CN2373685Y - Inertial gradation vortex coal powder burner - Google Patents
Inertial gradation vortex coal powder burner Download PDFInfo
- Publication number
- CN2373685Y CN2373685Y CN 99210456 CN99210456U CN2373685Y CN 2373685 Y CN2373685 Y CN 2373685Y CN 99210456 CN99210456 CN 99210456 CN 99210456 U CN99210456 U CN 99210456U CN 2373685 Y CN2373685 Y CN 2373685Y
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- burner
- pulverized coal
- primary air
- combustion
- concentrator
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- 239000003245 coal Substances 0.000 title claims abstract description 41
- 239000000843 powder Substances 0.000 title abstract description 10
- 238000002485 combustion reaction Methods 0.000 abstract description 22
- 230000002265 prevention Effects 0.000 abstract description 6
- 230000007797 corrosion Effects 0.000 abstract description 5
- 238000005260 corrosion Methods 0.000 abstract description 5
- 238000009826 distribution Methods 0.000 abstract description 5
- 239000007921 spray Substances 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000005536 corrosion prevention Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003933 environmental pollution control Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
本实用新型涉及一种惯性浓淡旋流煤粉燃烧器,该燃烧器的主要特点是在现有燃烧器一次风通道距燃烧器喷口一定距离处安装煤粉浓缩器,一次风粉为直流形式,经过浓缩器后在一次风通道内形成由燃烧器中心一侧至靠近二次风的一侧煤粉浓度由高向低分布,浓缩器距离燃烧器喷口一定距离使一次风粉保持这种分布趋势喷入炉膛。本实用新型同时解决了煤粉燃烧的高效率、稳燃、低NOx排放、防止结渣和防止高温腐蚀的问题。
The utility model relates to an inertial thick-lean swirling pulverized coal burner. The main feature of the burner is that a pulverized coal concentrator is installed at a certain distance from the primary air channel of the existing burner to the nozzle of the burner. The primary air powder is in the form of direct current. After passing through the concentrator, the distribution of pulverized coal concentration from the center side of the burner to the side close to the secondary air is formed in the primary air channel, and the concentration of the concentrator is a certain distance from the nozzle of the burner to keep the distribution trend of the primary air powder. Spray into the furnace. The utility model simultaneously solves the problems of high efficiency of pulverized coal combustion, stable combustion, low NOx discharge, prevention of slagging and prevention of high-temperature corrosion.
Description
本实用新型涉及一种惯性浓淡旋流煤粉燃烧器。The utility model relates to an inertial density swirling pulverized coal burner.
我国是世界上少有的几个能源以煤为主的国家之一,电力工业用煤的特点是煤种多变,煤质较差。在煤粉锅炉燃烧技术中,对煤粉燃烧的基本要求是:高效率、稳燃、低污染、防止结渣和防止高温腐蚀。为节省能源,需保证高效率燃烧;由于我国电厂用煤煤质较差、煤种多变,稳燃问题突出,特别是在低负荷运行时,常常不得不投油助燃,从而增加了发电成本;随着人民生活水平的提高,对环境污染的控制要求越来越高,对煤粉燃烧的低污染要求越来越强烈;燃烧器区的结渣、水冷壁管的高温腐蚀严重威胁着锅炉的安全、经济、稳定运行。而我国有些煤粉燃烧装置虽然可实现变负荷、低NOx燃烧,其一次风弯头分叉分离器位于燃烧器外部,浓相一次风经过浓相燃烧器进入炉膛,而稀相一次风经过稀相一次风口进入炉膛,结构复杂;由于一次风中的稀相一次风(占一次风量的45~65%)未进入浓相燃烧器,使浓相燃烧器供风的过量空气系数小于1,从而影响煤粉的燃烧效率,易造成浓相燃烧器区的结渣及高温腐蚀。my country is one of the few countries in the world where coal is the main source of energy. The coal used in the power industry is characterized by variable coal types and poor coal quality. In the combustion technology of pulverized coal boilers, the basic requirements for pulverized coal combustion are: high efficiency, stable combustion, low pollution, prevention of slagging and prevention of high temperature corrosion. In order to save energy, it is necessary to ensure high-efficiency combustion; due to the poor coal quality and variable coal types used in power plants in my country, the problem of stable combustion is prominent, especially when operating at low loads, oil is often used to support combustion, which increases the cost of power generation ; With the improvement of people's living standards, the requirements for environmental pollution control are getting higher and higher, and the requirements for low pollution in pulverized coal combustion are becoming stronger and stronger; slagging in the burner area and high-temperature corrosion of water-cooled wall tubes seriously threaten the boiler safe, economical and stable operation. Although some pulverized coal combustion devices in my country can achieve variable load and low NOx combustion, the primary air elbow bifurcated separator is located outside the burner, and the dense-phase primary air enters the furnace through the dense-phase burner, while the dilute-phase primary air passes through the dilute phase. The phase primary tuyere enters the furnace, and the structure is complex; because the dilute-phase primary air (accounting for 45-65% of the primary air volume) in the primary air does not enter the dense-phase burner, the excess air coefficient of the air supplied by the dense-phase burner is less than 1, thus Affect the combustion efficiency of pulverized coal, and easily cause slagging and high temperature corrosion in the dense phase burner area.
