CN107620961A - The novel super-low nitrogen combustion apparatus that a kind of non-premixed combustion and premixed combustion are combined - Google Patents
The novel super-low nitrogen combustion apparatus that a kind of non-premixed combustion and premixed combustion are combined Download PDFInfo
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- CN107620961A CN107620961A CN201711061029.0A CN201711061029A CN107620961A CN 107620961 A CN107620961 A CN 107620961A CN 201711061029 A CN201711061029 A CN 201711061029A CN 107620961 A CN107620961 A CN 107620961A
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- 238000002485 combustion reaction Methods 0.000 title claims abstract description 109
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 title claims abstract description 45
- 229910052757 nitrogen Inorganic materials 0.000 title claims abstract description 23
- 239000000567 combustion gas Substances 0.000 claims abstract description 61
- 239000007789 gas Substances 0.000 claims abstract description 47
- 239000003546 flue gas Substances 0.000 claims abstract description 39
- 239000008246 gaseous mixture Substances 0.000 claims abstract description 39
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 38
- 238000002347 injection Methods 0.000 claims abstract description 29
- 239000007924 injection Substances 0.000 claims abstract description 29
- 239000000203 mixture Substances 0.000 claims abstract description 27
- 239000000411 inducer Substances 0.000 claims abstract description 19
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 18
- 238000002156 mixing Methods 0.000 claims abstract description 18
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 18
- 239000007921 spray Substances 0.000 claims abstract description 10
- 238000005516 engineering process Methods 0.000 claims abstract description 8
- 239000002737 fuel gas Substances 0.000 claims abstract description 8
- 239000000446 fuel Substances 0.000 claims description 7
- 238000005474 detonation Methods 0.000 claims description 6
- 230000000694 effects Effects 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 230000007613 environmental effect Effects 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- 238000007865 diluting Methods 0.000 claims description 3
- 230000006641 stabilisation Effects 0.000 claims description 3
- 238000011105 stabilization Methods 0.000 claims description 3
- 235000019504 cigarettes Nutrition 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000008240 homogeneous mixture Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 206010020843 Hyperthermia Diseases 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000036031 hyperthermia Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
Abstract
The present invention relates to the novel super-low nitrogen combustion apparatus that a kind of non-premixed combustion and premixed combustion are combined,Include burner housing,Air duct,Blast tube,Spray head,Flue gas/air Mixture inducer,Premix blender,Non- pre- mixed gas inlet and pre- mixed fuel gas inlet,Injection head is non-mixed,It is interior to be provided with conventional low nitrogen technology basic configuration,Combustion gas is divided into non-pre- mixed and pre- mixed two kinds,Premix combustion gas is contained in mixing composition in premix blender using elder generation,The synthesis gaseous mixture of combustion air and circulating flue gas,Injection head is delivered to through air duct,Non- pre- mixed combustion gas delivers to injection head by blast tube,Comprehensive gaseous mixture is respectively fed to burner hearth with non-pre- mixed combustion gas by injection head,Performed in burner hearth based on the non-premixed combustion on the basis of full premix combustion pattern,Two kinds of combustion modes are organically combined,The novel burner constructed has concentrated the advantages of two kinds of combustion systems,And breach the power limit of premix burner,Improve work applicable surface,There is very strong practicality.
Description
Technical field
It is particularly a kind of using high heating value combustion gas as the non-pre- of fuel the present invention relates to gas fired-boiler heater element technical field
The novel super-low nitrogen combustion apparatus that mixed burning and premixed combustion are combined.
Background technology
NOx is a kind of important atmosphere pollution, is one of arch-criminal for triggering acid rain, haze.As China is controlled environmental protection
The increasing of reason dynamics and going deep into for energy-saving and emission-reduction policy, the limitation for industrial combustion gas emission of NOx of boiler amount is also increasingly strict,
Put into effect a series of standards of restriction boiler pollutant emission limits, monitoring and monitoring requirement, Beijing in 2017
Area must be decreased to 30mg/Nm on newly-built gas fired-boiler NOx emission3It is exactly one below.Therefore, industry is just in boiler flue gas
Carry out largely exploring and innovating in terms of the low-NO_x combustion technology of burner.
