CN108397767B - Low-bed-pressure low-air-volume combustion operation method for circulating fluidized bed boiler - Google Patents

Low-bed-pressure low-air-volume combustion operation method for circulating fluidized bed boiler Download PDF

Info

Publication number
CN108397767B
CN108397767B CN201810182448.8A CN201810182448A CN108397767B CN 108397767 B CN108397767 B CN 108397767B CN 201810182448 A CN201810182448 A CN 201810182448A CN 108397767 B CN108397767 B CN 108397767B
Authority
CN
China
Prior art keywords
air pipeline
secondary air
primary air
air
pipeline
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.)
Active
Application number
CN201810182448.8A
Other languages
Chinese (zh)
Other versions
CN108397767A (en
Inventor
刘国发
陶冬
毛雄伟
刘伟
费旭勇
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang Zhefeng Energy Development Co ltd
Original Assignee
Zhejiang Zhefeng Energy Development Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Zhejiang Zhefeng Energy Development Co ltd filed Critical Zhejiang Zhefeng Energy Development Co ltd
Priority to CN201810182448.8A priority Critical patent/CN108397767B/en
Publication of CN108397767A publication Critical patent/CN108397767A/en
Application granted granted Critical
Publication of CN108397767B publication Critical patent/CN108397767B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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 
    • F23C10/00Fluidised bed combustion apparatus
    • F23C10/18Details; Accessories
    • F23C10/20Inlets for fluidisation air, e.g. grids; Bottoms
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L1/00Passages or apertures for delivering primary air for combustion 
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L5/00Blast-producing apparatus before the fire
    • F23L5/02Arrangements of fans or blowers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L9/00Passages or apertures for delivering secondary air for completing combustion of fuel 

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

The invention provides a low-bed-pressure low-air-volume combustion operation method of a circulating fluidized bed boiler, which comprises the following steps of: the fuel sequentially passes through a first oxygen-deficient combustion zone, a second reduction combustion zone and a third burnout zone from bottom to top to be combusted; a primary air pipeline is arranged at the lower part of the hearth of the first oxygen-deficient combustion area, primary air enters the air distribution plate through the primary air pipeline, and the thickness of a bottom material on the air distribution plate is less than 500 mm; the bottom material is slag discharged in the operation of a boiler, the grain size of the slag is less than 8mm, and the content of combustible substances is not more than 5%; and in the combustion operation process, the primary air quantity is controlled not to exceed 1.25 times of the critical fluidization air quantity. The invention reduces the bed pressure, reduces the air quantity, reduces the energy consumption of a thermal power plant, and simultaneously can reduce the abrasion to a hearth.

