CN109945189B - A low-concentration gas pulsating burner with improved main pipe - Google Patents
A low-concentration gas pulsating burner with improved main pipe Download PDFInfo
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 188
- 238000002485 combustion reaction Methods 0.000 claims abstract description 65
- 230000010349 pulsation Effects 0.000 claims abstract description 10
- 239000000779 smoke Substances 0.000 claims abstract description 6
- 239000007789 gas Substances 0.000 description 124
- 238000000034 method Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 3
- 238000004088 simulation Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000009841 combustion method Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004200 deflagration Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
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Abstract
Description
技术领域technical field
本发明属于瓦斯燃烧领域。The invention belongs to the field of gas combustion.
背景技术Background technique
脉动燃烧作为一种特殊的燃烧方式,既非爆燃也非正常燃烧而是介于其中间。给予其一定条件的激励,使其产生的声学脉动与燃烧过程中产生的热脉动达到一定的声热耦合,便可以产生周期性的脉动燃烧。燃烧过程中压力、温度以及热释放率等表征燃烧特性的状态参数随时间做周期性的变化,具有高燃烧效率、较大传热系数、较小污染排放量、可以自吸增压的优点,利用脉动燃烧技术可以有效处理低浓度瓦斯的燃烧;As a special combustion method, pulse combustion is neither deflagration nor normal combustion but in between. Give it the excitation of certain conditions, so that the acoustic pulsation generated by it and the thermal pulsation generated in the combustion process achieve a certain acoustic-thermal coupling, and then periodic pulsating combustion can be generated. During the combustion process, the state parameters that characterize the combustion characteristics, such as pressure, temperature and heat release rate, change periodically with time, which has the advantages of high combustion efficiency, large heat transfer coefficient, small pollution emission, and self-priming supercharging. The use of pulse combustion technology can effectively deal with the combustion of low-concentration gas;
由于瓦斯源的浓度并非稳定值,从主管压入燃烧室中的低浓度瓦斯可能存在甲烷浓度过低的问题,即使在燃烧室脉动供气的情形下,燃烧室中也存在无法顺利点燃,或是无法保持多个脉动周期燃烧的连续性。Since the concentration of the gas source is not a stable value, the low-concentration gas that is pressed into the combustion chamber from the main pipe may have the problem of too low methane concentration. It is impossible to maintain the continuity of multiple pulsation cycle combustion.
发明内容Contents of the invention
发明目的:为了克服现有技术中存在的不足,本发明提供一种能在瓦斯甲烷浓度低的状况下对燃烧室进行加浓的一种改进主管的低浓度瓦斯脉动燃烧器。Purpose of the invention: In order to overcome the deficiencies in the prior art, the present invention provides a low-concentration gas pulsation burner that can enrich the combustion chamber under the condition of low gas methane concentration.
技术方案:为实现上述目的,本发明的一种改进主管的低浓度瓦斯脉动燃烧器,包括瓦斯燃烧器,所述瓦斯燃烧器为柱状筒体结构,所述瓦斯燃烧器的内腔为柱状燃烧室,所述燃烧室的两端分别设置有低浓度瓦斯进气口和排烟出气口;所述瓦斯燃烧器的外侧一体化设置有环状的甲烷加浓箱体,所述环状甲烷加浓箱体内为环状的纯甲烷蓄压腔;所述纯甲烷蓄压腔与所述燃烧室之间还同轴心设置有环状的甲烷加浓空腔层;所述纯甲烷蓄压腔与所述甲烷加浓空腔层之间由第一环壁分隔,所述甲烷加浓空腔层与所述燃烧室之间有第二环壁分隔;所述第二环壁的两侧沿轴线呈圆周阵列均布有若干甲烷加浓孔,各所述甲烷加浓孔将所述甲烷加浓空腔层与所述燃烧室之间相互连通;Technical solution: In order to achieve the above object, an improved main pipe low-concentration gas pulsation burner of the present invention includes a gas burner, the gas burner is a columnar cylinder structure, and the inner cavity of the gas burner is a columnar combustion The two ends of the combustion chamber are respectively provided with a low-concentration gas inlet and a smoke exhaust outlet; the outer side of the gas burner is integrated with an annular methane enrichment box, and the annular methane enrichment box There is an annular pure methane pressure accumulator in the thick box; an annular methane enrichment cavity layer is arranged concentrically between the pure methane pressure accumulator and the combustion chamber; the pure methane accumulator The methane enrichment cavity layer is separated by a first ring wall, and the methane enrichment cavity layer is separated from the combustion chamber by a second ring wall; the two sides of the second ring wall are along the A number of methane enrichment holes are evenly distributed on the axis in a circular array, and each of the methane enrichment holes connects the methane enrichment cavity layer and the combustion chamber with each other;
