CN201145271Y - Three-stage pulverized coal burner - Google Patents
Three-stage pulverized coal burner Download PDFInfo
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- CN201145271Y CN201145271Y CNU2007200612094U CN200720061209U CN201145271Y CN 201145271 Y CN201145271 Y CN 201145271Y CN U2007200612094 U CNU2007200612094 U CN U2007200612094U CN 200720061209 U CN200720061209 U CN 200720061209U CN 201145271 Y CN201145271 Y CN 201145271Y
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- 239000003245 coal Substances 0.000 title claims abstract description 89
- 238000002485 combustion reaction Methods 0.000 claims abstract description 175
- 230000006641 stabilisation Effects 0.000 claims abstract description 82
- 238000011105 stabilization Methods 0.000 claims abstract description 82
- 238000009841 combustion method Methods 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 9
- 230000000087 stabilizing effect Effects 0.000 description 9
- 239000000203 mixture Substances 0.000 description 5
- 230000009471 action Effects 0.000 description 4
- 238000004939 coking Methods 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000010881 fly ash Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 230000002452 interceptive effect Effects 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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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
Abstract
本实用新型公开了一种三阶煤粉燃烧器,其包括用于输送煤粉和一次风的混合通道、连接于混合通道尾部的稳燃室、以及延伸设置于稳燃室入口端的点火装置,其中,稳燃室包括纵向布置的第一级稳燃腔、第二级稳燃腔以及第三级稳燃腔,第一级稳燃腔、第二级稳燃腔以及第三级稳燃腔均为圆筒状结构,第二级稳燃腔的径向尺寸大于第一级稳燃腔及第三级稳燃腔的径向尺寸。本实用新型的稳燃室本体为阶梯型结构,稳燃性强,并采用分级送风旋流燃烧方式,燃烧效率高,NOx排放量低。
The utility model discloses a three-stage pulverized coal burner, which comprises a mixing passage for conveying pulverized coal and primary air, a combustion stabilization chamber connected to the tail of the mixing passage, and an ignition device extended and arranged at the inlet end of the combustion stabilization chamber. Among them, the combustion chamber includes a first-stage combustion chamber, a second-stage combustion chamber and a third-stage combustion chamber arranged longitudinally, and the first-stage combustion chamber, the second-stage combustion chamber and the third-stage combustion chamber They are all cylindrical structures, and the radial dimension of the second-stage combustion stabilization chamber is larger than the radial dimensions of the first-stage combustion stabilization chamber and the third-stage combustion stabilization chamber. The stable combustion chamber body of the utility model has a stepped structure, which has strong combustion stability, and adopts a graded air-supply swirling combustion method, with high combustion efficiency and low NOx emissions.
Description
技术领域 technical field
本实用新型涉及一种燃烧装置,尤其是涉及一种煤粉燃烧器。The utility model relates to a combustion device, in particular to a pulverized coal burner.
背景技术 Background technique
我国是一个以煤为主要燃料的国家,这种状况在今后相当长一段时间内不会发展根本性的变化。目前煤炭占我国能源总需求的70%左右,在我国煤炭资源中低挥发份煤(如无烟煤、贫煤等)和劣质煤占很大的比重,在这些煤炭的使用过程中存在一些问题,一是锅炉燃烧器对于煤质及负荷变化的适应性差,当锅炉高负荷运行时,炉内结焦比较严重,而当锅炉低负荷运行时,燃烧又难以稳定,燃烬率低,造成对能源的浪费和环境的污染;二是未燃烬的煤粉粒子对燃烧器内壁面产生挂壁现象,从而产生结焦和高温腐蚀现象,大大降低了燃烧器的使用寿命;三是煤粉燃烧器在燃烧过程中将产生大量的NOx,对环境造成巨大的污染。my country is a country that uses coal as its main fuel, and this situation will not change fundamentally for a long time to come. At present, coal accounts for about 70% of China's total energy demand. Low-volatile coal (such as anthracite, lean coal, etc.) and low-quality coal account for a large proportion of China's coal resources. There are some problems in the use of these coals. The reason is that the boiler burner has poor adaptability to coal quality and load changes. When the boiler is operating at high load, the coking in the furnace is serious. When the boiler is operating at low load, the combustion is difficult to stabilize and the burnout rate is low, resulting in waste of energy. and environmental pollution; the second is that the unburned pulverized coal particles will hang on the inner wall of the burner, resulting in coking and high-temperature corrosion, which greatly reduces the service life of the burner; A large amount of NO x will be produced, which will cause huge pollution to the environment.
