CN107940446A - A kind of big volume inhales jet stream after-flame wind system and injection method - Google Patents

A kind of big volume inhales jet stream after-flame wind system and injection method Download PDF

Info

Publication number
CN107940446A
CN107940446A CN201711294863.4A CN201711294863A CN107940446A CN 107940446 A CN107940446 A CN 107940446A CN 201711294863 A CN201711294863 A CN 201711294863A CN 107940446 A CN107940446 A CN 107940446A
Authority
CN
China
Prior art keywords
burnout degree
nozzle
jet stream
burnout
layer
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.)
Granted
Application number
CN201711294863.4A
Other languages
Chinese (zh)
Other versions
CN107940446B (en
Inventor
张定海
孔红兵
杨章宁
韦耿
聂立
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.)
Dongfang Boiler Group Co Ltd
Original Assignee
Dongfang Boiler Group 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 Dongfang Boiler Group Co Ltd filed Critical Dongfang Boiler Group Co Ltd
Priority to CN201711294863.4A priority Critical patent/CN107940446B/en
Publication of CN107940446A publication Critical patent/CN107940446A/en
Application granted granted Critical
Publication of CN107940446B publication Critical patent/CN107940446B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • F23C7/002Combustion apparatus characterised by arrangements for air supply the air being submitted to a rotary or spinning motion
    • 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 
    • F23C9/00Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
    • F23C9/06Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber for completing combustion

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

The top layer fire air nozzle on jet stream after-flame wind system, including burner hearth, the front wall arranged on burner hearth and rear wall is inhaled the invention discloses a kind of big volume, it is characterised in that:At least one layer of burnout degree nozzle is equipped with front wall and rear wall between top layer fire air nozzle and main burner, every layer of burnout degree nozzle includes several burnout degree nozzles, at least one layer of burnout degree nozzle on front wall and/or rear wall inhales jet stream burnout degree nozzle for Y types volume, the nozzle includes connected a blast pipe and two discharge pipes, and two discharge pipes are located at the both sides in blast pipe axis horizontal direction;The invention also discloses the injection method that a kind of big volume inhales jet stream burnout degree;The present invention can also reduce furnace outlet carbonomonoxide concentration and unburned carbon in flue dust while nitrogen oxides is further reduced, and improve efficiency of combustion.