Description

Low-bed-pressure low-air-volume combustion operation method for circulating fluidized bed boiler
Technical Field
The invention relates to the technical field of boiler equipment of coal-fired power plants, in particular to a low-bed-pressure low-air-volume combustion operation method of a circulating fluidized bed boiler.
Background
More than 70% of electricity in China comes from thermal power plants, wherein the coal-electricity accounts for 92% and the gas-electricity accounts for 4%. Coal-fired power plants use coal as an energy source, convert the chemical energy of the coal into mechanical energy, and convert the mechanical energy into electric energy through a turbine generator.
In recent years, with the rapid increase of economy, the problems of large resource consumption, large waste and low resource utilization rate in China become more and more prominent, and resource shortage becomes a serious problem facing the economic development in China, so that the energy conservation and emission reduction is vigorously advocated by the nation at present. Thermal power generation plays a leading role in the power generation pattern of China, reduces energy consumption in various aspects of thermal power generation, and is also an important channel for realizing energy conservation and emission reduction.
Disclosure of Invention
The invention provides a low-bed-pressure low-air-volume combustion operation method for a circulating fluidized bed boiler, which reduces the energy consumption of a thermal power plant by reducing bed pressure and air volume and can also reduce the abrasion to a hearth.
In order to achieve the purpose, the technical scheme of the invention is as follows:
a low-bed-pressure low-air-volume combustion operation method of a circulating fluidized bed boiler comprises the following steps:
the fuel sequentially passes through a first oxygen-deficient combustion zone, a second reduction combustion zone and a third burnout zone from bottom to top to be combusted;
a primary air pipeline is arranged at the lower part of the hearth of the first oxygen-deficient combustion area, primary air enters the air distribution plate through the primary air pipeline, the thickness of a bed charge on the air distribution plate is less than 500mm, and a lower secondary air pipeline and an upper secondary air pipeline are respectively arranged at the lower part and the upper part of the hearth of the second reduction combustion area; the outer end of the primary air pipeline is connected with the primary air fan, and the outer ends of the lower secondary air pipeline and the upper secondary air pipeline are respectively connected with the lower secondary air fan and the upper secondary air fan;
the bottom material is slag discharged in the operation of a boiler, the grain size of the slag is less than 8mm, and the content of combustible substances is not more than 5%;
and in the combustion operation process, the primary air quantity is controlled not to exceed 1.25 times of the critical fluidization air quantity.
Furthermore, a mushroom-shaped cap is arranged at the inner end of the primary air pipeline extending into the hearth, air outlet holes are obliquely and outwards penetrated in the cap, the inner diameter of the middle section of each air outlet hole is smaller than that of the front section and the rear section, and the front section is in oblique line smooth connection with the middle section and the middle section is in oblique line smooth connection with the rear section.
Further, the outer surface of the cap is coated with a wear resistant anti-stick coating.
Further, the primary air pipeline, the lower secondary air pipeline and the upper secondary air pipeline stretch into the hearth by 5-10 cm, and the vibrators are arranged at the ends, close to the outer part of the hearth, of the primary air pipeline, the lower secondary air pipeline and the upper secondary air pipeline.
Furthermore, the minimum wind pressure at the outlet of the primary wind pipeline is more than or equal to the bed pressure.
Furthermore, the inner diameter of the middle section of the air outlet hole is 1/4-1/3 of the inner diameter of the front section/the inner diameter of the rear section.
Further, the thickness of the base material is d, when d is larger than 250mm and smaller than 350mm, the opening degree of the primary air fan is 55-62%, when d is larger than or equal to 350mm and smaller than 450mm, the opening degree of the primary air fan is 63-65%, and when d is larger than or equal to 450mm and smaller than or equal to 500mm, the opening degree of the primary air fan is 66-70%.
Further, the opening degree of the lower secondary air fan is 90-95%.
Further, go up the overgrate air pipeline and evenly be provided with four groups along furnace is radial, go up the one end that the overgrate air pipeline stretched into furnace and be 30~45 contained angle with the furnace tangent line.
The circulating fluidized bed boiler low-bed-pressure low-air-volume combustion operation method has the following advantages:
(1) the hearth is divided into a first oxygen-deficient combustion area, a second reduction combustion area and a third burnout area, so that more fuel is concentrated in the second reduction combustion area 6 for combustion, the air volume of primary air can be reduced, and the coking phenomenon caused by temperature rise due to reduction of the air volume of the primary air is avoided.
(2) The slag is used as a bottom material, the slag is light in texture, and the fluidity of the fuel can be improved, the bed pressure is reduced and the bed temperature is controlled by controlling the particle size.