Win initial success at present and the drop nitrogen type gas burner of more application mainly there are two kinds:
One is the diffusion combustion formula burner more early released, also known as " non-premix burner ", be characterized in by combustion air with
Burner hearth is respectively fed in the case that combustion gas is unmixed in burner, because combustion air does not mix with combustion gas in burner internal
Close, so need the low nitrogen burning such as adapted flue gas recirculation ancillary technique to carry out drop nitrogen during this non-premix burner work, though
So have that itself is simple in construction, easily manufactured, flameholding, it is safe and easy to adjust the advantages that, but due to must be simultaneously
The low nitrogen burning such as adapted flue gas recirculation ancillary technique can just be effectively reduced boiler NOx discharge capacity, not only increase setting
Cost, and also result in the unstability for bringing increase to burn;
The second is the full premixed type surface combustion formula burner researched and developed in recent years, also known as " all-premixing burner ", be characterized in by
Combustion air is first mixed into homogeneous mixture comprehensively with combustion gas in the metallic cylinder before burner throat, then makes uniformly to mix
Gas only carries out abundant and efficient burning on metallic cylinder surface, rather than in round metal cylinder roasting, and because calory burning is equal
It is even, be not in extreme high heat in combustion chamber, thus the more non-premix burner of NOx discharge will lack, and flue gas can not be used to follow again
The low nitrogen burning ancillary technique such as ring.It is disadvantageous in that work applicable surface is not wide, and existing all-premixing burner is only applicable to
On the boiler that combustion gas and combustion air requirement are less, contribute less than 4t/h, it can just achieve effective control mixability and ensure
Safe operation, for the boiler contributed more than 4t/h, because the requirement of combustion gas and combustion air is big, combustion air and combustion gas ten thousand
One premix section head wire netting in mix it is uneven or occur block wire netting situation when, easily trigger detonation, thus
Cause the accident rate of high-power all-premixing burner higher, potential safety hazard be present.In addition, during existing all-premixing burner operation
Stricter is required to air distribution, tempering detonation easily occurs when the oxygen content in described homogeneous mixture is less than 6%, is higher than
De- fire easily occurs when 9%, and when longtime running is under elevated oxygen level homogeneous mixture state, wherein excessive combustion air
Caused heat during burning can be taken away, causes to produce boiler heat loss, reduces the thermal efficiency.So from operability, work
Make state controllability, safety in operation and stability angle consider, owe ideal, thus in the market using it is more still
The diffusion combustion formula burner more first to come out, i.e., non-premix burner.
Therefore super low-NO_x combustion technology only exists in the innovation stage constantly explored at present, technology is not also overripened, effect
Fruit also owes ideal.And gas fired-boiler realize NOx it is ultralow it is nitrogen discharged be the objective situation demand faced at present, and the realization of the demand
It must also start with from the initial ejection for reducing low NO NOx, replacement formula innovative design is updated to burner structure, is allowed to
Reduction NOx initial ejection amount can be ensured from the combination of theory and practice, is met conscientiously using the boiler of this burner
Increasingly harsh environmental requirement.
The content of the invention
The shortcomings that the invention aims to overcome existing low NO, from the existing high power gas burner of change
Traditional combustion mode is started with, there is provided one kind, which can be taken into account, reaches safe and stable equipment operation and ultralow nitrogen discharged dual-purpose non-pre-
The novel super-low nitrogen combustion apparatus that mixed burning and premixed combustion are combined.