Description

A kind of big volume inhales jet stream after-flame wind system and injection method
Technical field
The present invention relates to a kind of after-flame wind system and injection method, the particularly big volume for pulverized-coal fired boiler to inhale jet stream after-flame Wind system and injection method.
Background technology
Air staged combustion technology is one of low-NO_x combustion technology that current pulverized-coal fired boiler generally uses, its basic principle is The combustion process of fuel is completed stage by stage.The air less than theoretical air requirement is fed in main burner region, fuel is fuel-rich Burn under the conditions of material, combustion zone temperature is horizontal to be reduced, while forms the generation of reducing atmosphere reduction nitrogen oxides.In main burner Fire air nozzle is arranged in top, and the introducing of burnout degree can provide enough oxygen, with uncompleted burned carbon of the after-flame from reducing zone, Ensure efficiency of combustion, reduce unburned carbon in flue dust;Since primary zone is fuel-rich combustion region, and burner arrangement is in forward and backward wall, Therefore all it is distributed in after-flame region major part unburnt gas and uncompleted burned carbon etc. among burner hearth(Depth direction), and nitrogen oxygen Compound is then distributed in close to the region of forward and backward wall.And traditional burnout degree is direct current penetrating, reducing zone can be caused to be broken rapidly Bad, the nitrogen oxides being reduced can generate again in later stage after-flame region because of burnings such as uncompleted burned carbons, results even in flying dust and contains Carbon amounts is bigger than normal, burning-out zone water-cooling wall slagging, outlet gas temperature windage increase, while also reduces air classification emission reduction nitrogen oxides Effect.
The content of the invention
The purpose of the present invention is the above-mentioned deficiency for the prior art, there is provided a kind of big volume inhales jet stream after-flame wind system and spray Shooting method, it can also reduce furnace outlet carbonomonoxide concentration and unburned carbon in flue dust while nitrogen oxides is further reduced, Improve efficiency of combustion.
In order to achieve the above object, big volume of the invention inhales jet stream after-flame wind system, including burner hearth, the front wall arranged on burner hearth With the top layer fire air nozzle on rear wall, it is characterised in that:Front wall between top layer fire air nozzle and main burner and after It is equipped with least one layer of burnout degree nozzle on wall, every layer of burnout degree nozzle includes several burnout degree nozzles, on front wall and/or rear wall At least one layer of burnout degree nozzle inhale jet stream burnout degree nozzle for Y types volume, which includes a connected blast pipe and two outlet air Pipe, two discharge pipes are located at the both sides in blast pipe axis horizontal direction;
Each layer burnout degree nozzle on above-mentioned front wall and rear wall can be that Y types volume inhales jet stream burnout degree nozzle;
Each layer burnout degree nozzle of one of them can be that Y types volume inhales jet stream burnout degree nozzle on above-mentioned front wall and rear wall, separately Each layer burnout degree nozzle on one wall can be direct current burnout degree nozzle;
As a further improvement on the present invention, the depth-width ratio for two discharge pipes that the Y types volume inhales jet stream burnout degree nozzle is 1-6; The angle of two discharge pipes and blast pipe center line is 5 ° -45 °;Larger depth-width ratio and suitable angle, can improve two discharge pipes The jet stream rigidity of the burnout degree of ejection, increase entrainment block domain, strengthens volume and inhales effect;
The present invention is used for the injection method that above-mentioned big volume inhales jet stream after-flame wind system, it is characterised in that comprises the following steps:In stove Spray into several strands of burnout degrees, at least one layer of burnout degree, which passes through Y types volume, to be inhaled jet stream and fire the front wall of thorax reducing zone and rear wall higher slice Wind nozzle forms two high-speed jet burnout degrees in a certain angle in the horizontal direction to the greatest extent, and big recirculating zone is formed in jet expansion, Flue gas among burner hearth is rolled up again to suck back and flows to forward and backward wall both sides, will be distributed over the nitrogen oxides weight close to the forward and backward wall of burner hearth Newly reduced;Remaining each layer sprays into direct current burnout degree by direct current burnout degree nozzle, and the air outlet velocity of direct current burnout degree is less than The air outlet velocity of two strands of high-speed jet burnout degrees, or roll up suction jet stream burnout degree nozzle also by Y types and spray into several strands in the horizontal direction Two high-speed jet burnout degrees in a certain angle.
As a further improvement on the present invention, the air outlet velocity of two strands of high-speed jet burnout degrees is 30m/s≤V≤70m/s; The air outlet velocity of direct current burnout degree is 20m/s≤V≤40m/s;Low-speed DC burnout degree air outlet velocity is relatively low, coordinates the big volume of Y types Jet stream burnout degree is inhaled, the NOX near front-back wall can be sent among big volume suction vortex, further strengthens volume suction effect;
Through being found in many experiments:The flue gas of fuel-rich still has very strong nitrogen oxides reducing power, and the present invention passes through design The burnout degree of entraining type rolls up the flue gas among burner hearth to suck back again flows to forward and backward wall both sides, since reducing zone is fuel-rich cigarette Gas, burner hearth centre fuel-rich flue gas come into full contact with the NOX being distributed near the forward and backward wall of burner hearth, can further reduce NOX, Air classification effect can be strengthened, reduce furnace outlet amount of nitrogen oxides, while the reflux of flue gas can carry unburned particle secretly, prolong The long grain residence time, can reduce outlet CO concentration and unburned carbon in flue dust while nitrogen oxides is reduced, and improve burning effect Rate.
In conclusion it is dense can also to reduce furnace outlet carbon monoxide while nitrogen oxides is further reduced by the present invention Degree and unburned carbon in flue dust, improve efficiency of combustion.
Brief description of the drawings
