CN113757668B - A spiral ring rib water-cooled cold flame gas burner - Google Patents
A spiral ring rib water-cooled cold flame gas burner Download PDFInfo
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- 238000002485 combustion reaction Methods 0.000 claims abstract description 61
- 238000001816 cooling Methods 0.000 claims abstract description 47
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 239000000498 cooling water Substances 0.000 claims abstract description 41
- 230000000149 penetrating effect Effects 0.000 claims abstract 2
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- 238000005253 cladding Methods 0.000 claims 1
- 239000000446 fuel Substances 0.000 abstract description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 27
- 239000007789 gas Substances 0.000 description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 238000005496 tempering Methods 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000003345 natural gas Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
- F23D14/72—Safety devices, e.g. operative in case of failure of gas supply
- F23D14/78—Cooling burner parts
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- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2214/00—Cooling
-
- 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
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gas Burners (AREA)
Abstract
Description
技术领域technical field
本发明属于冷焰燃气燃烧器技术领域,具体涉及一种螺旋环肋水冷型冷焰燃气燃烧器。The invention belongs to the technical field of cold flame gas burners, in particular to a water-cooled cold flame gas burner with spiral ring ribs.
背景技术Background technique
天然气作为一种清洁能源,具有燃烧效率高,污染物控制成本低且污染物排放少等优点,天然气在燃烧的过程中仍会产生一些大气污染物如氮氧化物等,根据其来源主要分为热力型、快速型和燃料型,其中燃料型和快速型的生成几乎可以忽略不计,热力型NOx占据全部氮氧化物排放的90%以上。As a kind of clean energy, natural gas has the advantages of high combustion efficiency, low pollutant control cost and less pollutant emission. Natural gas will still produce some atmospheric pollutants such as nitrogen oxides in the process of combustion. According to its source, it is mainly divided into Thermal type, fast type and fuel type, in which the generation of fuel type and fast type is almost negligible, and the thermal type NOx accounts for more than 90% of all nitrogen oxide emissions.
控制NOx的排放关键:一是控制氮氧化物的生成,二是控制将已经产生的氮氧化物还原成N2。控制氮氧化物的生成主要是控制燃烧温度,通过降低燃烧温度减少氮氧化物的排放。热力型NOx生成的主要影响因素有燃烧温度、氧气浓度和反应物停留时间等。当燃烧的温度高于1300℃时,反应速率就会增长5~6倍,此时氮氧化物的生成量成指数增加。由于天然气的热值很高,燃烧温度通常可以高达2000K以上,而在燃烧温度高于1300℃时,温度每增加100℃,反应速度将增大6~7倍,此时导致氮氧化物的原始排放呈指数增加。虽然国内现阶段燃气锅炉低氮燃烧技术已经得到一定发展,如分级燃烧、烟气再循环、贫燃预混、水冷预混等,然而部分技术仍然存在成本高、效果差、不适用于高压及超临界锅炉等缺点。The key to controlling the emission of NOx: one is to control the formation of nitrogen oxides, and the other is to control the reduction of nitrogen oxides that have been produced to N 2 . Controlling the formation of nitrogen oxides is mainly to control the combustion temperature, and reduce the emission of nitrogen oxides by lowering the combustion temperature. The main influencing factors of thermal NO x generation are combustion temperature, oxygen concentration and residence time of reactants. When the combustion temperature is higher than 1300 ℃, the reaction rate will increase by 5 to 6 times, and the amount of nitrogen oxides generated at this time increases exponentially. Due to the high calorific value of natural gas, the combustion temperature can usually be as high as 2000K or more. When the combustion temperature is higher than 1300°C, the reaction rate will increase by 6 to 7 times for every 100°C increase in temperature, resulting in the original nitrogen oxides. Emissions are increasing exponentially. Although domestic low-nitrogen combustion technologies for gas-fired boilers have been developed to some extent, such as staged combustion, flue gas recirculation, lean-burn premixing, water-cooling premixing, etc., some technologies still have high costs, poor effects, and are not suitable for high pressure and Disadvantages of supercritical boilers, etc.