所述第一环壁上呈圆周阵列分布有若干第一导气通道,各所述第一导气通道的内端均连通所述甲烷加浓空腔层,所述纯甲烷蓄压腔内还包括旋转配气环体,所述旋转配气环体转动套接在所述第一环壁外侧,所述旋转配气环体的内圈中部一体化同轴心设置有环形凸缘,所述环形凸缘的内壁封堵各所述第一导气通道的外端,所述环形凸缘上呈圆周阵列分布有若干第二导气通道,各所述第二导气通道的外端均连通所述纯甲烷蓄压腔,各所述第二导气通道的内端能随环形凸缘同步旋转至分别对齐连通若干第一导气通道的外端;还包括纯甲烷增压供给管,所述纯甲烷增压供给管的出气端连通所述纯甲烷蓄压腔。A number of first air guide channels are distributed in a circular array on the first ring wall, and the inner ends of each of the first air guide channels are connected to the methane enrichment cavity layer, and the pure methane pressure storage chamber is also It includes a rotating gas distribution ring body, the rotating gas distribution ring body is rotatably socketed on the outside of the first ring wall, and the middle part of the inner ring of the rotating gas distribution ring body is integrated and coaxially provided with an annular flange. The inner wall of the annular flange blocks the outer ends of each of the first air guide channels, and a plurality of second air guide channels are distributed in a circular array on the annular flange, and the outer ends of each of the second air guide channels are connected to each other. In the pure methane pressure storage chamber, the inner ends of each of the second gas guide channels can be rotated synchronously with the annular flange to align with the outer ends of several first gas guide channels; The gas outlet end of the pure methane pressurized supply pipe communicates with the pure methane pressure storage chamber.
进一步的,各所述第一导气通道内均设置有防止气体反流的单向阀,所述单向阀能防止甲烷加浓空腔层内的气体通过第一导气通道反流至纯甲烷蓄压腔内;所述旋转配气环体内圈的环形凸缘两侧还对称转动安装有两轴承;所述旋转配气环体的外圈设置有一圈齿体,所述纯甲烷蓄压腔还固定安装有电机,所述电机的输出轴上同步连接有输出齿轮,所述输出齿轮与所述旋转配气环体上的一圈齿体啮合连接,所述电机通过输出齿轮带动所述旋转配气环体沿轴线旋转。Further, each of the first gas guide channels is provided with a one-way valve to prevent gas backflow, and the one-way valve can prevent the gas in the methane-enriched cavity layer from flowing back through the first gas guide channel to pure In the methane pressure storage chamber; two bearings are installed symmetrically on both sides of the annular flange of the inner ring of the rotary gas distribution ring; The cavity is also fixedly installed with a motor, the output shaft of the motor is synchronously connected with an output gear, and the output gear is meshed with a ring of teeth on the rotating gas distribution ring body, and the motor drives the The rotating gas distribution ring body rotates along the axis.
进一步的,还包括长柱状的瓦斯分流箱,所述瓦斯分流箱的一侧分别垂直连通有五个所述瓦斯燃烧器的低浓度瓦斯进气口,所述瓦斯分流箱远离五个瓦斯燃烧器的一侧垂直连通有低浓度脉动瓦斯供给管;五个所述瓦斯燃烧器沿所述瓦斯分流箱的长度方向阵列分布,且所述低浓度脉动瓦斯供给管的出口不对正任意一个所述瓦斯燃烧器的进气口。Further, it also includes a long columnar gas distribution box, one side of the gas distribution box is vertically connected with the low-concentration gas inlets of the five gas burners, and the gas distribution box is far away from the five gas burners There is a low-concentration pulsating gas supply pipe vertically connected to one side of the gas distribution box; five of the gas burners are distributed in an array along the length of the gas distribution box, and the outlet of the low-concentration pulsating gas supply pipe is not aligned with any one of the gas The air inlet of the burner.