本实用新型的目的是针对现在技术存在的问题提出一种结构简单、可同时实现煤粉燃烧的高效率、稳燃、低污染、防止结渣和防止高温腐蚀的惯性浓淡旋流煤粉燃烧器。The purpose of this utility model is to propose an inertial thick-lean swirl pulverized coal burner which is simple in structure and can realize high efficiency, stable combustion, low pollution, slagging prevention and high temperature corrosion prevention of pulverized coal combustion at the same time. .
本实用新型的目的是这样实现的,本实用新型由炉膛1、火嘴2、浓缩器3、旋流器4、直流二次风通5、环形隔板6、旋流二次风道7、燃烧器一次风通8、中心管9、一次风输粉管道10、风门挡板11、二次风道12、风门挡板13组成,本发明创造的要点是:在燃烧器一次风通道距燃烧器喷口一定距离处安装煤粉浓缩器。从一次风输粉管道送来的煤粉空气流入燃烧器一次风道8后,以直流的形式经过装在燃烧器一次风通8内的浓缩器3后由原来的煤粉浓度均匀分布变成由燃烧器中心一侧至靠近二次风的一侧煤粉浓度由高向低分布,由于浓缩器3距离炉膛1有一定的距离,且一次风粉为直流,使煤粉由煤粉浓度较高一侧向较低一侧扩散较慢,从而使一次风粉保持这样一种由燃烧器中心向外煤粉浓度由高向低的这种分布趋势由火嘴2喷入炉膛1,二次风通过二次风道12进入燃烧器后分为旋流、直流两部分,它们分别经过旋流二次风道7、直流二次风通5进入炉膛1,调节风门挡板11、13的开度,可以改变旋流二次风、直流二次风的比例。靠近燃烧器中心的煤粉气流煤粉浓度较高,进入高温回流区,进而形成高温、高浓度区域,有利于煤粉着火和火焰稳定。由于煤粉气流形成了浓淡分布,同时二次风也分成了旋流和直流两股,燃料偏离燃烧及二次风分级燃烧能有效抑制NOx的形成,降低NOx的排放。内侧较高煤粉浓度的煤粉气流着火后,外侧较低煤粉浓度的煤粉气流、二次风及时混入,保证了燃烧所需的氧,符合随燃烧进行供风的原则,且一次风粉一次风率不变,保证了高效燃烧。新型燃烧器一次风粉为直流,煤粉向燃烧器中心集中,从而在燃烧器区水冷壁附近形成了较强的氧化性气氛,而灰的熔点在氧化性气氛下较高,从而防止了结渣,防止形成了高温腐蚀。The purpose of this utility model is achieved in this way. The utility model consists of a furnace 1, a burner 2, a concentrator 3, a cyclone 4, a direct current secondary air passage 5, an annular partition 6, a swirl secondary air duct 7, Burner primary air passage 8, central pipe 9, primary air powder delivery pipe 10, damper baffle 11, secondary air duct 12, damper baffle 13, the main points of the invention are: in the primary air passage of the burner, the combustion Install a pulverized coal concentrator at a certain distance from the nozzle. After the pulverized coal air sent from the primary air powder conveying pipeline flows into the primary air duct 8 of the burner, it passes through the concentrator 3 installed in the primary air duct 8 of the burner in the form of direct current, and then changes from the original uniform distribution of pulverized coal concentration to The concentration of pulverized coal is distributed from high to low from the side of the center of the burner to the side close to the secondary air. Since the concentrator 3 is a certain distance from the furnace 1, and the primary air is direct current, the pulverized coal concentration is higher than that of the pulverized coal. The diffusion from the high side to the lower side is slower, so that the primary air powder maintains such a distribution trend of coal powder concentration from high to low from the center of the burner to the outside. The burner 2 is sprayed into the furnace 1, and the secondary After the wind enters the burner through the secondary air duct 12, it is divided into two parts: swirling flow and direct flow. They enter the furnace 1 through the swirling secondary air duct 7 and the direct current secondary air passage 5 respectively, and the opening of the damper baffles 11 and 13 is adjusted. The ratio of swirling secondary air and direct current secondary air can be changed. The pulverized coal flow near the center of the burner has a high concentration of pulverized coal, and enters the high-temperature recirculation zone, forming a high-temperature, high-concentration zone, which is conducive to the ignition of pulverized coal and flame stability. Since the pulverized coal air flow forms a density distribution, and the secondary air is also divided into swirl and direct flow, the fuel deviation combustion and secondary air staged combustion can effectively inhibit the formation of NOx and reduce NOx emissions. After the pulverized coal airflow with higher pulverized coal concentration on the inside is on fire, the pulverized coal airflow with lower pulverized coal concentration outside and the secondary air are mixed in time to ensure the oxygen required for combustion, which conforms to the principle of air supply with combustion, and the primary air The primary air rate of the powder remains unchanged, which ensures efficient combustion. The primary air powder of the new burner is direct flow, and the coal powder is concentrated to the center of the burner, thus forming a strong oxidizing atmosphere near the water wall in the burner area, and the melting point of ash is higher in the oxidizing atmosphere, thus preventing slagging , to prevent the formation of high temperature corrosion.