如中国专利第CN 93244359.1号所揭示的一种径向浓淡旋流煤粉燃烧器,它包括一浓煤粉通道,一个具有环状空间的淡煤粉通道和一个具有环状空间的二次风管道,二次风管道的环状空间中安装有旋流器,浓煤粉通道的入口通过输送管与煤粉浓缩器的浓煤粉出口通道、其出口通过火嘴与炉膛连通,煤粉浓缩器的入口接一次风道,二次风管道的入口连通二次风道、其出口与炉膛连通,其特征在于浓煤粉通道,淡煤粉通道和二次风管道由里向外依次排列,淡煤粉通道的环状空间中安装有旋流器。但是,这种径向浓淡旋流煤粉燃烧器中心管的煤粉磨损非常大,需要经常换管,而且煤粉浓缩器在负荷变化较大时,容易发生堵粉现象。As disclosed in Chinese Patent No. CN 93244359.1, a radial thick-lean swirl pulverized coal burner includes a thick pulverized coal channel, a light pulverized coal channel with an annular space and a secondary air with an annular space. Pipeline, the cyclone is installed in the annular space of the secondary air pipe, the inlet of the thick coal powder channel is connected with the thick coal powder outlet channel of the coal powder concentrator through the conveying pipe, and its outlet is connected with the furnace through the burner, and the coal powder is concentrated The inlet of the device is connected to the primary air duct, the entrance of the secondary air duct is connected to the secondary air duct, and its outlet is connected to the furnace. A cyclone is installed in the annular space of the light coal powder channel. However, the pulverized coal wear of the central tube of the radial thick-lean swirling pulverized coal burner is very large, and the tube needs to be replaced frequently, and the pulverized coal concentrator is prone to clogging when the load changes greatly.
又如中国专利第CN 98117424.8号所揭示的一种煤粉燃烧器,它包括一个喷射煤粉和一次风混合物的煤粉喷嘴,一个二次风喷嘴和一个三次风喷嘴,它们围绕煤粉喷嘴的外周边同轴布置,和一个在分隔两个邻近的空气喷嘴的分隔壁的末端的管道扩展部分;设置一个变换二次风喷嘴中二次风的流动变换装置,以便使二次风沿管道扩展部分流动。二次风由于导向板朝外喷射,二次风、三次风与煤粉混合延迟,由此产生的NOx的量减少。虽然这种煤粉燃烧器有效能降低NOx的排放量,但对于煤种的适应性比较差,对于难以着火的低挥发份煤和劣质煤稳燃性差,且同样存在煤粉喷嘴磨损严重的问题。Another example is a pulverized coal burner disclosed in Chinese Patent No. CN 98117424.8, which includes a pulverized coal nozzle for injecting a mixture of pulverized coal and primary air, a secondary air nozzle and a tertiary air nozzle, which surround the pulverized coal nozzle. Arranged coaxially at the outer periphery, and a duct extension at the end of the partition wall separating two adjacent air nozzles; providing a flow changing device for transforming the secondary air in the secondary air nozzle so that the secondary air expands along the duct Partial flow. Due to the outward injection of the secondary air by the guide plate, the mixing of the secondary air, the tertiary air and the pulverized coal is delayed, and the amount of NO x produced thereby is reduced. Although this kind of pulverized coal burner can effectively reduce the emission of NOx , it has poor adaptability to coal types, poor combustion stability for low-volatile coal and low-quality coal that are difficult to ignite, and there is also the problem of severe wear of pulverized coal nozzles. question.
针对我国环保要求不断提高以及我国市场上大量着火难、稳燃难、燃烬更难的低挥发份煤和劣质煤不能有效利用的实际情况,提供一种煤种适应性强、负荷调节范围大、低NOx排放、燃烧效率高且使用寿命长的煤粉燃烧器成为业界需要解决的问题。In view of the continuous improvement of China's environmental protection requirements and the fact that a large number of low-volatility coal and low-quality coal that are difficult to catch fire, stable combustion, and more difficult to burn can not be effectively utilized in the Chinese market, a coal type with strong adaptability and a large load adjustment range is provided. Pulverized coal burners with low NOx emissions, high combustion efficiency and long service life have become problems that the industry needs to solve.
