CN107131496B - Split type burner structure and split method of power station boiler - Google Patents

Split type burner structure and split method of power station boiler Download PDF

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Publication number
CN107131496B
CN107131496B CN201710223326.4A CN201710223326A CN107131496B CN 107131496 B CN107131496 B CN 107131496B CN 201710223326 A CN201710223326 A CN 201710223326A CN 107131496 B CN107131496 B CN 107131496B
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China
Prior art keywords
split
combustion
burner
tertiary air
boiler
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CN201710223326.4A
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CN107131496A (en
Inventor
陈玉忠
石践
肖建
余兴明
罗小鹏
钟晶亮
黄锡兵
席光辉
陈晓
王世远
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Electric Power Research Institute of Guizhou Power Grid Co Ltd
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Electric Power Research Institute of Guizhou Power Grid Co Ltd
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C7/00Combustion apparatus characterised by arrangements for air supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K3/00Feeding or distributing of lump or pulverulent fuel to combustion apparatus
    • F23K3/02Pneumatic feeding arrangements, i.e. by air blast

Abstract

The invention discloses a split type burner structure of a power station boiler and a split method. The invention firstly solves the problems of the combustion stability and the economy of the boiler. Through a great deal of research and calculation by the applicant, the current independent tertiary air nozzle is found, and the existing independent tertiary air nozzle is difficult to burn completely due to the fact that the pulverized coal content is low, the temperature is low, the wind speed is high (50-55 m/s), and the arrangement position is far away from the place with high temperature of the combustion center of the hearth. And the combustion stability of the furnace is greatly influenced due to the poor combustion effect of tertiary air. On the other hand, the coal gas is easy to catch fire due to low ignition temperature, and has good combustion stabilizing effect on the boiler. Therefore, if the advantage of easy combustion of the gas can be utilized as a stable combustion source of the tertiary air, the defect of combustion of the tertiary air can be overcome, and the better combustion effect of the tertiary air can be achieved, so that the combustion stability and the economy of the boiler are integrally improved.