发明内容SUMMARY OF THE INVENTION
为了克服以上技术问题,本发明的目的在于提供一种螺旋环肋水冷型冷焰燃气燃烧器,该燃气装置能够实现等压进气,燃气均匀、低温低NOx表面燃烧,同时可以有效防止回火,保证气体燃料燃烧时的稳定、高效、清洁和安全,冷却管道组成闭合的循环回路,还可以实现火焰表面水冷。In order to overcome the above technical problems, the purpose of the present invention is to provide a spiral ring rib water-cooled cold flame gas burner, which can realize equal pressure intake, uniform gas, low temperature and low NOx surface combustion, and can effectively prevent backfire at the same time , to ensure the stability, efficiency, cleanliness and safety of gas fuel combustion, the cooling pipeline forms a closed circulation loop, and can also achieve water cooling on the flame surface.
为了实现上述目的,本发明采用的技术方案是:In order to achieve the above object, the technical scheme adopted in the present invention is:
一种螺旋环肋水冷型冷焰燃气燃烧器,包括表面燃烧装置和三级水冷循环装置:A spiral annular rib water-cooled cold flame gas burner, comprising a surface combustion device and a three-stage water-cooled circulation device:
所述表面燃烧装置包含螺旋环肋8,螺旋环肋8设置多层,围绕点火枪孔/中心二次风管3设置,所述多层螺旋环肋8与燃烧器轴线成角度布置,构成螺旋阶梯状等压进气室11;The surface combustion device includes a
所述三级水冷循环装置包含进水集箱2和出水集箱4,进水集箱2和出水集箱4分别和环置冷却水管5连接形成闭合水循环回路,环置冷却水管5沿燃烧器轴线贯穿螺旋环肋8上设置,构成第一级水冷表面,燃烧室7内部设置有低U型管束10和高U型管束9,低U型管束10和高U型管束9呈十字交叉高低布置,构成第二级水冷表面和第三级水冷表面,整体形成类球体冷焰燃烧表面,所述燃烧室7为圆筒状包覆在U型管束外。The three-stage water-cooling circulation device includes an
所述低U型管束10和高U型管束9均为环置冷却水管5的延伸,出入口均与半圆环出水集箱4、进水集箱2连接,共同构成该装置的水冷循环结构。The low
所述环置冷却水管5沿圆周方向等间距斜置于螺旋环肋8,倾斜角度和螺旋环肋8结构倾斜角度相同,贯穿整个螺旋环肋,构成防回火进气微通道6。The annular cooling water pipes 5 are obliquely placed on the spiral
所述进水集箱2和出水集箱4均为半圆环结构,平行布置于进气室11上方,所述环置冷却水管5包括环置冷却水管5a和环置冷却水管5b,冷却水由进水集箱2进入,流经环置冷却水管5a、高U型管束9和低U型管束10后经对角布置的环置冷却水管5b汇集于出水集箱4。The
所述角度呈45°-75°布置。The angles are arranged at 45°-75°.
本发明的有益效果:Beneficial effects of the present invention:
本发明借助沿螺旋环肋周向环置的冷却水管和高低交叉布置的U型管束,充分降低燃烧温度,同时保证换热效率和燃烧安全性,实现低温低NOx均匀表面燃烧,且适用于常压锅炉、高压锅炉和超临界锅炉。同时也可以作为一种冷却装置,应用于冷却技术领域,起到充分降低热气流温度,保证发热元件安全运行的作用。By means of the cooling water pipes arranged in the circumferential direction of the spiral ring rib and the U-shaped tube bundles arranged in a high and low cross, the invention can fully reduce the combustion temperature, ensure the heat exchange efficiency and combustion safety at the same time, realize the uniform surface combustion with low temperature and low NOx, and is suitable for atmospheric boilers , high pressure boilers and supercritical boilers. At the same time, it can also be used as a cooling device in the field of cooling technology, which can fully reduce the temperature of the hot air flow and ensure the safe operation of the heating element.