发明内容 Contents of the invention
本实用新型的目的在于提供一种低负荷稳燃能力强、煤种适应性好、燃烧效率高、NOx排放量低的三阶煤粉燃烧器。The purpose of the utility model is to provide a three-stage pulverized coal burner with strong low-load stable combustion capability, good coal type adaptability, high combustion efficiency and low NO x emission.
本实用新型的技术方案是这样实现的:提供一种三阶煤粉燃烧器,包括用于输送煤粉和一次风的混合通道、连接于混合通道尾部的稳燃室、以及延伸设置于稳燃室入口端的点火装置,其中,稳燃室包括纵向布置的第一级稳燃腔、第二级稳燃腔以及第三级稳燃腔,第一级稳燃腔、第二级稳燃腔以及第三级稳燃腔均为圆筒状结构,第二级稳燃腔的径向尺寸大于第一级稳燃腔及第三级稳燃腔的径向尺寸。The technical scheme of the utility model is achieved by providing a three-stage pulverized coal burner, including a mixing channel for conveying pulverized coal and primary air, a combustion stabilization chamber connected to the tail of the mixing channel, and a combustion stabilization chamber extended to The ignition device at the entrance of the chamber, wherein the combustion chamber includes a longitudinally arranged first-stage combustion chamber, a second-stage chamber and a third chamber, the first chamber, the second chamber and The third-stage combustion stabilization chambers are all cylindrical structures, and the radial dimension of the second-stage combustion stabilization chamber is larger than the radial dimensions of the first-stage combustion stabilization chamber and the third-stage combustion stabilization chamber.
优选地,第一级稳燃腔、第二级稳燃腔以及第三级稳燃腔大致布置在同一条轴心线上。Preferably, the first-stage combustion stabilization chamber, the second-stage combustion stabilization chamber and the third-stage combustion stabilization chamber are roughly arranged on the same axis.
更优选地,第一级稳燃腔沿切线方向设置两个或两个以上的用于向第一级稳燃腔内输送第一级二次风的第一级二次风管。第二级稳燃腔沿切线方向设置两个或两个以上的用于向第二级稳燃腔内输送第二级二次风的第二级二次风管。第三级稳燃腔沿切线方向设置两个或两个以上的用于向第三级稳燃腔内输送第三级二次风的第三级二次风管。More preferably, the first-stage combustion stabilization chamber is provided with two or more first-stage secondary air ducts along the tangential direction for delivering the first-stage secondary air into the first-stage combustion stabilization chamber. Two or more second-stage secondary air pipes for delivering second-stage secondary air into the second-stage combustion-stabilizing chamber are arranged along the tangential direction in the second-stage combustion-stabilizing chamber. The third-stage combustion stabilization chamber is provided with two or more third-stage secondary air pipes for delivering the third-stage secondary air into the third-stage combustion stabilization chamber along the tangential direction.
其中,第三级稳燃腔的径向尺寸大于第一级稳燃腔的径向尺寸。可选择地,第二级稳燃腔的径向尺寸为第一级稳燃腔径向尺寸的1.5倍到3倍,比如1.8倍或2倍;第三级稳燃腔的径向尺寸为第一级稳燃腔径向尺寸的1倍到1.5倍,比如1.2或1.3倍。Wherein, the radial dimension of the third-stage combustion stabilization chamber is larger than the radial dimension of the first-stage combustion stabilization chamber. Optionally, the radial dimension of the second-stage combustion stabilization chamber is 1.5 to 3 times the radial dimension of the first-stage combustion stabilization chamber, such as 1.8 times or 2 times; the radial dimension of the third-stage combustion stabilization chamber is the first 1 to 1.5 times, such as 1.2 or 1.3 times, the radial dimension of the primary stable combustion chamber.
