CN102777891A - Furnace combustion structure for reducing NOx (nitrogen oxide) discharge - Google Patents
Furnace combustion structure for reducing NOx (nitrogen oxide) discharge Download PDFInfo
- Publication number
- CN102777891A CN102777891A CN2012102503307A CN201210250330A CN102777891A CN 102777891 A CN102777891 A CN 102777891A CN 2012102503307 A CN2012102503307 A CN 2012102503307A CN 201210250330 A CN201210250330 A CN 201210250330A CN 102777891 A CN102777891 A CN 102777891A
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- China
- Prior art keywords
- discharge
- spout
- nox
- furnace combustion
- combustion structure
- 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.)
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Links
- 238000002485 combustion reaction Methods 0.000 title abstract description 7
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 title abstract 21
- 239000000446 fuel Substances 0.000 claims abstract description 22
- 239000000126 substance Substances 0.000 claims abstract description 10
- 238000007599 discharging Methods 0.000 claims description 11
- 238000009434 installation Methods 0.000 claims description 9
- 239000002817 coal dust Substances 0.000 claims description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 6
- 239000003595 mist Substances 0.000 claims description 3
- 239000003245 coal Substances 0.000 abstract description 4
- 238000006722 reduction reaction Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 abstract 4
- 238000005516 engineering process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000010883 coal ash Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The invention provides a furnace combustion structure for reducing NOx (nitrogen oxide) discharge. The NOx generated in a main combustion area generates reduction reaction to reduce discharge of NOx of a boiler when passing through a reburning zone, thereby reducing the NOx and ensuring the discharge accords with national requirements. The furnace combustion structure comprises a hearth, wherein a pulverized coal main combustor is arranged on an inner wall of the hearth. The furnace combustion structure is characterized in that: a gas fuel reburning nozzle is arranged above the pulverized coal main combustor; a burn-out air nozzle is arranged above the gas fuel reburning nozzle, and the fuel led by the gas fuel reburning nozzle is tail gas generated by a chemical device.
Description
Technical field
The present invention relates to the technical field of structures of boiler, be specially and reduce NO
xThe burner hearth burning structure of discharging.
Background technology
Existing pulverized-coal fired boiler generally all can allow to mix the burning proportion of gas; And the arrangement of this gas spout has two kinds; A kind of is that it directly is arranged in the overfiren air port of coal burner; Another kind is to arrange a gas specific spout separately in the main burner district, and these arrangements all are so that gas is mixed burning as purpose of design.Along with the development of improving day by day of requiring of Environmental Protection in China and economic technology, particularly country in 2011 has issued after " thermal power plant's atmosphere pollutants emission standards ", to the pollutant of new and old power plant NO particularly
xDischarging has proposed very harsh requirement, and wherein coal-fired power station boiler reduces NO
xIt is top priority.
Summary of the invention
To the problems referred to above, the invention provides and reduce NO
xThe burner hearth burning structure of discharging, it makes at the NO of main combustion zone generation
xProduce reduction reaction during through the reburning zone and reduce boiler NO
xDischarging, thereby reduce NO
x, guarantee that discharging meets national requirements.
Reduce NO
xThe burner hearth burning structure of discharging; Its technical scheme is such: it comprises burner hearth; The inwall of said burner hearth is provided with the coal dust main burner; It is characterized in that: the top of said coal dust main burner is provided with gaseous fuel and fires spout again, and the top that said gaseous fuel fires spout again is provided with the burnt wind spout, and the fuel that said gaseous fuel fires the spout feeding again is the tail gas that chemical plant installations produced.
It is further characterized in that: the volume content that the tail gas that said chemical plant installations produced is specially methane is greater than 30% mist.
After adopting said structure of the present invention; At the boiler coal-ash main burner; The top that is the primary zone arranges that gaseous fuel fires spout again and forms the reducing zone; Arrange that above gaseous fuel fires spout again the burnt wind spout forms burnt zone, and gaseous fuel to fire the fuel that spout feeds again be the tail gas that chemical plant installations produced, it makes the NO that generates in main combustion zone
xThe tail gas generation reduction reaction that is produced with chemical plant installations when firing spout again through gaseous fuel reduces boiler NO
xDischarging, thereby reduce NO
x, guarantee that discharging meets national requirements; On the other hand, the tail gas that chemical plant installations produced is turned waste into wealth, practiced thrift production cost.
Description of drawings
Fig. 1 is a front view structural representation of the present invention.
The specific embodiment
See Fig. 1; It comprises burner hearth 1; The inwall of burner hearth 1 is provided with coal dust main burner 2, and the distance H spaced above of coal dust main burner 2 is provided with gaseous fuel and fires spout 3 again, and the area of space that gaseous fuel fires spout 3 pairing burner hearths again is the reducing zone; The distance B spaced above that gaseous fuel fires spout 3 again is provided with burnt wind spout 4; The area of space of burnt wind spout 4 pairing burner hearths is a burnt zone, and it is the tail gas that chemical plant installations produced that gaseous fuel fires the fuel that spout 4 feeds again, and the volume content that the tail gas that chemical plant installations produced is specially methane is greater than 30% mist.
