CN101101115A - A small amount of oil gasification combustion side-ignition center-feeding powder swirl burner - Google Patents
A small amount of oil gasification combustion side-ignition center-feeding powder swirl burner Download PDFInfo
- Publication number
- CN101101115A CN101101115A CNA2007100725773A CN200710072577A CN101101115A CN 101101115 A CN101101115 A CN 101101115A CN A2007100725773 A CNA2007100725773 A CN A2007100725773A CN 200710072577 A CN200710072577 A CN 200710072577A CN 101101115 A CN101101115 A CN 101101115A
- Authority
- CN
- China
- Prior art keywords
- burner
- oil gun
- air channel
- main oil
- truncated cone
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Abstract
一种小油量气化燃烧侧向点燃中心给粉旋流燃烧器,它涉及一种旋流燃烧器。本发明的目的是为解决目前采用旋流燃烧器的大型煤粉锅炉在降低NOx排放的同时电站锅炉启动、停止以及低负荷稳燃情况下的节油问题。本发明第一圆锥台形分离环、第二圆锥台形分离环和第三圆锥台形分离环依次设置在燃烧器一次风道内的中部,倒“V”形隔板固定在第三圆锥台形分离环右侧的燃烧器一次风道内。本发明大大减少了煤粉燃烧所需引燃能量,满足了锅炉启、停及低负荷稳燃的需求。煤粉在低氧还原性气氛下燃烧,延长煤粉的停留时间,可控制燃烧型NOx的生成。由于二次风被分成了内、外两部分,因而形成了分级燃烧,与中心给粉相结合,实现了低NOx排放。
The utility model relates to a small-volume oil gasification combustion side-ignition center powder feeding swirl burner, which relates to a swirl burner. The purpose of the present invention is to solve the problem of fuel saving in the case of starting, stopping and low-load stable combustion of a large pulverized coal boiler using a swirl burner while reducing NOx emissions. In the present invention, the first truncated conical separating ring, the second truncated conical separating ring and the third truncated conical separating ring are sequentially arranged in the middle of the primary air duct of the burner, and the inverted "V"-shaped partition is fixed on the right side of the third truncated conical separating ring in the primary air duct of the burner. The invention greatly reduces the ignition energy required for pulverized coal combustion, and satisfies the requirements of boiler startup and shutdown and low-load stable combustion. Pulverized coal is burned in a low-oxygen reducing atmosphere, prolonging the residence time of pulverized coal and controlling the generation of combustion-type NOx. Since the secondary air is divided into inner and outer parts, staged combustion is formed, and combined with central powder feeding, low NOx emissions are achieved.
Description
技术领域technical field
本发明涉及一种旋流燃烧器。The invention relates to a swirl burner.
背景技术Background technique
在我国运行的大容量电站锅炉中,锅炉点火和低负荷稳燃用油量巨大,发电企业为了节约燃油,节油重点由低负荷稳燃过程转向锅炉点火与停炉过程(电厂锅炉启停时耗油占60%,低负荷稳燃耗油占40%)。按照传统方式,点火油枪布置在燃烧器的二次风口中,油枪与煤粉喷口的距离比较远,而且这两股气流又互相平行,因此在点火时,燃油产生的热量直接用于加热煤粉的部分比较少,热量利用率低,使得锅炉点火时,燃油的消耗量很大。微油点火技术是一种应用于电厂锅炉启动、停止以及低负荷稳燃的新方法。中国专利号为ZL200520145352.2、授权公告号为CN2854368、授权公告日为2007年1月3日的实用新型专利公开了一种“宽煤种微油点火燃烧器”。该装置结构简单,稳定可靠,不爆燃,不结焦,点火出力大,速度快,节油率可达90%以上,适合各种类型的煤粉。中国专利申请号为200610053092.5、公开号为CN1912462、公开日为2007年2月14日的发明专利公开了一种“微油冷炉点火和超低负荷稳燃且具有低NOx排放的旋流燃烧器”,通过该装置节油率达95%以上,具有低负荷和超低负荷稳燃能力。但是这两种装置的油枪都伸入燃烧器一次风道内。燃烧器运行时,油枪套管长时间处于煤粉颗粒的冲刷,易造成主油枪套管的磨损,一旦产生磨损,小油点火将无法启动,不易满足所要求的使用寿命,而大机组对设备的使用寿命要求是较高的。另一方面,两种装置的多级燃烧室位于导流锥或煤粉浓缩器后且与油枪出口相连,整套油枪燃烧装置占据燃烧器一次风管道中心一定的面积,在停用油枪时,煤粉浓缩器浓缩的煤粉集中在中心回流区的外侧,使NOx没有最大限度的降低。In the large-capacity power plant boilers operating in my country, the amount of oil used for boiler ignition and low-load stable combustion is huge. In order to save fuel, power generation companies shift the focus of fuel saving from the low-load stable combustion process to the boiler ignition and shutdown process (when the power plant boiler starts and stops Fuel consumption accounts for 60%, low-load stable fuel consumption accounts for 40%). According to the traditional method, the ignition oil gun is arranged in the secondary air port of the burner. The distance between the oil gun and the pulverized coal nozzle is relatively far, and the two airflows are parallel to each other. Therefore, the heat generated by the fuel oil is directly used for heating during ignition. The part of pulverized