可选择地,第二级稳燃腔的纵向尺寸为第一级稳燃腔纵向尺寸的1倍到2倍,比如1.2倍或1.5倍;第三级稳燃腔的纵向尺寸为第一级稳燃腔纵向尺寸的1倍到2倍,比如1.5或2倍。Optionally, the longitudinal dimension of the second-stage combustion stabilization chamber is 1 to 2 times the longitudinal dimension of the first-stage combustion stabilization chamber, such as 1.2 times or 1.5 times; the longitudinal dimension of the third-stage combustion stabilization chamber is the first-stage stabilization chamber. 1 to 2 times the longitudinal size of the combustion chamber, such as 1.5 or 2 times.
优选地,进一步设置一个三次风道,三次风道围绕稳燃室的外壁设置并从稳燃室的入口端延伸到稳燃室的出口端。更优选地,三次风道的尾部向内收缩形成圆锥段。Preferably, a tertiary air channel is further provided, the tertiary air channel is arranged around the outer wall of the stabilizing chamber and extends from the inlet end of the stabilizing chamber to the outlet end of the stabilizing chamber. More preferably, the tail of the tertiary air channel shrinks inward to form a conical section.
优选地,混合通道与第一级稳燃腔连接处设置扰流叶片。Preferably, spoiler vanes are provided at the connection between the mixing channel and the first-stage combustion stabilization chamber.
具体地,点火装置包括点火油枪,点火油枪的末端延伸设置在稳燃室入口端的中央处,扰流叶片环绕点火油枪设置。Specifically, the ignition device includes an oil ignition gun, the end of the oil ignition gun is extended to the center of the inlet end of the stable combustion chamber, and the spoiler vanes are arranged around the oil ignition gun.
本实用新型三阶煤粉燃烧器的使用方法如下:(一)、通过混合通道向稳燃室内输送煤粉以及占煤粉完全燃烧所需空气总量5%~15%的一次风;(二)、通过第一级二次风管向第一级稳燃腔内输送占煤粉完全燃烧所需空气总量10%~20%的第一级二次风;(三)、通过第二级二次风管向第二级稳燃腔内输送占煤粉完全燃烧所需空气总量45%~55%的第二级二次风;(四)、通过第三级二次风管向第三级稳燃腔内输送占煤粉完全燃烧所需空气总量20%~30%的第三级二次风;(五)、启动点火装置点火。其中,根据具体需要,上述步骤可以同步进行也可以分步进行,各步骤执行的顺序不受上述排列顺序的限制。The using method of the third-order pulverized coal burner of the present utility model is as follows: (1), transport pulverized coal and account for the primary wind of 5%~15% of the total amount of air needed for the complete combustion of pulverized coal to the stable combustion chamber through the mixing channel; (2) ), through the first-stage secondary air pipe to deliver the first-stage secondary air that accounts for 10% to 20% of the total amount of air required for the complete combustion of pulverized coal to the first-stage stable combustion chamber; (3), through the second-stage The secondary air pipe transports the secondary air of the second stage accounting for 45% to 55% of the total amount of air required for the complete combustion of pulverized coal to the second-stage stable combustion chamber; (4), through the third-stage secondary air pipe to the The third-stage secondary air that accounts for 20% to 30% of the total amount of air required for complete combustion of pulverized coal is transported in the three-stage stable combustion chamber; (5) Start the ignition device to ignite. Wherein, according to specific needs, the above steps can be performed synchronously or step by step, and the execution order of each step is not limited by the above arrangement order.
优选地,在煤粉与一次风混合物进入稳燃室之前采用扰流叶片使煤粉与一次风混合物形成旋流。更优选地,该方法进一步包括向三次风道内输送三次风。Preferably, before the mixture of pulverized coal and primary air enters the stabilizing chamber, spoiler blades are used to make the mixture of pulverized coal and primary air swirl. More preferably, the method further includes delivering tertiary air into the tertiary air duct.
