CN107559882B - An axially graded low-pollution combustion chamber - Google Patents
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- 238000002485 combustion reaction Methods 0.000 title claims abstract description 159
- 239000000446 fuel Substances 0.000 claims description 42
- 238000002347 injection Methods 0.000 claims description 23
- 239000007924 injection Substances 0.000 claims description 23
- 238000001704 evaporation Methods 0.000 claims description 10
- 230000008020 evaporation Effects 0.000 claims description 9
- 238000005516 engineering process Methods 0.000 abstract description 10
- 230000002269 spontaneous effect Effects 0.000 abstract description 8
- 238000005496 tempering Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 38
- 239000003921 oil Substances 0.000 description 20
- 238000010586 diagram Methods 0.000 description 10
- 239000000203 mixture Substances 0.000 description 7
- 239000003344 environmental pollutant Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000010793 Steam injection (oil industry) Methods 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
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Abstract
本发明涉及一种轴向分级低污染燃烧室,采用轴向分级燃烧技术,将燃烧室分为值班级和主燃级,值班级和主燃级均采用多个预混模,有效的控制值班燃烧区和主燃烧区的当量比,提高油气混合程度,降低降低了燃烧室不同工况下的污染排放水平,而且预混模采用合理的结构设计防止自燃、回火等问题的产生。
The invention relates to an axially graded low-pollution combustion chamber. The axially graded combustion technology is used to divide the combustion chamber into a duty class and a main combustion class. Both the duty class and the main combustion class adopt multiple premixed models to effectively control the duty The equivalence ratio between the combustion zone and the main combustion zone improves the degree of oil-gas mixing and reduces the pollution emission level of the combustion chamber under different working conditions, and the pre-mixing model adopts a reasonable structural design to prevent problems such as spontaneous combustion and tempering.
Description
技术领域technical field
本发明属于燃气轮机燃烧室领域,涉及一种轴向分级低污染燃烧室,具体是一种值班级、主燃级均采用多点喷射贫油预混预蒸发的轴向分级低污染燃烧室。The invention belongs to the field of gas turbine combustors, and relates to an axially graded low-pollution combustor, in particular to an axially graded low-pollution combustor in which both the duty class and the main combustion stage adopt multi-point injection lean oil premixing and pre-evaporation.
背景技术Background technique
近年来,由于燃气轮机单机功率大、参与联合循环的燃气轮机组使整个系统达到更高的热效率,因此燃气轮机在电力、石化、冶金等领域的应用越来越广泛。燃气轮机在工作中要产生大量的污染物,环境问题的日益严重使得对燃气轮机污染排放的要求越来越严格,在15%的O2浓度下,对于天然气燃料来说,NOx排放小于25ppm,CO排放小于50ppm,对于柴油燃料来说,NOx排放小于65ppm,CO排放小于100ppm,低污染燃烧技术成为先进地面燃气轮机的发展趋势,但燃气轮机总体性能的提升对主燃绕室设计提出了更高的要求。In recent years, due to the high power of a single gas turbine and the gas turbine unit participating in the combined cycle to achieve higher thermal efficiency of the entire system, the application of gas turbines in electric power, petrochemical, metallurgy and other fields has become more and more extensive. Gas turbines will produce a large amount of pollutants during work. The increasingly serious environmental problems have made the requirements for gas turbine pollution emissions more and more stringent. Under 15% O2 concentration, for natural gas fuel, NOx emissions are less than 25ppm, and CO emissions are less than For diesel fuel, NOx emissions are less than 65ppm, and CO emissions are less than 100ppm. Low-pollution combustion technology has become the development trend of advanced ground gas turbines, but the improvement of the overall performance of gas turbines puts forward higher requirements for the design of the main combustion chamber.