Claims (2)
1. reduce NO
xThe burner hearth burning structure of discharging; It comprises burner hearth; The inwall of said burner hearth is provided with the coal dust main burner; It is characterized in that: the top of said coal dust main burner is provided with gaseous fuel and fires spout again, and the top that said gaseous fuel fires spout again is provided with the burnt wind spout, and the fuel that said gaseous fuel fires the spout feeding again is the tail gas that chemical plant installations produced.
2. reduction NO according to claim 1
xThe burner hearth burning structure of discharging is characterized in that: the volume content that the tail gas that said chemical plant installations produced is specially methane is greater than 30% mist.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012102503307A CN102777891A (en) | 2012-07-19 | 2012-07-19 | Furnace combustion structure for reducing NOx (nitrogen oxide) discharge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012102503307A CN102777891A (en) | 2012-07-19 | 2012-07-19 | Furnace combustion structure for reducing NOx (nitrogen oxide) discharge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102777891A true CN102777891A (en) | 2012-11-14 |
Family
ID=47122908
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012102503307A Pending CN102777891A (en) | 2012-07-19 | 2012-07-19 | Furnace combustion structure for reducing NOx (nitrogen oxide) discharge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102777891A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102980174A (en) * | 2012-11-30 | 2013-03-20 | 山东大学 | Coal-gas combined efficient low-emission grate firing combustion apparatus and technology |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2501564Y (en) * | 2001-10-31 | 2002-07-24 | 清华大学 | Apparatus by bio-matter pyrolytic gas refiring denitration |
| CN1387006A (en) * | 2001-05-18 | 2002-12-25 | 清华大学 | Method and apparatus for reducing exhaustion of nitrogen oxides from coal-fired boiler |
| CN1415891A (en) * | 2001-10-31 | 2003-05-07 | 清华大学 | Combustion method and device for denitration by refueling pyrolysis gas of biomass |
| CN101016986A (en) * | 2007-02-28 | 2007-08-15 | 哈尔滨工业大学 | Method for burning of low nitrogen oxides in coal-burning boiler |
| CN101021316A (en) * | 2007-03-14 | 2007-08-22 | 哈尔滨工业大学 | Method and device of denitration utilizing biomass direct burning and re-burning as well as smoke gas recirculating technology |
| CN101050853A (en) * | 2007-04-03 | 2007-10-10 | 哈尔滨工业大学 | Method for reducing nitrogen oxide of powder coal boiler mixed burning gas fuel |
| CN101062461A (en) * | 2007-04-27 | 2007-10-31 | 南京师范大学 | Method and system for combinablenably removing SO2, NOx and Hg in coal smoke gas by using recombustion of biomass |
| CN202791991U (en) * | 2012-07-19 | 2013-03-13 | 无锡华光锅炉股份有限公司 | Hearth combustion structure capable of lowing NOx discharge |
-
2012
- 2012-07-19 CN CN2012102503307A patent/CN102777891A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1387006A (en) * | 2001-05-18 | 2002-12-25 | 清华大学 | Method and apparatus for reducing exhaustion of nitrogen oxides from coal-fired boiler |
| CN2501564Y (en) * | 2001-10-31 | 2002-07-24 | 清华大学 | Apparatus by bio-matter pyrolytic gas refiring denitration |
| CN1415891A (en) * | 2001-10-31 | 2003-05-07 | 清华大学 | Combustion method and device for denitration by refueling pyrolysis gas of biomass |
| CN101016986A (en) * | 2007-02-28 | 2007-08-15 | 哈尔滨工业大学 | Method for burning of low nitrogen oxides in coal-burning boiler |
| CN101021316A (en) * | 2007-03-14 | 2007-08-22 | 哈尔滨工业大学 | Method and device of denitration utilizing biomass direct burning and re-burning as well as smoke gas recirculating technology |
| CN101050853A (en) * | 2007-04-03 | 2007-10-10 | 哈尔滨工业大学 | Method for reducing nitrogen oxide of powder coal boiler mixed burning gas fuel |
| CN101062461A (en) * | 2007-04-27 | 2007-10-31 | 南京师范大学 | Method and system for combinablenably removing SO2, NOx and Hg in coal smoke gas by using recombustion of biomass |
| CN202791991U (en) * | 2012-07-19 | 2013-03-13 | 无锡华光锅炉股份有限公司 | Hearth combustion structure capable of lowing NOx discharge |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102980174A (en) * | 2012-11-30 | 2013-03-20 | 山东大学 | Coal-gas combined efficient low-emission grate firing combustion apparatus and technology |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20121114 |