在本实用新型中,煤粉燃烧所需要的空气分为五级送风,分别为一次风、第一级二次风、第二级二次风、第三级二次风以及三次风,其中一次风、第一级二次风、第二级二次风和第三级二次风为旋流风,一次风通过扰流叶片实现旋流。第一级二次风、第二级二次风和第三级二次风通过第一级二次风管、第二级二次风管和第三级二次风管分别切向进入第一级稳燃腔、第二级稳燃腔及第三级稳燃腔而实现旋流。其中,第一级二次风的作用在于点火助燃,第二级二次风的作用在于实现强旋流稳燃,第三级二次风的作用在于使煤粉燃烬。三次风道环绕燃烧器外壁安装,其内的三次风为直流风,其作用在于一方面冷却燃烧器外壁,一方面调节燃烧器产生火焰的形状。In the utility model, the air required for pulverized coal combustion is divided into five levels of air supply, which are primary air, first level secondary air, second level secondary air, third level secondary air and tertiary air, among which The primary wind, the first secondary air, the second secondary air and the third secondary air are swirling winds, and the primary wind realizes swirling through spoiler blades. The first-stage secondary air, the second-stage secondary air, and the third-stage secondary air enter the first stage tangentially through the first-stage secondary air pipe, the second-stage secondary air pipe, and the third-stage secondary air pipe respectively. The first-stage stable combustion chamber, the second-stage stable combustion chamber and the third-stage stable combustion chamber realize the swirling flow. Among them, the role of the first level of secondary air is to ignite and support combustion, the role of the second level of secondary air is to achieve strong swirl and stable combustion, and the role of the third level of secondary air is to make the pulverized coal burn. The tertiary air channel is installed around the outer wall of the burner, and the tertiary air in it is straight air, and its function is to cool the outer wall of the burner on the one hand, and to adjust the shape of the flame produced by the burner on the other hand.
本实用新型的有益效果是:一、稳燃室本体为阶梯型结构,稳燃性强,并采用分级送风旋流燃烧方式,燃烧效率高,NOx排放量低。二、通过调节各腔风量,对锅炉低负荷运行具有极强的稳燃能力,因为第一级稳燃腔、第二级稳燃腔以及第三级稳燃腔均为绝热结构,具有良好的保温稳燃作用,是一个优良的蓄热体,也是一个稳定的点火源,最低负荷可调至1/3以下,兼有着火和强化燃烬的双重功能;通过控制各稳燃腔中的氧气浓度来避免高温结焦现象的发生,同时还可以抑制NOx的生成;三、在燃烧器外围设置有风冷夹套(即,三次风道),可根据需要调节风冷夹套的三次风流量防止燃烧器壁面过热,以防止高温腐蚀;四、在燃烧器换热空间内部无中心管等机械部件,无明显的磨损现象发生,进一步提高了燃烧器的使用寿命。The beneficial effects of the utility model are as follows: 1. The body of the stabilizing combustion chamber has a stepped structure, which has strong combustion stabilizing properties, and adopts the staged air supply swirl combustion mode, which has high combustion efficiency and low NO x emission. 2. By adjusting the air volume of each chamber, it has a very strong combustion stability ability for the low-load operation of the boiler, because the first-stage combustion chamber, the second-stage combustion chamber and the third-stage combustion chamber are all heat-insulating structures, which have good The function of heat preservation and stable combustion is an excellent heat storage body and a stable ignition source. The minimum load can be adjusted to less than 1/3, and it has dual functions of ignition and enhanced combustion; by controlling the oxygen in each stable combustion chamber concentration to avoid the occurrence of high-temperature coking, and at the same time suppress the formation of NOx ; 3. An air-cooled jacket (that is, a tertiary air duct) is installed around the burner, and the tertiary air flow of the air-cooled jacket can be adjusted according to needs Prevent overheating of the burner wall to prevent high-temperature corrosion; 4. There is no central tube and other mechanical parts in the heat exchange space of the burner, and no obvious wear occurs, which further improves the service life of the burner.
以下结合附图和实施例,来进一步说明本实用新型,但本实用新型不局限于这些实施例,任何在本实用新型基本精神上的改进或替代,仍属于本实用新型权利要求书中所要求保护的范围。Below in conjunction with accompanying drawing and embodiment, the utility model is further described, but the utility model is not limited to these embodiments, and any improvement or substitution on the basic spirit of the utility model still belongs to the requirement in the claims of the utility model scope of protection.
附图说明 Description of drawings
图1为本实用新型煤粉燃烧器的结构示意图。Fig. 1 is the structural representation of the utility model pulverized coal burner.