目前地面燃气轮机,常用的燃烧污染物控制技术主要包括向燃烧室喷水/喷蒸汽的“湿”低排放技术、“干”低NOx DLN排放技术、催化燃烧等。“湿”低排放技术由于喷水、喷蒸汽进一步降低NOx排放的方法会对燃机循环性能、部件寿命等产生影响,同时一氧化碳、未燃碳氢化合物的排放量也开始增加。目前应用较多、发展最为成熟的是“干”式低NOx燃烧技术,这是根据热力NOx的生成机理,通过将主燃烧区的火焰温度控制在1670-1900K之间来实现降低NOx的排放,采用预混预蒸发方式,燃料在进入燃烧区之前与空气混合形成均匀的油气混合物,通过调节油气比来达到控制燃烧温度,进而控制NOx的排放水平。RR公司的RB211工业燃气轮机采用的DLN燃烧室,包含9个径向安装的逆流单管燃烧室,每个火焰筒有一个2级燃烧室组件,在两极间的供油和供气是独立的,分级的目的是在部分负荷下维持高油气比和降低排放量;RR公司的Trent干低排放燃烧室包含串联的贫油预混燃油喷射系统,在不同的工况下不改变空气分配比,而是调节从一个区到另一个区的燃料分配,从而维持一个相对恒定的燃烧温度,以降低污染排放水平;GE公司的LM6000燃气轮机采用环形DLN燃烧室,通过燃料分级和超贫油火焰温度来降低污染排放,其中环包括30个预混燃烧器,在整个发动机工作范围内工作,内环和外环各有15个和30个预混燃烧器,实现可调,保证燃烧室在狭窄的温度范围内工作;PW公司发展的低排放燃烧室主要采用径向分级、分段燃烧、燃料预混和预燃来降低污染排放水平,比如E3发动机燃烧室、Vorbix燃烧室、FT8-2燃气轮机燃烧室等。At present, the commonly used combustion pollutant control technologies for ground gas turbines mainly include "wet" low emission technology of spraying water/steam into the combustion chamber, "dry" low NOx DLN emission technology, catalytic combustion, etc. The "wet" low emission technology further reduces NOx emissions due to water injection and steam injection, which will have an impact on the cycle performance and component life of the gas turbine. At the same time, the emissions of carbon monoxide and unburned hydrocarbons have also begun to increase. At present, the most widely used and most developed is the "dry" low-NOx combustion technology, which is based on the formation mechanism of thermal NOx and reduces NOx emissions by controlling the flame temperature in the main combustion zone between 1670-1900K. Using the pre-mixing and pre-evaporation method, the fuel is mixed with air to form a uniform oil-air mixture before entering the combustion zone, and the combustion temperature is controlled by adjusting the oil-air ratio, thereby controlling the NOx emission level. The DLN combustor used by RR's RB211 industrial gas turbine includes 9 radially installed counter-flow single-tube combustors, each flame tube has a 2-stage combustor assembly, and the oil supply and gas supply between the two poles are independent. The purpose of staging is to maintain a high fuel-air ratio and reduce emissions under partial load; RR's Trent dry low-emission combustion chamber contains a series of lean-oil premixed fuel injection systems, which do not change the air distribution ratio under different operating conditions, while It is to adjust the distribution of fuel from one zone to another, so as to maintain a relatively constant combustion temperature to reduce the level of pollution emissions; GE's LM6000 gas turbine uses an annular DLN combustor, which is reduced by fuel staging and ultra-lean flame temperature Pollution emission, the ring includes 30 premixed burners, which work in the entire engine operating range, and the inner and outer rings have 15 and 30 premixed burners respectively, which can be adjusted to ensure that the combustion chamber is in a narrow temperature range Internal work; the low-emission combustors developed by PW mainly use radial staging, staged combustion, fuel premixing and pre-combustion to reduce pollution emission levels, such as E3 engine combustors, Vorbix combustors, FT8-2 gas turbine combustors, etc.
国内针对地面燃气轮机燃烧室也进行了相关的研究,南京航空航天大学的专利201610054669.8发明了一种地面燃机单管燃烧室,以天然气为燃料,带有旋转方向相反的双级斜切径向旋流器,加强空气和天然气的混合;西北工业大学的专利201610016396.8涉及一种地面燃机燃烧室结构及其分级燃烧组织方式,值班级燃烧区单独在前部采用末端带有收敛段的小火焰筒,后部主燃区采用带有火焰稳定器的大火焰筒,值班级形成稳定的点火源,主燃级预混合提高燃烧效率。Relevant research has also been carried out on the combustion chamber of ground gas turbines in China. The patent 201610054669.8 of Nanjing University of Aeronautics and Astronautics invented a single-tube combustion chamber for ground gas turbines. flow device to strengthen the mixing of air and natural gas; Northwestern Polytechnical University's patent 201610016396.8 relates to a ground gas turbine combustion chamber structure and its hierarchical combustion organization mode. The duty-level combustion area uses a small flame tube with a converging section at the front. , The rear main combustion zone adopts a large flame tube with a flame stabilizer, the duty level forms a stable ignition source, and the main combustion level is pre-mixed to improve combustion efficiency.
通过国内外研究现状可以看出,现在使用的轻型燃气轮机大多都是航改燃气轮机,其燃烧室基本上沿用了航空发动机的环形结构,但做了相应的改动,以满足地面污染排放的要求。地面燃气轮机燃烧室既要保证稳定工作,又要保证在整个工作范围内有很低的污染排放水平。燃烧室的稳定工作包括拓宽贫油熄火边界、避免自燃、回火、燃烧不稳定性的产生;燃烧室低污染排放水平通过避免燃烧区以化学恰当比燃烧、消除局部高温区、控制燃烧区当量比、减小燃气在高温区的停留时间等方法来降低整个工作范围的污染排放。It can be seen from the research status at home and abroad that most of the light gas turbines currently in use are aeroderivative gas turbines, and their combustion chambers basically follow the annular structure of aeroengines, but corresponding changes have been made to meet the requirements of ground pollution emissions. The ground gas turbine combustor must not only ensure stable operation, but also ensure a very low level of pollution emissions within the entire operating range. The stable work of the combustion chamber includes widening the boundary of lean flameout, avoiding spontaneous combustion, backfire, and combustion instability; the low pollution emission level of the combustion chamber avoids combustion in the combustion zone at a chemically appropriate ratio, eliminates the local high temperature zone, and controls the equivalent of the combustion zone Reduce the pollution emission in the whole working range by reducing the residence time of the gas in the high temperature area and other methods.