The novel super-low nitrogen combustion apparatus that the non-premixed combustion and premixed combustion of the present invention is combined, main body include burning
Device shell, air duct, blast tube and injection head, it is characterised in that:Combustion gas used divide into non-pre- mixed combustion gas and
Pre- two kinds of mixed combustion gas, also comprising being provided with flue gas/air Mixture inducer, premix mixing in novel super-low nitrogen combustion apparatus
Device, non-pre- mixed gas inlet and pre- mixed fuel gas inlet, wherein:
The front end of described flue gas/air Mixture inducer be mutually connected with the tail end of described premix blender and with premix
Blender, air duct and injection head are coaxially set gradually by airflow direction;
Described blast tube main body is arranged in air duct, is made up of air inlet port, air outlet and intermediate conduit, it enters
Gas port is fixed to stretch and put on the wall body outer surface of air duct, fills the post of described non-pre- mixed gas inlet, its outlet side
Mouth is on the tail end shaft core position of described injection head;
Described flue gas/air Mixture inducer has the mixing of flue gas recycled and combustion air by evenly mixing
Gas transfers to the function of premix blender;
Described pre- mixed gas inlet, its tail end and described cigarette are fixedly installed in the cavity wall of described premix blender
The front end of gas/air Mixture inducer is mutually connected, and its front end is mutually connected with the tail end of described air duct, has to receive and
Gaseous mixture from described flue gas/air Mixture inducer and the pre- mixed combustion from described pre- mixed gas inlet
Both are simultaneously sufficiently mixed the synthesis gaseous mixture containing premix combustion gas, circulating flue gas and combustion air component in composition by gas, then
Described synthesis gaseous mixture is transferred to by the function of spraying in head by air duct 2;
Described injection head is non-premixed type, and inside is low based on fuel staging, gas classification, bias combustion etc. comprising being provided with
Combustion gas spout, air supply channel, air gun and the steady flame device for the conventional low NO that nitrogen combustion technology mechanism is laid, have and perform
By the non-pre- mixed combustion gas from described blast tube and from premix blender synthesis gaseous mixture respectively with fuel staging,
Gas classification, the conventional spray pattern of bias combustion layout are sent into the function of burner hearth;
During work, the pre- mixed combustion gas being sent into by pre- mixed fuel gas inlet enter after premix blender with from flue gas/
The described gaseous mixture of air Mixture inducer is sufficiently mixed, form in containing premix combustion gas, combustion air and circulation cigarette
The synthesis gaseous mixture of gas component, and pass through described air duct and enter in injection head, comprehensive gaseous mixture is direct through air supply channel
It is sent into burner hearth and burns, performs premixed type combustion mode;The described non-pre- mixed combustion being sent into by non-pre- mixed gas inlet
Gas is directly classified is spurted into burner hearth on demand after being sent to by blast tube in injection head by the interior combustion gas spout set or spray gun,
Burning is mixed with the comprehensive gas phase that mixes being sent directly into by air supply channel again afterwards, synthesis gaseous mixture now has filled the post of non-premix combustion
The role of combustion air in burner, execution is non-premixed combustion mode of operation, but based on described combustion air by performing
The synthesis gaseous mixture substitution of premixed type combustion mode, thus the burner to construct has non-premixed combustion and premixed combustion
The working features being combined, the advantages of with full mixing burner and unmixed combustion device;In addition, the part exported by air gun
When non-pre- mixed combustion gas performs ignition operation, igniting combustion supporting air is comprehensive gaseous mixture, because circulating flue gas is to comprehensive mixed
Mixing combustion gas, combustion air in conjunction gas have diluting effect, thus the oxygen content in comprehensive gaseous mixture is totally relatively low, meeting
Ignition point position is slightly had retardation, will not closely be ignited before steady flame device, help to ensure the stabilization of root flame, stabilization
Flame root can also be located at steady flame device downstream, avoid occurring the generation of backfire detonation phenomenon, be advantageous to safe for operation, and follow
Caused partial heat when ring flue gas can take away ignition immediately, it can ensure that temperature rise will not be too at spraying machine head surface aditus laryngis
Height, it is advantageously ensured that the functional reliability and service life of burner apparatus, the security and stability of operation and environmental protection and energy saving.