Description

Split type burner structure and split method of power station boiler
Technical Field
The invention relates to a split type burner structure and a split method of a power station boiler, belonging to the field of boiler combustion and design.
Background
The combustion principle of the boiler with tangential circles at the four corners of the power station is that the airflow of the burner at the four corners of the hearth tangentially rotates in the hearth to form a stable combustion tangential circle. The fire side of the burner is the side close to the center of the hearth in the air flow direction, and the side close to the furnace wall is the back fire side.
The main burner type of the prior utility boiler is mainly a pulverized coal nozzle, the nozzle containing pulverized coal can be divided into a primary air nozzle and a tertiary air nozzle according to different pulverized coal concentrations, and the nozzle of hot air (350-370 ℃) without pulverized coal is called secondary air. The primary air nozzle has high pulverized coal concentration and is generally called as a pulverized coal burner; the tertiary air is the exhaust gas of powder making, and contains about 10% of coal dust in the total amount, which is generally called tertiary air nozzle.
The tertiary air is characterized by low pulverized coal content, finer pulverized coal, low temperature (80-90 ℃) and difficult ignition and combustion, and is generally arranged at the uppermost layer of the boiler burner group.
The steelmaking process can produce a large amount of blast furnace gas, and the blast furnace gas is characterized by lower heat value, but is easy to catch fire due to the characteristics of a gas medium.
The blast furnace gas is used as the blended fuel in the utility boiler and mainly plays a role in stabilizing combustion, and is generally used as an independent nozzle or is arranged in a secondary air nozzle at present.
Disclosure of Invention
The invention aims to solve the technical problem of providing a burner design method and a burner design structure capable of improving the combustion stability and economy of a boiler, and overcoming the defects of the prior art.
The technical scheme of the invention is as follows: the utility model provides a split type burner structure of power plant boiler, includes coal gas spout, split type burner, tertiary air spout, baffle, furnace, split type burner inside has a baffle, splits split type burner into coal gas spout and tertiary air spout; the installation position of the split burner is tangential to the center of the hearth.
The number of the divided type burners is 4.
The partition board (4) is connected with the inner wall of the split burner in a welding mode.
The segmentation method comprises the following steps: the split burner adopts a coal gas and tertiary air split burner structure, the split burner adopts vertical split, the fire side of the split burner is a coal gas nozzle, and the back fire side of the split burner is a tertiary air nozzle; the hearth is in a tangential combustion mode, and the split type burner is positioned on the upper layer of the hearth combustion group.
The tertiary air nozzle can be replaced by primary air pulverized coal or secondary air.
The tangential firing is positioned in the center of the hearth, and four pulverized coal burners positioned in the center of the hearth form a quadrangle tangential; the opposite firing is positioned at two sides of the hearth, and each side can be provided with one or two groups of symmetrical pulverized coal burners.
The burner type of the invention makes full use of the characteristic of the burning mode of the die-cut circles. Because tangential firing is located at the center of the hearth, pulverized coal airflow with high rigidity and high penetrating power is needed to meet the requirement of tangential firing quantity, and stable tangential firing is formed at the center of the hearth. Opposite firing is located on two sides of the hearth, far from the firing center of the hearth, the static stable firing capability of a single burner needs to be improved, and stable firing support is provided for dynamic tangential firing in the center of the hearth, so that the whole firing of the hearth is maintained.
Drawings
FIG. 1 is a schematic diagram of the structure of the present invention;
FIG. 2 is a schematic diagram of the combustion of a burner within a boiler;
the marks in the figure are as follows: 1. the device comprises a gas nozzle, a 2-part burner, a 3-part tertiary air nozzle, a 4-part baffle, a 5-part hearth.
Detailed Description
Preferred embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
The embodiment of the invention comprises the following steps: as shown in fig. 1, a split burner structure of a utility boiler comprises a gas nozzle 1, a split burner 2, a tertiary air nozzle 3, a partition plate 4 and a hearth 5, wherein the partition plate 4 is arranged in the split burner 2 to divide the split burner 2 into the gas nozzle 1 and the tertiary air nozzle 3; the installation position of the split burner 2 is tangential to the center of the hearth 5.
The number of the divided type burners 2 is 4 in total.
The partition board 4 is connected with the inner wall of the split burner 2 in a welding mode.
The method for dividing the gas burner comprises the steps that a gas and tertiary air dividing type burner structure is adopted by a dividing type burner 2, vertical and vertical division is adopted by the dividing type burner 2, a gas nozzle 1 is arranged on the fire side of the dividing type burner, and a tertiary air nozzle 3 is arranged on the back fire side of the dividing type burner; the hearth is in a tangential combustion mode, and the split burner 2 is positioned at the upper layer of the combustion group of the hearth 1.
The tertiary air nozzle 3 can be replaced by primary air pulverized coal or secondary air.
Fig. 1 is a gas and tertiary air split burner. The specific method is that the split type burner (2) adopts vertical and vertical split, and the split areas of the gas nozzle 1 part and the tertiary air nozzle 3 part are based on the design wind speed of tertiary air and gas.
Fig. 2 is a schematic diagram of the combustion of a burner in a boiler, wherein the gas is arranged on the fire-facing side and the tertiary air is arranged on the back fire side. The combustion tangential circle is positioned at the center of the hearth (5), and a four-corner tangential circle combustion technology is formed by four gas and tertiary air split type burners (2) positioned at the center of the hearth.

Claims (4)

1. A method for partitioning a partitioned burner structure of a utility boiler, the partitioned burner (2) comprising a gas nozzle (1), a tertiary air nozzle (3) and a partition (4); the method is characterized in that: the inside of the split type burner (2) is provided with a partition plate (4) for dividing the split type burner (2) into a gas nozzle (1) and a tertiary air nozzle (3); the installation position of the split burner (2) is tangential to the center of the hearth (5); the segmentation method comprises the following steps: the split type burner (2) adopts a coal gas and tertiary air split type burner structure, the split type burner (2) adopts vertical split, a fire side of the split type burner is a coal gas nozzle (1), and a back fire side of the split type burner is a tertiary air nozzle (3); the hearth is in a tangential combustion mode, and the split type burner (2) is positioned at the upper layer of the combustion group of the hearth (5).
2. The method for partitioning a split burner structure of a utility boiler as set forth in claim 1, wherein: the number of the divided type burners (2) is 4 in total.
3. The method for partitioning a split burner structure of a utility boiler as set forth in claim 1, wherein: the partition plate (4) is connected with the inner wall of the split burner (2) in a welding mode.
4. The method for partitioning a split burner structure of a utility boiler as set forth in claim 1, wherein: the tertiary air nozzle (3) can be replaced by primary air pulverized coal or secondary air.
CN201710223326.4A 2017-04-07 2017-04-07 Split type burner structure and split method of power station boiler Active CN107131496B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710223326.4A CN107131496B (en) 2017-04-07 2017-04-07 Split type burner structure and split method of power station boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710223326.4A CN107131496B (en) 2017-04-07 2017-04-07 Split type burner structure and split method of power station boiler