具体实施方式 Detailed ways
实施例1Example 1
请参照图1,本实用新型的煤粉燃烧器包括混合通道1、设置于混合通道尾部的扰流叶片2、小型点火油枪3、第一级稳燃腔4、第一级二次风管5、第二级稳燃腔6、第二级二次风管7、第三级稳燃腔8、第三级二次风管9、三次风道10。其中,第一级稳燃腔4、第二级稳燃腔6以及第三级稳燃腔8均为大致位于同一轴心线上的圆筒状结构,第一级稳燃腔4、第二级稳燃腔6以及第三级稳燃腔8纵向分布形成一个稳燃室。Please refer to Figure 1, the pulverized coal burner of the present invention includes a mixing channel 1, a
其中,第二级稳燃腔6的径向尺寸大于第三级稳燃腔8的径向尺寸,第三级稳燃腔8的径向尺寸大于第一级稳燃腔4的径向尺寸。具体地,第二级稳燃腔6的径向尺寸约为第一级稳燃腔4径向尺寸的2倍;第三级稳燃腔8的径向尺寸约为第一级稳燃腔4径向尺寸的1.2倍。Wherein, the radial dimension of the second-stage combustion stabilization chamber 6 is larger than the radial dimension of the third-stage
另外,第二级稳燃腔6的纵向尺寸约为第一级稳燃腔4纵向尺寸的1.2倍;第三级稳燃腔8的纵向尺寸也约为第一级稳燃腔4纵向尺寸的1.2倍。In addition, the longitudinal dimension of the second-stage combustion stabilization chamber 6 is about 1.2 times the longitudinal dimension of the first-stage
其中,一次风和煤粉的混合物在其混合通道1内通过若干扰流叶片2旋流进入第一级稳燃腔4后,在第一级稳燃腔4内煤粉被点火油枪2点燃,在煤粉着火燃烧的开始阶段,只加入部分二次风,即第一级二次风,第一级二次风由第一级二次风管5从第一级稳燃腔4切线方向高速喷出,煤粉在高速旋转的第一级二次风作用下,形成富燃料燃烧的旋涡区,使煤粉迅速着火。着火后的气流进入第二级稳燃腔6,在高速旋流的第二级二次风强烈作用下,在第二级稳燃腔四角部位形成涡流区,在涡流区形成局部高温区,具有极强的稳燃作用。高速旋转的高温烟气进入第三级稳燃腔8,第三级稳燃腔8为煤粉的燃烬区,其内安装有第三级二次风管9,使煤粉在这里完成完全燃烧,大大降低飞灰的含碳量。环绕燃烧室外壁安装有三次风道10,三次风为直流风,其作用一方面在于调节火焰的形状,一方面可避免燃烧室壁面过热,防止高温腐蚀。Among them, the mixture of primary air and coal powder enters the first-stage
本实用新型的工作原理为:一次风和煤粉的混合物通过若干扰流叶片2旋流进入第一级稳燃腔4后,在第一级稳燃腔4内煤粉被点火油枪3点燃。在煤粉着火燃烧的开始阶段,只加入部分二次风,即第一级二次风,煤粉在高速旋转的第一级二次风作用下,形成富燃料燃烧的旋涡区,使煤粉迅速着火。一次风占煤粉完全燃烧所需要的空气的10%左右,第一级二次风占煤粉完全燃烧所需要空气的15%左右,使得在燃烧室入口端附近的煤粉最早着火区形成强烈的还原性气氛,从而有效抑制燃料型NOx的生成。着火后的气流进入第二级稳燃腔,在高速旋流的第二级二次风强烈作用下,在第二级稳燃腔6四角部位形成涡流区,在涡流区形成局部高温区,具有极强的稳燃作用,通过调节风量,使第二级稳燃腔6内部同样处于贫氧燃烧状态,过量空气系数小于0.8,温度不超过1200℃,可进一步抑制热力型NOx的生成,第二级二次风占煤粉完全燃烧所需要空气50%左右。高速旋转的高温烟气进入第三级稳燃腔8,第三级稳燃腔8为煤粉的燃烬区,其内安装有第三级二次风管,以使煤粉在这里完全燃烬,大大降低飞灰的含碳量。环绕燃烧室外壁流动着三次风,三次风为直流风,在三次风道10末端为收缩型圆锥段,其作用在于使三次风形成一段风道圈,防止三次风散流,还可以控制火焰的形状,以适应不同的锅炉,三次风的另外一个作用在于冷却燃烧室外壁。The working principle of the utility model is: after the mixture of primary wind and coal powder enters the first-stage
实施例2Example 2
请参照图2,作为本实用新型的另一种方案,其它部分与实施例1相同,不同之处在于:Please refer to Fig. 2, as another kind of scheme of the present utility model, other parts are identical with embodiment 1, difference is:
不采用三次风道10。第二级稳燃腔6的径向尺寸约为第一级稳燃腔4径向尺寸的1.5倍;第三级稳燃腔8的径向尺寸约为第一级稳燃腔4径向尺寸的1.1倍。第二级稳燃腔6的纵向尺寸约为第一级稳燃腔4纵向尺寸的1.5倍;第三级稳燃腔8的纵向尺寸也约为第一级稳燃腔4纵向尺寸的1.5倍。The
