CN107559819A - A kind of spiral-flow powdered coal burning mechanism that gradually expanded form precombustion chamber is carried for Industrial Boiler - Google Patents
A kind of spiral-flow powdered coal burning mechanism that gradually expanded form precombustion chamber is carried for Industrial Boiler Download PDFInfo
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Abstract
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技术领域technical field
本发明涉及一种工业锅炉煤粉燃烧机构,具体涉及一种用于工业锅炉带有渐扩形预燃 室的旋流煤粉燃烧机构。The invention relates to an industrial boiler pulverized coal combustion mechanism, in particular to a swirling pulverized coal combustion mechanism with a gradually expanding pre-combustion chamber for an industrial boiler.
背景技术Background technique
在我国,燃煤工业锅炉是除电站锅炉以外的主要用煤装备,总数接近60万台,年消耗煤炭近6.4亿吨。近年来,随着煤粉加工、运输及储存技术的发展,以及煤粉燃烧技术 的不断成熟,燃用煤粉的中小型工业锅炉得以不断发展。但受到炉膛尺寸及燃烧方式的限制,现有中小型工业煤粉锅炉存在NOx排放量高、预燃室易结渣等问题。随着我国环保 问题的日益严峻,如果不对工业煤粉锅炉现存问题采取有效的解决措施,将难以满足日益 严苛的环保标准。In my country, coal-fired industrial boilers are the main coal-consuming equipment except power plant boilers, with a total of nearly 600,000 units and an annual coal consumption of nearly 640 million tons. In recent years, with the development of pulverized coal processing, transportation and storage technology, and the continuous maturity of pulverized coal combustion technology, small and medium-sized industrial boilers using pulverized coal have been continuously developed. However, limited by the size of the furnace and the combustion method, the existing small and medium-sized industrial pulverized coal boilers have problems such as high NOx emissions and easy slagging in the pre-combustion chamber. With the increasingly severe environmental protection problems in our country, it will be difficult to meet the increasingly stringent environmental protection standards if effective solutions are not taken to the existing problems of industrial pulverized coal boilers.
目前在我国使用的带预燃室的煤粉燃烧装置,例如实用新型专利《一种防结渣的劣质 煤预燃室燃烧器》(中国专利号为ZL201320145975.4、授权公告日为2014年3月26日、申请公布号为CN203501168U,下称“文件一”),将预燃室筒壁分为四段,第一段为渐扩 型,后三段为直筒型,二次风从筒壁之间的间隙分三段喷入,前两段贴壁喷入,第三段斜 向喷入。实用新型专利《一种带扩展段的煤粉预燃室的燃烧器》(中国专利号为ZL201320724053.9、授权公告日为2014年9月24日、申请公布号为CN203848280U,下 称“文件二”),将预燃室本体分为进口端和出口端,所述预燃室本体的进口端呈圆筒状且 用于安装主燃烧器,所述预燃室本体的出口端呈渐扩型。“文件一”提出的预燃室采用前 段渐扩后段直筒的形式;“文件二”提出的预燃室采用前段直筒后段渐扩的形式。The pulverized coal combustion device with pre-combustion chamber currently used in our country, such as the utility model patent "An Inferior Coal Pre-combustion Chamber Burner with Anti-Slagging" (Chinese Patent No. ZL201320145975.4, authorized announcement date is March 2014 On February 26, the application publication number is CN203501168U, hereinafter referred to as "Document 1"), the wall of the pre-combustion chamber is divided into four sections, the first section is gradually expanding, the last three sections are straight, and the secondary air flows from the wall The gap between them is sprayed in three sections, the first two sections are sprayed against the wall, and the third section is sprayed obliquely. Utility model patent "A burner for pulverized coal pre-combustion chamber with extended section" (Chinese patent number is ZL201320724053.9, date of authorization announcement is September 24, 2014, application publication number is CN203848280U, hereinafter referred to as "Document 2 ”), the pre-chamber body is divided into an inlet end and an outlet end, the inlet end of the pre-chamber body is cylindrical and is used for installing the main burner, and the outlet end of the pre-chamber body is gradually expanding . The pre-combustion chamber proposed in "Document 1" adopts the form of the front section gradually expanding and the rear section straight cylinder; the "Document 2" proposes the pre-chamber adopting the form of the front section straight cylinder and the rear section gradually expanding.
