CN110319436A - A kind of deep or light classification vortex burner of compact - Google Patents
A kind of deep or light classification vortex burner of compact Download PDFInfo
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- CN110319436A CN110319436A CN201910518542.0A CN201910518542A CN110319436A CN 110319436 A CN110319436 A CN 110319436A CN 201910518542 A CN201910518542 A CN 201910518542A CN 110319436 A CN110319436 A CN 110319436A
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- air
- airflow channel
- secondary air
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- 239000003245 coal Substances 0.000 claims abstract description 151
- 239000002817 coal dust Substances 0.000 claims abstract description 46
- 239000000843 powder Substances 0.000 claims abstract description 17
- 210000003205 muscle Anatomy 0.000 claims description 7
- 125000004122 cyclic group Chemical group 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 18
- 230000008901 benefit Effects 0.000 abstract description 4
- 238000012545 processing Methods 0.000 abstract description 3
- 239000007921 spray Substances 0.000 description 6
- 238000010304 firing Methods 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- 230000003134 recirculating effect Effects 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 210000001519 tissue Anatomy 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D1/00—Burners for combustion of pulverulent fuel
- F23D1/02—Vortex burners, e.g. for cyclone-type combustion apparatus
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING 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
- F23L1/00—Passages or apertures for delivering primary air for combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING 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
- F23L9/00—Passages or apertures for delivering secondary air for completing combustion of fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2201/00—Burners adapted for particulate solid or pulverulent fuels
- F23D2201/20—Fuel flow guiding devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2203/00—Feeding arrangements
- F23K2203/008—Feeding devices for pulverulent fuel
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
The present invention provides a kind of deep or light classification vortex burner of compact, thick coal culm airflow channel is located at the middle part of First air coal dust streamtube, thin powdered coal airflow channel is located at the outside of thick coal culm airflow channel, and it is connected to by conical ring channel with First air coal dust streamtube, axial swirl blades are equipped in the lower part of thin powdered coal airflow channel, it is equipped with secondary air channel in the outside of thin powdered coal airflow channel, tangential vane is equipped in secondary air channel；The cricoid Pulverized Coal Concentration ring of cone is additionally provided in First air coal dust streamtube.The present invention has the advantages that promote coal powder ignition, steady combustion and after-flame under the conditions of more coals and varying duty；It is compact-sized and inhibit NO x It generates, while reducing burner processing cost, solve that load regulation range existing for existing pulverized-coal fired boiler is narrow, coal dust burn-off rate is low, poor combustion stability and NO x The high problem of discharge amount.
Description
Technical field
The present invention relates to a kind of coal-burning boiler coal burners, and in particular to a kind of promotion coal-powder steady flame, after-flame and drop
Low NO x The deep or light classification vortex burner of the compact of generation, has that coal adaptability is strong, load regulation range is wide and structure
Compact feature.
Background technique
Coal is the main fossil fuel in China, and coal dust firing mode accounts in power industry and other industry power device
According to biggish ratio.Nitrogen oxides (NO x ) it is to generate the predecessor of acid rain and photochemical pollution, and the coal in power industry fires
Burning is to generate NO x Main source.Growing with pollution reduction demand, each state has formulated stringent standard all to limit
Make the NO that large-scale combustion apparatus generates x Discharge." fossil-fuel power plant atmospheric pollutant emission standard " requirement that Chinese environmental protection portion promulgates: existing
From having boiler on July 1st, 2014, from newly constructed boiler on January 1st, 2012, in addition to W flame boiler and circulating fluidized bed boiler,
Remaining boiler NO x Emission limit is 100mg/Nm3 (at 6% O2).In addition, promoting as country is to coal-burning boiler flexibility is promoted
The pay attention to day by day of electric power Green Transformation has realized the discharge of low pollution object, flexible peak regulation and the raising coal adaptability of coal-burning boiler
Inexorable trend as the development of coal-burning boiler technology.
In response to China, increasingly harsh environmental protection standard, the rich and changeful coal resource of scientific utilization are developed efficient, low
Nitrogen, coal adaptability are wide, varying duty is adaptable and compact-sized coal burner to promote coal-burning boiler development and
Clean coal utilization plays a crucial role.