Fig. 1 is the stereogram for the burner hearth that jet stream after-flame wind system is inhaled using the big volume of the present invention.
Fig. 2 is the vertical view for every layer of burnout degree nozzle of forward and backward wall that the big volume of the present invention inhales jet stream burnout degree system embodiment one Figure.
Fig. 3 is the front view that Y types volume inhales jet stream burnout degree nozzle in Fig. 2.
Fig. 4 is the top view of Fig. 3.
Fig. 5 is the vertical view for every layer of burnout degree nozzle of forward and backward wall that the big volume of the present invention inhales jet stream burnout degree system embodiment two Figure.
Fig. 6 is the vertical view for every layer of burnout degree nozzle of forward and backward wall that the big volume of the present invention inhales jet stream burnout degree system embodiment three Figure.
Embodiment
Below in conjunction with the accompanying drawings, the present invention is described in further detail.
As shown in Figure 1, front wall 1 and rear wall in Pulverized Coal fired Boiler Furnace 5(It is not shown)On along short transverse layering setting There are main burner 2, top layer fire air nozzle 3, top layer fire air nozzle 3 is located at the top of main burner 2, therebetween for burner hearth also Former area;Burnout degree nozzle 4 is equipped with front wall 1 and rear wall between top layer fire air nozzle 3 and main burner 2;
Embodiment one
As shown in Figures 2 to 4, the big volume of the present embodiment inhales jet stream after-flame wind system, including burner hearth 5, the front wall 1 arranged on burner hearth 5 With the top layer fire air nozzle 3 on rear wall 6, on the front wall 1 and rear wall 6 between top layer fire air nozzle 3 and main burner Equipped with two layers of burnout degree nozzle, every layer of burnout degree nozzle includes several burnout degree nozzles 4, the burnout degree nozzle on front wall and rear wall 4 inhale jet stream burnout degree nozzle for Y types volume, which includes connected a blast pipe 7 and two discharge pipes 8, and two discharge pipes 8 are located at The both sides in 7 axis horizontal direction of blast pipe, the depth-width ratio H/K of two discharge pipes is 1-6;Two discharge pipes and blast pipe center line Angle α is 5 ° -45 °;
The injection method of jet stream after-flame wind system is inhaled for above-mentioned big volume, is comprised the following steps:1 He of front wall in burner hearth reducing zone Point four layers of ground spray into several strands of burnout degrees on wall 6 afterwards, and every layer of burnout degree rolls up two outlet air for inhaling jet stream burnout degree nozzle 4 by Y types Pipe 8 forms two strands of high-speed jet burnout degrees in a certain angle in the horizontal direction, its air outlet velocity is 30m/s≤V≤70m/s, Big recirculating zone is formed in jet expansion, the flue gas among burner hearth 5 is rolled up to suck back again flows to forward and backward wall both sides, will be distributed over Nitrogen oxides close to the forward and backward wall of burner hearth re-starts reduction;Top layer fire air nozzle 3 sprays into direct current burnout degree, it goes out one's intention as revealed in what one says Speed is 20m/s≤V≤40m/s, and the air outlet velocity of consistently lower than two strands high-speed jet burnout degrees.
Since through sedimentation furnace, experimental results demonstrate the flue gas of fuel-rich still has very strong nitrogen oxides reducing power, originally Flue gas among burner hearth 5 is rolled up to suck back by designing the burnout degree of reducing zone entraining type by invention again flows to forward and backward wall both sides, by It is fuel-rich flue gas in reducing zone, burner hearth centre fuel-rich flue gas comes into full contact with the NOX being distributed near the forward and backward wall of burner hearth, NOX can be further reduced, air classification effect can be strengthened, furnace outlet amount of nitrogen oxides is reduced, before and after tradition Wall burnout degree liquidates feeding mode, and NOX can reduce about 10% or so;The reflux of flue gas at the same time can carry unburned particle, extension secretly The grain residence time, can reduce outlet CO concentration and unburned carbon in flue dust while nitrogen oxides is reduced, and improve efficiency of combustion;Compared with Big depth-width ratio H/K and suitable angle α, can improve the jet stream rigidity of the burnout degree of two discharge pipes 8 ejection, increase entrainment block Domain, strengthens volume and inhales effect.
As shown in Figure 5 to Figure 6, compared with embodiment one, the big volume of embodiment two and three inhales jet stream after-flame wind system, it is poor It is not only that:One layer of burnout degree nozzle is equipped with front wall 1 and rear wall 6 respectively, every layer of burnout degree nozzle includes several after-flames Burnout degree nozzle 4 on wind nozzle, only front wall 1 or rear wall 6 is rolled up for Y types inhales jet stream burnout degree nozzle, each on another wall 6 or 1 Layer burnout degree nozzle is direct current burnout degree nozzle 9;
Big volume for embodiment two or three inhales the injection method of jet stream after-flame wind system, comprises the following steps:Reduced in burner hearth Point four floor ground sprays into several strands of burnout degrees on the front wall 1 in area or rear wall 6, and every layer of burnout degree is inhaled jet stream burnout degree by Y types volume and sprayed Two discharge pipes 8 of mouth 4 form two strands of high-speed jet burnout degrees in a certain angle in the horizontal direction, its air outlet velocity is 30m/s ≤ V≤70m/s, forms big recirculating zone in jet expansion, the flue gas among burner hearth 5 is rolled up to suck back again flows to forward and backward wall two Side, the nitrogen oxides that will be distributed over close to the forward and backward wall of burner hearth re-start reduction;Lead on corresponding rear wall 6 or front wall 1 To cross direct current burnout degree nozzle 9 and spray into four layers of direct current burnout degree, its air outlet velocity is 20m/s≤V≤40m/s, and consistently lower than two The air outlet velocity of stock high-speed jet burnout degree.Using front wall(Or rear wall)Arrange that the big volume of Y types inhales jet stream burnout degree, then wall(Before Wall)Using low-speed DC burnout degree, low-speed DC burnout degree air outlet velocity is relatively low, coordinates the big volume of Y types to inhale jet stream burnout degree, can be with Among NOX near front-back wall is sent to big volume suction vortex, further strengthen volume suction effect.