附图说明Description of drawings
图1为本发明正视刨面图。Fig. 1 is the front plan view of the present invention.
图2为本发明燃烧器结构图。Figure 2 is a structural diagram of the burner of the present invention.
图3为本发明下视图。Figure 3 is a bottom view of the present invention.
图4为本发明上视图。Figure 4 is a top view of the present invention.
图5为本发明进水集箱和出水集箱结构图。FIG. 5 is a structural diagram of the water inlet header and the water outlet header of the present invention.
图6为本发明螺旋环肋结构图。Fig. 6 is the structure diagram of the spiral ring rib of the present invention.
其中:法兰盘1、进水集箱2、点火枪孔/中心二次风管3、出水集箱4、环置冷却水管5a、环置冷却水管5b、防回火进气微通道6、燃烧室7、螺旋环肋8、高U型管束9、低U型管束10、进气室11。Among them:
具体实施方式Detailed ways
下面结合附图对本发明作进一步详细说明。The present invention will be further described in detail below in conjunction with the accompanying drawings.
参考图1-图6,一种螺旋环肋水冷型冷焰燃气燃烧器,其主要结构为,混合气流由图1的上方多组螺旋环肋8构成的“阶梯”状混合气体入口进入;环置水冷管5通过焊接的方式与多组螺旋环肋8相连接,构成带肋冷却水管,所述多组螺旋环肋8与燃烧器轴线成θ角布置;环置水冷管5沿圆周方向等间距斜置,安装角度与螺旋环肋8倾斜角相同;所述多组螺旋环肋8与一级环置冷却水管5构成防回火进气微通道6,出口构成“阶梯”状燃烧平面;环置水冷管5与高U型管束9和低U型管束10连接,高U型管束9和低U型管束10分别构成二级水冷和三级水冷结构;所述进水集箱2和出水集箱4和环置水冷管5另一端连接,和高U型管束9和低U型管束10构成该冷却装置的水循环系统。Referring to Figures 1 to 6, a spiral ring rib water-cooled cold flame gas burner, the main structure of which is that the mixed gas flow is entered from the "step"-shaped mixed gas inlet formed by multiple sets of
本发明可以保证混合气体在燃烧器表面形成表面燃烧,设有螺旋环肋8,借助圆周方向等间距安装的冷却水管以及高低布置冷却管束降低火焰燃烧温度,有效增加换热量及换热效率。The invention can ensure that the mixed gas forms surface combustion on the surface of the burner, and is provided with
所述环置水冷管5与燃烧器轴线成θ角度等间距圆周方向斜置,螺旋环肋8与环置冷却水管5构成了防回火进气微通道6;所述与燃烧器轴线成θ角布置的多组螺旋环肋8呈现出“阶梯”状结构的气流入口,当混合气流经“阶梯”状进气表面进入防回火进气微通道6时,形成等压进气,保证混合气流在流动方向上均匀进气,进而在出口形成均匀的表面燃烧;所述螺旋环肋8使得气流呈旋转状态进入燃烧器,高湍动度的出口气流使低温燃烧效果进一步加强,同时有助于点火,强化燃烧;螺旋上升的结构使得流通截面积沿进气方向逐渐减小,有效防止预混燃烧出现回火,保证了预混燃烧的安全性。The annular water-cooling pipe 5 and the burner axis are obliquely arranged at an angle θ at equal intervals in the circumferential direction, and the spiral
与燃烧器轴线成θ角布置的多组螺旋环肋8、环置冷却水管5贯穿螺旋环肋8构成第一级水冷表面,进水集箱2和出水集箱4分别和环置冷却水管5连接形成闭合水循环回路,高U型管束9和低U型管束10十字交叉高低布置构成第二级和第三级水冷,同时网状球形错列结构可以增加烟气与冷却水管的换热面积,增加燃烧的湍动度,强化换热。网状火焰表面水冷管道结构为U型循环管束,三级水冷整体形成类球体冷焰,多重水冷表面布置充分吸收预混火焰和高温烟气热量,有效降低其温度,从而实现低温低NOx燃烧。Multiple groups of
