CN201190993Y - Pulverized coal combustion device for small and medium-sized boilers - Google Patents
Pulverized coal combustion device for small and medium-sized boilers Download PDFInfo
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- CN201190993Y CN201190993Y CNU2008200112581U CN200820011258U CN201190993Y CN 201190993 Y CN201190993 Y CN 201190993Y CN U2008200112581 U CNU2008200112581 U CN U2008200112581U CN 200820011258 U CN200820011258 U CN 200820011258U CN 201190993 Y CN201190993 Y CN 201190993Y
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- pulverized coal
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Abstract
Description
技术领域 technical field
本实用新型涉及一种中小型锅炉燃烧系统中的煤粉燃烧装置。The utility model relates to a pulverized coal combustion device in a medium and small boiler combustion system.
背景技术 Background technique
我国大型锅炉以循环流化床锅炉为主,技术成熟度高,而数量众多的中小型锅炉的燃烧系统普遍采用链条炉,其燃烧过程属于移动层燃,热效率只有60~70%,造成了资源巨大浪费。存在的主要问题是:1、煤点火困难,着火点后移,造成燃烧时间不足,灰渣中固定碳含量高达10~25%,不完全燃烧损失大,导致煤炭燃尽率低;2、空气过剩系数高,一般为1.3~1.5,实际操作中甚至达到1.5~1.8,造成烟气热损失增加,导致锅炉热效率低。my country's large-scale boilers are mainly circulating fluidized bed boilers, with high technical maturity, while chain furnaces are generally used in the combustion systems of a large number of small and medium-sized boilers. Huge waste. The main problems are: 1. Coal is difficult to ignite, and the ignition point moves backward, resulting in insufficient combustion time. The fixed carbon content in the ash is as high as 10-25%, and the loss of incomplete combustion is large, resulting in low coal burnout rate; 2. Excessive air The coefficient is high, generally 1.3 to 1.5, and even 1.5 to 1.8 in actual operation, resulting in increased flue gas heat loss and low boiler thermal efficiency.
发明内容 Contents of the invention
本实用新型的目的是提供一种煤炭燃尽率高、锅炉热效率高的中小型锅炉煤粉燃烧装置。The purpose of the utility model is to provide a pulverized coal combustion device for small and medium-sized boilers with high coal burnout rate and high boiler thermal efficiency.
本实用新型的技术方案是:本实用新型包括煤粉制备系统、煤粉输送系统、煤粉燃烧器和煤粉燃烧室。煤粉制备系统由输送带、碎煤机、碎煤提升机、碎煤斗、震动给煤机、雷蒙磨、旋风分离器、煤粉提升机和煤粉仓组成。煤粉输送系统由煤粉定量装置、一次风煤管道组成。煤粉燃烧器的内腔为耐火层构成的圆柱形空腔,在耐火层的外侧设有环形水冷腔。煤粉燃烧器的输入端通过法兰与旋流涡壳、点火孔连接,煤粉输送系统的一次风煤管道与旋流涡壳内腔相通,在旋流涡壳的内腔与煤粉燃烧器的内腔相通处设一喇叭喷口,旋流涡壳的内腔中安有钝体,该钝体伸入到煤粉燃烧器内腔的一端呈喇叭状。点火孔的外端通过螺纹与点火孔盖连接。在煤粉燃烧器的耐火层上设有二次风口,二次风口与圆柱形的耐火层内壁相切并与圆柱形耐火层轴线成一定夹角,二次风口与煤粉燃烧器外侧的二次风管相连。在水冷腔内设有冷却进水管和冷却出水管。煤粉燃烧器内腔通过燃烧器烟气出口与锅炉本体内的煤粉燃烧室相通,煤粉燃烧室的下部为集渣室,在煤粉燃烧室的底部设有除渣机,在煤粉燃烧室的上部设有烟气出口。The technical scheme of the utility model is: the utility model comprises a pulverized coal preparation system, a pulverized coal conveying system, a pulverized coal burner and a pulverized coal combustion chamber. The pulverized coal preparation system consists of a conveyor belt, a coal crusher, a pulverized coal hoist, a pulverized coal hopper, a vibrating coal feeder, a Raymond mill, a cyclone separator, a pulverized coal hoist and a pulverized coal bin. The pulverized coal conveying system is composed of a pulverized coal quantitative device and a primary wind coal pipeline. The inner cavity of the pulverized coal burner is a cylindrical cavity formed by a refractory layer, and an annular water cooling chamber is arranged outside the refractory layer. The input end of the pulverized coal burner is connected with the swirl volute and the ignition hole through the flange. The primary air coal pipeline of the pulverized coal conveying system communicates with the inner cavity of the swirl volute, and the inner cavity of the swirl volute is burned with the pulverized coal. A trumpet nozzle is arranged at the intercommunication of the inner cavity of the device, and a blunt body is installed in the inner cavity of the swirl volute, and the end of the blunt body extending into the inner cavity of the pulverized coal burner is in the shape of a trumpet. The outer end of the ignition hole is connected with the ignition hole cover by threads. There is a secondary tuyere on the refractory layer of the pulverized coal burner. The secondary tuyere is tangent to the inner wall of the cylindrical refractory layer and forms a certain angle with the axis of the cylindrical refractory layer. The secondary air duct is connected. A cooling water inlet pipe and a cooling water outlet pipe are arranged in the water cooling cavity. The inner cavity of the pulverized coal burner communicates with the pulverized coal combustion chamber in the boiler body through the outlet of the burner flue gas. The lower part of the pulverized coal combustion chamber is a slag collection chamber. The upper part of the combustion chamber is provided with a flue gas outlet.