Claims (6)

1. a kind of big volume inhales the top layer burnout degree spray on jet stream after-flame wind system, including burner hearth, the front wall arranged on burner hearth and rear wall Mouthful, it is characterised in that:At least one layer of after-flame is equipped with front wall and rear wall between top layer fire air nozzle and main burner Wind nozzle, every layer of burnout degree nozzle include several burnout degree nozzles, and at least one layer of burnout degree nozzle on front wall and/or rear wall is Y types volume inhales jet stream burnout degree nozzle, which includes connected a blast pipe and two discharge pipes, and two discharge pipes are located at blast pipe axis The both sides of line horizontal direction.
2. a kind of big volume according to claim 1 inhales jet stream after-flame wind system, it is characterised in that:It is each on front wall and rear wall Layer burnout degree nozzle is that Y types volume inhales jet stream burnout degree nozzle.
3. a kind of big volume according to claim 1 or 2 inhales jet stream after-flame wind system, it is characterised in that:On front wall and rear wall Each layer burnout degree nozzle of one of them is rolled up for Y types inhales jet stream burnout degree nozzle, and each layer burnout degree nozzle on another wall is straight Flow burnout degree nozzle.
4. a kind of big volume according to any one of claims 1 to 3 inhales jet stream after-flame wind system, it is characterised in that:The Y types volume The depth-width ratio for inhaling two discharge pipes of jet stream burnout degree nozzle is 1-6;The angle of two discharge pipes and blast pipe center line is 5 °- 45°。
5. the injection method of jet stream after-flame wind system is inhaled for big volume as claimed in claim 1, it is characterised in that including following step Suddenly:Several strands of burnout degrees are sprayed into the front wall of burner hearth reducing zone and rear wall higher slice, at least one layer of burnout degree passes through Y types volume and inhales Jet stream burnout degree nozzle forms two high-speed jet burnout degrees in a certain angle in the horizontal direction, and big return is formed in jet expansion Area is flowed, the flue gas among burner hearth is rolled up again to suck back flows to forward and backward wall both sides, will be distributed over the nitrogen oxygen close to the forward and backward wall of burner hearth Compound re-starts reduction;Remaining each layer sprays into direct current burnout degree or also sprays into several strands in a certain angle two high in the horizontal direction Rapid fire stream burnout degree, the air outlet velocity of direct current burnout degree are less than the air outlet velocity of two strands of high-speed jet burnout degrees.
6. the injection method of jet stream burnout degree is inhaled according to big volume as claimed in claim 5, it is characterised in that two bursts of high-speed jet combustions The air outlet velocity of wind to the greatest extent is 30m/s≤V≤70m/s;The air outlet velocity of direct current burnout degree is 20m/s≤V≤40m/s.
CN201711294863.4A 2017-12-08 2017-12-08 Large entrainment jet flow over-fire air system and jet method Active CN107940446B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711294863.4A CN107940446B (en) 2017-12-08 2017-12-08 Large entrainment jet flow over-fire air system and jet method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711294863.4A CN107940446B (en) 2017-12-08 2017-12-08 Large entrainment jet flow over-fire air system and jet method