The novel super-low nitrogen combustion apparatus that non-premixed combustion and premixed combustion of the invention based on above-mentioned design are combined, by
Use, employ combustion air and circulating flue gas first with pre- mixed combustion gas two parts in combustion gas is divided into non-pre- mixed combustion gas
Mixing forms gaseous mixture, is then again further sufficiently mixed pre- mixed combustion gas in composition containing pre- therewith in premix blender
The synthesis gaseous mixture of mixed combustion gas, combustion air and circulating flue gas, then be sent into through non-premixed type injection head in burner hearth, in burner hearth
Interior burning, the mode of operation for being comparable to all-premixing burner of execution, rather than pre- mixed combustion gas are sent to spray through blast tube
Burner hearth is sent into classification on demand after penetrating in head, then with having the comprehensive of the mode of operation function of performing all-premixing burner in burner hearth
Close gaseous mixture to be sufficiently mixed and burn, so being the equal of to have combined the non-pre- of all-premixing burner mode of operation function
Mixed burner.Compared with existing non-premix burner, hence it is evident that can make in burner hearth combustion gas and the mixing of combustion air evenly,
Burning is more abundant, can effectively avoid the generation in area of localized hyperthermia, so as to greatly reduce thermal NO x generation, and then
The ultralow nitrogen discharged positive technique effects of boiler NOx.Compared with existing all-premixing burner, mixed as a result of in premix
Being sufficiently mixed combustion gas, combustion air and circulating flue gas in device in advance turns into the mode of comprehensive gaseous mixture, injection head is turned into non-
Mixed type, thus injection head in be not present be possible to trigger security incident mixing section, therefore can prevent in the prior art because
Combustion gas and combustion air mixing inequality block wire netting and trigger detonation situation in mixing section, also make the work of injection head
Influenceed from the dosage of combustion gas and combustion air, the burner of the present invention is effectively breached power limit, expand work and fit
With face, the requirement of various power requirements boilers can be met.Therefore the present invention changes traditional combustion gas and combustion-supporting sky
The conventional thought that gas mixes at burner nozzle and in burner hearth, burner safe combustion mode and functional structure wound are carried out
Newly, the combination of non-premixed combustion and premixed combustion is realized, the advantages of having concentrated non-premixed combustion and premixed combustion, and it is prominent
The power limit of premix burner has been broken, has reached the stable operation of equipment combustion completion and ultralow nitrogen discharged dual purpose, has been
The renewal product of existing boiler-burner, there are very strong practicality and wide market prospects.
Brief description of the drawings
Fig. 1 is the basic structure schematic diagram of the embodiment of the present invention.
In figure:
1. the air inlet port of 2. air duct of burner housing, 3. blast tube 31.
32. 5. flue gases of the intermediate conduit 4. of air outlet 33. injection head/air Mixture inducer
6. premix the non-pre- mixed pre- mixed fuel gas inlet of gas inlet 8. of blender 7..
Embodiment
The invention will be further described with reference to the accompanying drawings and examples.
In Fig. 1, the novel super-low nitrogen combustion apparatus that non-premixed combustion and premixed combustion of the invention are combined, main body bag
Contain burner housing 1, air duct 2, blast tube 3 and injection head 4, it is characterised in that:Combustion gas used is divided into non-
Pre- mixed combustion gas and pre- mixed two kinds of combustion gas, also enter comprising being provided with flue gas/air Mixture in novel super-low nitrogen combustion apparatus
Mouth section 5, premix blender 6, non-pre- mixed gas inlet 7 and pre- mixed fuel gas inlet 8, wherein:
The front end of described flue gas/air Mixture inducer 5 be mutually connected with the tail end of described premix blender 6 and with it is pre-
Dark clutch 6, air duct 2 and injection head 4 are coaxially set gradually by airflow direction;
The described main body of blast tube 3 is arranged in air duct 2, by air inlet port 31, air outlet 32 and intermediate conduit 33
Form, its air inlet port 31 is fixed to stretch and put on the wall body outer surface of air duct 2, fills the post of described non-pre- mixed gas inlet
Mouth 7, its air outlet 32 is located in described injection head 4;
Described flue gas/air Mixture inducer 5 has the mixed of flue gas recycled by evenly mixing and combustion air
Close the function that gas transfers to premix blender;
Be fixedly installed described pre- mixed gas inlet 8 in the cavity wall of described premix blender 6, its tail end with it is described
The front end of flue gas/air Mixture inducer 4 is mutually connected, and its front end is mutually connected with the tail end of described air duct 2, has and connects
Receive the gaseous mixture from described flue gas/air Mixture inducer 5 and the premix from described pre- mixed gas inlet 8
The comprehensive mixing containing premix combustion gas, circulating flue gas and combustion air component in forming is sufficiently mixed with combustion gas and by both
Gas, then described synthesis gaseous mixture is transferred to by the function of spraying in head 4 by air duct 2;
Described injection head 4 is non-premixed type, and inside includes and is provided with based on fuel staging, gas classification, bias combustion etc.
