CN103438449A - Cyclone pulverized coal burner with secondary concentration - Google Patents
Cyclone pulverized coal burner with secondary concentration Download PDFInfo
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- CN103438449A CN103438449A CN2013103373714A CN201310337371A CN103438449A CN 103438449 A CN103438449 A CN 103438449A CN 2013103373714 A CN2013103373714 A CN 2013103373714A CN 201310337371 A CN201310337371 A CN 201310337371A CN 103438449 A CN103438449 A CN 103438449A
- Authority
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- Prior art keywords
- air duct
- pulverized coal
- concentration
- airduct
- wind
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title abstract description 10
- 239000003245 coal Substances 0.000 title abstract description 10
- 239000003570 air Substances 0.000 claims abstract description 32
- 241001646071 Prioneris Species 0.000 claims description 7
- 229910002089 NOx Inorganic materials 0.000 abstract description 4
- 238000000034 methods Methods 0.000 abstract description 2
- 239000012141 concentrates Substances 0.000 abstract 1
- 230000003247 decreasing Effects 0.000 abstract 1
- 230000003111 delayed Effects 0.000 abstract 1
- 230000002349 favourable Effects 0.000 abstract 1
- 239000002817 coal dust Substances 0.000 description 4
- 238000002485 combustion reactions Methods 0.000 description 4
- 238000005516 engineering processes Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000000843 powders Substances 0.000 description 3
- 239000000446 fuels Substances 0.000 description 2
- 239000000203 mixtures Substances 0.000 description 2
- 230000003134 recirculating Effects 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 1
- 239000000686 essences Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reactions Methods 0.000 description 1
- 230000036651 mood Effects 0.000 description 1
- 230000001105 regulatory Effects 0.000 description 1
Abstract
Description
Technical field
The present invention relates to combustion apparatus processing and manufacturing field, be specifically related to a kind of vortex burner with secondary concentration.
Background technology
Bi-register swirl burner (referring to Fig. 1) is the Typical Representative of the station boiler vortex burner of generally acknowledging in the world, its main feature is to be all adjustable inside and outside two parts of air quantity and swirl strength by secondary air separating, be equipped with and be axially moveable blade in the inner second air road, adjustable tangential or axial blade is installed, with the ratio of regulating inside and outside Secondary Air and the swirl strength of air-flow in the outer second air road.In an airduct of this vortex burner, the current equalizer that breeze airflow is evenly distributed is housed, the primary wind and powder mixture is non-rotary direct jet, at the burner outlet place, wind and inner second air are mixed to form rich fuel fire district, required remaining air when outer second air feeds the completing combustion of stove fuel.But this vortex burner still has weak point, mainly is: (1) current equalizer is far away apart from furnace outlet, and the enrichment effect of coal dust weakens at the burner outlet place; (2) Secondary Air is sneaked into wind in advance one time, makes the required ignition heat of burning increase, and breeze airflow reaches ignition temperature needs more heat, causes the postponement of catching fire; (3) Secondary Air is sneaked into wind in advance one time, causes the NOx discharge bigger than normal.
Summary of the invention
The object of the invention is to provide a kind of vortex burner with secondary concentration, and it can solve existing problem in background technology effectively.
In order to solve existing problem in background technology, vortex burner with secondary concentration comprises an airduct 1 and is arranged on inner second air pipe 2 and the outer second air pipe 3 of one end, the circle centre position of a described airduct 1 is equipped with concentric central tube 4, the port of export of a described airduct 1 is equipped with saw-tooth ring 5 along circumference, the outside of described central tube 4 is equipped with guide vane 6 along circumference, and this guide vane 6 is positioned at the middle part of an airduct 1.
The port of export of a described airduct 1 is equipped with wind reamer 7 one time.
Owing to having adopted above technical scheme, the present invention has following beneficial effect:
(1) realize the secondary enrichment of coal dust by directing vane and saw-tooth ring, make the burner outlet coal powder density increase, to reduce ignition heat;
(2) saw-tooth ring and a wind reamer are in conjunction with forming recirculating zone, for catching fire of high concentration pulverized coal provides advantage;
(3) postpone Secondary Air by a wind reamer and sneak into, further reduce ignition heat, and reduce NOx discharge in combustion process.
The accompanying drawing explanation
In order to be illustrated more clearly in the present invention, below in conjunction with accompanying drawing, embodiment is briefly described.
Fig. 1 is the structural representation of Bi-register swirl burner in background technology of the present invention;
Fig. 2 is structural representation of the present invention.
The specific embodiment
For technological means, creation characteristic that the present invention is realized, reach purpose and effect is easy to understand, below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described.
Referring to Fig. 2, this specific embodiment is to be achieved by the following technical solutions, vortex burner with secondary concentration comprises an airduct 1 and is arranged on inner second air pipe 2 and the outer second air pipe 3 of one end, the circle centre position of a described airduct 1 is equipped with concentric central tube 4, the port of export of a described airduct 1 is equipped with saw-tooth ring 5 along circumference, the outside of described central tube 4 is equipped with guide vane 6 along circumference, and this guide vane 6 is positioned at the middle part of an airduct 1.
The port of export of a described airduct 1 is equipped with wind reamer 7 one time.
Below in conjunction with accompanying drawing, the technical scheme in this specific embodiment and principle thereof are further elaborated: after flowing to airduct 1 of burner containing a general mood of powder, process is arranged on the centrifugation of the guide vane 6 of central tube 4, denseer breeze airflow flows along the wall in an air channel, realizes the enrichment for the first time of coal dust; Be separated to the denseer breeze airflow of airduct 1 wall along with air-flow continues motion, the secondary enrichment that the saw-tooth ring 5 of installing airduct 1 outlet is realized coal dust, form the high concentration pulverized coal that is easy to catch fire at burner outlet, reduced the ignition heat of breeze airflow; Airduct 1 outlet, a wind reamer 7 is installed, catching fire that the recirculating zone that saw-tooth ring 5 and wind reamer 7 combinations form is high concentration pulverized coal provides advantage; When the needed Secondary Air of burning, during respectively by inner second air pipe 2 and outer second air pipe 3, one time wind reamer 7 has been postponed sneaking into of Secondary Air, reduces on the one hand the ignition heat of breeze airflow, reduces on the other hand NOx discharge in combustion process.
Finally it should be noted that: above embodiment only, in order to technical scheme of the present invention to be described, is not intended to limit; Although with reference to previous embodiment, the present invention is had been described in detail, those of ordinary skill in the art should be appreciated that its technical scheme that still can put down in writing aforementioned each embodiment modifies, or part technical characterictic wherein is equal to replacement; And these modifications or replacement do not make the essence of appropriate technical solution break away from the spirit and scope of various embodiments of the present invention technical scheme.
Claims (2)
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CN2013103373714A CN103438449A (en) | 2013-07-30 | 2013-07-30 | Cyclone pulverized coal burner with secondary concentration |
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CN2013103373714A CN103438449A (en) | 2013-07-30 | 2013-07-30 | Cyclone pulverized coal burner with secondary concentration |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105465780A (en) * | 2015-12-23 | 2016-04-06 | 杭州燃油锅炉有限公司 | Ultralow NOx pulverized coal burner |
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CN201496957U (en) * | 2009-07-31 | 2010-06-02 | 戴卫军 | Cyclone pulverized coal burner |
CN201517769U (en) * | 2009-10-16 | 2010-06-30 | 东方锅炉(集团)股份有限公司 | Swirl burner |
CN101832550A (en) * | 2010-06-18 | 2010-09-15 | 上海交通大学 | Swirl pulverized-coal burner based on multi-level pulverized-coal concentration |
CN102393015A (en) * | 2011-05-27 | 2012-03-28 | 上海锅炉厂有限公司 | Dense-phase spiral-flow pulverized-coal burner |
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2013
- 2013-07-30 CN CN2013103373714A patent/CN103438449A/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN201496957U (en) * | 2009-07-31 | 2010-06-02 | 戴卫军 | Cyclone pulverized coal burner |
CN201517769U (en) * | 2009-10-16 | 2010-06-30 | 东方锅炉(集团)股份有限公司 | Swirl burner |
CN101832550A (en) * | 2010-06-18 | 2010-09-15 | 上海交通大学 | Swirl pulverized-coal burner based on multi-level pulverized-coal concentration |
CN102393015A (en) * | 2011-05-27 | 2012-03-28 | 上海锅炉厂有限公司 | Dense-phase spiral-flow pulverized-coal burner |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105465780A (en) * | 2015-12-23 | 2016-04-06 | 杭州燃油锅炉有限公司 | Ultralow NOx pulverized coal burner |
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