有益效果:本发明的结构简单,本方案增加了加浓的结构,在瓦斯浓度相对较低的状态下,呈周期性的给燃烧室供给纯甲烷,进而对燃烧室进行加浓,解决了浓度过低无法连续燃烧的问题。Beneficial effects: the structure of the present invention is simple, and this scheme adds a enriched structure, and in the state of relatively low gas concentration, it periodically supplies pure methane to the combustion chamber, and then enriches the combustion chamber, solving the problem of gas concentration Too low to burn continuously.
附图说明Description of drawings
附图1为改造后的燃烧器组合结构;Accompanying drawing 1 is the combined structure of the burner after transformation;
附图2为改造后的燃烧器组合结构的CFD分析速度云图;Accompanying drawing 2 is the CFD analysis speed nephogram of the combined structure of the combustor after transformation;
附图3为瓦斯燃烧器的CFD分析局部矢量速度云图;Accompanying drawing 3 is the CFD analysis local vector velocity nephogram of gas burner;
附图4为在燃烧器上加装甲烷加浓箱体后的结构示意图;Accompanying drawing 4 is the structural representation after adding the methane enrichment box on the burner;
附图5为附图4的第一立体剖视图;Accompanying drawing 5 is the first three-dimensional sectional view of accompanying drawing 4;
附图6为附图4的第二立体剖视图;Accompanying drawing 6 is the second perspective sectional view of accompanying drawing 4;
附图7为附图4的第三立体剖视图;Accompanying drawing 7 is the 3rd perspective sectional view of accompanying drawing 4;
附图8为旋转配气环体结构示意图。Accompanying drawing 8 is the schematic diagram of the structure of the rotating gas distribution ring body.
具体实施方式Detailed ways
下面结合附图对本发明作更进一步的说明。The present invention will be further described below in conjunction with the accompanying drawings.
如附图1至8所示的一种改进主管的低浓度瓦斯脉动燃烧器,包括瓦斯燃烧器10,所述瓦斯燃烧器10为柱状筒体结构,所述瓦斯燃烧器10的内腔为柱状燃烧室12,所述燃烧室12的两端分别设置有低浓度瓦斯进气口和排烟出气口;所述瓦斯燃烧器10的外侧一体化设置有环状的甲烷加浓箱体18,所述环状甲烷加浓箱体18内为环状的纯甲烷蓄压腔2;所述纯甲烷蓄压腔2与所述燃烧室12之间还同轴心设置有环状的甲烷加浓空腔层7;所述纯甲烷蓄压腔2与所述甲烷加浓空腔层7之间由第一环壁1分隔,所述甲烷加浓空腔层7与所述燃烧室12之间有第二环壁9分隔;所述第二环壁9的两侧沿轴线呈圆周阵列均布有若干甲烷加浓孔11,各所述甲烷加浓孔11将所述甲烷加浓空腔层7与所述燃烧室12之间相互连通;As shown in accompanying drawings 1 to 8, an improved main pipe low-concentration gas pulsation burner includes a gas burner 10, the gas burner 10 is a columnar cylinder structure, and the inner cavity of the gas burner 10 is columnar Combustion chamber 12, the two ends of the combustion chamber 12 are respectively provided with a low-concentration gas inlet and smoke exhaust outlet; the outer side of the gas burner 10 is integrally provided with an annular methane enrichment box 18, the The annular methane enrichment box 18 is an annular pure methane accumulator chamber 2; an annular methane enrichment chamber is coaxially arranged between the pure methane accumulator chamber 2 and the combustion chamber 12. Chamber layer 7; the pure methane pressure storage chamber 2 and the methane enrichment cavity layer 7 are separated by the first ring wall 1, and the methane enrichment cavity layer 7 and the combustion chamber 12 are separated by The second ring wall 9 is separated; both sides of the second ring wall 9 are evenly distributed with a number of methane enrichment holes 11 in a circular array along the axis, and each of the methane enrichment holes 11 enriches the methane cavity layer 7 communicate with the combustion chamber 12;
