种煤粉旋流燃烧器。The invention relates to the technical field of pulverized coal combustion, in particular to a pulverized coal swirl burner.
背景技术Background technique
旋流燃烧器是当前电站锅炉和工业锅炉上广泛应用的一种燃烧煤粉的装置。随着近年来环保要求的不断提高和超低排放改造的进行,低氮燃烧器的的应用作为最为经济的氮氧化物减排手段,成了脱硝的必然选择,但由于现有燃烧器的过度空气分级燃烧及过度的追求更低的炉膛出口NOx排放,给锅炉的运行带来了一系列的问题。The swirl burner is a device for burning pulverized coal widely used in power plant boilers and industrial boilers. With the continuous improvement of environmental protection requirements and the progress of ultra-low emission transformation in recent years, the application of low-nitrogen burners, as the most economical means of reducing nitrogen oxides, has become an inevitable choice for denitrification. Air staged combustion and excessive pursuit of lower NOx emissions at the furnace outlet have brought a series of problems to the operation of the boiler.
目前市面上的燃烧器中心风筒置于一次煤粉气流中,易磨损,频繁更换,增加运行和维护成本,降低系统运行的可靠性。该燃烧器配套的燃烧系统所采用的燃尽风用量大,通常燃尽风在总送风量的占比在25%以上,易造成炉膛区域过度欠氧燃烧,易造成高温腐蚀,燃烧推迟,锅炉减温水量上升甚至满开,锅炉经济性变差;中心风在锅炉运行时需要通少量的冷却风,这部分风的存在容易在燃烧器喷口区域形成氧化性氛围,降低燃烧过程中NOx的降低;燃烧器利用扩锥的方式来延迟一次风/和二次风的混合,通过推迟燃烧的方式来控制燃烧中NOx的形成,降低NOx的能力弱,而且过大的扩锥张角所卷席的烟气易烧损喷口和扩锥。At present, the central air duct of the burner on the market is placed in the primary pulverized coal air flow, which is easy to wear and replace frequently, which increases the operation and maintenance cost and reduces the reliability of the system operation. The combustion system matched with this burner uses a large amount of over-burning air. Usually, the over-burning air accounts for more than 25% of the total air supply volume. The amount of desuperheating water in the boiler increases or even fully opens, and the economy of the boiler becomes poor; the central air needs to pass a small amount of cooling air during the operation of the boiler. The existence of this part of the air is easy to form an oxidizing atmosphere in the nozzle area of the burner, reducing the NOx during the combustion process. Lowering; the burner delays the mixing of primary air/secondary air by means of expanding cone, and controls the formation of NOx in combustion by means of delaying combustion, the ability to reduce NOx is weak, and the excessive cone expansion angle is rolled up The smoke from the seat is easy to burn and damage the nozzle and expanding cone.
此外,随着电厂燃煤来源的日益广泛,煤质愈发不稳定,燃煤机组又越发频繁的参与深度调峰,给燃烧器系统的运行提出了新的调整,因此现有的双调风旋流煤粉燃烧器在综合水平需要进一步提升。In addition, with the increasingly wide range of coal-fired sources in power plants, the coal quality is becoming more and more unstable, and coal-fired units are more and more frequently participating in deep peak regulation, which brings new adjustments to the operation of the burner system. The swirl pulverized coal burner needs to be further improved at the comprehensive level.
发明内容SUMMARY OF THE INVENTION
为了解决上述技术问题,本发明提供了一种煤粉旋流燃烧器。In order to solve the above technical problems, the present invention provides a pulverized coal swirl burner.