(3) The invention can effectively reduce the air quantity, the bed pressure and the energy consumption of a thermal power plant, simultaneously reduce the impact of primary air and secondary air on the inner wall of the hearth, reduce the abrasion phenomenon in the boiler and have better popularization and application prospects.
Drawings
Fig. 1 is a schematic front view of the present invention.
Fig. 2 is a schematic cross-sectional enlarged structure of the cap.
In the figure, a primary air pipeline 1, a first oxygen-deficient combustion area 2, a lower secondary air pipeline 3, an upper secondary air pipeline 4, a third burnout area 5, a second reduction combustion area 6, an air distribution plate 7, a cap 8 and an air outlet 9.
Detailed Description
The present invention is further illustrated by the following examples, but the scope of the present invention is not limited to the following examples.
A low-bed-pressure low-air-volume combustion operation method of a circulating fluidized bed boiler comprises the following steps:
the fuel sequentially passes through a first oxygen-deficient combustion zone 2, a second reduction combustion zone 6 and a third burnout zone 5 from bottom to top for combustion; a primary air pipeline 1 is arranged at the lower part of a hearth of the first oxygen-deficient combustion zone 2, primary air enters an air distribution plate 7 through the primary air pipeline 1, the thickness of a bottom material on the air distribution plate 7 is less than 500mm, and a lower secondary air pipeline 3 and an upper secondary air pipeline 4 are respectively arranged at the lower part and the upper part of the hearth of the second reduction combustion zone 6; the outer end of the primary air pipeline 1 is connected with a primary air blower, and the outer ends of the lower secondary air pipeline 3 and the upper secondary air pipeline 4 are respectively connected with a lower secondary air blower and an upper secondary air blower; the hearth is divided into a first oxygen-deficient combustion area 2, a second reduction combustion area 6 and a third burnout area 5, so that more fuel is concentrated in the second reduction combustion area 6 for combustion, the air volume of primary air can be reduced, and the coking phenomenon caused by temperature rise due to reduction of the air volume of the primary air is avoided.
The bottom material of the fluidized bed boiler is slag discharged in the operation of the boiler, the grain size of the slag is less than 8mm, the content of combustible substances is not more than 5 percent, the slag is light, and the flowing property of fuel can be improved, the bed pressure is reduced, and the bed temperature is controlled by controlling the grain size; and in the combustion operation process, the primary air quantity is controlled not to exceed 1.25 times of the critical fluidization air quantity.
Further, for making wind-distributing even once, improve the whole mobility of bed material, reduce bed pressure, the inner that a wind pipeline 1 deepened furnace is provided with mushroom type cap 8, the downward outside venthole 9 that wears to be equipped with of slope in the cap 8, the internal diameter in venthole 9 middle section is less than the internal diameter of anterior segment and back end, and anterior segment and middle section, the middle segment is slash smooth connection with the back end, the cap 8 of mushroom type enables the dregs of a fall and can not produce and pile up along the cap downward flow, also avoid being blockked up in venthole department, and lead to a wind pressure to increase. In addition, because gas can form densely at the middle section of venthole 9, lead to pressure increase, can make gas jet get into furnace with the pressure differential of bed pressure, better acceleration the flow of bed material to reduce the bed pressure, the internal diameter of venthole 9 middle section is 1/4~1/3 suitable for anterior segment/back end internal diameter. Also, to prevent debris from clogging cap 8, the outer surface of cap 8 is coated with a wear resistant anti-stick coating.
Further, the primary air pipeline 1, the lower secondary air pipeline 3 and the upper secondary air pipeline 4 extend into the hearth by 5-10 cm, one ends, located outside the hearth and close to the hearth, of the primary air pipeline 1, the lower secondary air pipeline 3 and the upper secondary air pipeline 4 are provided with vibrators, the vibrators can prevent blocking caused by coking or fuel enrichment, and stable operation of the fluidized bed boiler under the condition of low air volume is further guaranteed.
Furthermore, the minimum air pressure at the outlet of the primary air pipeline 1 is more than or equal to the bed pressure so as to ensure that the bed material can stably flow. Similarly, in order to ensure the normal flow of bed materials and prevent the temperature of the first oxygen-deficient combustion area 2 from being too high, the thickness of the bed materials is d, when d is more than 250mm and less than 350mm, the opening degree of the primary air fan is 55-62%, when d is more than or equal to 350mm and less than 450mm, the opening degree of the primary air fan is 63-65%, and when d is more than or equal to 450mm and less than or equal to 500mm, the opening degree of the primary air fan is 66-70%.
In second reduction combustion area 6, for forming the whirl here with higher speed, make temperature distribution more even, reduce because of the possibility of high temperature formation nitrogen oxide, lower secondary fan's aperture is 90~95%, and goes up secondary air pipeline 3 and evenly be provided with four groups along furnace is radial, goes up the secondary air pipeline and stretches into furnace's one end and furnace tangent line and be 30~45 contained angle.