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CN107131496A CN107131496A (en) 2017-09-05
CN107131496B true CN107131496B (en) 2023-10-27

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Citations (16)

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Publication number Priority date Publication date Assignee Title
CN2385221Y (en) * 1999-09-13 2000-06-28 孙昌楷 Gas burner
CN2559889Y (en) * 2002-08-21 2003-07-09 牛锦林 Coal and gas integral clean combustion boiler
JP2005241107A (en) * 2004-02-25 2005-09-08 Mitsubishi Heavy Ind Ltd Biomass mixing and burning device and mixing and burning method
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CN201041356Y (en) * 2007-03-21 2008-03-26 鞍钢股份有限公司 Coal dust gas dual-purpose boiler
CA2608054A1 (en) * 2006-10-24 2008-04-24 Air Products And Chemicals, Inc. Pulverized solid fuel burner
CN201093503Y (en) * 2007-08-01 2008-07-30 黄显宝 Middle thermal value coal gas and powder dual-purpose combustor
CN101881443A (en) * 2010-07-21 2010-11-10 山西蓝天环保设备有限公司 Fuel-free gas igniting and combustion stabilizing method for industrial coal powder boiler
CN102042614A (en) * 2009-10-19 2011-05-04 章礼道 Natural gas ignition system for coal burning boiler in generating plant
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WO2013073366A1 (en) * 2011-11-16 2013-05-23 三菱重工業株式会社 Oil-fired burner, solid fuel-fired burner unit and solid fuel-fired boiler
CN103672862A (en) * 2013-12-31 2014-03-26 北京国电龙高科环境工程技术有限公司 Low-nitrogen combustion device without primary air and secondary air, and application method
CN106090894A (en) * 2016-08-23 2016-11-09 翼特新能源科技(上海)有限公司 The all-oxygen combustion device of a kind of low NOx and combustion method thereof and application
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2385221Y (en) * 1999-09-13 2000-06-28 孙昌楷 Gas burner
CN2559889Y (en) * 2002-08-21 2003-07-09 牛锦林 Coal and gas integral clean combustion boiler
JP2005241107A (en) * 2004-02-25 2005-09-08 Mitsubishi Heavy Ind Ltd Biomass mixing and burning device and mixing and burning method
CN1789806A (en) * 2004-12-13 2006-06-21 中国科学院过程工程研究所 Multi-side stereo combustion boiler capable of realizing clean combustion of coal and combustion method thereof
CN101122385A (en) * 2006-08-10 2008-02-13 北京众恒力热能环保科技有限公司 Coal, gas integral cleaning combustion boiler
CA2608054A1 (en) * 2006-10-24 2008-04-24 Air Products And Chemicals, Inc. Pulverized solid fuel burner
CN1959205A (en) * 2006-11-30 2007-05-09 上海交通大学 Combustion method of anthracite coal
CN201041356Y (en) * 2007-03-21 2008-03-26 鞍钢股份有限公司 Coal dust gas dual-purpose boiler
CN201093503Y (en) * 2007-08-01 2008-07-30 黄显宝 Middle thermal value coal gas and powder dual-purpose combustor
CN102042614A (en) * 2009-10-19 2011-05-04 章礼道 Natural gas ignition system for coal burning boiler in generating plant
CN101881443A (en) * 2010-07-21 2010-11-10 山西蓝天环保设备有限公司 Fuel-free gas igniting and combustion stabilizing method for industrial coal powder boiler
CN102213422A (en) * 2011-04-21 2011-10-12 扬州市银焰机械厂 Multi-channel mixed gas burner
WO2013073366A1 (en) * 2011-11-16 2013-05-23 三菱重工業株式会社 Oil-fired burner, solid fuel-fired burner unit and solid fuel-fired boiler
CN103672862A (en) * 2013-12-31 2014-03-26 北京国电龙高科环境工程技术有限公司 Low-nitrogen combustion device without primary air and secondary air, and application method
CN106090894A (en) * 2016-08-23 2016-11-09 翼特新能源科技(上海)有限公司 The all-oxygen combustion device of a kind of low NOx and combustion method thereof and application
CN207006124U (en) * 2017-04-07 2018-02-13 贵州电网有限责任公司电力科学研究院 A kind of Splittable burner structure of station boiler

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