发明内容Contents of the invention
本发明为了解决现有技术中燃用煤粉的中小型工业锅炉受到炉膛尺寸及燃烧方式的 限制,以及NOx排放量高、预燃室易结渣的问题,进而提供一种用于工业锅炉带有渐扩形预燃室的旋流煤粉燃烧机构。The present invention aims to solve the problems that the small and medium-sized industrial boilers using pulverized coal in the prior art are limited by the size of the furnace and the combustion method, as well as the problems of high NOx emissions and easy slagging in the pre-combustion chamber, and further provides a belt boiler for industrial boilers. A swirling pulverized coal combustion mechanism with a gradually expanding pre-combustion chamber.
本发明为解决上述问题而采用的技术方案是:The technical scheme that the present invention adopts for solving the above problems is:
它包括旋流煤粉燃烧器和预燃室,预燃室的内侧壁由入口端至出口端呈渐扩形设置, 旋流煤粉燃烧器的出口端与预燃室的入口端连接,且旋流煤粉燃烧器的出口端与预燃室的 入口平齐对应设置。It includes a swirl pulverized coal burner and a pre-combustion chamber, the inner wall of the pre-combustion chamber is gradually expanded from the inlet end to the outlet end, the outlet end of the swirl pulverized coal burner is connected with the inlet end of the pre-combustion chamber, and The outlet end of the swirl pulverized coal burner is flush with the inlet of the pre-combustion chamber and arranged correspondingly.
本发明的有益效果是:The beneficial effects of the present invention are:
(1)本发明有利于降低NOx生成量(1) The present invention is conducive to reducing the amount of NOx generation
①“文件二”所述燃烧器采用前段直筒后段渐扩形式的预燃室,前端的直筒限制了气 流的充分发展,不利于回流区的形成。与对比“文件二”相比本发明装置采用渐扩式预燃室,有利于中心回流区的形成,将高浓度煤粉由燃烧器中心喷入低氧强还原性气氛的高温中心回流区,煤粉长时间于富燃料低氧的气氛中燃烧,有利于抑制NOx的形成。① The burner described in "Document 2" adopts a pre-combustion chamber with a straight cylinder at the front and a gradual expansion at the rear. The straight cylinder at the front restricts the full development of the airflow, which is not conducive to the formation of the recirculation zone. Compared with the comparison "Document 2", the device of the present invention adopts a gradually expanding pre-combustion chamber, which is beneficial to the formation of the central recirculation zone, and sprays high-concentration pulverized coal from the center of the burner into the high-temperature central recirculation zone of a low-oxygen and strong reducing atmosphere. Combustion of pulverized coal in a fuel-rich and low-oxygen atmosphere for a long time is beneficial to suppress the formation of NOx.
②“文件一”所述燃烧器采用前段渐扩后段直筒形式的预燃室,后端的直筒段不利于 气流的充分发展。与对比“文件一”相比本发明装置的预燃室为渐扩的,有利于旋转气流的发展,推迟内、外二次风的混合,强化了燃烧器的空气分级燃烧程度,并且推迟二次风 与煤粉气流的混合,有利于降低燃料型NOx的生成。同时,采用渐扩型的预燃室有利于中 心回流区的形成,稳定存在的中心回流区使煤粉长时间处于还原性气氛,有利于抑制NOx 的形成。②The burner described in "Document 1" adopts a pre-combustion chamber in the form of a straight cylinder in the front section that gradually expands in the rear section, and the straight cylinder section at the rear end is not conducive to the full development of the airflow. Compared with the comparison "Document 1", the pre-combustion chamber of the device of the present invention is gradually expanded, which is conducive to the development of the swirling airflow, delays the mixing of the internal and external secondary air, strengthens the air staged combustion degree of the burner, and delays the secondary airflow. The mixing of secondary air and pulverized coal airflow is beneficial to reduce the formation of fuel-type NOx. At the same time, the use of a gradually expanding pre-combustion chamber is conducive to the formation of the central recirculation zone. The stable central recirculation zone keeps the pulverized coal in a reducing atmosphere for a long time, which is beneficial to suppress the formation of NOx.