所述环置冷却水管5上端与进水集箱2和出水集箱4连接,下端与低U型管束10和高U型管束9连接,进水集箱中的冷却水分别从环置冷却水管5a进入,后流经U型管束从环置冷却水管5b流出至对角出水集箱,共同构成该装置的冷却水循环系统。The upper end of the annular cooling water pipe 5 is connected to the
所述点火枪孔/中心二次风管3焊接在螺旋环肋8内侧,作为点火枪孔时,形成完全预混表面低温燃烧;作为中心二次风管时,形成贫氧部分预混低温表面燃烧及富氧补燃,避开气体燃料燃烧NOx排放最高时的过量空气系数。The ignition gun hole/central
本发明的工作原理为:The working principle of the present invention is:
本发明多组螺旋环肋8与燃烧器轴线成θ(45°<θ<75°)角布置,构成连续的“阶梯”状气流入口,保证混合气流均匀等压进气。多组螺旋环肋8与环置水冷管5构成防回火进气微通道6,当混合气流由连续的“阶梯”状气流入口进入防回火进气微通道6时,被环置水冷管5冷却,充分降低预混火焰根部燃烧温度,减少氮氧化物的原始排放,同时由于流通截面积沿气流方向逐渐减小,导致预混火焰无法由燃烧室向燃烧器内扩散,有效防止了预混火焰易回火的燃烧安全隐患,保证燃烧的安全性。火焰在燃烧器表面燃烧产生的烟气先后被由低U型管束10和高U型管束9构成的二级水冷和三级水冷冷却,充分吸收高温烟气的热量,降低烟气中热力型氮氧化物的生成,使低温清洁燃烧效果更佳,同时连续的“山”字型冷却表面结构布置使得气流湍动度增加,换热效果进一步增强。The multiple groups of helical
本发明设有进水集箱2和出水集箱4,分别和环置水冷管5连接,与高U型管束9和低U型管束10构成该装置的冷却水循环系统。水箱为半圆环结构,本发明所有管式结构均采用可承压圆管,可以在高压条件下安全运行,结构简单,制造方便,适用于批量生产,且可以在多种工作环境下运行。The present invention is provided with a
本发明针对该燃烧器提供了两种结构方案:The present invention provides two structural solutions for the burner:
方案一在燃烧器中心布置了中心二次风管3,避开气体燃料燃烧NOx排放最高时的过量空气系数,形成贫氧部分预混低温表面燃烧及富氧补燃,低氮燃烧效果更佳。
方案二在燃烧器中心布置了点火孔3,形成全预混低温表面燃烧,燃烧效率更高。In the second scheme, the
本发明的具体运行方式为:The specific operation mode of the present invention is:
在混合气体进入燃烧装置前首先将冷却水通入进水集箱2,当冷却水在该装置中形成水循环后,再将混合气流通入防回火进气微通道6,最后进行点火。在具体的运行过程中根据实际情况调节环置冷却水管中冷却水的量对燃烧火焰温度进行调节,保证燃气在燃烧装置内的低温低NOx均匀燃烧。Before the mixed gas enters the combustion device, the cooling water is firstly passed into the
以上内容仅为说明本发明的技术思想,不能以此限定本发明的保护范围,凡是按照本发明提出的技术思想,在技术方案基础上所做的任何改动,如变换冷却水管根数、螺旋环肋形状等均落入本发明权利要求书的保护范围之内。The above content is only to illustrate the technical idea of the present invention, and it cannot limit the protection scope of the present invention. Any changes made on the basis of the technical solution according to the technical idea proposed by the present invention, such as changing the number of cooling water pipes, the spiral ring The rib shape and the like all fall within the protection scope of the claims of the present invention.
Claims (5)
Priority Applications (1)
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CN111853747A (en) * | 2020-08-25 | 2020-10-30 | 博瑞特热能设备股份有限公司 | A cylindrical low-nitrogen energy-saving pressurized water tube boiler |
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