Claims (2)

1. A low-bed-pressure low-air-volume combustion operation method of a circulating fluidized bed boiler is characterized by comprising the following steps of:
the fuel sequentially passes through a first oxygen-deficient combustion zone, a second reduction combustion zone and a third burnout zone from bottom to top to be combusted;
a primary air pipeline is arranged at the lower part of the hearth of the first oxygen-deficient combustion area, primary air enters the air distribution plate through the primary air pipeline, the thickness of a bed charge on the air distribution plate is less than 500mm, and a lower secondary air pipeline and an upper secondary air pipeline are respectively arranged at the lower part and the upper part of the hearth of the second reduction combustion area; the outer end of the primary air pipeline is connected with the primary air fan, and the outer ends of the lower secondary air pipeline and the upper secondary air pipeline are respectively connected with the lower secondary air fan and the upper secondary air fan;
the bottom material is slag discharged in the operation of a boiler, the grain size of the slag is less than 8mm, and the content of combustible substances is not more than 5%;
in the combustion operation process, the primary air quantity is controlled not to exceed 1.25 times of the critical fluidization air quantity;
the inner end of the primary air pipeline, which extends into the hearth, is provided with a mushroom-shaped cap, an air outlet hole is obliquely and downwards and outwards arranged in the cap, the inner diameter of the middle section of the air outlet hole is smaller than that of the front section and the rear section, and the front section is smoothly connected with the middle section and the rear section in a diagonal manner;
the outer surface of the cap is coated with a wear-resistant anti-sticking coating;
the primary air pipeline, the lower secondary air pipeline and the upper secondary air pipeline extend into the hearth by 5-10 cm, and the primary air pipeline, the lower secondary air pipeline and the upper secondary air pipeline are positioned outside the hearth and are provided with vibrators at the ends close to the primary air pipeline, the lower secondary air pipeline and the upper secondary air pipeline;
four groups of upper secondary air pipelines are uniformly arranged along the radial direction of the hearth, and an included angle of 30-45 degrees is formed between one end of each upper secondary air pipeline extending into the hearth and the tangent line of the hearth;
the inner diameter of the middle section of the air outlet hole is 1/4-1/3 of the inner diameter of the front section/the inner diameter of the rear section;
the thickness of the base material is d, when d is larger than 250mm and smaller than 350mm, the opening degree of the primary air fan is 55-62%, when d is larger than or equal to 350mm and smaller than 450mm, the opening degree of the primary air fan is 63-65%, and when d is larger than or equal to 450mm and smaller than or equal to 500mm, the opening degree of the primary air fan is 66-70%;
the opening degree of the lower secondary air fan is 90-95%.
2. The circulating fluidized bed boiler low bed pressure low air volume combustion operation method according to claim 1, characterized in that:
the minimum wind pressure at the outlet of the primary wind pipeline is more than or equal to the bed pressure.
CN201810182448.8A 2018-03-06 2018-03-06 Low-bed-pressure low-air-volume combustion operation method for circulating fluidized bed boiler Active CN108397767B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810182448.8A CN108397767B (en) 2018-03-06 2018-03-06 Low-bed-pressure low-air-volume combustion operation method for circulating fluidized bed boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810182448.8A CN108397767B (en) 2018-03-06 2018-03-06 Low-bed-pressure low-air-volume combustion operation method for circulating fluidized bed boiler

Publications (2)

Publication Number Publication Date
CN108397767A CN108397767A (en) 2018-08-14
CN108397767B true CN108397767B (en) 2020-09-01

Family

ID=63091973

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810182448.8A Active CN108397767B (en) 2018-03-06 2018-03-06 Low-bed-pressure low-air-volume combustion operation method for circulating fluidized bed boiler

Country Status (1)

Country Link
CN (1) CN108397767B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110410775A (en) * 2019-07-18 2019-11-05 山东圣坤环保科技有限公司 Solid fuel combustion apparatus

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10103641A (en) * 1996-10-01 1998-04-21 Takuma Co Ltd Method for supplying combustion air for fluidized bed combustion equipment
CN102003701A (en) * 2010-11-23 2011-04-06 浙江大学 Low NOx coal dust combustion method and device based on underfire air and overfire air
CN103216821A (en) * 2013-04-27 2013-07-24 东方电气集团东方锅炉股份有限公司 Multi-stage stratified combustion system and method for primary air and secondary air of boiler
CN103604117A (en) * 2013-11-04 2014-02-26 武汉和信益科技有限公司 Multi-grade high-efficiency low-nitrogen combustion method and multi-grade high-efficiency low-nitrogen combustion system for circulating fluidized bed boiler
CN103712208A (en) * 2013-12-25 2014-04-09 北京兴侨国际工程技术有限公司 Combustion method of circulating fluidized bed boiler with low nitrogen oxide emission
CN104373934A (en) * 2014-11-03 2015-02-25 中国华能集团清洁能源技术研究院有限公司 Device and method for preparing, storing and adding circulating material of circulating fluidized bed boiler
CN105258113A (en) * 2015-10-26 2016-01-20 隋恒睿 Low-heating-value liquid and solid fluidized bed boiler and combustion technology
CN206112913U (en) * 2016-07-29 2017-04-19 任浩 Special pressure boost hood in corner