根据本申请的一个方面,提供了一种煤粉旋流燃烧器,包括:沿径向从内向外依次布置的一次风通道、内二次风通道和外二次风通道,一次风通道的出风口设置有喷嘴,煤粉旋流燃烧器为均流燃烧器,还包括用于控制和调节二次风的调风器;调风器包括外二次风套筒挡板和外二次风套筒挡板调节部、外二次风旋流叶片和外二次风旋流叶片调节部;外二次风套筒挡板套设在外二次风通道的进风口处,外二次风套筒挡板调节部可驱动外二次风套筒挡板在轴向方向的预定范围内移动以调节外二次风通道的进风口的开度;外二次风旋流叶片环向设置在外二次风通道中,外二次风旋流叶片调节部可驱动外二次风旋流叶片在轴向方向上移动以调节外二次风旋流叶片在外二次风通道的位置。According to one aspect of the present application, a pulverized coal swirl burner is provided, comprising: a primary air passage, an inner secondary air passage and an outer secondary air passage arranged in order from the inside to the outside in the radial direction, and an outlet of the primary air passage is The tuyere is provided with a nozzle, the pulverized coal swirl burner is an equal flow burner, and also includes an air regulator for controlling and adjusting the secondary air; the air regulator includes an outer secondary air sleeve baffle and an outer secondary air jacket The barrel baffle adjustment part, the outer secondary air swirl blade and the outer secondary air swirl blade adjustment part; the outer secondary air sleeve baffle is sleeved at the air inlet of the outer secondary air passage, and the outer secondary air sleeve The baffle adjustment part can drive the outer secondary air sleeve baffle to move within a predetermined range in the axial direction to adjust the opening of the air inlet of the outer secondary air passage; the outer secondary air swirl blades are circumferentially arranged on the outer secondary air In the air passage, the outer secondary air swirl blade adjusting part can drive the outer secondary air swirl blade to move in the axial direction to adjust the position of the outer secondary air swirl blade in the outer secondary air passage.
可选择地,调风器还包括套设在内二次风通道的进风口处的内二次风套筒挡板和内二次风套筒挡板调节部);内二次风套筒挡板调节部可驱动内二次风套筒挡板在轴向方向上移动以调节内二次风通道的进风口的开度。Optionally, the air regulator further comprises an inner secondary air sleeve baffle and an inner secondary air sleeve baffle adjustment part sleeved at the air inlet of the inner secondary air passage); the inner secondary air sleeve baffle The plate adjusting part can drive the inner secondary air sleeve baffle plate to move in the axial direction to adjust the opening of the air inlet of the inner secondary air passage.
可选择地,内二次风通道中设置有环内二次风通道周向分布的若干个内旋流叶片。Optionally, the inner secondary air passage is provided with a plurality of inner swirl blades distributed in the circumferential direction of the inner secondary air passage.
可选择地,外二次风通道的进风口安装有外二次风均流筒,外二次风均流筒与外二次风通道连通且表面密布有均流孔,燃烧器外部的气体从外二次风均流筒周向进入外二次风道;内二次风通道的进风口安装有内二次风均流筒,内二次风均流筒与内二次风通道连通且表面密布有均流孔,外二次风道中的部分外二次风通过内二次风均流筒周向进入内二次风道。Optionally, an outer secondary air equalizing cylinder is installed at the air inlet of the outer secondary air passage, and the outer secondary air equalizing cylinder is communicated with the outer secondary air passage and is densely covered with equalizing holes. The outer secondary air equalizing cylinder enters the outer secondary air duct circumferentially; the air inlet of the inner secondary air passage is equipped with an inner secondary air equalizing cylinder, and the inner secondary air equalizing cylinder is communicated with the inner secondary air passage and has a surface The distribution holes are densely distributed, and part of the outer secondary air in the outer secondary air duct enters the inner secondary air duct circumferentially through the inner secondary air equalizing cylinder.
可选择地,外二次风套筒挡板调节部包括沿燃烧器的轴向设置的轮滑导轨、装配在轮滑导轨中的轮滑装置以及与轮滑装置连接的外二次风套筒挡板拉杆,外二次风套筒挡板与轮滑装置连接,外二次风套筒挡板拉杆可推动轮滑装置在轮滑导轨中滑动进而调节外二次风套筒挡板的位置。Optionally, the baffle adjustment part of the outer secondary air sleeve includes a roller skating guide rail arranged along the axial direction of the burner, a roller skating device assembled in the roller skating guide rail, and a pull rod of the outer secondary air sleeve baffle plate connected with the roller skating device, The outer secondary air sleeve baffle is connected with the roller skating device, and the pull rod of the outer secondary air sleeve baffle can push the roller skating device to slide in the roller skating guide rail to adjust the position of the outer secondary air sleeve baffle.
可选择地,喷嘴包括若干沿周向交替设置的内缩部和外扩部,内缩部和外扩部沿一次风的流向延伸,且内缩部沿喷嘴的径向收缩、外扩部沿喷嘴的径向外扩。Optionally, the nozzle includes a plurality of inner constricted parts and outer expanded parts arranged alternately in the circumferential direction, the inner constricted part and the outer expanded part extend along the flow direction of the primary air, and the inner constricted part is constricted along the radial direction of the nozzle, and the outer expanded part is along the flow direction of the primary air. Radial expansion of the nozzle.