Summary of the invention
The present invention provides a kind of deep or light classification vortex burner of compact, to solve to bear existing for existing pulverized-coal fired boiler
Lotus adjustable range is narrow, coal dust burn-off rate is low, poor combustion stability and NO x The high problem of discharge amount.
The present invention is achieved through the following technical solutions: a kind of deep or light classification vortex burner of compact, special
Sign is, including thin powdered coal airflow channel, internal stripper loop, conical ring channel, thick coal culm airflow channel, fixing muscle, coal dust are dense
Contracting ring, First air coal dust streamtube, axial swirl blades, external stripper loop, secondary air channel and tangential vane；
Thick coal culm airflow channel is located at the middle part of First air coal dust streamtube, and thin powdered coal airflow channel is located at thick coal culm airflow channel
Outside, and be connected to First air coal dust streamtube by conical ring channel, the lower part of thin powdered coal airflow channel be provided with axis
To swirl vane, the outside of thin powdered coal airflow channel is provided with secondary air channel, tangential leaf is provided in secondary air channel
Piece；The cricoid Pulverized Coal Concentration ring of cone is additionally provided in First air coal dust streamtube.
Further, thick coal culm airflow channel is connect with thin powdered coal airflow channel by internal stripper loop, thin powdered coal air-flow
Channel is connect with secondary air channel by external stripper loop；The Pulverized Coal Concentration ring is fixed on First air coal dust gas by fixing muscle
The middle part of flow tube.
Further, thick coal culm airflow channel is straight barrel type.
Further, the secondary air channel is the cyclic annular airflow channel with inverted "L" shape section；The tangential vane position
In the inlet of secondary air channel.
Further, the secondary air channel has two layers, is connected between two layers of secondary air channel by external stripper loop, two
Tangential vane is respectively set in layer secondary air channel.
Advantages of the present invention is as follows:
Promote coal powder ignition, steady combustion and after-flame under the conditions of coal more than 1. and varying duty；
First air breeze airflow makes coal powder density in thick coal culm air-flow increase to the 2 times or more before concentration, is conducive to by concentration
Ignition heat needed for reducing different types of coal coal dust firing, makes this part coal dust advanced combustion form main flame, heats and light light coal
Powder air-flow.
High-speed rotating thin powdered coal air-flow and Secondary Air help to form high temperature gases recirculating area, point at burner outlet
Fire the coal dust in thin powdered coal air-flow and thick coal culm air-flow.
2. low NO x It generates；
After concentration, coal powder density greatly improves First air breeze airflow in thick coal culm air-flow, realizes effective coal powder light-dark
Fractional combustion advantageously forms the strong reducing zone in pulverized coal flame, and the N element of release is largely to NH3Or N2Conversion inhibits
NO x It generates.
Oxygen amount needed for coal dust firing initial stage is successively supplied by thin powdered coal air-flow, secondary air separating two-stage, protects coal dust always
It holds in the lower burning of also Primordial Qi point, to reduce the NO in process of coal combustion x It generates.
Be arranged between thick coal culm airflow channel and thin powdered coal airflow channel internal stripper loop and thin powdered coal airflow channel with
External stripper loop is set between secondary air channel, makes to keep certain distance between thick coal culm air-flow, thin powdered coal air-flow and Secondary Air three
It sprays burner and further extends coal to postpone thick coal culm air-flow, thin powdered coal air-flow and the triangular mixing of Secondary Air
Residence time of the powder under also Primordial Qi point, inhibit NO x It generates.
3. compact-sized and reduce cost；
First air breeze airflow is divided into positioned at the dense of inside by the Pulverized Coal Concentration ring being arranged in First air coal dust streamtube
Breeze airflow and thin powdered coal air-flow positioned at outside, while realizing coal powder light-dark fractional combustion, further by being arranged in
Axial swirl blades in thin powdered coal airflow channel spray thin powdered coal air-flow high speed rotation at burner outlet.This kind combustion
Thin powdered coal air-flow can be made while have tissue pulverized coal bias combustion and building burner outlet high temperature recirculation zone by burning organizational form
Effect, avoid in general type vortex burner by building multi-layer rotational flow Secondary Air realize burner outlet height
Warm recirculating zone simplifies burner structure, keeps burner structure more compact, burner dimensions accordingly reduce, and are conducive to burner
Flexible arrangement and reduction burner processing cost in actual application.