所述第一环壁1上呈圆周阵列分布有若干第一导气通道14,各所述第一导气通道14的内端均连通所述甲烷加浓空腔层7,所述纯甲烷蓄压腔2内还包括旋转配气环体6,所述旋转配气环体6转动套接在所述第一环壁1外侧,所述旋转配气环体6的内圈中部一体化同轴心设置有环形凸缘21,所述环形凸缘21的内壁封堵各所述第一导气通道14的外端,所述环形凸缘21上呈圆周阵列分布有若干第二导气通道17,各所述第二导气通道17的外端均连通所述纯甲烷蓄压腔2,各所述第二导气通道17的内端能随环形凸缘21同步旋转至分别对齐连通若干第一导气通道14的外端;还包括纯甲烷增压供给管8,所述纯甲烷增压供给管8的出气端连通所述纯甲烷蓄压腔2。A plurality of first air guide channels 14 are distributed in a circular array on the first ring wall 1, and the inner ends of each of the first air guide channels 14 are connected to the methane enrichment cavity layer 7, and the pure methane storage The pressure chamber 2 also includes a rotary gas distribution ring body 6, which is rotatably socketed on the outside of the first ring wall 1, and the middle part of the inner ring of the rotary gas distribution ring body 6 is integrated and coaxial The center is provided with an annular flange 21, the inner wall of the annular flange 21 blocks the outer ends of each of the first air guide passages 14, and a plurality of second air guide passages 17 are distributed in a circular array on the annular flange 21. The outer ends of each of the second air guide passages 17 are connected to the pure methane pressure storage chamber 2, and the inner ends of each of the second air guide passages 17 can be rotated synchronously with the annular flange 21 to be respectively aligned and communicated with several first air guide passages. The outer end of a gas guide channel 14 also includes a pure methane pressurized supply pipe 8 , and the gas outlet end of the pure methane pressurized supply pipe 8 communicates with the pure methane pressure storage chamber 2 .
各所述第一导气通道14内均设置有防止气体反流的单向阀13,所述单向阀13能防止甲烷加浓空腔层7内的气体通过第一导气通道14反流至纯甲烷蓄压腔2内;所述旋转配气环体6内圈的环形凸缘21两侧还对称转动安装有两轴承16;所述旋转配气环体6的外圈设置有一圈齿体25,所述纯甲烷蓄压腔2还固定安装有电机5,所述电机5的输出轴4上同步连接有输出齿轮3,所述输出齿轮3与所述旋转配气环体6上的一圈齿体25啮合连接,所述电机5通过输出齿轮3带动所述旋转配气环体6沿轴线旋转。Each of the first gas guide channels 14 is provided with a one-way valve 13 to prevent gas backflow, and the one-way valve 13 can prevent the gas in the methane-enriched cavity layer 7 from flowing back through the first gas guide channel 14 into the pure methane pressure storage chamber 2; two bearings 16 are mounted on both sides of the annular flange 21 of the inner ring of the rotating gas distribution ring body 6 for symmetrical rotation; the outer ring of the rotating gas distribution ring body 6 is provided with a ring of teeth body 25, the pure methane pressure storage chamber 2 is also fixedly installed with a motor 5, the output shaft 4 of the motor 5 is synchronously connected with an output gear 3, and the output gear 3 is connected to the rotary gas distribution ring body 6 A ring of tooth bodies 25 is engaged and connected, and the motor 5 drives the rotating gas distribution ring body 6 to rotate along the axis through the output gear 3 .
还包括长柱状的瓦斯分流箱91,所述瓦斯分流箱91的一侧分别垂直连通有五个所述瓦斯燃烧器10的低浓度瓦斯进气口,所述瓦斯分流箱91远离五个瓦斯燃烧器10的一侧垂直连通有低浓度脉动瓦斯供给管90;五个所述瓦斯燃烧器10沿所述瓦斯分流箱91的长度方向阵列分布,且所述低浓度脉动瓦斯供给管90的出口不对正任意一个所述瓦斯燃烧器10的进气口。It also includes a long columnar gas distribution box 91. One side of the gas distribution box 91 is respectively vertically connected with five low-concentration gas inlets of the gas burner 10. The gas distribution box 91 is far away from the five gas combustion chambers. One side of the device 10 is vertically connected with a low-concentration pulsating gas supply pipe 90; the five gas burners 10 are distributed in an array along the length direction of the gas splitter box 91, and the outlet of the low-concentration pulsating gas supply pipe 90 is incorrect It is the air inlet of any one of the gas burners 10 .
