CN201715533U - Powder feeding device of pulverized coal boiler at power station - Google Patents
Powder feeding device of pulverized coal boiler at power station Download PDFInfo
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- CN201715533U CN201715533U CN2010202585360U CN201020258536U CN201715533U CN 201715533 U CN201715533 U CN 201715533U CN 2010202585360 U CN2010202585360 U CN 2010202585360U CN 201020258536 U CN201020258536 U CN 201020258536U CN 201715533 U CN201715533 U CN 201715533U
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- pulverized coal
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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
本实用新型涉及一种电站煤粉锅炉送粉装置。现有装置在降低着火热方面存在不足。本实用新型包括粉仓和送粉气流管,送粉气流管的入口端与电站煤粉锅炉系统的低温过热器与省煤器之间的烟道连通,出口端与电站煤粉锅炉系统的燃烧器连通;粉仓的出粉口通过给粉机与送粉气流管连通,送粉气流管上设置有调节阀和循环风机,调节阀与循环风机之间的一段送粉气流管上连通有邻炉高温烟气管路和蒸汽管路;循环风机与出口端之间的送粉气流管外设置有管外加热装置。本实用新型结构简单,可以有效降低煤粉气流的着火热,并且利用了锅炉尾部烟气的部分余热,提高了热能利用效率。
The utility model relates to a powder feeding device for a pulverized coal boiler of a power station. Existing devices have deficiencies in reducing ignition heat. The utility model comprises a powder bin and a powder feeding airflow pipe, the inlet end of the powder feeding airflow pipe communicates with the flue between the low-temperature superheater and the economizer of the pulverized coal boiler system of the power station, and the outlet end connects with the combustion chamber of the pulverized coal boiler system of the power station. The powder outlet of the powder bin is connected with the powder feeding air pipe through the powder feeder, and the powder feeding air pipe is provided with a regulating valve and a circulating fan, and a section of the powder feeding air pipe between the regulating valve and the circulating fan is connected with an adjacent The high-temperature flue gas pipeline and steam pipeline of the furnace; the powder feeding airflow tube between the circulating fan and the outlet end is equipped with an external heating device. The utility model has a simple structure, can effectively reduce the ignition heat of the pulverized coal airflow, and utilizes part of the waste heat of the flue gas at the tail of the boiler to improve the heat energy utilization efficiency.
Description
技术领域technical field
本实用新型涉及一种电站煤粉锅炉送粉装置,适用以煤粉为燃料的锅炉。The utility model relates to a pulverized coal boiler powder feeding device of a power station, which is suitable for boilers using pulverized coal as fuel.
技术背景technical background
电站锅炉启停与低负荷稳燃过程中,都需要想方设法降低煤粉气流的着火热,以达到煤粉快速点燃,稳定燃烧的目的。In the process of start-up and shutdown of power plant boilers and low-load stable combustion, it is necessary to find ways to reduce the ignition heat of the pulverized coal airflow, so as to achieve the purpose of rapid ignition of pulverized coal and stable combustion.
对于电厂来说,在特定的煤种以及煤粉粒度分布的情况下,常用的降低着火热的方法:1、热风送粉:采用温度为300℃左右的热空气送粉,但温度不能过高,否则会使得煤粉在送粉管道中提前燃烧,引发事故;2、提高煤粉浓度:正常一次风送粉浓度为0.6kg/kg左右,过高浓度容易使得煤粉沉积,堵塞送粉管,故而常在燃烧器内部增加浓淡分离装置,将煤粉浓度分为浓淡两股,先点燃浓相煤粉气流,再点燃整个煤粉气流,浓淡分离装置的增加使得燃烧器的结构复杂化;3、加入可燃性气体:研究表明少量的可燃性气体的加入可以显著降低煤粉气流的着火热,故而有研究者采用水电解的方式产生布朗气,进行送粉,或将煤气化装置上的煤气引入点火燃烧器中,以降低着火热,这两种方式都需要额外的水电解或煤气化装置。For power plants, in the case of specific coal types and coal powder particle size distribution, commonly used methods to reduce ignition heat: 1. Hot air powder feeding: use hot air with a temperature of about 300°C to feed powder, but the temperature should not be too high , otherwise it will cause the pulverized coal to burn in advance in the powder feeding pipeline, causing accidents; 2. Increase the concentration of pulverized coal: the normal primary air powder feeding concentration is about 0.6kg/kg, too high a concentration will easily cause the pulverized coal to deposit and block the powder feeding pipe Therefore, a thick-thin separation device is often added inside the burner to divide the pulverized coal concentration into two streams, the dense-phase pulverized-coal flow is ignited first, and then the entire pulverized-coal flow is ignited. The increase of the thick-thin separation device complicates the structure of the burner; 3. Adding flammable gas: Studies have shown that the addition of a small amount of flammable gas can significantly reduce the heat of ignition of the pulverized coal flow. Therefore, some researchers use water electrolysis to generate Brown gas for powder feeding, or put the gas on the coal gasification device Coal gas is introduced into the pilot burner to reduce the heat of ignition, both of which require additional water electrolysis or coal gasification.
发明内容Contents of the invention
本实用新型的目的是针对现有技术的不足,提供一种可以有效降低着火热的电站煤粉锅炉送粉装置。The purpose of the utility model is to provide a power plant pulverized coal boiler powder feeding device that can effectively reduce the fire heat in view of the deficiencies in the prior art.
本实用新型包括粉仓和送粉气流管,送粉气流管的入口端与电站煤粉锅炉系统的低温过热器与省煤器之间的烟道连通,出口端与电站煤粉锅炉系统的燃烧器连通;粉仓的出粉口通过给粉机与送粉气流管连通,送粉气流管上设置有调节阀和循环风机,其中循环风机设置在送粉气流管与给粉机连接处和入口端之间的送粉气流管上,调节阀设置在循环风机和入口端之间的送粉气流管上,调节阀与循环风机之间的一段送粉气流管上连通有邻炉高温烟气管路和蒸汽管路;循环风机与出口端之间的送粉气流管外设置有管外加热装置。The utility model comprises a powder bin and a powder feeding airflow pipe, the inlet end of the powder feeding airflow pipe communicates with the flue between the low-temperature superheater and the economizer of the pulverized coal boiler system of the power station, and the outlet end connects with the combustion chamber of the pulverized coal boiler system of the power station. The powder outlet of the powder bin is connected with the powder feeding air pipe through the powder feeder, and the powder feeding air pipe is equipped with a regulating valve and a circulation fan, and the circulation fan is set at the connection between the powder feeding air pipe and the powder feeder and at the entrance On the powder feeding air pipe between the two ends, the regulating valve is set on the powder feeding air pipe between the circulating fan and the inlet end, and the powder feeding air pipe between the regulating valve and the circulating fan is connected with the high temperature flue gas pipe of the adjacent furnace Road and steam pipeline; the powder feeding airflow tube between the circulating fan and the outlet is provided with an external heating device.
所述的邻炉高温烟气管路与邻炉电站煤粉锅炉系统的低温过热器与省煤器之间的烟道连通;所述的蒸汽管路与电厂公用站的中压蒸汽管路连通。The high-temperature flue gas pipeline of the adjacent furnace communicates with the flue between the low-temperature superheater and the economizer of the pulverized coal boiler system of the adjacent furnace power station; the steam pipeline communicates with the medium-pressure steam pipeline of the utility station of the power plant .
所述的管外加热装置为套置在管路外的电阻加热装置或中频加热装置。The external heating device is a resistance heating device or an intermediate frequency heating device sleeved outside the pipeline.
本实用新型结构简单,可以利用电站煤粉锅炉系统产生的高温烟气,将一次风煤粉气流浓度提高到0.8~2kg/kg,有效降低煤粉气流的着火热。在此过程中,煤粉气流进入燃烧器着火前产生热解,析出部分挥发分,并使送粉气流中的CO2、H2O、O2等气体与煤焦产生部分气化,生成CO、H2等可燃性气体,也能有效降低煤粉气流的着火热。反应方程式如下:The utility model has a simple structure, and can use the high-temperature flue gas produced by the pulverized coal boiler system of the power station to increase the concentration of the pulverized coal airflow in the primary air to 0.8-2kg/kg, effectively reducing the ignition heat of the pulverized coal airflow. During this process, the pulverized coal airflow enters the burner before it is ignited to generate pyrolysis, and part of the volatile matter is precipitated, and CO2 , H2O , O2 and other gases in the powder feeding airflow are partially gasified with coal char to generate CO , H 2 and other flammable gases can also effectively reduce the ignition heat of pulverized coal airflow. The reaction equation is as follows:
C+H2O→CO+H2-135kJC+H 2 O→CO+H 2 -135kJ
2C+O2→2CO+221kJ2C+O 2 →2CO+221kJ
C+CO2→2CO-170kJC+CO 2 →2CO-170kJ
由于挥发分的大量析出,煤粉颗粒表面的孔隙面积大大增加,即加大了煤粉表面与氧气的反应面积,也使得煤粉气流更易于点燃。Due to the large amount of volatile matter precipitation, the pore area on the surface of the pulverized coal particles is greatly increased, which increases the reaction area between the pulverized coal surface and oxygen, and makes the pulverized coal flow easier to ignite.