Publications (2)

Publication Number Publication Date
CN107940446A true CN107940446A (en) 2018-04-20
CN107940446B CN107940446B (en) 2024-01-16

Family

ID=61946209

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711294863.4A Active CN107940446B (en) 2017-12-08 2017-12-08 Large entrainment jet flow over-fire air system and jet method

Country Status (1)

Country Link
CN (1) CN107940446B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111146544A (en) * 2019-12-30 2020-05-12 电子科技大学 Efficient cooling structure for small high-power millimeter wave device

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999066261A1 (en) * 1998-06-17 1999-12-23 John Zink Company, L.L.C. LOW NOx AND LOW CO BURNER AND METHOD FOR OPERATING SAME
US20050058958A1 (en) * 2003-09-16 2005-03-17 Hisashi Kobayashi Low NOx combustion using cogenerated oxygen and nitrogen streams
WO2009152654A1 (en) * 2008-06-17 2009-12-23 哈尔滨工业大学 Horizontal thick and thin direct-current pulverized coal burner arranged by wall type
CN101737771A (en) * 2009-12-18 2010-06-16 上海锅炉厂有限公司 Multistage over fire air distributing mode
CN101900325A (en) * 2010-07-16 2010-12-01 浙江大学 Pulverized coal fired boiler wall type oscillating low NOx over-fire air device
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
CN203907595U (en) * 2014-06-13 2014-10-29 烟台龙源电力技术股份有限公司 Boiler
CN105114944A (en) * 2015-09-17 2015-12-02 西安西热锅炉环保工程有限公司 Air staged-combustion vertical and horizontal combined arrangement type over fire air system for tangential boiler
CN106247320A (en) * 2016-07-29 2016-12-21 东方电气集团东方锅炉股份有限公司 A kind of opposed firing boiler degree of depth denitration combustion method
CN207674431U (en) * 2017-12-08 2018-07-31 东方电气集团东方锅炉股份有限公司 A kind of big volume suction jet stream after-flame wind system