发明内容Contents of the invention
要解决的技术问题technical problem to be solved
为了避免现有技术的不足之处,本发明提出一种轴向分级低污染燃烧室,有效的控制值班燃烧区和主燃烧区的当量比,提高油气混合程度,降低降低了燃烧室不同工况下的污染排放水平,而且预混模采用合理的结构设计防止自燃、回火等问题的产生。In order to avoid the deficiencies of the prior art, the present invention proposes an axially graded low-pollution combustion chamber, which can effectively control the equivalence ratio between the on-duty combustion zone and the main combustion zone, improve the degree of oil-gas mixing, and reduce the different working conditions of the combustion chamber. The lower pollution emission level, and the pre-mixed mold adopts a reasonable structural design to prevent spontaneous combustion, tempering and other problems.
技术方案Technical solutions
一种轴向分级低污染燃烧室,包括短突扩扩压器、燃烧室火焰筒、燃烧室机匣、值班级10和主燃级12;其特征在于:所述值班级10为多个预混模沿周向均布在燃烧室头部端壁11上,预混模收敛段出口与燃烧室头部端壁内侧平齐;所述主燃级12为多个预混模的组合,组合形式为:在下游火焰筒内壁13和火焰筒外壁14上多排设置预混模,预混模收敛段出口与火焰筒壁内侧平齐,一排预混模与值班级预混模在同一周向位置;所述值班级10预混模的数目与设置在下游火焰筒内壁13和火焰筒外壁14上每排的预混模的数目相等;所述每个预混模上设有燃油管路,值班级所有预混模由一条燃油管路供油;所述主燃级所有预混模由另外一条燃油管路供油。An axially graded low-pollution combustion chamber, including a short burst diffuser, a combustion chamber flame tube, a combustion chamber casing, a duty level 10 and a main combustion level 12; it is characterized in that: the duty level 10 is a plurality of pre-combustion The mixed mode is evenly distributed on the end wall 11 of the combustion chamber head along the circumferential direction, and the outlet of the premixed mode convergence section is flush with the inner side of the end wall of the combustion chamber head; the main combustion stage 12 is a combination of multiple premixed modes, and the combination form is : Multiple rows of premixed molds are arranged on the inner wall 13 of the downstream flame cylinder and the outer wall 14 of the flame cylinder, the outlet of the convergent section of the premixed mold is flush with the inner side of the flame cylinder wall, and one row of premixed molds is at the same circumferential position as the duty level premixed mold The number of the premixed molds of the duty level 10 is equal to the number of the premixed molds arranged on the downstream flame tube inner wall 13 and the flame tube outer wall 14; each of the premixed molds is provided with a fuel pipeline, and the on-duty All the premixed models of the main combustion stage are supplied by one fuel pipeline; all the premixed modules of the main combustion stage are supplied by another fuel pipeline.
所述多排设置预混模为1~5排。The multi-row setting premixed mode is 1 to 5 rows.
所述值班级10和主燃级12的预混模采用多点喷射贫油预混预蒸发结构,包括燃油喷嘴15、旋流器17,集油环18,燃油喷孔21和预混环腔22;旋流器17的后端设有由平直段19和收敛段20组成的预混环腔22,燃油喷嘴15通过燃油喷嘴安装座16安装在旋流器17的轴心,且喷嘴出口与旋流器出口平齐;旋流器17的外部设有集油环18,在旋流器下游3-5mm处,沿周向在平直段19上均布10-30个燃油喷孔21,连通集油环18与预混环腔22,喷孔直径0.2~0.8mm;所述预混环腔22的长度为环腔平均流速与燃料自燃时间乘积的0.25~0.75倍,收敛段与轴向夹角30°~45°。The premixing model of the duty stage 10 and the main combustion stage 12 adopts a multi-point injection lean fuel premixing pre-evaporation structure, including fuel nozzles 15, swirlers 17, oil collector rings 18, fuel injection holes 21 and premixing ring chambers 22. The rear end of the swirler 17 is provided with a premixing ring cavity 22 composed of a straight section 19 and a converging section 20. The fuel nozzle 15 is installed on the axis of the swirler 17 through the fuel nozzle mounting seat 16, and the outlet of the nozzle It is flush with the outlet of the swirler; the exterior of the swirler 17 is provided with an oil collecting ring 18, and 10-30 fuel injection holes 21 are evenly distributed on the straight section 19 along the circumferential direction at 3-5mm downstream of the swirler , connecting the oil collecting ring 18 and the premixing annular chamber 22, the diameter of the nozzle hole is 0.2-0.8mm; the length of the premixing annular chamber 22 is 0.25-0.75 times the product of the average flow velocity of the annular chamber and the spontaneous combustion time of the fuel, and the convergence section and the shaft The included angle is 30°~45°.