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10103641A (en) * 1996-10-01 1998-04-21 Takuma Co Ltd Method for supplying combustion air for fluidized bed combustion equipment
CN102003701A (en) * 2010-11-23 2011-04-06 浙江大学 Low NOx coal dust combustion method and device based on underfire air and overfire air
CN103216821A (en) * 2013-04-27 2013-07-24 东方电气集团东方锅炉股份有限公司 Multi-stage stratified combustion system and method for primary air and secondary air of boiler
CN103604117A (en) * 2013-11-04 2014-02-26 武汉和信益科技有限公司 Multi-grade high-efficiency low-nitrogen combustion method and multi-grade high-efficiency low-nitrogen combustion system for circulating fluidized bed boiler
CN103712208A (en) * 2013-12-25 2014-04-09 北京兴侨国际工程技术有限公司 Combustion method of circulating fluidized bed boiler with low nitrogen oxide emission
CN104373934A (en) * 2014-11-03 2015-02-25 中国华能集团清洁能源技术研究院有限公司 Device and method for preparing, storing and adding circulating material of circulating fluidized bed boiler
CN105258113A (en) * 2015-10-26 2016-01-20 隋恒睿 Low-heating-value liquid and solid fluidized bed boiler and combustion technology
CN206112913U (en) * 2016-07-29 2017-04-19 任浩 Special pressure boost hood in corner

Also Published As

Publication number Publication date
CN108397767A (en) 2018-08-14

Similar Documents

Publication Publication Date Title
CN100451447C (en) Combustion method of anthracite coal
CN110260301B (en) Ultralow-emission energy-saving biomass circulating fluidized bed boiler
CN107940448B (en) Pulverized coal particle circulating fluidized bed combustion system and combustion method thereof
CN210772139U (en) Circulating fluidized bed boiler hood and air distribution plate with same
CN108397767B (en) Low-bed-pressure low-air-volume combustion operation method for circulating fluidized bed boiler
CN206881826U (en) Improve the medium-speed pulverizer unit pulverized-coal system contributed with quality of pc
CN111396867A (en) Boiler pulverized coal combustion method with adjustable combustion tangent circle diameter
CN204100231U (en) A kind of CFB boiler
CN206944137U (en) CFBB based on denitration minimum discharge technology
CN104154532A (en) Center air ring concentrated type turbulent burner
CN103697467B (en) Method for coal slime combustion of circulating fluidized bed boiler
CN108343948B (en) Beam type air distribution slag discharging device for circulating fluidized bed boiler
CN111592915A (en) Fluidized bed gasification device and gasification method
CN208776673U (en) A kind of high-temperature burner
CN208504375U (en) A kind of low NOx drainage circulating fluidized bed boiler using high nitrogen biomass
WO2013020360A1 (en) Differential-velocity multi-cyclone conical-bed air distribution structure
CN109931597A (en) A kind of fuel staging gasification and low NOXBurning boiler
CN213924675U (en) Gasification furnace with double-helix burners
CN101280915B (en) W flame boiler furnace arranging air nozzle on side wall
CN109724086B (en) Oxygen-enriched multi-flame direct-current burner suitable for inferior coal
CN209445349U (en) A kind of composite rotating coupling nonuniform air distribution plate
CN207999809U (en) Circulating fluidized bed boiler beam type cloth wind slag-draining device
CN207247192U (en) The side wind and side combustion exhausted wind apparatus of front-back wall burning
CN216667660U (en) Coal feeding air structure
CN108167824B (en) Circulating fluidized bed power station boiler system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant