CN102022723A - Circulating fluidized bed boiler for papermaking thermal power plant - Google Patents
Circulating fluidized bed boiler for papermaking thermal power plant Download PDFInfo
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- CN102022723A CN102022723A CN2010106154170A CN201010615417A CN102022723A CN 102022723 A CN102022723 A CN 102022723A CN 2010106154170 A CN2010106154170 A CN 2010106154170A CN 201010615417 A CN201010615417 A CN 201010615417A CN 102022723 A CN102022723 A CN 102022723A
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- China
- Prior art keywords
- hearth
- material returning
- separator
- communicated
- papermaking
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- 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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- 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
The invention relates to a circulating fluidized bed boiler for a papermaking thermal power plant. The circulating fluidized bed boiler comprises a tail smoke well, a separator, a material returning device and a hearth, wherein the bottom of the hearth is communicated with the material returning device; the top of the hearth is communicated with the separator; the top of the separator is communicated with the tail smoke well; the bottom of the separator is communicated with the material returning device; the bottom of the hearth is provided with a raw coal port; the bottom of the side wall of the hearth is provided with a secondary air opening and the bottom of the hearth is provided with a primary air opening; the bottom of the material returning device is provided with a material returning air opening; and the bottom of the hearth is provided with a slag port. Medium and high multiplying power circulation fluidization technology is adopted, and the coal types have high adaptability and combustion efficiency; oxygen-poor combustion is performed in a dense phase region on the lower part of a combustion chamber so as to form a reducing atmosphere; oxygen-enriched combustion is performed on the upper part of the secondary air port so as to form an oxidizing atmosphere; and ideal combustion efficiency can be realized and the emission of sulfur and NOX can be greatly reduced.
Description
Technical field
The present invention relates to field of energy-saving technology, particularly relate to the CFBB of papermaking thermo-power station.
Background technology
The papermaking thermo-power station is conventional to adopt clockwise chain-grate boiler, and its efficiency of combustion is low, and is less economical, and the coal consumption height is relatively poor to the adaptability of fire coal, and the processing of fume emission also difficulty reach environmental protection requirement, the content of flue gas NOX is higher.
Summary of the invention
The CFBB that the objective of the invention is to avoid weak point of the prior art and a kind of papermaking thermo-power station is provided.
Purpose of the present invention realizes by following technical measures.
The CFBB of papermaking thermo-power station comprises afterbody cigarette well, separator, material returning device and burner hearth; The bottom of described burner hearth is communicated with described material returning device, and the top of described burner hearth is communicated with described separator, and the top of described separator is connected with afterbody cigarette well, and the bottom of described separator is communicated with described material returning device.
The bottom of described burner hearth offers the raw coal mouth.
The sidewall bottom of described burner hearth offers overfiren air port, and primary air nozzle is offered in the bottom of described burner hearth.
The returning charge air port is offered in the bottom of described material returning device.
The slag mouth is offered in the bottom of described burner hearth.
The present invention adopts half open-air the layout, full steel structure, 8 meters of running layer absolute altitudes, the running platform is a concrete large platform structure in boiler steelframe scope, burner hearth adopts all-welded fin panel casing, guaranteed the tightness of combustion chamber, CFBB has adopted the ciculation fluidized technology of middle high magnification, and the adaptability of its coal is good, the efficiency of combustion height, emulsion zone in the bottom of combustion chamber is oxygen debt burning, forming reducing atmosphere, is oxygen-enriched combusting on overfiren air port top, forms oxidizing atmosphere, the efficiency of combustion that can realize ideal, and can reduce the discharging of sulphur and NOX significantly.
Description of drawings
The present invention will be further described to utilize accompanying drawing, but the content in the accompanying drawing does not constitute any limitation of the invention.
Fig. 1 is the structural representation of an embodiment of the CFBB of papermaking thermo-power station of the present invention.
Reference numeral:
Afterbody cigarette well 1, separator 2, material returning device 3, burner hearth 4, returning charge air port 5, primary air nozzle 6, overfiren air port 7, raw coal mouth 8, slag mouth 9.
The specific embodiment
The invention will be further described with the following Examples.
An embodiment of the CFBB of papermaking thermo-power station of the present invention comprises afterbody cigarette well 1, separator 2, material returning device 3 and burner hearth 4 as shown in Figure 1; The bottom of described burner hearth 4 is communicated with described material returning device 3, and the top of described burner hearth 4 is communicated with described separator 2, and the top of described separator 2 is connected with afterbody cigarette well 1, and the bottom of described separator 2 is communicated with described material returning device 3.
The bottom of described burner hearth 4 offers raw coal mouth 8.
The sidewall bottom of described burner hearth 4 offers overfiren air port 7, and primary air nozzle 6 is offered in the bottom of described burner hearth.
Returning charge air port 5 is offered in the bottom of described material returning device 3.
Should be noted that at last; above embodiment only is used to illustrate technical scheme of the present invention but not limiting the scope of the invention; although the present invention has been done detailed description with reference to preferred embodiment; those of ordinary skill in the art is to be understood that; can make amendment or be equal to replacement technical scheme of the present invention, and not break away from the essence and the scope of technical solution of the present invention.
Claims (5)
1. the CFBB of papermaking thermo-power station is characterized in that: comprise afterbody cigarette well, separator, material returning device and burner hearth; The bottom of described burner hearth is communicated with described material returning device, and the top of described burner hearth is communicated with described separator, and the top of described separator is connected with afterbody cigarette well, and the bottom of described separator is communicated with described material returning device.
2. the CFBB of papermaking thermo-power station according to claim 1 is characterized in that: the bottom of described burner hearth offers the raw coal mouth.
3. the CFBB of papermaking thermo-power station according to claim 1 is characterized in that: the sidewall bottom of described burner hearth offers overfiren air port, and primary air nozzle is offered in the bottom of described burner hearth.
4. the CFBB of papermaking thermo-power station according to claim 1 is characterized in that: the returning charge air port is offered in the bottom of described material returning device.
5. the CFBB of papermaking thermo-power station according to claim 1 is characterized in that: the slag mouth is offered in the bottom of described burner hearth.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010106154170A CN102022723A (en) | 2010-12-31 | 2010-12-31 | Circulating fluidized bed boiler for papermaking thermal power plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010106154170A CN102022723A (en) | 2010-12-31 | 2010-12-31 | Circulating fluidized bed boiler for papermaking thermal power plant |
Publications (1)
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CN102022723A true CN102022723A (en) | 2011-04-20 |
Family
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Family Applications (1)
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CN2010106154170A Pending CN102022723A (en) | 2010-12-31 | 2010-12-31 | Circulating fluidized bed boiler for papermaking thermal power plant |
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CN (1) | CN102022723A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106122949A (en) * | 2016-07-22 | 2016-11-16 | 福建省联盛纸业有限责任公司 | A kind of circulating fluidized bed boiler of paper grade (stock) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2909012Y (en) * | 2006-03-16 | 2007-06-06 | 刘学冰 | Circulation fluid-bed boiler with high-temp wear-resistant ceramic component |
CN200972112Y (en) * | 2006-11-13 | 2007-11-07 | 济南锅炉集团有限公司 | Wind distribution device of return apparatus |
CN201281345Y (en) * | 2008-07-01 | 2009-07-29 | 北京博奇电力科技有限公司 | Fluidized bed incinerator, circulating fluidized bed incinerator and incineration system |
CN201351914Y (en) * | 2008-12-20 | 2009-11-25 | 交城义望铁合金有限责任公司 | Return material air supply system of circulating fluidized bed boiler |
CN101832565A (en) * | 2010-04-06 | 2010-09-15 | 赵德智 | Electricity-generating method by incinerating paper-making wet sludge |
-
2010
- 2010-12-31 CN CN2010106154170A patent/CN102022723A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2909012Y (en) * | 2006-03-16 | 2007-06-06 | 刘学冰 | Circulation fluid-bed boiler with high-temp wear-resistant ceramic component |
CN200972112Y (en) * | 2006-11-13 | 2007-11-07 | 济南锅炉集团有限公司 | Wind distribution device of return apparatus |
CN201281345Y (en) * | 2008-07-01 | 2009-07-29 | 北京博奇电力科技有限公司 | Fluidized bed incinerator, circulating fluidized bed incinerator and incineration system |
CN201351914Y (en) * | 2008-12-20 | 2009-11-25 | 交城义望铁合金有限责任公司 | Return material air supply system of circulating fluidized bed boiler |
CN101832565A (en) * | 2010-04-06 | 2010-09-15 | 赵德智 | Electricity-generating method by incinerating paper-making wet sludge |
Non-Patent Citations (5)
Title |
---|
《东北电力技术》 19990228 王力,等 35t/h循环流化床锅炉特性研究 , * |
《中华纸业》 20060531 吴福骞 谈造纸工业循环经济(十) 第27卷, 第5期 2 * |
《中华纸业》 20071031 张庆国 等 JX-300X集散控制系统在造纸自备电厂中的应用 第28卷, * |
《中华纸业》 20071031 张庆国 等 JX-300X集散控制系统在造纸自备电厂中的应用 第28卷, 2 * |
《中国优秀博硕士学位论文全文数据库(硕士)工程科技Ⅱ辑》 20070415 张栋 470t/h循环流化床锅炉一次风室流场特性研究 , * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106122949A (en) * | 2016-07-22 | 2016-11-16 | 福建省联盛纸业有限责任公司 | A kind of circulating fluidized bed boiler of paper grade (stock) |
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Application publication date: 20110420 |