同时,本实用新型利用锅炉尾部烟气的部分余热,节约了能量,提高了热能利用效率。并能有效减少了锅炉排放尾气中的CO2以及NOX。At the same time, the utility model utilizes part of the waste heat of the flue gas at the tail of the boiler, which saves energy and improves the utilization efficiency of heat energy. And can effectively reduce the CO 2 and NO x in the boiler exhaust tail gas.
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.
具体实施方式Detailed ways
如图1所示,一种电站煤粉锅炉送粉装置包括粉仓9和送粉气流管7。送粉气流管7的入口端与电站煤粉锅炉系统1的低温过热器2与省煤器3之间的烟道连通,出口端与电站煤粉锅炉系统1的燃烧器12连通。粉仓9的出粉口通过给粉机10与送粉气流管7连通。送粉气流管7上设置有调节阀4和循环风机8,其中循环风机8设置在送粉气流管与给粉机连接处和入口端之间的送粉气流管7上,调节阀4设置在循环风机8和入口端之间的送粉气流管7上。调节阀4与循环风机8之间的一段送粉气流管7上连通有邻炉高温烟气管路5和蒸汽管路6,邻炉高温烟气管路5与邻炉电站煤粉锅炉系统的低温过热器与省煤器之间的烟道连通,蒸汽管路6与电厂公用站的中压蒸汽管路连通。循环风机8与出口端之间的送粉气流管7外设置有管外加热装置11,管外加热装置为套置在管路外的电阻加热装置或中频加热装置。As shown in FIG. 1 , a power plant pulverized coal boiler powder feeding device includes a powder bin 9 and a powder
工作中通过循环风机8由送粉气流管7抽取部分高温烟气作为送粉烟气,然后在送粉烟气中通过蒸汽管路6混入水蒸汽形成送粉混合气,利用管外加热装置11将送粉混合气加热,使其保持800~1000℃高温。给粉机10将粉仓9中的煤粉送入送粉气流管7中,利用加热后的送粉混合气将浓度为0.8~2kg/kg的煤粉送入电站煤粉锅炉的燃烧器中,在送粉过程中继续使用管外加热装置11进行加热,保持送粉混合气气流温度为800~1000℃。During work, part of the high-temperature flue gas is extracted from the powder
当电站煤粉锅炉系统启动时,送粉烟气通过邻炉高温烟气管路5由正在运行的邻炉电站煤粉锅炉系统中抽取;当电站煤粉锅炉系统稳定运行时,送粉烟气来自于自身的电站煤粉锅炉系统。When the pulverized coal boiler system of the power station is started, the powder feeding flue gas is extracted from the running pulverized coal boiler system of the adjacent furnace power station through the high temperature
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| CN2010202585360U CN201715533U (en) | 2010-07-13 | 2010-07-13 | Powder feeding device of pulverized coal boiler at power station |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010202585360U CN201715533U (en) | 2010-07-13 | 2010-07-13 | Powder feeding device of pulverized coal boiler at power station |
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| CN201715533U true CN201715533U (en) | 2011-01-19 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102607049A (en) * | 2012-03-20 | 2012-07-25 | 安徽省科捷再生能源利用有限公司 | Technology for combusting pulverized coal fed by circulating air for industrial boiler |
| CN110332524A (en) * | 2019-08-20 | 2019-10-15 | 烟台龙源电力技术股份有限公司 | Boiler system |
-
2010
- 2010-07-13 CN CN2010202585360U patent/CN201715533U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102607049A (en) * | 2012-03-20 | 2012-07-25 | 安徽省科捷再生能源利用有限公司 | Technology for combusting pulverized coal fed by circulating air for industrial boiler |
| CN110332524A (en) * | 2019-08-20 | 2019-10-15 | 烟台龙源电力技术股份有限公司 | Boiler system |
| CN110332524B (en) * | 2019-08-20 | 2024-01-09 | 烟台龙源电力技术股份有限公司 | Boiler system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110119 Termination date: 20140713 |
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| EXPY | Termination of patent right or utility model |