(2)本发明有利于避免预燃室内结渣(2) The present invention is beneficial to avoid slagging in the pre-combustion chamber
①“文件一”所述燃烧器采用前段渐扩后段直筒形式的预燃室,后端的直筒段不利于 气流将灰、渣带出预燃室,需要采用其他措施来解决预燃室内积灰及结渣的问题。与对比 “文件一”相比本发明装置的预燃室全部为渐扩的,在旋转射流的带动下,可有效的将壁面的灰吹出预燃室。同时,本发明装置的预燃室长度仅设为旋流外二次风管外径的0.8~2倍,预燃室长度短,有利于预燃室内煤粉烟气气流吹出预燃室,避免预燃室内结渣。① The burner described in "Document 1" adopts a pre-combustion chamber in the form of a straight cylinder in the front section gradually expanding and a rear section. The straight cylinder section at the rear end is not conducive to the airflow to bring ash and slag out of the pre-combustion chamber. Other measures need to be taken to solve the ash accumulation in the pre-combustion chamber and the problem of slagging. Compared with the comparison "Document 1", all the pre-combustion chambers of the device of the present invention are gradually expanded, and driven by the rotating jet, the ash on the wall can be effectively blown out of the pre-combustion chamber. Simultaneously, the length of the pre-combustion chamber of the device of the present invention is only set as 0.8 to 2 times of the external diameter of the secondary air pipe outside the swirling flow, and the length of the pre-combustion chamber is short, which is conducive to blowing out the pre-combustion chamber by the pulverized coal flue gas flow in the pre-combustion chamber, avoiding Slagging in pre-chamber.
②本发明装置将颗粒集中于燃烧器中心喷入,防止煤粉被二次风甩到预燃室壁上,从 而有效避免预燃室结渣和高温腐蚀的发生。②The device of the present invention concentrates the particles into the center of the burner and injects them to prevent pulverized coal from being thrown onto the wall of the pre-combustion chamber by the secondary air, thereby effectively avoiding the occurrence of slagging and high-temperature corrosion in the pre-combustion chamber.
(3)本发明有利于煤粉的着火及稳定燃烧(3) The present invention is beneficial to the ignition and stable combustion of pulverized coal
①本发明装置设置预燃室使得即使是在低负荷或煤质变差时也能维持煤粉气流的稳定 着火和燃烧。同时,本发明装置的预燃室为渐扩的,有利于中心回流区的形成,中心回流 区卷吸炉内的高温烟气加热煤粉气流,稳定存在的中心回流区保证了煤粉的着火及稳定燃 烧。① The device of the present invention is provided with a pre-combustion chamber so that the stable ignition and combustion of the pulverized coal airflow can be maintained even when the load is low or the coal quality is deteriorating. At the same time, the pre-combustion chamber of the device of the present invention is gradually expanded, which is beneficial to the formation of the central recirculation zone, where the high-temperature flue gas in the entrainment furnace in the central recirculation zone heats the pulverized coal airflow, and the stable central recirculation zone ensures the ignition of the pulverized coal and stable combustion.
②本发明装置将高浓度煤粉气流由燃烧器中心给入,使得喷入炉内的煤粉全部集中在 高温中心回流区,在中心回流区内形成高温、高浓度区域,延长了煤粉在高温区的停留时 间,强化了煤粉气流的着火和稳燃性能,使锅炉能够在较低负荷下运行,燃烧稳定性也能 得到充分保证。②The device of the present invention feeds the high-concentration pulverized coal airflow from the center of the burner, so that all the pulverized coal injected into the furnace is concentrated in the high-temperature central recirculation zone, forming a high-temperature and high-concentration zone in the central recirculation zone, prolonging the life of the pulverized coal in the furnace. The residence time in the high temperature zone strengthens the ignition and stable combustion performance of the pulverized coal flow, enabling the boiler to operate at a lower load, and the combustion stability can also be fully guaranteed.
附图说明Description of drawings
图1是本发明装置布置在卧式锅炉前墙3的示意图,中心回流区域5位于预燃室2的入口处。FIG. 1 is a schematic diagram of the device of the present invention arranged on the front wall 3 of a horizontal boiler, and the central recirculation area 5 is located at the entrance of the pre-combustion chamber 2 .
图2是本发明装置布置在立式锅炉炉顶4的示意图,中心回流区域5位于预燃室2的入口处。FIG. 2 is a schematic diagram of the arrangement of the device of the present invention on the roof 4 of the vertical boiler, and the central recirculation area 5 is located at the entrance of the pre-combustion chamber 2 .
具体实施方式detailed description
具体实施方式一:结合图1-图2说明本实施方式,本实施方式所述一种用于工业锅炉带有渐扩形预燃室的旋流煤粉燃烧机构,它包括旋流煤粉燃烧器1和预燃室2,预燃室 2的内侧壁由入口端至出口端呈渐扩形设置,旋流煤粉燃烧器1的出口端与预燃室2的入 口端连接,且旋流煤粉燃烧器1的出口端与预燃室2的入口平齐对应设置。Specific Embodiment 1: This embodiment is described in conjunction with Fig. 1-Fig. 2. The swirl pulverized coal combustion mechanism for an industrial boiler with a gradually expanding pre-combustion chamber described in this embodiment includes a swirl pulverized coal combustion mechanism. Device 1 and pre-combustion chamber 2, the inner wall of pre-combustion chamber 2 is gradually expanded from the inlet end to the outlet end, the outlet end of swirl pulverized coal burner 1 is connected with the inlet end of pre-combustion chamber 2, and the swirl flow The outlet end of the pulverized coal burner 1 is arranged flush with the inlet of the pre-combustion chamber 2 .
具体实施方式二:结合图1-图2说明本实施方式,本实施方式所述一种用于工业锅炉带 有渐扩形预燃室的旋流煤粉燃烧机构,旋流煤粉燃烧器1包括一次风管1-1、旋流内二次风 管1-2、旋流外二次风管1-3、第一轴向旋流叶片1-4和第二轴向旋流叶片1-5;旋流外二次风 管1-3和旋流内二次风管1-2由外向内依次套设在一次风管1-1上,且一次风管1-1、旋流内二 次风管1-2和旋流外二次风管1-3同轴设置,第一轴向旋流叶片1-4设置在一次风管1-1和旋流 内二次风管1-2之间,第二轴向旋流叶片1-5设置在旋流内二次风管1-2和旋流外二次风管1-3 之间,其它与具体实施方式一相同。Specific embodiment two: This embodiment is described in conjunction with Fig. 1-Fig. 2, a swirl pulverized coal combustion mechanism for an industrial boiler with a gradually expanding pre-combustion chamber described in this embodiment, a swirl pulverized coal burner 1 Including the primary air duct 1-1, the secondary air duct 1-2 in the swirl flow, the secondary air duct 1-3 outside the swirl flow, the first axial swirl blade 1-4 and the second axial swirl blade 1- 5. The secondary air pipe 1-3 outside the swirl flow and the secondary air pipe 1-2 inside the swirl flow are set on the primary air pipe 1-1 in turn from the outside to the inside, and the primary air pipe 1-1, the second air pipe inside the swirl flow The secondary air duct 1-2 and the secondary air duct 1-3 outside the swirl flow are coaxially arranged, and the first axial swirl blade 1-4 is arranged on the primary air duct 1-1 and the secondary air duct 1-2 inside the swirl flow Between them, the second axial swirl vanes 1-5 are arranged between the inner swirl secondary air duct 1-2 and the swirl outer secondary air duct 1-3, and the others are the same as in the first embodiment.
煤粉气流经由旋流煤粉燃烧器1中心的一次风管1-1喷出,二次风气流在轴向旋流叶 片的作用下形成旋转射流进入预燃室2,旋转射流在气流中心形成回流区,卷吸炉内高温 烟气加热并点燃煤粉气流。The pulverized coal airflow is sprayed out through the primary air duct 1-1 in the center of the swirling pulverized coal burner 1, and the secondary airflow forms a rotating jet under the action of the axial swirling blades and enters the pre-combustion chamber 2, and the rotating jet is formed in the center of the airflow In the reflow zone, the high-temperature flue gas in the entrainment furnace heats up and ignites the pulverized coal flow.
具体实施方式三:结合图1-图2说明本实施方式,本实施方式所述一种用于工业锅炉带有渐扩形预燃室的旋流煤粉燃烧机构,预燃室2的入口端至出口端具有扩展角,扩展角的角度为α,α的取值范围为0-10。其它与具体实施方式一相同。Specific embodiment three: this embodiment is described in conjunction with Fig. 1-Fig. 2, a kind of swirl pulverized coal combustion mechanism that is used for industrial boiler with expanding pre-combustion chamber described in this embodiment, the inlet end of pre-combustion chamber 2 There is an expansion angle to the exit end, and the angle of the expansion angle is α, and the value range of α is 0-10. Others are the same as in the first embodiment.
具体实施方式四:结合图1-图2说明本实施方式,本实施方式所述一种用于工业锅炉带有渐扩形预燃室的旋流煤粉燃烧机构,预燃室2由高强度的耐火材料浇注而成预燃室。其它与具体实施方式一相同。Specific embodiment four: This embodiment is described in conjunction with Fig. 1-Fig. 2, a kind of swirl pulverized coal combustion mechanism that is used for industrial boiler with expanding pre-combustion chamber described in this embodiment, pre-combustion chamber 2 is made of high-strength The refractory material is poured into the pre-combustion chamber. Others are the same as in the first embodiment.
具体实施方式五:结合图1-图2说明本实施方式,本实施方式所述一种用于工业锅炉带有渐扩形预燃室的旋流煤粉燃烧机构,预燃室2入口端的直径为旋流外二次风管1-3外径的1.5倍至3倍,预燃室2的长度为旋流外二次风管1-3外径的0.8倍至2倍。其它 与具体实施方式一、二、三或四相同。Specific embodiment five: This embodiment is described in conjunction with Fig. 1-Fig. 2, a kind of swirl pulverized coal combustion mechanism that is used for industrial boilers with a gradually expanding pre-combustion chamber described in this embodiment, the diameter of the inlet end of the pre-combustion chamber 2 It is 1.5 times to 3 times the outer diameter of the secondary air pipe 1-3 outside the swirling flow, and the length of the pre-combustion chamber 2 is 0.8 times to 2 times the outer diameter of the secondary air pipe 1-3 outside the swirling flow. Others are the same as the specific embodiment one, two, three or four.
Claims (5)
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|---|---|---|---|---|
| CN109631018A (en) * | 2018-12-18 | 2019-04-16 | 哈尔滨工业大学 | A kind of gradual-enlargement type Anti-slagging burner for industrial coal powder boiler |
| CN109631023A (en) * | 2018-12-18 | 2019-04-16 | 哈尔滨工业大学 | There is the cyclone burner of precombustion chamber using the multiple radial grading of flue gas recirculation |
| CN109631025A (en) * | 2018-12-18 | 2019-04-16 | 哈尔滨工业大学 | A kind of Anti-slagging swirling pulverized coal combustion device suitable for industrial coal powder boiler |
| CN112902149A (en) * | 2021-02-07 | 2021-06-04 | 哈尔滨工业大学 | Combustion system with pre-combustion chamber burners arranged on walls on two sides of boiler and combustion method |
| CN112902150A (en) * | 2021-02-07 | 2021-06-04 | 哈尔滨工业大学 | Combustion system and method for boiler on front wall or rear wall of power station |
| CN113007698A (en) * | 2021-02-07 | 2021-06-22 | 哈尔滨工业大学 | Combustion system for lower layer of opposed combustion boiler and use method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3310500A1 (en) * | 1983-03-23 | 1984-10-04 | Steag Ag, 4300 Essen | Burner for the combustion of pulverized fuels and process for the operation of a fuel dust burner flame |
| US4523530A (en) * | 1982-02-26 | 1985-06-18 | Sumitomo Metal Industries, Ltd. | Powdery coal burner |
| US4690075A (en) * | 1984-08-16 | 1987-09-01 | Stein Industrie | Ignition and combustion supporting burner for pulverized solid fossil fuel and combustion chamber comprising same |
| CN102353049A (en) * | 2011-08-10 | 2012-02-15 | 深圳东方锅炉控制有限公司 | Stable combustion device for pulverized coal ignition |
-
2017
- 2017-09-21 CN CN201710861185.9A patent/CN107559819A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4523530A (en) * | 1982-02-26 | 1985-06-18 | Sumitomo Metal Industries, Ltd. | Powdery coal burner |
| DE3310500A1 (en) * | 1983-03-23 | 1984-10-04 | Steag Ag, 4300 Essen | Burner for the combustion of pulverized fuels and process for the operation of a fuel dust burner flame |
| US4690075A (en) * | 1984-08-16 | 1987-09-01 | Stein Industrie | Ignition and combustion supporting burner for pulverized solid fossil fuel and combustion chamber comprising same |
| CN102353049A (en) * | 2011-08-10 | 2012-02-15 | 深圳东方锅炉控制有限公司 | Stable combustion device for pulverized coal ignition |
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| CN109631023A (en) * | 2018-12-18 | 2019-04-16 | 哈尔滨工业大学 | There is the cyclone burner of precombustion chamber using the multiple radial grading of flue gas recirculation |
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| CN112902149A (en) * | 2021-02-07 | 2021-06-04 | 哈尔滨工业大学 | Combustion system with pre-combustion chamber burners arranged on walls on two sides of boiler and combustion method |
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| CN113007698B (en) * | 2021-02-07 | 2021-12-03 | 哈尔滨工业大学 | Combustion system for lower layer of opposed combustion boiler and use method |
| CN112902150B (en) * | 2021-02-07 | 2022-02-22 | 哈尔滨工业大学 | Combustion system and method for boiler on front wall or rear wall of power station |
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Application publication date: 20180109 |