一次风约占煤粉完全燃烧所需空气总量的15%。第一级二次风约占煤粉完全燃烧所需空气总量的20%。第二级二次风约占煤粉完全燃烧所需空气总量的40%。第三级二次风约占煤粉完全燃烧所需空气总量的25%。The primary air accounts for about 15% of the total air required for the complete combustion of pulverized coal. The first secondary air accounts for about 20% of the total air required for the complete combustion of pulverized coal. The secondary air of the second stage accounts for about 40% of the total amount of air required for the complete combustion of pulverized coal. The third secondary air accounts for about 25% of the total amount of air required for the complete combustion of pulverized coal.
实施例3Example 3
作为本实用新型的另一种方案,其它部分与实施例1相同,不同之处在于:As another kind of scheme of the present utility model, other parts are identical with embodiment 1, and difference is:
第一级稳燃腔4设置二个第一级二次风管5,第二级稳燃腔6设置四个第二级二次风管7,第三级稳燃腔8设置三个第三级二次风管9。The first-
第二级稳燃腔6的径向尺寸约为第一级稳燃腔4径向尺寸的1.5倍;第三级稳燃腔8的径向尺寸约为第一级稳燃腔4径向尺寸的1.1倍。第二级稳燃腔6的纵向尺寸约为第一级稳燃腔4纵向尺寸的1.5倍;第三级稳燃腔8的纵向尺寸也约为第一级稳燃腔4纵向尺寸的1.5倍。The radial dimension of the second-stage combustion stabilization chamber 6 is about 1.5 times the radial dimension of the first-stage
一次风约占煤粉完全燃烧所需空气总量的8%。第一级二次风约占煤粉完全燃烧所需空气总量的10%。第二级二次风约占煤粉完全燃烧所需空气总量的60%。第三级二次风约占煤粉完全燃烧所需空气总量的22%。The primary air accounts for about 8% of the total air required for the complete combustion of pulverized coal. The first secondary air accounts for about 10% of the total air required for the complete combustion of pulverized coal. The secondary air of the second stage accounts for about 60% of the total amount of air required for the complete combustion of pulverized coal. The third secondary air accounts for about 22% of the total amount of air required for the complete combustion of pulverized coal.
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| CN104896469A (en) * | 2015-05-25 | 2015-09-09 | 山东百川同创能源有限公司 | Process for preparing steam by combusting biomass solid waste and hazardous waste |
| CN105371301A (en) * | 2015-10-08 | 2016-03-02 | 北京航空航天大学 | Staged combustor of high-temperature jet flow ignition self-stabilization flame |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104896469A (en) * | 2015-05-25 | 2015-09-09 | 山东百川同创能源有限公司 | Process for preparing steam by combusting biomass solid waste and hazardous waste |
| CN104896469B (en) * | 2015-05-25 | 2018-09-25 | 山东百川同创能源有限公司 | A kind of biomass class solid waste and dangerous waste are burnt vapour technique processed |
| CN105371301A (en) * | 2015-10-08 | 2016-03-02 | 北京航空航天大学 | Staged combustor of high-temperature jet flow ignition self-stabilization flame |
| CN105371301B (en) * | 2015-10-08 | 2017-12-08 | 北京航空航天大学 | A kind of high temp jet is lighted a fire from the fractional combustion room of steady flame |
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