来自煤粉输送系统的一次风粉在旋流涡壳的作用下,以螺旋运动方式通过喇叭喷口进入到煤粉燃烧器内腔,通过点火孔将煤粉点燃。进入正常燃烧工况后,二次风通过二次风口进入煤粉燃烧器内形成螺旋线的运动轨迹,同时在钝体共同作用下,在靠近钝体呈喇叭状端的区域形成一个高温烟气的回流区,将高温烟气的回流区中的煤粉点燃,煤粉燃烧器内的煤粉则沿螺旋线轨迹的运动并快速燃烧,形成的高温烟气夹带着未燃尽的半焦颗粒通过燃烧器烟气出口进入锅炉本体内的煤粉燃烧室进行完全燃烧,生成的灰渣在高温烟气的作用下,发生团聚,生成颗粒较大的灰尘渣,由于煤粉燃烧室的空间大,高温烟气流速骤然下降,一部分灰渣在重力作用下沉降到下部集渣室;另一方面,由于夹带灰渣的高温烟气是以螺旋运动方式进入煤粉燃烧室的,灰渣在离心力的作用下,被分离出来,落入下部集渣室。灰渣中固定碳含量小于2%,灰渣经除渣机排出炉外,除渣后的高温烟气通过烟气出口进入锅炉加热。经测试,本实用新型可使煤碳的燃尽率达到98%以上,锅炉热效率达到到90%。The primary air powder from the pulverized coal conveying system enters into the inner cavity of the pulverized coal burner through the trumpet nozzle in a spiral motion under the action of the swirling volute, and ignites the pulverized coal through the ignition hole. After entering the normal combustion condition, the secondary air enters the pulverized coal burner through the secondary air port to form a helical trajectory, and at the same time, under the joint action of the blunt body, a high-temperature flue gas is formed in the area near the horn-shaped end of the blunt body. The recirculation zone ignites the pulverized coal in the recirculation zone of the high-temperature flue gas, and the pulverized coal in the pulverized coal burner moves along the helical trajectory and burns rapidly, and the formed high-temperature flue gas carries unburned semi-coke particles through The flue gas outlet of the burner enters the pulverized coal combustion chamber in the boiler body for complete combustion, and the generated ash is agglomerated under the action of the high-temperature flue gas to generate dust with large particles. Due to the large space of the pulverized coal combustion chamber, The flow rate of the high-temperature flue gas drops suddenly, and part of the ash and slag settles to the lower slag collection chamber under the action of gravity; Under the action, it is separated and falls into the lower slag collection chamber. The fixed carbon content in the ash is less than 2%, and the ash is discharged out of the furnace through the slag remover, and the high-temperature flue gas after the slag removal enters the boiler through the flue gas outlet for heating. After testing, the utility model can make the burnout rate of coal reach more than 98%, and the thermal efficiency of the boiler can reach 90%.
附图说明 Description of drawings
图1为本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
图2为煤粉燃烧器和煤粉燃烧室的结构示意图。Fig. 2 is a schematic structural view of a pulverized coal burner and a pulverized coal combustion chamber.
附图中的部件标号为:1为输送带、2为碎煤机、3为碎煤提升机、4为碎煤斗、5为震动给煤机、6为雷蒙磨、7为旋风分离器、8为煤粉提升机、9为煤粉仓、10为煤粉定量装置、11为锅炉本体、12为二次风管、13为煤粉燃烧器、14为次风煤管道、15为点火孔盖、16为点火孔、17为钝体、18为旋流涡壳、19为法兰、20为喇叭喷口、21为冷却出水管、22为二次风口、23为耐火层、24为水冷腔、25为冷却进水管、26为燃烧器烟气出口、27为集渣室、28为烟气出口、29为除渣机。The part numbers in the drawings are: 1 is the conveyor belt, 2 is the coal crusher, 3 is the coal crushing hoist, 4 is the crushing coal hopper, 5 is the vibrating coal feeder, 6 is the Raymond mill, 7 is the cyclone separator , 8 is the pulverized coal elevator, 9 is the pulverized coal bin, 10 is the pulverized coal quantitative device, 11 is the boiler body, 12 is the secondary air duct, 13 is the pulverized coal burner, 14 is the secondary air coal pipeline, and 15 is the ignition Hole cover, 16 is ignition hole, 17 is blunt body, 18 is swirl volute, 19 is flange, 20 is trumpet nozzle, 21 is cooling outlet pipe, 22 is secondary air outlet, 23 is refractory layer, 24 is water cooling Cavity, 25 are cooling inlet pipes, 26 are burner flue gas outlets, 27 are slag collecting chambers, 28 are flue gas outlets, and 29 are slag removers.