Detailed description of the invention
Fig. 1 is the present invention along axial section structural schematic diagram；
Fig. 2 is side view of the present invention；
Fig. 3 is Section A-A cross-sectional view of the present invention；
Fig. 4 is section B-B cross-sectional view of the present invention；
Fig. 5 is axial swirl blades perspective view of the present invention；
Fig. 6 is principle of the invention figure；
Fig. 7 is one embodiment of the present of invention structural schematic diagram.
Description of symbols: 1: thin powdered coal airflow channel, 2: internal stripper loop, 3: conical ring channel, 4: thick coal culm air-flow
Channel, 5: fixing muscle, 6: Pulverized Coal Concentration ring, 7: First air coal dust streamtube, 8: axial swirl blades, 9: external stripper loop, 10:
Secondary air channel, 11: tangential vane.
Specific embodiment
In order to which clear the objectives, technical solutions, and advantages of the present invention carry out invention further detailed by following embodiment
It describes in detail bright.It should be pointed out that described herein, specific examples are only used to explain the present invention, is not used to limit this hair
It is bright.
It is logical for a kind of deep or light classification vortex burner of compact of the present invention, including thin powdered coal air-flow as shown in figs. 1-7
Road 1, internal stripper loop 2, conical ring channel 3, thick coal culm airflow channel 4, fixing muscle 5, Pulverized Coal Concentration ring 6, First air coal dust gas
Flow tube 7, axial swirl blades 8, external stripper loop 9, secondary air channel 10 and tangential vane 11；
Thick coal culm airflow channel 4 is located at the middle part of First air coal dust streamtube 7, and thin powdered coal airflow channel 1 is located at thick coal culm air-flow
The outside in channel 4, and be connected to by conical ring channel 3 with First air coal dust streamtube 7, in the lower part of thin powdered coal airflow channel 1
Axial swirl blades 8 are provided with, the outside of thin powdered coal airflow channel 1 are provided with secondary air channel 10, in secondary air channel 10
Inside it is provided with tangential vane 11；The cricoid Pulverized Coal Concentration ring 6 of cone is additionally provided in First air coal dust streamtube 7.
Preferably, thick coal culm airflow channel 4 is connect with thin powdered coal airflow channel 1 by internal stripper loop 2, thin powdered coal air-flow
Channel 1 is connect with secondary air channel 10 by external stripper loop 9；The Pulverized Coal Concentration ring 6 is fixed on First air by fixing muscle 5
The middle part of coal dust streamtube 7.
Preferably, thick coal culm airflow channel 4 is straight barrel type.
Preferably, the secondary air channel 11 is the cyclic annular airflow channel with inverted "L" shape section；The tangential vane 11
Positioned at the inlet of secondary air channel 10.
Preferably, the secondary air channel 10 has two layers, is connected between two layers of secondary air channel 10 by external stripper loop 9
It connects, tangential vane 11 is respectively set in two layers of secondary air channel 10.
Positional relationship is as follows before specific each component: as shown in Figure 1, thick coal culm airflow channel 4, internal stripper loop 2, light
Breeze airflow channel 1, external stripper loop 9 and secondary air channel 10 are to set gradually from inside to outside；Pulverized Coal Concentration ring 6 is located at primary
The inside of wind coal dust streamtube 7 can have multiple, vertical spacing setting；Thick coal culm airflow channel 4 is located at First air breeze airflow
At the export center of pipe 7, thick coal culm airflow channel 4 is straight barrel type；Conical ring channel 3 is located at going out for First air coal dust streamtube 7
At mouthful, and it is connected to and in communication with First air coal dust streamtube 7；Thin powdered coal airflow channel 1 is located at the exit in conical ring channel 3,
And it is connected to and in communication with conical ring channel 3.
As shown in Figures 1 and 5, the axial swirl blades 8 are located at the exit of thin powdered coal airflow channel 1, and connect light
The inner cylinder and outer cylinder wall surface in breeze airflow channel 1；Internal stripper loop 2 is connect with the inner cylinder of thin powdered coal airflow channel 1, outer portion every
Ring 9 is connect with the outer cylinder of thin powdered coal airflow channel 1.
The working principle of the invention and process are as follows: First air carries coal dust and is entered by First air coal dust streamtube, first
Be located at First air coal dust streamtube inside Pulverized Coal Concentration ring meet, Pulverized Coal Concentration ring be it is hollow pyramidal and up big and down small,
During hitting Pulverized Coal Concentration ring, air-flow swerves First air breeze airflow, since pulverized coal particle density is larger, big partial size
Pulverized coal particle is during hitting Pulverized Coal Concentration ring, by the inertia effect, it is easier to be repelled into First air coal dust streamtube
It at the heart and is enriched with, forms the higher thick coal culm air-flow of coal powder density, at the same time, (predominantly partial size is smaller for a small amount of pulverized coal particle
Pulverized coal particle), the effect of inertia being subject to due to itself is weaker, follows the mobility of air-flow preferable, makes a small amount of coal dust in this part
It is still flowed along air current flow direction, to be formed about around thick coal culm air-flow close to First air breeze airflow inside pipe wall
The lower thin powdered coal air-flow of coal powder density.The thick coal culm air-flow formed at First air breeze airflow tube hub is directly by thick coal culm
Airflow channel sprays, in the thin powdered coal air-flow that First air breeze airflow inside pipe wall is formed about along in First air coal dust streamtube
Wall flowing, initially enters conical ring channel, by the guiding role in conical ring channel, thin powdered coal air-flow finally by conical ring channel into
Enter the inside of thin powdered coal airflow channel, and the guiding role by axial swirl blades, the high speed ejection in a manner of rotational flow,
To form low-pressure area at the center of high speed rotation air-flow, the formation of the low-pressure area can be such that thin powdered coal air-flow returns after ejection
Low-pressure area is flowed to, to form the high temperature recirculation zone at burner outlet.At the same time, Secondary Air is entered by secondary air channel,
First by the guiding role of tangential vane, biggish tangential rotational velocity component is generated, and by secondary air channel exit high speed
Eddy flow sprays, and similarly, further promotes the formation of high temperature recirculation zone at burner outlet.
In structure of the invention, First air breeze airflow makes coal powder density in thick coal culm air-flow increase to concentration by concentration
Preceding 2 times or more, ignition heat needed for advantageously reducing different types of coal coal dust firing make this part coal dust advanced combustion form main fire
Flame heats and lights thin powdered coal air-flow.High-speed rotating thin powdered coal air-flow and Secondary Air facilitate at burner outlet to be formed
The coal dust in thin powdered coal air-flow and thick coal culm air-flow is lighted in high temperature gases recirculating area.So as in more coals and varying duty item
Promote coal powder ignition, steady combustion and after-flame under part.
Meanwhile First air breeze airflow, after concentration, coal powder density greatly improves in thick coal culm air-flow, realizes effective
Coal powder light-dark fractional combustion advantageously forms the strong reducing zone in pulverized coal flame, makes the N element of release largely to NH3Or N2
Conversion inhibits NO x It generates.Also, oxygen amount needed for coal dust firing initial stage is successively supplied by thin powdered coal air-flow, secondary air separating two-stage
It gives, so that coal dust is remained at the lower burning of also Primordial Qi point, to reduce the NO in process of coal combustion x It generates.In thick coal culm gas
Internal stripper loop is set between circulation road and thin powdered coal airflow channel and is arranged between thin powdered coal airflow channel and secondary air channel outer
Part spacer ring makes to keep certain distance to spray burner between thick coal culm air-flow, thin powdered coal air-flow and Secondary Air three, to postpone
Thick coal culm air-flow, thin powdered coal air-flow and the triangular mixing of Secondary Air further extend coal dust and stop under also Primordial Qi point
The time is stayed, is conducive to inhibit NO x It generates, reduces NOx emission.
First air breeze airflow is divided into positioned inside by the Pulverized Coal Concentration ring being arranged in First air coal dust streamtube
Thick coal culm air-flow and thin powdered coal air-flow positioned at outside further pass through cloth while realizing coal powder light-dark fractional combustion
The axial swirl blades being placed in thin powdered coal airflow channel spray thin powdered coal air-flow high speed rotation at burner outlet.It should
Kind combustion method can make thin powdered coal air-flow while there is tissue pulverized coal bias combustion and building burner outlet high temperature to return
The effect for flowing area avoids in general type vortex burner and realizes burner outlet by building multi-layer rotational flow Secondary Air
High temperature recirculation zone, simplify burner structure, burner dimensions accordingly reduce, and keep burner structure more compact, are conducive to
The flexible arrangement and reduction burner processing cost of burner in actual application.
The present invention, which passes through, postpones mixing between tissue pulverized coal bias combustion, bias pulverized coal air-flow and Secondary Air, realize that coal dust is steady
Fixed burning promotes coal dust after-flame and reduces NO x The purpose of generation, with coal adaptability is strong, load regulation range is wide, low NO x It is raw
At and compact-sized advantage.
Connection of the present invention includes but is not limited to the modes such as be spirally connected, weld, and based on used by the prior art
Corresponding manner.
A specific embodiment of the invention above described embodiment only expresses is only used as the explanation to the present invention program
And explanation, it cannot be construed as a limitation to the scope of the present invention.It should be pointed out that for the common of this field
For technical staff, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to this
The protection scope of invention.Therefore, the scope of protection of the patent of the invention shall be subject to the appended claims.
Claims (5)
1. a kind of deep or light classification vortex burner of compact, which is characterized in that including thin powdered coal airflow channel (1), inside
Stripper loop (2), conical ring channel (3), thick coal culm airflow channel (4), fixing muscle (5), Pulverized Coal Concentration ring (6), First air coal dust
Gas flow tube (7), axial swirl blades (8), external stripper loop (9), secondary air channel (10) and tangential vane (11)；
Thick coal culm airflow channel (4) is located at the middle part of First air coal dust streamtube (7), and thin powdered coal airflow channel (1) is located at dense coal
The outside of powder airflow channel (4), and be connected to by conical ring channel (3) with First air coal dust streamtube (7), in thin powdered coal air-flow
The lower part in channel (1) is provided with axial swirl blades (8), and the outside of thin powdered coal airflow channel (1) is provided with secondary air channel
(10), tangential vane (11) are provided in secondary air channel (10)；Conical ring is additionally provided in First air coal dust streamtube (7)
The Pulverized Coal Concentration ring (6) of shape.
2. the deep or light classification vortex burner of compact according to claim 1, which is characterized in that thick coal culm air-flow is logical
Road (4) is connect with thin powdered coal airflow channel (1) by internal stripper loop (2), thin powdered coal airflow channel (1) and secondary air channel
(10) it is connected by external stripper loop (9), the Pulverized Coal Concentration ring (6) is fixed on First air breeze airflow by fixing muscle (5)
Manage the middle part of (7).
3. the deep or light classification vortex burner of compact according to claim 1, which is characterized in that thick coal culm air-flow is logical
Road (4) is straight barrel type.
4. the deep or light classification vortex burner of compact according to claim 1, which is characterized in that the Secondary Air is logical
Road (11) is the cyclic annular airflow channel with inverted "L" shape section；The tangential vane (11) is located at entering for secondary air channel (10)
At mouthful.
5. the deep or light classification vortex burner of compact according to claim 1, which is characterized in that the Secondary Air is logical
Road (10) has two layers, is connected between two layers of secondary air channel (10) by external stripper loop (9), in two layers of secondary air channel (10)
Tangential vane (11) are respectively set.
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| CN201910518542.0A CN110319436A (en) | 2019-06-15 | 2019-06-15 | A kind of deep or light classification vortex burner of compact |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910518542.0A CN110319436A (en) | 2019-06-15 | 2019-06-15 | A kind of deep or light classification vortex burner of compact |
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| CN110319436A true CN110319436A (en) | 2019-10-11 |
Family
ID=68120853
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| CN201910518542.0A Pending CN110319436A (en) | 2019-06-15 | 2019-06-15 | A kind of deep or light classification vortex burner of compact |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111237796A (en) * | 2020-02-28 | 2020-06-05 | 沈阳环境科学研究院 | High-efficient buggy concentrator of low energy consumption |
| CN111365712A (en) * | 2020-03-16 | 2020-07-03 | 清华大学 | Stable combustion cyclone burner based on similar quasi-side and operation method thereof |
| CN112178633A (en) * | 2020-09-29 | 2021-01-05 | 湖北赤焰热能工程有限公司 | Concentrated double-air-regulation cyclone burner and method |
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| CN109737393A (en) * | 2019-02-19 | 2019-05-10 | 沈阳环境科学研究院 | Big Pulverized Coal Concentration is than postponing hybrid vortex burner |
Cited By (4)
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