可选择地,喷嘴的内缩部自喷嘴的喷口沿一次风流通相反的方向延伸至一次风通道内部,内缩部的延伸长度L为一次风通道直径D的0.5~1.5。Optionally, the indented portion of the nozzle extends from the nozzle of the nozzle to the inside of the primary air passage along the opposite direction of the primary air flow, and the extension length L of the indented portion is 0.5-1.5 of the diameter D of the primary air passage.
可选择地,喷嘴的出口处的流通面积与一次风通道的流通面积相同。Optionally, the flow area at the outlet of the nozzle is the same as the flow area of the primary air channel.
可选择地,外扩部在喷嘴的出口处设置有沿喷嘴的径向方向向外延伸的稳燃齿。Optionally, the flared portion is provided with combustion stabilizing teeth extending outward along the radial direction of the nozzle at the outlet of the nozzle.
可选择地,第一风通道的进风口与燃烧器弯头连接通过燃烧器弯头进风,燃烧器弯头中设置有煤粉均流板。Optionally, the air inlet of the first air passage is connected with the burner elbow to enter the air through the burner elbow, and a pulverized coal flow equalizing plate is arranged in the burner elbow.
本申请的煤粉旋流燃烧器无中心风设计,在燃烧器喷口形成更大的还原性区域,进入炉膛的煤粉能够快速着火和快速升温,在有限的时间内,可释放出煤种中更多CH基团,用以来还原燃烧器主燃区所生成的NOx,实现火焰内还原降低NOx。The pulverized coal swirl burner of the present application has no central air design, and a larger reducing area is formed at the nozzle of the burner. The pulverized coal entering the furnace can quickly ignite and heat up quickly, and can be released into the coal within a limited time. More CH groups are used to reduce the NOx generated in the main combustion zone of the burner to achieve reduction in the flame and reduce NOx.
附图说明Description of drawings
构成本发明的一部分的附图用来提供对本发明的进一步理解,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。在附图中:The accompanying drawings constituting a part of the present invention are used to provide further understanding of the present invention, and the exemplary embodiments of the present invention and their descriptions are used to explain the present invention and do not constitute an improper limitation of the present invention. In the attached image:
图1是本申请的煤粉旋流燃烧器的结构示意图。FIG. 1 is a schematic structural diagram of the pulverized coal swirl burner of the present application.
具体实施方式Detailed ways
为使本发明实施例的目的、技术方案和优点更加清楚,下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。需要说明的是,在不冲突的情况下,本申请中的实施例及实施例中的特征向量可以相互任意组合。In order to make the purposes, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments These are some embodiments of the present invention, but not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention. It should be noted that the embodiments in this application and the feature vectors in the embodiments may be arbitrarily combined with each other unless there is a conflict.