本实用新型同时解决了煤粉燃烧的高效率、稳燃、低NOx排放、防止结渣和防止高温腐蚀,这对我国特有的劣质煤的高效、低污染利用有非常积极的作用。The utility model simultaneously solves the problems of high efficiency, stable combustion, low NOx emission, slagging prevention and high temperature corrosion prevention of pulverized coal combustion, which has a very positive effect on the efficient and low-pollution utilization of my country's unique low-quality coal.
图1为本实用新型原理结构图Fig. 1 is a schematic structure diagram of the utility model
实施例:本实用新型中浓缩器结构可多种多样,如采用一个或几个锥形叶片构成百叶窗式煤粉浓缩器,煤粉浓度均匀的煤粉气流经过锥形叶片时,由于颗粒与叶片碰撞产生气固分离,从而形成由燃烧器中心一侧至靠近二次风的一侧煤粉浓度由高向低分布。Embodiment: The structure of the concentrator in the utility model can be varied, such as adopting one or several conical blades to form a louver type pulverized coal concentrator. The collision produces gas-solid separation, thus forming a distribution of pulverized coal concentration from high to low from the side of the burner center to the side close to the secondary air.
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CN 99210456 CN2373685Y (en) | 1999-05-12 | 1999-05-12 | Inertial gradation vortex coal powder burner |
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CN 99210456 CN2373685Y (en) | 1999-05-12 | 1999-05-12 | Inertial gradation vortex coal powder burner |
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CN2373685Y true CN2373685Y (en) | 2000-04-12 |
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CN 99210456 Expired - Fee Related CN2373685Y (en) | 1999-05-12 | 1999-05-12 | Inertial gradation vortex coal powder burner |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101363625B (en) * | 2008-09-26 | 2010-06-02 | 哈尔滨工业大学 | A center-feeding swirl pulverized coal burner with large speed ratio |
CN101832551A (en) * | 2010-06-18 | 2010-09-15 | 上海交通大学 | Adjustable center weak swirl pulverized coal burner |
CN104197326A (en) * | 2014-07-15 | 2014-12-10 | 北京神雾环境能源科技集团股份有限公司 | Novel swirl pulverized coal burner |
CN111023148A (en) * | 2020-01-14 | 2020-04-17 | 薛芳 | Adjustable spiral multi-stage oil-free coal powder igniter |
-
1999
- 1999-05-12 CN CN 99210456 patent/CN2373685Y/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101363625B (en) * | 2008-09-26 | 2010-06-02 | 哈尔滨工业大学 | A center-feeding swirl pulverized coal burner with large speed ratio |
CN101832551A (en) * | 2010-06-18 | 2010-09-15 | 上海交通大学 | Adjustable center weak swirl pulverized coal burner |
CN104197326A (en) * | 2014-07-15 | 2014-12-10 | 北京神雾环境能源科技集团股份有限公司 | Novel swirl pulverized coal burner |
CN111023148A (en) * | 2020-01-14 | 2020-04-17 | 薛芳 | Adjustable spiral multi-stage oil-free coal powder igniter |
CN111023148B (en) * | 2020-01-14 | 2024-06-07 | 薛芳 | Adjustable screw type multi-stage oil-free coal powder igniter |
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C19 | Lapse of patent right due to non-payment of the annual fee | ||
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