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999066261A1 (en) * 1998-06-17 1999-12-23 John Zink Company, L.L.C. LOW NOx AND LOW CO BURNER AND METHOD FOR OPERATING SAME
US20050058958A1 (en) * 2003-09-16 2005-03-17 Hisashi Kobayashi Low NOx combustion using cogenerated oxygen and nitrogen streams
WO2009152654A1 (en) * 2008-06-17 2009-12-23 哈尔滨工业大学 Horizontal thick and thin direct-current pulverized coal burner arranged by wall type
CN101737771A (en) * 2009-12-18 2010-06-16 上海锅炉厂有限公司 Multistage over fire air distributing mode
CN101900325A (en) * 2010-07-16 2010-12-01 浙江大学 Pulverized coal fired boiler wall type oscillating low NOx over-fire air device
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
CN203907595U (en) * 2014-06-13 2014-10-29 烟台龙源电力技术股份有限公司 Boiler
CN105114944A (en) * 2015-09-17 2015-12-02 西安西热锅炉环保工程有限公司 Air staged-combustion vertical and horizontal combined arrangement type over fire air system for tangential boiler
CN106247320A (en) * 2016-07-29 2016-12-21 东方电气集团东方锅炉股份有限公司 A kind of opposed firing boiler degree of depth denitration combustion method
CN207674431U (en) * 2017-12-08 2018-07-31 东方电气集团东方锅炉股份有限公司 A kind of big volume suction jet stream after-flame wind system

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
成庆刚,李争起,滕玉强,庄前玉,贾自臣,张寅,庄国中,果志明: "低NO_x排放燃烧技术及燃烧优化的试验研究", 锅炉技术, no. 05 *
李晓敏;王立军;: "基于降低NO_x的超临界机组锅炉燃烧器优化改造", 发电设备, no. 04 *
钱培东;张刚;: "330MW机组低氮氧化物燃烧系统改造", 内蒙古科技与经济, no. 09 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111146544A (en) * 2019-12-30 2020-05-12 电子科技大学 Efficient cooling structure for small high-power millimeter wave device

Also Published As

Publication number Publication date
CN107940446B (en) 2024-01-16

Similar Documents

Publication Publication Date Title
CN104748104B (en) A kind of coupling fractional combustion and the low NOx chain furnace of flue gas recirculation
CN100451447C (en) Combustion method of anthracite coal
CN106247321B (en) A kind of W flame boiler for deeply denitration combustion method
CN101074775A (en) Densed-phase back-flushing split-pole NOx combustion
CN107559817A (en) A kind of swirling pulverized coal combustion device and method using flue gas recirculation
CN105114944B (en) A kind of tangential boiler Researched of Air Staging Combustion Burning Pulverized Coal vertical-horizontal combination arrangement after-flame wind system
CN104595892B (en) Improve the ejection grading combustion W flame boiler of coal powder ignition burning
CN106090900A (en) A kind of secondary wind low NO of wall deep-gradedxcombustion method and device
CN108895430A (en) A kind of efficient low NO of coupled rotational flow coal dust firing and enhanced flue gas recirculationxChain furnace
JP3679998B2 (en) Pulverized coal burner
CN103041686A (en) NOx removing device and method by means of exhaust gas recycle and ammonia agent spray
CN1295460C (en) Device and method for w shape flame boiler completely burning
CN104406160B (en) A kind of coupling air classification and fuel staging low NOx tetra-arch form W flame boiler
CN204574001U (en) A kind of low NOx chain furnace of be coupled fractional combustion and flue gas recirculation
CN206257656U (en) Chain furnace system
CN208566673U (en) Quadrangle tangential circle pulverized coal firing boiler and coal generating system
CN103697465A (en) Boiler capable of achieving reignition of exhaust gas coal powder and reducing NOx by using high-temperature flue gas
CN207674431U (en) A kind of big volume suction jet stream after-flame wind system
CN104154532A (en) Center air ring concentrated type turbulent burner
CN107940446A (en) A kind of big volume inhales jet stream after-flame wind system and injection method
CN101569829B (en) Method for jointly controlling emission of NOx by utilizing multi-stage bias combustion and fuel reburning
CN102454982A (en) After-flaming air nozzle arrangement structure
CN201925914U (en) Over-fire air spout layout structure
CN203043834U (en) Device for removing NOx through smoke recycling and ammonia agent jetting
CN203656909U (en) Front-rear wall type opposed firing boiler

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