Combustion gas spout, air supply channel, air gun and the steady flame device for the conventional low NO that low-NO_x combustion technology mechanism is laid, have and hold
It is about to the non-pre- mixed combustion gas from described blast tube 3 and the synthesis gaseous mixture from premix blender 6 respectively with fuel
The conventional spray pattern that classification, gas classification, bias combustion are laid out is sent into the function of burner hearth;
During work, the pre- mixed combustion gas being sent into by pre- mixed fuel gas inlet 8 enters after premix blender 6 with coming from cigarette
The described gaseous mixture of gas/air Mixture inducer 4 is sufficiently mixed, form in containing premix combustion gas, combustion air and follow
The synthesis gaseous mixture of ring flue gas composition, and pass through described air duct 2 and enter in injection head 4, comprehensive gaseous mixture is logical through supplying
Road, which is sent directly into burner hearth, to burn, and performs premixed type combustion mode;Described being sent into by non-pre- mixed gas inlet 7 is non-pre-
Mixed combustion gas is directly classified spray on demand after being sent to by blast tube 3 in injection head 4 by the interior combustion gas spout set or spray gun
Burner hearth is injected, mixes burning with the comprehensive gas phase that mixes being sent directly into by air supply channel again afterwards, synthesis gaseous mixture now is filled the post of
The role of combustion air in non-premix burner, execution is non-premixed combustion mode of operation, but based on described combustion-supporting sky
Gas is substituted by the synthesis gaseous mixture of execution premixed type combustion mode, thus the burner to construct has non-premixed combustion
The working features being combined with premixed combustion, the advantages of with full mixing burner and unmixed combustion device;In addition, by air gun
When the non-pre- mixed combustion gas in part of output performs ignition operation, igniting combustion supporting air is comprehensive gaseous mixture, due to circulating cigarette
Gas has diluting effect, thus the oxygen content in comprehensive gaseous mixture to the mixing combustion gas in comprehensive gaseous mixture, combustion air
It is overall relatively low, ignition point position can be made to slightly have retardation, will not closely be ignited before steady flame device, help to ensure root flame
Stable, stable flame root can also be located at steady flame device downstream, avoid occurring the generation of backfire detonation phenomenon, be advantageous to run
Safely, caused partial heat when and circulating flue gas can take away ignition immediately, it can ensure that the injection surface aditus laryngis of head 4
Locating temperature rise will not be too high, it is advantageously ensured that the functional reliability and service life of burner apparatus, the security and stability of operation and
Environmental protection and energy saving.
Claims (1)
1. the novel super-low nitrogen combustion apparatus that a kind of non-premixed combustion and premixed combustion are combined, main body include burner housing
(1), air duct(2), blast tube(3)With injection head(4), it is characterised in that:Combustion gas used is divided into non-pre- mixed
Combustion gas and pre- mixed two kinds of combustion gas, also comprising being provided with flue gas/air Mixture inducer in novel super-low nitrogen combustion apparatus
(5), premix blender(6), non-pre- mixed gas inlet(7)With pre- mixed fuel gas inlet(8), wherein:
Described flue gas/air Mixture inducer(5)Front end and described premix blender(6)Tail end be mutually connected, simultaneously
With premixing blender(6), air duct(2)With injection head(4)Coaxially set gradually by airflow direction;
Described blast tube(3)Main body is arranged on air duct(2)It is interior, by air inlet port(31), air outlet(32)With in
Between pipeline(33)Form, its air inlet port(31)Fixed stretch is put in air duct(2)Wall body outer surface on, fill the post of described non-
Pre- mixed gas inlet(7), its air outlet(32)Positioned at described injection head(4)It is interior;
Described flue gas/air Mixture inducer(5)With by flue gas recycled by evenly mixing and combustion air
Gaseous mixture transfers to premix blender(6)Function;
Described premix blender(6)Cavity wall on be fixedly installed described pre- mixed gas inlet(8), its tail end and institute
The flue gas stated/air Mixture inducer(4)Front end be mutually connected, its front end and described air duct(2)Tail end mutually hold in the mouth
Connect, have and receive from described flue gas/air Mixture inducer(5)Gaseous mixture enter with from described pre- mixed combustion gas
Gas port(8)Pre- mixed combustion gas and by both be sufficiently mixed composition in contain premix combustion gas, circulating flue gas and combustion air group
The synthesis gaseous mixture divided, then pass through air duct(2)Described synthesis gaseous mixture is transferred into injection head(4)Interior function;