coal is relatively small, and the heat utilization rate is low, so that when the boiler is ignited, the fuel consumption is very large. Micro-oil ignition technology is a new method applied to power plant boiler start-up, stop and low-load stable combustion. The utility model patent whose Chinese patent number is ZL200520145352.2, authorized announcement number is CN2854368, and authorized announcement date is January 3, 2007 discloses a kind of "wide coal type micro-oil ignition burner". The device is simple in structure, stable and reliable, does not deflagrate, does not coke, has large ignition output, fast speed, and the fuel saving rate can reach more than 90%, and is suitable for various types of pulverized coal. The Chinese patent application number is 200610053092.5, the publication number is CN1912462, and the invention patent published on February 14, 2007 discloses a swirling flow burner with "micro-oil cold furnace ignition, ultra-low load stable combustion and low NOx emissions" ", through this device, the fuel saving rate can reach more than 95%, and it has low-load and ultra-low-load stable combustion capabilities. But the oil guns of these two devices all extend into the primary air duct of the burner. When the burner is running, the casing of the oil gun is scoured by pulverized coal particles for a long time, which will easily cause the wear of the casing of the main oil gun. Once the wear occurs, the ignition of the small oil will not start, and it is difficult to meet the required service life. The service life requirements of the equipment are relatively high. On the other hand, the multi-stage combustion chamber of the two devices is located behind the diversion cone or the pulverized coal concentrator and is connected to the outlet of the oil gun. The whole set of oil gun combustion device occupies a certain area in the center of the primary air duct of the burner. At this time, the pulverized coal concentrated by the pulverized coal concentrator is concentrated outside the central recirculation zone, so that the NOx is not reduced to the maximum extent.
旋流燃烧器在我国电站锅炉及其它煤粉应用领域占有一定的比例。采用旋流燃烧器的大型煤粉锅炉有其独特的优点:首先可以避免过热器区产生的热偏差;其次是对炉膛形状没有严格的要求。旋流燃烧器靠高温回流区作为稳定的热源,使煤粉气流能够及时着火并稳定燃烧,普通旋流燃烧器一、二次风混合强烈,温度峰值高,氮氧化物(NOx)生成量大。火电厂NOx控制主要有两种途径,一是采用低NOx燃烧技术减少NOx的生成,二是从烟气中脱除NOx,在我国目前的经济水平下,前者较为有效、经济可行的方法;后者的主要问题是投资太高,并不适合于我国国情。随着我国机组日益向大容量发展,对旋流煤粉燃烧技术的发展提出了迫切的要求。因此,研究微油点火旋流燃烧技术对我国电力工业及整个国民经济的发展都是有十分重要的意义。Swirl burners occupy a certain proportion in my country's power plant boilers and other pulverized coal applications. The large pulverized coal boiler with swirl burner has its unique advantages: firstly, it can avoid the thermal deviation in the superheater area; secondly, there is no strict requirement on the shape of the furnace. The swirl burner relies on the high-temperature recirculation zone as a stable heat source, so that the pulverized coal airflow can be ignited in time and burn stably. Ordinary swirl burners have strong mixing of primary and secondary air, high temperature peaks, and large amounts of nitrogen oxides (NOx) . There are two main ways to control NOx in thermal power plants. One is to use low-NOx combustion technology to reduce the generation of NOx, and the other is to remove NOx from flue gas. Under the current economic level of our country, the former is more effective and economically feasible; the latter is the method. The main problem of the investors is that the investment is too high, which is not suitable for our country's national conditions. With the development of large-capacity units in my country, there is an urgent requirement for the development of swirling pulverized coal combustion technology. Therefore, the research on micro-oil ignition swirling combustion technology is of great significance to the development of my country's electric power industry and the entire national economy.