本方的加浓过程的脉动燃烧方法,过程以及技术进步整理:The pulsating combustion method, process and technical progress of our enrichment process:
瓦斯源为包含CH4、O2、N2、CO2的混合气体,其中O2的浓度足够CH4的燃烧反应:The gas source is a mixed gas containing CH4, O2, N2, and CO2, where the concentration of O2 is sufficient for the combustion reaction of CH4:
瓦斯源中CH4浓度超过4%时,不用对燃烧室22进行CH4加浓;此时纯甲烷增压供给管8不向纯甲烷蓄压腔2内供给纯甲烷即可;此时单向阀13能防止甲烷加浓空腔层7内的气体通过若干第一导气通道14反流至纯甲烷蓄压腔2内;然后在瓦斯泵的作用下将瓦斯通过低浓度脉动瓦斯供给管90呈脉动周期的形式连续向瓦斯分流箱91内供给瓦斯;进而使瓦斯分流箱91的内部形成连续的脉动气压,进而瓦斯分流箱91内的瓦斯呈脉动周期的向各个瓦斯燃烧器10的燃烧室12内喷射瓦斯气体;燃烧室12内的瓦斯经点火装置点燃后,燃烧室12内形成连续的脉动火焰,进而燃烧室12内因燃烧产生的高温尾气持续通过燃烧室12的排烟端以尾焰的形式喷出,进而各个排气直管20所喷出的尾焰对用热设备进行加热;进而实现了对瓦斯的利用;When the concentration of CH4 in the gas source exceeds 4%, there is no need to enrich CH4 in the combustion chamber 22; at this time, the pure methane pressurized supply pipe 8 does not supply pure methane to the pure methane pressure storage chamber 2; at this time, the check valve 13 It can prevent the gas in the methane-enriched cavity layer 7 from flowing back into the pure methane pressure storage chamber 2 through several first gas guide channels 14; then, under the action of the gas pump, the gas is pulsated through the low-concentration pulsating gas supply pipe 90 Gas is continuously supplied to the gas distribution box 91 in the form of a period; then the inside of the gas distribution box 91 forms a continuous pulsating air pressure, and then the gas in the gas distribution box 91 is pulsating periodically to the combustion chamber 12 of each gas burner 10 Gas injection; after the gas in the combustion chamber 12 is ignited by the ignition device, a continuous pulsating flame is formed in the combustion chamber 12, and the high-temperature exhaust gas generated by combustion in the combustion chamber 12 continues to pass through the exhaust end of the combustion chamber 12 in the form of a tail flame. and then the tail flames ejected from each exhaust straight pipe 20 heat the heat-using equipment; thereby realizing the utilization of gas;
当瓦斯源中CH4浓度小于4%时,然后在瓦斯泵的作用下将瓦斯通过低浓度脉动瓦斯供给管90呈脉动周期的形式连续向瓦斯分流箱91内供给瓦斯;进而使瓦斯分流箱91的内部形成连续的脉动气压,进而瓦斯分流箱91内的瓦斯呈脉动周期的向各个瓦斯燃烧器10的燃烧室12内喷射瓦斯气体;由于通过若干瓦斯导气孔77喷出的瓦斯气体中CH4浓度小于4%,燃烧室12中无法顺利点燃或是无法保持多个脉动周期燃烧的连续性,需要对燃烧室12进行CH4加浓;此时纯甲烷增压供给管8将纯甲烷压入纯甲烷蓄压腔2内,并且纯甲烷增压供给管8持续维持纯甲烷蓄压腔2内的气压,且保证纯甲烷蓄压腔2内的气压始终大于燃烧室12内的气压,此时启动电机5,进而电机5通过输出齿轮3带动所述旋转配气环体6沿轴线旋转,进而环形凸缘21随旋转配气环体6同步旋转,环形凸缘21的呈周期性旋转使各第二导气通道17的内端呈周期性的旋转至对齐连通若干第一导气通道14的外端,进而使纯甲烷蓄压腔2与甲烷加浓空腔层7之间呈周期性的相互连通,进而使纯甲烷蓄压腔2内的甲烷通过若干第一导气通道14呈周期性的向甲烷加浓空腔层7内压入射纯CH4,进而使甲烷加浓空腔层7内形成纯CH4脉动气压,进而甲烷加浓空腔层7内的CH4脉动气体通过若干甲烷加浓孔11呈脉动周期性的向燃烧室12内压入纯CH4,通过控制电机5的输出齿轮3转速,进而控制旋转配气环体6,使纯甲烷蓄压腔2与甲烷加浓空腔层7之间呈周期性的相互连通周期和步调与瓦斯分流箱91向燃烧室12内喷射瓦斯气体的周期和步调一致;进而实现对燃烧室12内每个脉动燃烧周期都进行了燃气加浓,保证燃烧室12能连续的脉动燃烧;进而燃烧室12内因燃烧产生的高温尾气持续通过通过燃烧室12的排烟端以尾焰的形式喷出,,进而各个排气直管20所喷出的尾焰对用热设备进行加热;进而实现了对瓦斯的利用;与此同时甲烷加浓空腔层7内的纯甲烷气体能通过第二环壁9吸收燃烧室12内燃烧后产生的热量,进而使若干甲烷加浓孔11向燃烧室12内喷射的是已经预热的纯CH4,进而有效提高燃烧室12内的燃烧效率。When the concentration of CH4 in the gas source is less than 4%, then under the action of the gas pump, the gas will be continuously supplied to the gas distribution box 91 in the form of pulsating cycle through the low-concentration pulsating gas supply pipe 90; Continuous pulsating air pressure is formed inside, and then the gas in the gas distribution box 91 is pulsating and cyclically spraying gas gas into the combustion chamber 12 of each gas burner 10; due to the CH4 concentration in the gas ejected through several gas gas guide holes 77 is less than 4%, the combustor 12 cannot be ignited smoothly or cannot maintain the continuity of multiple pulsation cycle combustion, it is necessary to enrich the CH4 in the combustor 12; at this time, the pure methane pressurized supply pipe 8 presses the pure methane into the pure methane storage In the pressure chamber 2, and the pure methane pressurized supply pipe 8 continuously maintains the air pressure in the pure methane pressure storage chamber 2, and ensures that the air pressure in the pure methane pressure storage chamber 2 is always greater than the air pressure in the combustion chamber 12. At this time, start the motor 5 , and then the motor 5 drives the rotating gas distribution ring body 6 to rotate along the axis through the output gear 3, and then the annular flange 21 rotates synchronously with the rotating gas distribution ring body 6, and the periodic rotation of the annular flange 21 makes each second guide The inner end of the gas channel 17 is periodically rotated to align with the outer ends of the first gas guide channels 14, so that the pure methane pressure storage chamber 2 and the methane enrichment cavity layer 7 are periodically connected to each other, Further, the methane in the pure methane pressure storage chamber 2 is periodically injected into the methane-enriched cavity layer 7 with pure CH4 through several first gas-guiding channels 14, so that pure CH4 is formed in the methane-enriched cavity layer 7 The pulsating air pressure, and then the CH4 pulsating gas in the methane enrichment cavity layer 7 passes through several methane enrichment holes 11 to pulsate and periodically press pure CH4 into the combustion chamber 12. By controlling the output gear 3 speed of the motor 5, and then control Rotate the gas distribution ring body 6 to make the period and pace of the pure methane pressure storage chamber 2 and the methane enrichment cavity layer 7 periodically communicate with each other and the cycle and pace of the gas distribution box 91 injecting gas into the combustion chamber 12 Consistent; further realize the enrichment of gas for each pulsating combustion cycle in the combustion chamber 12, to ensure continuous pulsating combustion in the combustion chamber 12; furthermore, the high-temperature exhaust gas generated by combustion in the combustion chamber 12 continues to pass through the exhaust smoke of the combustion chamber 12 end is ejected in the form of tail flame, and then the tail flame ejected from each exhaust straight pipe 20 heats the heat-using equipment; thereby realizing the utilization of gas; at the same time, methane enriches the gas in the cavity layer 7 The pure methane gas can absorb the heat generated after combustion in the combustion chamber 12 through the second ring wall 9, and then what the several methane enrichment holes 11 inject into the combustion chamber 12 is preheated pure CH4, thereby effectively improving the combustion chamber 12. internal combustion efficiency.