所述旋流器17采用轴向旋流器,叶片形状采用直叶片,叶片个数6~18个,叶片角度30°~60°。The swirler 17 is an axial swirler, the shape of the blades is straight blades, the number of blades is 6-18, and the blade angle is 30°-60°.
所述相邻值班级预混模中心距为预混模直径的1.25~2.5倍,且不大于125mm。The center-to-center distance of the premixed molds of adjacent duty classes is 1.25 to 2.5 times the diameter of the premixed molds and not greater than 125mm.
所述第一排预混模距值班级的轴向距离为火焰筒直径的0.75~1.5倍。The axial distance between the first row of premixed molds and the duty class is 0.75 to 1.5 times the diameter of the flame cylinder.
所述相邻两排预混模之间的轴向距离为预混模直径的1.25~2.5倍。The axial distance between two adjacent rows of premixed molds is 1.25 to 2.5 times the diameter of the premixed molds.
有益效果Beneficial effect
本发明提出的一种轴向分级低污染燃烧室,采用轴向分级燃烧技术,将燃烧室分为值班级和主燃级,值班级和主燃级均采用多个预混模,有效的控制值班燃烧区和主燃烧区的当量比,提高油气混合程度,降低降低了燃烧室不同工况下的污染排放水平,而且预混模采用合理的结构设计防止自燃、回火等问题的产生。An axially graded low-pollution combustion chamber proposed by the present invention adopts the axially graded combustion technology to divide the combustion chamber into a duty class and a main combustion class. The equivalence ratio between the on-duty combustion zone and the main combustion zone improves the degree of oil-gas mixing, reduces the pollution emission level of the combustion chamber under different working conditions, and the pre-mixing model adopts a reasonable structural design to prevent spontaneous combustion, backfire and other problems.
本发明与现有技术相比所具有的优点如下:Compared with the prior art, the present invention has the following advantages:
1、本发明提供了一种轴向分级低污染燃烧室,采用轴向分级燃烧技术将燃烧室分为主燃级和值班级,小工况下只有值班级工作,值班级采用多点喷射贫油预混预蒸发结构,降低小工况下的污染排放水平,采用轴向分级避免了值班级、主燃级之间的相互干扰,确保了值班燃烧区的火焰稳定性。1. The present invention provides an axially graded low-pollution combustion chamber. The combustion chamber is divided into the main combustion stage and the duty stage by adopting the axial staged combustion technology. The oil pre-mixing and pre-evaporation structure reduces the pollution emission level under small working conditions, and adopts axial classification to avoid mutual interference between the duty class and the main combustion stage, ensuring the flame stability in the duty combustion area.
2、随着工况的增大,主燃级开始工作,值班级位于主燃级上游,值班燃烧区的高温燃气有利于主燃级的油气混合以及主燃级的点火,轴向分级改善了径向分级头部高温区集中的问题,主燃级采用多点喷射贫油预混预蒸发结构使主燃烧区油气混合均匀,避免了局部高温区,同时大量空气沿机匣从主燃级进入,导致火焰筒内燃气流速加快,缩短了燃气在高温区的停留时间,大大降低了大工况下的污染物排放水平。2. As the working conditions increase, the main combustion stage starts to work, and the duty stage is located upstream of the main combustion stage. The high-temperature gas in the duty combustion area is conducive to the oil-gas mixing of the main combustion stage and the ignition of the main combustion stage. The axial classification improves Concentration of the high temperature area in the radial classification head, the main combustion stage adopts the multi-point injection lean oil premixing pre-evaporation structure to make the oil and gas in the main combustion area mix evenly, avoiding the local high temperature area, and at the same time, a large amount of air enters from the main combustion stage along the casing , resulting in faster gas flow in the flame tube, shortening the residence time of gas in the high temperature zone, and greatly reducing the pollutant emission level under large working conditions.
3、主燃级多个预混模沿周向均布在火焰筒内外壁上,改善了燃烧室出口温度分布,从而省略了掺混孔,使更多的空气参与燃烧,增大了燃气轮机的功率。3. Multiple premixing modes of the main combustion stage are evenly distributed on the inner and outer walls of the flame tube along the circumferential direction, which improves the temperature distribution at the outlet of the combustion chamber, thereby omitting the mixing hole, allowing more air to participate in the combustion, and increasing the power of the gas turbine.
附图说明Description of drawings
图1:本发明实施例轴向分级低污染燃烧室示意图Figure 1: Schematic diagram of an axially graded low-pollution combustion chamber according to an embodiment of the present invention
图2:本发明实施例适用于不同工作范围的燃烧室火焰筒结构示意图Figure 2: Schematic diagram of the structure of the combustion chamber flame tube applicable to different working ranges according to the embodiment of the present invention
图3:本发明实施例值班级、主燃级预混模分布结构示意图Figure 3: Schematic diagram of the distribution structure of the duty class and the main combustion class premixed mode of the embodiment of the present invention
图4:本发明实施例轴向分级全环燃烧室结构示意图Figure 4: Schematic diagram of the structure of the axially graded full-ring combustion chamber of the embodiment of the present invention
图5:本发明实施例预混模结构示意图Figure 5: Schematic diagram of the premixed mold structure of the embodiment of the present invention
图中:1-前置扩压器内壁,2-前置扩压器外壁,3-前置扩压器流道,4-突扩段,5-燃烧室外机匣,6-外环腔,7-火焰筒支撑板,8-燃烧室内机匣,9-内环腔,10-值班级,11-燃烧室头部端壁,12-主燃级,13-火焰筒内壁,14-火焰筒外壁,15-燃油喷嘴,16-喷嘴安装座,17-旋流器,18-集油环,19-平直段,20-收敛段,21-燃油喷孔,22-预混环腔In the figure: 1-inner wall of the pre-diffuser, 2-outer wall of the pre-diffuser, 3-flow path of the pre-diffuser, 4-sudden expansion section, 5-combustion outer casing, 6-outer ring cavity, 7-flame tube support plate, 8-chassis in combustion chamber, 9-inner ring cavity, 10-duty level, 11-end wall of combustion chamber head, 12-main combustion level, 13-inner wall of flame tube, 14-flame tube Outer wall, 15-fuel nozzle, 16-nozzle mounting seat, 17-swirl, 18-oil collecting ring, 19-straight section, 20-converging section, 21-fuel injection hole, 22-premixing ring cavity
具体实施方式Detailed ways
现结合实施例、附图对本发明作进一步描述:Now in conjunction with embodiment, accompanying drawing, the present invention will be further described:
本发明采用以下技术方案:一种轴向分级低污染燃烧室,包括前置扩压器内壁、前置扩压器外壁、前置扩压器流道、突扩段、燃烧室外机匣、外环腔、火焰筒支撑板、燃烧室内机匣、内环腔、值班级、燃烧室头部端壁、主燃级、火焰筒内壁、火焰筒外壁,所述的前置扩压器流道由前置扩压器内壁和前置扩压器外壁围成,所述的前置扩压器和突扩段构成了短突扩扩压器,起到减速增压的作用,有利于点火和火焰稳定,所述的外环腔由燃烧室外机匣和火焰筒外壁围成,所述的内环腔由燃烧室内机匣和火焰筒内壁围成,主燃级空气和火焰筒冷却空气从外环腔和内环腔进入,所述的值班级和主燃级由多个预混模组成,值班级预混模沿周向均布在燃烧室头部端壁上,主燃级预混模沿周向均布在值班级下游火焰筒外壁和火焰筒内壁上,值班级和主燃级独立控制,满足燃烧室不同工况要求,所述的预混模由燃油喷嘴、喷嘴安装座、旋流器、集油环、平直段、收敛段、燃油喷孔、预混环腔组成,所述的预混环腔由平直段和收敛段围成,燃油和空气在预混环腔中预混预蒸发,形成均匀的油气混合物,通过合适的预混环腔长度防止自燃的产生,所述的收敛段增加油气混合物轴向速度,产生脱体火焰,防止回火的发生。The present invention adopts the following technical solutions: an axially graded low-pollution combustion chamber, including the inner wall of the pre-diffuser, the outer wall of the pre-diffuser, the flow channel of the pre-diffuser, the sudden expansion section, the casing outside the combustion chamber, and the outer wall of the pre-diffuser. ring cavity, flame tube support plate, combustion chamber casing, inner ring cavity, duty stage, combustion chamber head end wall, main combustion stage, flame tube inner wall, flame tube outer wall, the pre-diffuser flow path is composed of The inner wall of the pre-diffuser and the outer wall of the pre-diffuser are surrounded, and the pre-diffuser and the sudden expansion section constitute a short sudden expansion diffuser, which plays the role of deceleration and supercharging, which is beneficial to ignition and flame stable, the outer ring cavity is surrounded by the casing outside the combustion chamber and the outer wall of the flame tube, the inner ring cavity is surrounded by the casing inside the combustion chamber and the inner wall of the flame tube, and the main combustion stage air and the cooling air of the flame tube come from the outer ring cavity and the inner ring cavity, the duty level and the main combustion level are composed of multiple premixed molds, the duty level premixed molds are evenly distributed on the end wall of the combustion chamber head along the circumferential direction, and the main combustion level premixed molds are evenly distributed along the circumferential direction On the outer wall of the flame tube downstream of the duty level and on the inner wall of the flame tube, the duty level and the main combustion level are independently controlled to meet the requirements of different working conditions of the combustion chamber. ring, straight section, converging section, fuel injection hole, and premixing annular cavity, the premixing annular cavity is surrounded by a straight section and a converging section, fuel and air are premixed and pre-evaporated in the premixing annular cavity, A uniform mixture of oil and gas is formed, and spontaneous combustion is prevented through an appropriate length of the premixed ring cavity. The convergent section increases the axial velocity of the mixture of oil and gas, generates a detached flame, and prevents the occurrence of backfire.
进一步的,所述的值班级位于燃烧室头部端壁上,预混模收敛段出口与燃烧室头部端壁内侧平齐,主燃级位于火焰筒外壁以及火焰筒内壁上,预混模收敛段与火焰筒外壁内侧和火焰筒内壁外侧平齐,保证预混模的使用寿命。Further, the duty stage is located on the end wall of the combustion chamber head, the outlet of the premixed mode convergence section is flush with the inside of the end wall of the combustion chamber head, the main combustion stage is located on the outer wall of the flame tube and the inner wall of the flame tube, and the premixed mode The converging section is flush with the inner side of the outer wall of the flame tube and the outer side of the inner wall of the flame tube to ensure the service life of the premixed mold.
进一步的,值班级预混模沿周向均布在燃烧室头部端壁上,相邻预混模中心距为预混模直径的1.25~2.5倍,且不大于125mm,保证相邻预混模之间不会干扰,又能保证正常联焰。Further, the duty-level premixed molds are evenly distributed on the end wall of the combustion chamber head along the circumferential direction, and the center distance between adjacent premixed molds is 1.25 to 2.5 times the diameter of the premixed molds, and is not greater than 125mm, ensuring that the distance between adjacent premixed molds There will be no interference between them, and the normal joint flames can be guaranteed.
进一步的,主燃级预混模沿周向均布在值班级下游火焰筒外壁和火焰筒内壁上,预混模沿火焰筒方向布置1~5排,每排的预混模个数与值班级预混模个数相同,主燃级第一排预混模距值班级的轴向距离为火焰筒直径的0.75~1.5倍,并且与值班级预混模在同一周向位置,相邻两排预混模之间的轴向距离为预混模直径的1.25~2.5倍,保证相邻两排预混模之间不会相互干扰,相邻两排预混模采用叉排的方式布置,保证出口温度分布均匀性。Further, the premixing modules of the main combustion level are evenly distributed on the outer wall of the flame tube downstream of the duty class and on the inner wall of the flame tube along the circumferential direction, and the premixing models are arranged in 1 to 5 rows along the direction of the flame tube, and the number of premixing modules in each row is the same as that of the duty class premixed modules. The number of mixed models is the same, the axial distance between the first row of premixed molds of the main combustion stage and the duty class is 0.75 to 1.5 times the diameter of the flame tube, and it is at the same circumferential position as the duty class premixed molds, and the two adjacent rows of premixed The axial distance between the mixed molds is 1.25 to 2.5 times the diameter of the premixed molds to ensure that two adjacent rows of premixed molds will not interfere with each other. The two adjacent rows of premixed molds are arranged in a fork row to ensure that the outlet Uniformity of temperature distribution.
进一步的,所述的预混模采用多点喷射贫油预混预蒸发结构,旋流器采用轴向旋流器,叶片形状为直叶片,叶片个数6~18个,叶片角度30°~60°,收敛段与轴向夹角30°~45°,预混环腔的长度为环腔平均流速与燃料自燃时间乘积的0.25~0.75倍,喷嘴采用单油路离心喷嘴,喷嘴出口与旋流器出口平齐,燃油喷孔在旋流器下游3~5mm处,沿周向均布在平直段上,喷孔个数10~30个,喷孔直径0.2~0.8mm。Further, the pre-mixing model adopts a multi-point injection lean oil pre-mixing pre-evaporation structure, the swirler adopts an axial swirler, the blade shape is a straight blade, the number of blades is 6-18, and the blade angle is 30°- 60°, the angle between the convergent section and the axial direction is 30°~45°, the length of the premixing ring cavity is 0.25~0.75 times the product of the average flow velocity of the ring cavity and the fuel self-ignition time, the nozzle adopts a single oil circuit centrifugal nozzle, the nozzle outlet and the rotary The outlet of the swirler is flush, and the fuel injection holes are located 3 to 5 mm downstream of the swirler, and are evenly distributed on the straight section along the circumferential direction. The number of injection holes is 10 to 30, and the diameter of the injection holes is 0.2 to 0.8 mm.
下面结合具体实施例对本发明进行详细说明The present invention is described in detail below in conjunction with specific embodiment
如图1所示,本实施例的一种轴向分级低污染燃烧室示意图,燃烧室外机匣5与前置扩压器外壁2焊接,通过尾部火焰筒支撑板7与火焰筒外壁14连接,围成外环腔6,燃烧室内机匣8与前置扩压器内壁1焊接,通过尾部火焰筒支撑板7与火焰筒内壁13连接,围成内环腔9,火焰筒内壁13和火焰筒外壁14通过燃烧室头部端壁11连接,值班级预混模10沿周向均布在头部端壁11上,预混模收敛段出口与燃烧室头部端壁内侧平齐,主燃级预混模12沿周向均布在值班级下游火焰筒内壁和火焰筒外壁上,预混模收敛段与火焰筒外壁内侧和火焰筒内壁外侧平齐,保证预混模的使用寿命。As shown in Figure 1, a schematic diagram of an axially graded low-pollution combustion chamber of the present embodiment, the casing 5 outside the combustion chamber is welded to the outer wall 2 of the pre-diffuser, and is connected to the outer wall 14 of the flame tube through the tail flame tube support plate 7, Enclosing an outer ring cavity 6, the casing 8 in the combustion chamber is welded to the inner wall 1 of the pre-diffuser, and connected to the inner wall 13 of the flame tube through the rear flame tube support plate 7 to form an inner ring cavity 9, the inner wall 13 of the flame tube and the flame tube The outer wall 14 is connected by the head end wall 11 of the combustion chamber, and the duty-level premixed mold 10 is evenly distributed on the head end wall 11 along the circumferential direction. The mixed mold 12 is evenly distributed on the inner wall of the flame tube and the outer wall of the flame tube downstream of the duty class along the circumferential direction, and the convergence section of the premixed mold is flush with the inner side of the outer wall of the flame tube and the outer side of the inner wall of the flame tube to ensure the service life of the premixed mold.
如图2所示,为本实施例适用于不同工作范围的三种燃烧室火焰筒结构示意图,如图2a~c所示,主燃级预混模沿轴向布置1~5排,其工作范围依次增大,主燃级第一排预混模距值班级的轴向距离为火焰筒直径的0.75~1.5倍,并且与值班级预混模在同一周向位置,相邻两排预混模之间的轴向距离为预混模直径的1.25~2.5倍,保证相邻两排预混模之间不会相互干扰,相邻两排预混模采用叉排的方式布置,保证出口温度分布均匀性。As shown in Figure 2, it is a schematic diagram of the structure of three kinds of combustion chamber flame tubes suitable for different working ranges in this embodiment. The range increases successively. The axial distance between the first row of premixing molds in the main combustion stage and the duty class is 0.75 to 1.5 times the diameter of the flame tube, and it is at the same circumferential position as the duty class premixing molds. Two adjacent rows of premixing The axial distance between the molds is 1.25 to 2.5 times the diameter of the premixed molds to ensure that the two adjacent rows of premixed molds will not interfere with each other. The two adjacent rows of premixed molds are arranged in a fork row to ensure the outlet temperature. Uniformity of distribution.
本发明实施例值班级、主燃级预混模分布结构示意图如图3所示,值班级预混模均布在头部端壁11上,相邻值班级预混模中心距为预混模直径的1.25-2.5倍,且不大于125mm,既能保证相邻预混模之间不会干扰,又能保证正常联焰,主燃级第一排预混模与值班级预混模在同一周向位置。The schematic diagram of the distribution structure of the duty-level and main combustion-level premixed molds in the embodiment of the present invention is shown in Figure 3. The duty-level premixed molds are evenly distributed on the head end wall 11, and the center distance between the adjacent duty-level premixed molds is the premixed mold 1.25-2.5 times of the diameter, and not more than 125mm, which can not only ensure that there will be no interference between adjacent premixed models, but also ensure normal joint flames. circumferential position.
图4是实施例轴向分级全环燃烧室结构示意图,值班级预混模10沿周向均布在头部端壁11上,主燃级预混模12沿周向均布在值班级下游火焰筒内壁13和火焰筒外壁14上,保证全环燃烧室油气混合均匀、燃烧效率高、燃烧室出口温度分布均匀、污染排放水平低。Fig. 4 is a schematic diagram of the structure of the axially graded full-circle combustion chamber of the embodiment. The premixed mold 10 of the duty level is uniformly distributed on the head end wall 11 along the circumferential direction, and the premixed mold 12 of the main combustion level is uniformly distributed on the inner wall 13 of the downstream flame tube of the duty level along the circumferential direction. and on the outer wall 14 of the flame tube to ensure uniform oil and gas mixing in the full-ring combustion chamber, high combustion efficiency, uniform temperature distribution at the outlet of the combustion chamber, and low pollution emission levels.
图:5是预混模结构示意图,采用多点喷射预混预蒸发结构,包括燃油喷嘴15,喷嘴安装座16,旋流器17,集油环18,平直段19,收敛段20,燃油喷孔21,预混环腔22,所述的预混环腔22由平直段19和收敛段20组成,旋流器16采用轴向旋流器,叶片形状为直叶片,叶片个数6~18个,叶片角度30°~60°,收敛段与轴向夹角30°~45°,预混环腔22的长度为环腔平均流速与燃料自燃时间乘积的0.25~0.75倍,燃油分两路进入预混环腔,一路从燃油喷嘴15喷出,燃油喷嘴采用单油路离心喷嘴,喷嘴出口与旋流器出口平齐,一路经集油环18沿燃油喷孔21径向喷入预混环腔,燃油和空气在预混环腔22内形成均匀的油气混合物,燃油喷孔在旋流器下游3~5m处,沿轴向均布在平直段19上,喷孔个数10~30个,喷孔直径0.2~0.8mm。Figure: 5 is a schematic diagram of the premixed model structure, which adopts a multi-point injection premixed preevaporation structure, including fuel nozzle 15, nozzle mounting seat 16, swirler 17, oil collection ring 18, straight section 19, convergent section 20, fuel oil Spray hole 21, premixing ring cavity 22, said premixing ring cavity 22 is composed of straight section 19 and converging section 20, swirler 16 adopts axial swirler, blade shape is straight blade, number of blades is 6 ~18 blades, the blade angle is 30°~60°, the angle between the convergent section and the axial direction is 30°~45°, the length of the premixing annular cavity 22 is 0.25~0.75 times of the product of the average flow velocity of the annular cavity and the spontaneous combustion time of the fuel, and the fuel Two paths enter the premixing ring cavity, one path is sprayed from the fuel nozzle 15, the fuel nozzle adopts a single oil path centrifugal nozzle, the outlet of the nozzle is flush with the outlet of the swirler, and one path is sprayed radially through the oil collecting ring 18 along the fuel injection hole 21 In the pre-mixing ring chamber, fuel and air form a uniform oil-air mixture in the pre-mixing ring chamber 22. The fuel injection holes are located 3 to 5 m downstream of the swirler, and are evenly distributed on the straight section 19 along the axial direction. The number of injection holes 10 to 30, nozzle diameter 0.2 to 0.8mm.
本发明的工作过程如下:Working process of the present invention is as follows:
本发明的轴向分级低污染燃烧室,采用轴向分级燃烧技术将燃烧室分为值班级和主燃级,从扩压器出来的空气分为三路,分别进入外环腔、头部值班级、内环腔,内环腔和外环腔空气大部分通过主燃级进入火焰筒参与燃烧,小部分空气用来进行火焰筒冷却。The axially graded low-pollution combustion chamber of the present invention adopts axially graded combustion technology to divide the combustion chamber into a duty class and a main combustion stage, and the air coming out of the diffuser is divided into three paths, which enter the outer ring cavity and the head duty respectively. Stage, inner ring cavity, most of the air in the inner ring cavity and outer ring cavity enters the flame tube through the main combustion stage to participate in combustion, and a small part of the air is used to cool the flame tube.
小工况下,只有值班级工作,值班级采用多点喷射贫油预混预蒸发结构,燃油与值班级空气在值班级预混模中进行预混,形成均匀的油气混合物,在值班燃烧区燃烧,保证小工况下的污染排放水平,轴向分级避免了值班级和主燃级的相互干扰,拓宽了燃烧室的贫油熄火边界,保证了值班燃烧区火焰的稳定性。Under small working conditions, only the duty class works, and the duty class adopts a multi-point injection lean fuel premixed pre-evaporation structure. Combustion, to ensure the pollution emission level under small working conditions, the axial classification avoids the mutual interference between the duty class and the main combustion stage, widens the lean flameout boundary of the combustion chamber, and ensures the stability of the flame in the duty combustion area.
随着工况的增加,值班级和主燃级同时工作,主燃级预混模均布在全环燃烧室火焰筒内壁和火焰筒外壁上,预混模采用多点喷射贫油预混预蒸发结构,使得主燃区油气混合更加均匀,形成的均匀油气混合物被上游值班燃烧区的高温燃气点燃,在上游高温燃气的加热下以更高效率燃烧,同时大量空气沿内环腔和外环腔从主燃级进入燃烧室,导致火焰筒内燃气流速加快,缩短了燃气在高温区的停留时间,从而大大降低了大工况下的污染物排放水平。With the increase of working conditions, the on-duty stage and the main combustion stage work at the same time. The premixing models of the main combustion stage are evenly distributed on the inner wall of the flame tube and the outer wall of the flame tube in the full-ring combustion chamber. The evaporation structure makes the oil and gas mixture in the main combustion area more uniform, and the formed uniform oil and gas mixture is ignited by the high-temperature gas in the upstream on-duty combustion area, and burns with higher efficiency under the heating of the upstream high-temperature gas. The cavity enters the combustion chamber from the main combustion stage, which leads to the acceleration of the gas flow rate in the flame tube, shortens the residence time of the gas in the high temperature area, and thus greatly reduces the pollutant emission level under large working conditions.
本发明中预混模采用多点喷射预混预蒸发结构,通过合理设计预混段结构,避免了燃烧室自燃、回火问题的产生,保证了燃烧室的稳定工作。In the present invention, the pre-mixing mode adopts a multi-point injection pre-mixing and pre-evaporation structure, and by rationally designing the structure of the pre-mixing section, the problems of spontaneous combustion and tempering of the combustion chamber are avoided, and the stable operation of the combustion chamber is ensured.
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