发明内容Contents of the invention
本发明的目的是为解决目前采用旋流燃烧器的大型煤粉锅炉在降低NOx排放的同时电站锅炉启动、停止以及低负荷稳燃情况下的节油问题,以及长时间使用,造成磨损的问题,现提出一种小油量气化燃烧侧向点燃中心给粉旋流燃烧器。本发明由燃烧器一次风道1、第一圆锥台形分离环2-1、第二圆锥台形分离环2-2、第三圆锥台形分离环2-3、内旋流器3、燃烧器内二次风道4、外旋流器5、燃烧器外二次风道6、火嘴7、倒“V”形隔板8、二级燃烧室9、一级燃烧室10、辅助油枪11、主油枪套管12、点火枪13、主油枪14和火检管15组成,燃烧器一次风道1的出口端为火嘴7,燃烧器内二次风道4固定在燃烧器一次风道1出口端的外侧面上,内旋流器3固定在燃烧器一次风道1与燃烧器内二次风道4之间,外旋流器5固定在燃烧器内二次风道4的外侧面上,燃烧器外二次风道6固定在外旋流器5右侧的燃烧器内二次风道4的外侧面上,第一圆锥台形分离环2-1、第二圆锥台形分离环2-2和第三圆锥台形分离环2-3依次设置在燃烧器一次风道1内的中部,倒“V”形隔板8固定在第三圆锥台形分离环2-3右侧的燃烧器一次风道1内,辅助油枪11固定在燃烧器内二次风道4左侧的燃烧器一次风道1上,主油枪套管12固定在辅助油枪11左侧的燃烧器一次风道1上,点火枪13和主油枪14均固定在主油枪套管12内,火检管15固定在主油枪套管12左侧的燃烧器一次风道1上,倒“V”形隔板8右侧的燃烧器一次风道1内形成二级燃烧室9,倒“V”形隔板8的下面形成一级燃烧室10,辅助油枪11、主油枪套管12和火检管15与燃烧器一次风道1连接端均与倒“V”形隔板8下面的一级燃烧室10相连通。本发明的优点是:燃烧器一次风道1位于燃烧器的中心,油枪枪头方向指向煤粉中心,形成高温火焰。从一次风输粉管道送来的煤粉和空气流入燃烧器一次风通道1内的三个圆锥台形分离环后,煤粉被集中到燃烧器的中心,形成高浓度煤粉。部分高浓度煤粉进入一级燃烧室10,点火枪13首先点燃主油枪14,然后主油枪14形成的高温火焰和一级燃烧室10内的浓煤粉颗粒直接接触使煤粉颗粒的特性发生变化,极高的加热速率使挥发份析出速度大大加快,煤粉颗粒温度急剧升高、爆裂、粉碎和剧烈燃烧,然后进入二级燃烧室9与剩余的煤粉颗粒接触并点燃剩余的煤粉,实现了煤粉的分级燃烧,燃烧能量逐级放大,最后经过火嘴7喷入炉膛,达到点火并加速煤粉燃烧的目的,大大减少煤粉燃烧所需引燃能量,满足了锅炉启、停及低负荷稳燃的需求。辅助油枪11、主油枪套管12、点火枪13和主油枪14均在燃烧器一次风管1外,解决了主油枪套管12的磨损问题。火检管15可以随时检测一级燃烧室10内的火焰稳定性。当火焰不稳定时,可以及时启用辅助油枪11,帮助煤粉燃烧。一级燃烧室10的倒V字形隔板外侧始终通有一次风,燃烧器一次风管道外侧始终通有二次风,一、二次风起到风膜冷却的作用,可以冷却一级燃烧室10和二级燃烧室9,防止倒V字形隔板和燃烧器一次风管壁烧损。由于燃烧器一次风管道1内的部件少,占用燃烧器一次风管道1的面积小,对圆锥台形分离环的作用影响不大,停用油枪后燃烧器仍为浓淡燃烧,可正常做低NOx燃烧器使用。二次风通过二次风箱进入燃烧器后分成两部分,它们分别经过燃烧器外二次风道6、燃烧器内二次风道4进入炉膛8,调节内、外旋流器的开度,可以改变内、外旋流二次风的比例,由内旋流器3、外旋流器5使二次风旋转,在燃烧器的中心区域形成中心回流区。煤粉集中喷入位置正对燃烧器的中心回流区中心部分,穿越中心回流区的煤粉量增加,煤粉在低氧还原性气氛下燃烧,延长煤粉的停留时间,可控制燃烧型NOx的生成。由于二次风被分成了内、外两部分,因而形成了分级燃烧,与中心给粉相结合,实现了低NOx排放。因此,本发明是一种节省燃油、低NOx排放的旋流煤粉燃烧装置。