具体实施方式 Detailed ways
见图1和图2,本实用新型包括煤粉制备系统、煤粉输送系统、煤粉燃烧器和煤粉燃烧室。煤粉制备系统由输送带1、碎煤机2、碎煤提升机3、碎煤斗4、震动给煤机5、雷蒙磨6、旋风分离器7、煤粉提升机8和煤粉仓9组成。煤粉输送系统由煤粉定量装置10、一次风煤管道14组成。煤粉燃烧器13的内腔为耐火层23构成的圆柱形空腔,在耐火层23的外侧设有环形水冷腔24。煤粉燃烧器13的输入端通过法兰19与旋流涡壳18、点火孔16连接,煤粉输送系统的一次风煤管道14与旋流涡壳18内腔相通,在旋流涡壳18的内腔与煤粉燃烧器13的内腔相通处设一喇叭喷口20,旋流涡壳18的内腔中安有钝体17,该钝体17伸入到煤粉燃烧器13内腔的一端呈喇叭状。点火孔16的外端通过螺纹与点火孔盖15连接。在煤粉燃烧器13的耐火层23上设有二次风口22,二次风口22与煤粉燃烧器13内腔相切并与圆柱形空腔轴线成一定夹角,二次风口22与煤粉燃烧器13外侧的二次风管12相连。在水冷腔24内设有冷却进水管25和冷却出水管21。煤粉燃烧器13内腔通过燃烧器烟气出口26与锅炉本体11内的煤粉燃烧室相通,煤粉燃烧室的下部为集渣室27,在煤粉燃烧室的底部设有除渣机29,在煤粉燃烧室的上部设有烟气出口28。See Fig. 1 and Fig. 2, the utility model comprises pulverized coal preparation system, pulverized coal delivery system, pulverized coal burner and pulverized coal combustion chamber. The pulverized coal preparation system consists of a conveyor belt 1, a
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| Application Number | Priority Date | Filing Date | Title |
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| CNU2008200112581U CN201190993Y (en) | 2008-02-22 | 2008-02-22 | Pulverized coal combustion device for small and medium-sized boilers |
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| Application Number | Priority Date | Filing Date | Title |
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| CNU2008200112581U CN201190993Y (en) | 2008-02-22 | 2008-02-22 | Pulverized coal combustion device for small and medium-sized boilers |
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| CN201190993Y true CN201190993Y (en) | 2009-02-04 |
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| CNU2008200112581U Expired - Fee Related CN201190993Y (en) | 2008-02-22 | 2008-02-22 | Pulverized coal combustion device for small and medium-sized boilers |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102192515A (en) * | 2010-03-10 | 2011-09-21 | 中国石油天然气股份有限公司 | A kind of forced mixed tail gas burning furnace |
| WO2012088927A1 (en) * | 2010-12-28 | 2012-07-05 | Zhang Youjing | Pulverized coal boiler |
| CN102032566B (en) * | 2009-09-27 | 2013-06-12 | 烟台龙源电力技术股份有限公司 | Pulverized coal burner and boiler with same |
| CN103162313A (en) * | 2011-12-08 | 2013-06-19 | 易文翔 | Biomass direct combustion furnace |
| CN116481022A (en) * | 2023-04-28 | 2023-07-25 | 哈尔滨红光锅炉总厂有限责任公司 | A water-cooled oil ignition device for a circulating fluidized bed boiler |
-
2008
- 2008-02-22 CN CNU2008200112581U patent/CN201190993Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102032566B (en) * | 2009-09-27 | 2013-06-12 | 烟台龙源电力技术股份有限公司 | Pulverized coal burner and boiler with same |
| CN102192515A (en) * | 2010-03-10 | 2011-09-21 | 中国石油天然气股份有限公司 | A kind of forced mixed tail gas burning furnace |
| CN102192515B (en) * | 2010-03-10 | 2012-11-14 | 中国石油天然气股份有限公司 | A kind of forced mixed tail gas burning furnace |
| WO2012088927A1 (en) * | 2010-12-28 | 2012-07-05 | Zhang Youjing | Pulverized coal boiler |
| CN103162313A (en) * | 2011-12-08 | 2013-06-19 | 易文翔 | Biomass direct combustion furnace |
| CN103162313B (en) * | 2011-12-08 | 2015-12-09 | 易文翔 | Biomass direct-fired furnace |
| CN116481022A (en) * | 2023-04-28 | 2023-07-25 | 哈尔滨红光锅炉总厂有限责任公司 | A water-cooled oil ignition device for a circulating fluidized bed boiler |
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Granted publication date: 20090204 Termination date: 20100222 |