现有燃烧器结构设计普遍存在的缺点如下:中心风筒置于一次煤粉气流中,易磨损,频繁更换,增加运行和维护成本,降低系统运行的可靠性。中心风在锅炉运行时需要通少量的冷却风,这部分风的存在容易在燃烧器喷口区域形成氧化性氛围,降低燃烧过程中NOx的降低。稳燃齿布置于一次风喷口内壁,所形成的中心回火易烧损燃烧器喷口,目前锅炉运行燃烧器普遍存在喷口烧损的问题。燃烧器利用扩锥的方式来延迟一次风/和二次风风的混合,通过推迟燃烧的方式来控制燃烧中NOx的形成,降低NOx的能力弱,而且过大的扩锥张角所卷席的烟气易烧损喷口和扩锥。与燃烧器配套的燃烧系统所采用的燃尽风用量大,通常燃尽风在总送风量的占比在25%以上,易造成炉膛区域过度欠氧燃烧,易造成高温腐蚀,燃烧推迟,锅炉减温水量上升甚至满开,锅炉经济性变差,燃烧器总二次风调节套筒布置于锅炉风箱多灰的环境内,环向铰连结构的调整装置经常发生卡涩而使得燃烧器不可调燃烧器旋流强度叶片通过环向铰连结构调整角度的结构,因布置于锅炉风箱多灰的环境内而易发生卡涩而使得燃烧器不可调。The common shortcomings of the existing burner structure design are as follows: the central air duct is placed in the primary coal pulverized air flow, which is easy to wear and is frequently replaced, which increases the operation and maintenance cost and reduces the reliability of the system operation. The central air needs to pass a small amount of cooling air when the boiler is running. The existence of this part of the air is easy to form an oxidizing atmosphere in the nozzle area of the burner, which reduces the reduction of NOx during the combustion process. The combustion stabilizing teeth are arranged on the inner wall of the primary air nozzle, and the formed center tempering is easy to burn the nozzle of the burner. At present, the burner of the boiler operation generally has the problem of nozzle burning. The burner uses the method of expanding cone to delay the mixing of primary air/air and secondary air, and controls the formation of NOx in combustion by delaying the combustion. The ability to reduce NOx is weak, and the excessive cone expansion angle is swept away. The flue gas is easy to burn and damage the nozzle and expanding cone. The combustion system supporting the burner uses a large amount of over-burning air. Usually, the over-burning air accounts for more than 25% of the total air supply, which is easy to cause excessive oxygen-deficient combustion in the furnace area, which is easy to cause high temperature corrosion and delayed combustion. The amount of desuperheating water in the boiler increases or even fully opens, and the economy of the boiler becomes poor. The total secondary air adjustment sleeve of the burner is arranged in the dusty environment of the boiler wind box. The adjustment device of the annular hinge structure often jams, which makes the burner The structure of the non-adjustable burner swirl intensity blade adjusts the angle through the hoop hinge structure, because it is arranged in the dusty environment of the boiler bellows, it is easy to jam and the burner cannot be adjusted.
为此本申请提供了一种煤粉旋流燃烧器,包括:沿径向从内向外依次布置的一次风通道10、内二次风通道30和外二次风通道20,一次风通道10的出风口设置有喷嘴40,燃烧器还包括用于控制和调节二次风的调风器50。本申请的煤粉旋流燃烧器无中心风设计,在燃烧器喷口形成更大的还原性区域,进入炉膛的煤粉的快速着火和快速升温,在有限的时间内,可释放出煤种中更多CH基团,用以来还原燃烧器主燃区所生成的NOx,实现火焰内还原降低NOx。To this end, the present application provides a pulverized coal swirl burner, comprising: a
如图1所示,本申请的煤粉旋流燃烧器,包括:沿径向从内向外依次布置的一次风通道10、内二次风通道20和外二次风通道30,一次风通道10的出风口设置有喷嘴40,煤粉旋流燃烧器为均流燃烧器,燃烧器还包括用于控制和调节二次风的调风器50。其中,调风器50包括外二次风套筒挡板51和外二次风套筒挡板调节部57、外二次风旋流叶片53和外二次风旋流叶片调节部58。相比较常规的燃烧器通过调整叶片角度来控制总的进风量和旋流强度的设计,本申请实现了二次风总风量和外二次风旋流强度单独控制。As shown in FIG. 1 , the pulverized coal swirl burner of the present application includes: a
外二次风套筒挡板51套设在外二次风通道20的进风口处,外二次风套筒挡板调节部57可驱动外二次风套筒挡板51在轴向方向的预定范围内移动以调节外二次风通道20的进风口的开度进而控制进入燃烧器内部的总二次风量。The outer secondary
外二次风旋流叶片53环向设置在外二次风通道20中,外二次风旋流叶片调节部58可驱动外二次风旋流叶片53以调节外二次风旋流叶片53在轴向方向上的位置以调节通过外二次风旋流叶片53旋流增强的外二次风风量。外二次风旋流叶片调节部58将外旋流叶片53移动到外二次风通道20内部,从外二次风通道20的进风口进入的全部外二次风均通过外二次风旋流叶片53旋流增强,外二次风旋流叶片调节部58将外旋流叶片53移动到外二次风通道20的进风口,从外二次风通道20的进风口进入外二次风无法全部通过外二次风旋流叶片53,进而达到调节外二次风旋流强度的效果。The outer secondary
作为一种示例,外二次风通道20中设置有环外二次风通道20周向分布的若干个外旋流叶片53,若干个外旋流叶片53设置在环外二次风通道20周向设置的叶片底座上与叶片底座连接成一个整体,外二次风旋流叶片调节部58与叶片底座连接驱动叶片底座可整体驱动外旋流叶片53在外二次风通道20移动。As an example, the outer
作为一种示例,调风器50还包括套设在内二次风通道30的进风口处的内二次风套筒挡板54和内二次风套筒挡板调节部59;内二次风套筒挡板调节部59可驱动内二次风套筒挡板54在轴向方向上移动以调节内二次风通道30的进风口的开度进而控制进入内二次风通道30中的内二次风量。As an example, the
作为一种示例,内二次风通道30中设置有环内二次风通道30周向分布的若干个内旋流叶片56。As an example, the inner
基于上述示例,一种可行的实施方式中,内旋流叶片56在内二次风通道30中的位置固定,进入内二次风通道30中的内二次风全部通过内旋流叶片56旋流增强。Based on the above example, in a feasible implementation, the position of the
作为一种示例,如图1所示,外二次风套筒挡板调节部57包括沿燃烧器轴向设置的轮滑导轨571、装配在轮滑导轨571中的轮滑装置572以及外二次风套筒挡板拉杆573,外二次风套筒挡板51与轮滑装置572安装连接,外二次风套筒挡板拉杆与轮滑装置572连接可推动轮滑装置在轮滑导轨571中滑动进而移动外二次风套筒挡板51的位置。As an example, as shown in FIG. 1 , the outer secondary air sleeve
其中,轮滑导轨571可以根据装置需要设置为单轨轨道或双轨轨道,轮滑导轨571沿轴向方向设置在外二次风道20顶部,外二次风套筒挡板51可沿着轮滑导轨571滑动调节外二次风道20的进风口的开度,本申请的调节进入外二次风道20中的总二次风风量的方式更适宜锅炉多灰风道运行环境,调节方式灵活、不易卡涩,能够保障长时间灵活可调。Among them, the
基于上述示例,一种可行的实施方式中,本申请的燃烧器设置在燃烧器支架上,轮滑导轨571与燃烧器支架连接悬挂设置在燃烧器的外二次风道20的上方。Based on the above example, in a feasible implementation manner, the burner of the present application is arranged on the burner bracket, and the
基于上述示例,外二次风旋流叶片调节部58和内二次风套筒挡板调节部59均可以设计为推动拉杆。Based on the above examples, both the outer secondary air swirl
其中,外二次风通道20的进风口安装有外二次风均流筒52,外二次风均流筒52与外二次风通道20连通且表面密布有均流孔,二次风通过外二次风均流筒52周向进入外二次风道20向外二次风通道20中均匀进风,外二次风通道20的出风口的外二次风与一次风通道10喷出的一次风中的煤粉均衡燃烧,能够有效避免燃烧器火焰偏烧的情况发生。Wherein, the air inlet of the outer
进一步的,内二次风通道30的进风口安装有内二次风均流套筒55,内二次风均流筒55与内二次风通道30连通且表面密布有均流孔,部分外二次风通过内二次风均流套筒55周向进入内二次风道30向内二次风道30周向均匀进风,从内二次风通道30的出风口喷出的内二次风与一次风通道10喷出的一次风中的煤粉均衡燃烧,能够有效避免燃烧器火焰偏烧的情况发生。Further, the air inlet of the inner
作为一种示例,本申请的煤粉旋流燃烧器的喷嘴40包括若干沿周向交替设置的内缩部41和外扩部42,内缩部41和外扩部42沿一次风的流向延伸,且内缩部41沿喷嘴40的径向收缩、外扩部42沿所述喷嘴40的径向外扩。在此条件下,外扩部42与相邻的两个内缩部41形成切割通道,一次风通道10中的一次风进入喷嘴40后通过切割通道被切割成若干股煤粉气流,扩大了煤粉气流与炉膛高温烟气的接触面积,快速提高了煤粉气流的温升速率和温度,强化了煤粉气流的着火效率,有助于煤粉中挥发分的早期大量析出,同时,本申请的燃气器无中心风通道,多股煤粉气流可在燃烧器喷口区域形成更大的还原性区域,控制了燃烧器早期NOx的形成。As an example, the
基于上述示例,一种可行的实施方式中,喷嘴40包括4~8个内缩部41以及外扩部42,喷嘴40的内缩部41与外扩部42的尺寸相同。一次风通道的一次风煤粉气流进入喷嘴后,被切分为4~8股煤粉气流。Based on the above example, in a feasible implementation, the
基于上述示例,一种可行的实施方式中,喷嘴40的内缩部41自喷嘴40的喷口沿一次风流通相反的方向延伸至一次风通道10内部,内缩部41的延伸长度L为一次风通道10直径D的0.5~1.5。在此条件下,内缩部41的延伸长度足以将进入喷嘴40的一次风切割成若干股,从喷嘴40喷口的一次风与内二次风、外二次风均衡燃烧在喷口形成更大的还原性区域。Based on the above example, in a feasible implementation manner, the
基于上述示例,一种可行的实施方式中,喷嘴40的出口处的流通面积与一次风通道10的流通面积相同,一次风进入喷嘴40中有充足的流通空间,有助于加热煤粉,强化燃烧。Based on the above example, in a feasible implementation, the flow area at the outlet of the
基于上述示例,一种可行的实施方式中,外扩部42在喷嘴的出口处上设置有沿喷嘴40的径向方向向外延伸的稳燃齿43。从内二次风通道30、外二次风通道20喷出的二次风流到稳燃齿43处流向稳燃齿43两侧回流,有助于加热煤粉,强化燃烧。本申请的燃烧器的稳燃齿43沿喷嘴的径向方向向外延伸,与传统的燃烧器在喷嘴内侧设置稳燃齿结构相比,不易烧损喷口,喷嘴使用寿命更长。Based on the above example, in a feasible implementation, the flared portion 42 is provided with
作为一种示例,第一风通道10的进风口与燃烧器弯头连接通过燃烧器弯头60进风,燃烧器弯头60中设置有煤粉均流板61。使得进入第一风通道10的一次风中煤粉浓淡均匀,一次风通道10喷出的一次风中的煤粉能够均匀燃烧,避免一次风中风粉重量不同造成的煤粉聚集,第一风通道10中局部煤粉浓度过浓造成的燃尽效果变差,煤粉浓度过淡富氧造成过高的NOx生产的问题。As an example, the air inlet of the
基于上述示例,一种可行的实施方式中,燃烧器弯头60为直角弯头,燃烧器弯头60包括风粉气流入口、风粉气流出口以及设置在燃烧器弯头60中的煤粉均流板61,煤粉均流板61包括设置于弯头的水平段的第一均流板和倾斜设置在弯头的垂直段的第二均流板,第一均流板水平设置在弯头的水平段的中心线上,第二均流板与第一均流板的夹角为120~150°,从燃烧器弯头的风粉气流入口进入的煤粉气流通过煤粉均流板61,煤粉均流板61阻挡煤粉气流中的煤粉重量较大受离心力作用向上聚集以使进入第一风通道10的一次风中煤粉浓淡均匀。Based on the above example, in a feasible implementation, the
其中,在应用过程中,燃烧器弯头60的结构不限制于实施例中示出的结构,可以根据煤粉类别选用可实现将煤粉浓淡分离的任何燃烧器弯头结构。Wherein, in the application process, the structure of the
作为一种示例,本申请的旋流燃烧器在外二次风通道20的出风口还设置有外二次风扩锥42。As an example, the swirl burner of the present application is further provided with an outer secondary air expanding cone 42 at the air outlet of the outer
需要说明的是,在本文中,术语“包括”、“包含”或者其任何其他变体意在涵盖非排他性的包含,从而使得包括一系列要素的物品或者设备不仅包括那些要素,而且还包括没有明确列出的其他要素,或者是还包括为这种物品或者设备所固有的要素。在没有更多限制的情况下,由语句“包括……”限定的要素,并不排除在包括所述要素的物品或者设备中还存在另外的相同要素。It should be noted that, herein, the terms "comprising", "comprising" or any other variation thereof are intended to encompass non-exclusive inclusion, such that an article or device comprising a list of elements includes not only those elements, but also no Other elements expressly listed, or those inherent to the article or equipment are also included. Without further limitation, an element defined by the phrase "comprising" does not preclude the presence of additional identical elements in the article or device comprising said element.
以上实施例仅用以说明本发明的技术方案而非限制,仅仅参照较佳实施例对本发明进行了详细说明。本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,均应涵盖在本发明的权利要求范围当中。The above embodiments are only used to illustrate the technical solutions of the present invention and not to limit them, and the present invention is only described in detail with reference to the preferred embodiments. It should be understood by those of ordinary skill in the art that the technical solutions of the present invention can be modified or equivalently replaced without departing from the spirit and scope of the technical solutions of the present invention, and should be included in the scope of the claims of the present invention.
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| CN212252597U (en) * | 2020-05-27 | 2020-12-29 | 江苏申港锅炉有限公司 | Pulverized coal cyclone burner |
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