The purpose of the present invention is to solve the problem of fuel saving when the large pulverized coal boiler using the swirl burner reduces NOx emissions while the power plant boiler is started, stopped, and low-load stable combustion, and the problem of wear and tear caused by long-term use , a small amount of oil gasification combustion side ignition center to the powder swirl burner is now proposed. The present invention consists of a burner primary air duct 1, a first truncated conical separating ring 2-1, a second truncated conical separating ring 2-2, a third truncated conical separating ring 2-3, an
附图说明Description of drawings
图1是本发明的整体结构主剖视图,图2是图1的A-A剖视图。Fig. 1 is a main sectional view of the overall structure of the present invention, and Fig. 2 is a sectional view along A-A of Fig. 1 .
具体实施方式Detailed ways
具体实施方式一:(参见图1、图2)本实施方式由燃烧器一次风道1、第一圆锥台形分离环2-1、第二圆锥台形分离环2-2、第三圆锥台形分离环2-3、内旋流器3、燃烧器内二次风道4、外旋流器5、燃烧器外二次风道6、火嘴7、倒“V”形隔板8、二级燃烧室9、一级燃烧室10、辅助油枪11、主油枪套管12、点火枪13、主油枪14和火检管15组成,燃烧器一次风道1的出口端为火嘴7,燃烧器内二次风道4固定在燃烧器一次风道1出口端的外侧面上,内旋流器3固定在燃烧器一次风道1与燃烧器内二次风道4之间,外旋流器5固定在燃烧器内二次风道4的外侧面上,燃烧器外二次风道6固定在外旋流器5右侧的燃烧器内二次风道4的外侧面上,第一圆锥台形分离环2-1、第二圆锥台形分离环2-2和第三圆锥台形分离环2-3依次设置在燃烧器一次风道1内的中部,倒“V”形隔板8固定在第三圆锥台形分离环2-3右侧的燃烧器一次风道1内,辅助油枪11固定在燃烧器内二次风道4左侧的燃烧器一次风道1上,主油枪套管12固定在辅助油枪11左侧的燃烧器一次风道1上,点火枪13和主油枪14均固定在主油枪套管12内,火检管15固定在主油枪套管12左侧的燃烧器一次风道1上,倒“V”形隔板8右侧的燃烧器一次风道1内形成二级燃烧室9,倒“V”形隔板8的下面形成一级燃烧室10,辅助油枪11、主油枪套管12和火检管15与燃烧器一次风道1连接端均与倒“V”形隔板8下面的一级燃烧室10相连通。Specific embodiment one: (see Fig. 1, Fig. 2) this embodiment consists of a burner primary air duct 1, a first truncated conical separating ring 2-1, a second truncated conical separating ring 2-2, and a third truncated conical separating ring 2-3.
具体实施方式二:(参见图1)本实施方式的主油枪14、辅助油枪11、点火枪13和主油枪套管12的头部朝向燃烧器一次风道1的火嘴7的方向设置在燃烧器一次风道1的一侧上,主油枪14、辅助油枪11、点火枪13和主油枪套管12的尾部外翘,主油枪14、辅助油枪11、点火枪13和主油枪套管12与燃烧器中心线的夹角均为55°~65°。其它与具体实施方式一相同。Specific embodiment two: (see Fig. 1) the head of the
具体实施方式三:(参见图1)本实施方式的主油枪14、辅助油枪11、点火枪13和主油枪套管12与燃烧器中心线的夹角均为60°。其它与具体实施方式二相同。Specific embodiment three: (referring to Fig. 1) the included angle of
具体实施方式四:(参见图1)本实施方式的主油枪14、辅助油枪11、火检管15均为伸缩式结构,即在油枪装置停用时退出工作位置,从而保护了油枪装置不被烧坏。其它与具体实施方式三相同。Specific embodiment four: (referring to Fig. 1)
具体实施方式五:(参见图1、图2)本实施方式的倒“V”形隔板8的两下端与燃烧器一次风道1相连接,倒“V”形隔板8中心的顶端与燃烧器一次风道1的轴线重合,一级燃烧室10的截面积占燃烧器一次风道1截面积的四分之一至三分之一。其它与具体实施方式四相同。Specific embodiment five: (see Fig. 1, Fig. 2) the two lower ends of the inverted "V" shaped
具体实施方式六:(参见图1)本实施方式第三圆锥台形分离环2-3大端的直径小于第二圆锥台形分离环2-2小端的直径,第二圆锥台形分离环2-2大端的直径小于第一圆锥台形分离环2-1小端的直径。其它与具体实施方式五相同。Specific embodiment six: (referring to Fig. 1) the diameter of the 3rd truncated conical separating ring 2-3 large end of the present embodiment is less than the diameter of the second truncated conical separating ring 2-2 small end, the diameter of the second truncated conical separating ring 2-2 large end The diameter is smaller than the diameter of the small end of the first truncated conical separation ring 2-1. Others are the same as in the fifth embodiment.
具体实施方式七:(参见图1)本实施方式第一圆锥台形分离环2-1、第二圆锥台形分离环2-2和第三圆锥台形分离环2-3的小端一侧均朝向燃烧器一次风道1的火嘴7。其它与具体实施方式六相同。Specific embodiment seven: (see Fig. 1) the small end side of the first truncated conical separating ring 2-1, the second truncated conical separating ring 2-2 and the third truncated conical separating ring 2-3 of this embodiment are all facing the
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2007100725773A CN100532937C (en) | 2007-07-27 | 2007-07-27 | A swirl burner with gasification combustion of a small amount of oil and powder feeding in the center of side ignition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2007100725773A CN100532937C (en) | 2007-07-27 | 2007-07-27 | A swirl burner with gasification combustion of a small amount of oil and powder feeding in the center of side ignition |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101101115A true CN101101115A (en) | 2008-01-09 |
CN100532937C CN100532937C (en) | 2009-08-26 |
Family
ID=39035515
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2007100725773A Expired - Fee Related CN100532937C (en) | 2007-07-27 | 2007-07-27 | A swirl burner with gasification combustion of a small amount of oil and powder feeding in the center of side ignition |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN100532937C (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100585276C (en) * | 2008-06-20 | 2010-01-27 | 哈尔滨工业大学 | Small amount of oil gasification combustion side to side multi-stage open ignition center powder swirl burner |
CN101403497B (en) * | 2008-11-12 | 2010-10-06 | 哈尔滨工业大学 | Micro-oil ignition rotational flow breeze combustion device for preventing slag bonding of primary combustion chamber |
CN102418922A (en) * | 2011-11-07 | 2012-04-18 | 华北电力大学 | A Pulverized Coal Burner with Oxygen Enriched Ignition and Low Load Stable Combustion |
CN103486582A (en) * | 2013-09-29 | 2014-01-01 | 哈尔滨工业大学 | Center powder feeding turbulent burner with straight sleeve barrel in center |
CN109931605A (en) * | 2019-04-15 | 2019-06-25 | 北京国电龙高科环境工程技术有限公司 | A kind of outside dense interior light turbulent burner of diameter of multistage air distribution |
CN113701195A (en) * | 2021-09-03 | 2021-11-26 | 永旭腾风新能源动力科技(北京)有限公司 | Dual-fuel-tube combustion chamber and gas turbine |
CN114877314A (en) * | 2022-05-17 | 2022-08-09 | 哈尔滨工业大学 | Rotational flow pulverized coal boiler device and method for coupling combustion of gasified crude synthesis gas and coal |
-
2007
- 2007-07-27 CN CNB2007100725773A patent/CN100532937C/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100585276C (en) * | 2008-06-20 | 2010-01-27 | 哈尔滨工业大学 | Small amount of oil gasification combustion side to side multi-stage open ignition center powder swirl burner |
CN101403497B (en) * | 2008-11-12 | 2010-10-06 | 哈尔滨工业大学 | Micro-oil ignition rotational flow breeze combustion device for preventing slag bonding of primary combustion chamber |
CN102418922A (en) * | 2011-11-07 | 2012-04-18 | 华北电力大学 | A Pulverized Coal Burner with Oxygen Enriched Ignition and Low Load Stable Combustion |
CN102418922B (en) * | 2011-11-07 | 2013-12-18 | 华北电力大学 | Oxygen-enriched ignition and low-load stable combustion coal combustor |
CN103486582A (en) * | 2013-09-29 | 2014-01-01 | 哈尔滨工业大学 | Center powder feeding turbulent burner with straight sleeve barrel in center |
CN109931605A (en) * | 2019-04-15 | 2019-06-25 | 北京国电龙高科环境工程技术有限公司 | A kind of outside dense interior light turbulent burner of diameter of multistage air distribution |
CN109931605B (en) * | 2019-04-15 | 2024-05-28 | 北京国电龙高科环境工程技术有限公司 | Multistage air distribution radial outer thick and inner thin cyclone burner |
CN113701195A (en) * | 2021-09-03 | 2021-11-26 | 永旭腾风新能源动力科技(北京)有限公司 | Dual-fuel-tube combustion chamber and gas turbine |
CN114877314A (en) * | 2022-05-17 | 2022-08-09 | 哈尔滨工业大学 | Rotational flow pulverized coal boiler device and method for coupling combustion of gasified crude synthesis gas and coal |
Also Published As
Publication number | Publication date |
---|---|
CN100532937C (en) | 2009-08-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2770257A1 (en) | Plasma oil-free fire lighting system in oxygen-enriched environment | |
CN105737152B (en) | A kind of burner for being classified premixed swirl low nitrogen burning | |
CN100532937C (en) | A swirl burner with gasification combustion of a small amount of oil and powder feeding in the center of side ignition | |
CN101561138B (en) | Secondary Concentration Double Nozzle Minute Oil Quantity Ignition Coal Pulverized Device | |
CN107575859A (en) | The oxygenation start-up burner and its ignition smooth combustion method of a kind of coal burning boiler of power station | |
CN108870383B (en) | Low NOx combustion system of pulverized coal boiler | |
CN207455575U (en) | A kind of oxygenation start-up burner of coal burning boiler of power station | |
CN102519037B (en) | Plasma oil-free ignition combustor | |
CN101403497A (en) | Micro-oil ignition rotational flow breeze combustion device for preventing slag bonding of primary combustion chamber | |
CN205842639U (en) | A kind of band swirl vane strengthens the plasma burner caught fire | |
CN1207511C (en) | Central coal feed cyclone coal burner | |
CN201606876U (en) | Low-NOx coal burner | |
CN103836620B (en) | Oxygen-enriched micro-oil staged combustion device | |
CN100585276C (en) | Small amount of oil gasification combustion side to side multi-stage open ignition center powder swirl burner | |
CN108087871A (en) | A kind of coal burner | |
CN101526226B (en) | Double-helix pneumatic nebulized micro-oil igniting and flame stabilizing device | |
CN208025504U (en) | A kind of coal burner | |
CN1091501C (en) | Blast changeable coal burning method and equipment | |
CN214275703U (en) | Direct-flow burner using high-temperature raw gas | |
CN204786377U (en) | Whirl weak breath coal burner | |
CN201269523Y (en) | Micro-oil gasification oil gun igniting pulverized coal burner | |
CN204786376U (en) | Little oily coal burner of industrial boiler whirl | |
CN211424389U (en) | Gas burner | |
CN202709086U (en) | Novel coal cinder powder burning device of power station boiler | |
CN207990605U (en) | A kind of in due course oxygen supply decoupling burning device of multistage air distribution across Load Regulation |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090826 Termination date: 20120727 |