Described injection head(4)For non-premixed type, inside includes and is provided with based on fuel staging, gas classification, bias combustion
Combustion gas spout, air supply channel, air gun and the steady flame device for the conventional low NO laid Deng low-NO_x combustion technology mechanism, have
Perform from described blast tube(3)Non- pre- mixed combustion gas and from premix blender(6)Synthesis gaseous mixture difference
The function of burner hearth is sent into the conventional spray pattern of fuel staging, gas classification, bias combustion layout;
It is described by pre- mixed fuel gas inlet during work(8)The pre- mixed combustion gas being sent into enters premix blender(6)Afterwards with from
Flue gas/air Mixture inducer(4)Described gaseous mixture be sufficiently mixed, form in containing premix combustion gas, combustion air
With the synthesis gaseous mixture of circulating flue gas component, and described air duct is passed through(2)Into injection head(4)In, comprehensive gaseous mixture
It is sent directly into burner hearth and burns through air supply channel, performs premixed type combustion mode;It is described by non-pre- mixed gas inlet(7)
The non-pre- mixed combustion gas being sent into passes through blast tube(3)It is sent to injection head(4)In after directly by the interior combustion gas spout set or
Spray gun is classified on demand spurts into burner hearth, mixes burning with the comprehensive gas phase that mixes being sent directly into by air supply channel again afterwards, now
Comprehensive gaseous mixture has filled the post of the role of combustion air in non-premix burner, and execution is non-premixed combustion mode of operation, but base
Substituted by the synthesis gaseous mixture of execution premixed type combustion mode in described combustion air, thus the burner to construct is
The working features being combined with non-premixed combustion and premixed combustion, with the excellent of full mixing burner and unmixed combustion device
Point;In addition, when the non-pre- mixed combustion gas in the part exported by air gun performs ignition operation, light combustion air and mixed to be comprehensive
Gas, because circulating flue gas has diluting effect to the mixing combustion gas in comprehensive gaseous mixture, combustion air, thus mixed comprehensive
Oxygen content in gas is totally relatively low, and ignition point position can be made to slightly have retardation, will not closely be ignited before steady flame device, contributes to really
The stabilization of root flame is protected, stable flame root can also be located at steady flame device downstream, be avoided that and backfire detonation phenomenon occurs
Occur, be advantageous to safe for operation, and caused partial heat when circulating flue gas can take away ignition immediately, can ensure that spray
Penetrate head(4)Temperature rise will not be too high at the aditus laryngis of surface, it is advantageously ensured that the functional reliability and service life of burner apparatus, fortune
Capable security and stability and environmental protection and energy saving.
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Cited By (4)
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CN109654536A (en) * | 2018-12-16 | 2019-04-19 | 中国航发沈阳发动机研究所 | Autonomous reverse-flow can type combustor |
CN110566956A (en) * | 2019-10-14 | 2019-12-13 | 康柏森热能科技(苏州)有限公司 | Combustion device with air inlet mode switching function |
CN112856408A (en) * | 2021-01-28 | 2021-05-28 | 中冶南方(武汉)热工有限公司 | W-shaped radiant tube burner with gas classification and premixed combustion |
CN114216135A (en) * | 2021-12-01 | 2022-03-22 | 北京科技大学 | Based on CO2Circulating natural gas pure oxygen combustion zero-emission combustion system |
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CN202955696U (en) * | 2012-12-04 | 2013-05-29 | 中国石油化工股份有限公司 | Bottom gas burner for pre-mixing cracking furnace for discharging low nitrogen oxide |
CN204063038U (en) * | 2014-07-07 | 2014-12-31 | 洛阳瑞昌石油化工设备有限公司 | Low NO xflue gas is from return flow burner |
CN204901756U (en) * | 2015-08-17 | 2015-12-23 | 罗诺克兹(北京)能源设备技术有限公司 | Partly mix low NOx burner in advance |
CN205678672U (en) * | 2016-06-14 | 2016-11-09 | 江阴市海鸿石化机械有限公司 | Multipoint mode stable type low NO |
CN206112925U (en) * | 2016-09-27 | 2017-04-19 | 上海华之邦科技股份有限公司 | Flame of gas combustion ware surely fires device |
CN207702461U (en) * | 2017-11-02 | 2018-08-07 | 上海华之邦科技股份有限公司 | The novel super-low nitrogen combustion apparatus that a kind of non-premixed combustion and premixed combustion are combined |
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CN109654536B (en) * | 2018-12-16 | 2021-01-08 | 中国航发沈阳发动机研究所 | Autonomous backflow type combustion chamber |
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CN112856408A (en) * | 2021-01-28 | 2021-05-28 | 中冶南方(武汉)热工有限公司 | W-shaped radiant tube burner with gas classification and premixed combustion |
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