采用CFD数值模拟方法对燃烧器的结构合理性和技术进步进行验证:CFD numerical simulation method is used to verify the structural rationality and technical progress of the burner:
使用用ANSYS Fluent16.0完成该网格下的数值模拟,首先检验网格,确保其网格面积和体积没有负值的存在,不考虑重力影响。Use ANSYS Fluent16.0 to complete the numerical simulation under the grid. First, check the grid to ensure that there are no negative values in the grid area and volume, and the influence of gravity is not considered.
在模型中,设置流动过程为基于压力的稳态流动,同时由于我们主要关心低浓度瓦斯的流动状况,因此假定流体为CH4和空气的混合气,采用多组分模型数值计算其在燃烧器管道中的流场分布情况。In the model, the flow process is set as a pressure-based steady-state flow, and since we are mainly concerned about the flow of low-concentration gas, it is assumed that the fluid is a mixture of CH4 and air, and the multi-component model is used to numerically calculate its flow in the burner pipe. The distribution of the flow field in .
模型设置:能量方程、标准湍流方程、组分输运方程;Model settings: energy equation, standard turbulence equation, component transport equation;
材料设置:流体为methane-air、固体壁面为默认aluminum;Material settings: the fluid is methane-air, the solid wall is the default aluminum;
边界条件设置:入口边界条件:速度入口,设定低浓度脉动瓦斯供给管90的供给速度为1.5m/s;出口边界条件:燃烧室12的排烟出口为大气压力出口;湍流指标:湍流强度+水力直径;Boundary condition setting: inlet boundary condition: velocity inlet, set the supply velocity of the low-concentration pulsating gas supply pipe 90 to 1.5m/s; outlet boundary condition: the smoke exhaust outlet of the combustion chamber 12 is the atmospheric pressure outlet; turbulence index: turbulence intensity +hydraulic diameter;
温度:300K;Temperature: 300K;
组分:4%CH4、19.74%O2、2.82%CO2、73.44%N2;Components: 4% CH4, 19.74% O2, 2.82% CO2, 73.44% N2;
求解方法:SIMPLE单精度,梯度基于网格采用最小二乘法,压力采用二阶迎风,动量采用一阶迎风,湍流动能采用一阶迎风,湍流耗散率采用一阶迎风;Solution method: SIMPLE single precision, the gradient is based on the grid using the least squares method, the pressure uses the second-order upwind, the momentum uses the first-order upwind, the turbulent kinetic energy uses the first-order upwind, and the turbulent dissipation rate uses the first-order upwind;
残差监视:所有参数收敛精度设置为0.001;Residual monitoring: the convergence accuracy of all parameters is set to 0.001;
迭代步长:1000;Iteration step size: 1000;
初始化,运算过程中,在第324步时,各项指标均收敛至设定精度;Initialization, during the calculation process, at step 324, all indicators converge to the set accuracy;
模拟结束后得到的燃烧器整体速度云图如附图2,由速度云图可以看出低浓度脉动瓦斯供给管90的出口不对正任意一个所述瓦斯燃烧器10的进气口的结构进气能获得较好的速度场,在附图3为瓦斯燃烧器的CFD分析局部矢量速度云图中可以看出,燃烧室12中产生回流区,随着燃烧的进行高温烟气不断产生,同时伴随着回流现象被卷吸到火焰根部,与新进燃气进行热量传递,在初点火时期,回流区的作用将更加明显,高温烟气从开始回流到燃烧器根部,其流速将越来越大,在这期间被回流的烟气与主流中的介质相混合,进行高效的动量传输,促使在回流区的新旧燃气相互交换混合,从而进一步使得燃烧室内部的温度分布更加均匀;部分随着高温烟气回流到燃烧室根部的未燃尽的燃气,会和新进燃气一起在根部被重新燃烧,对于气体的完全燃烧有重要作用。The overall velocity cloud diagram of the burner obtained after the simulation is shown in Figure 2. From the velocity cloud diagram, it can be seen that the outlet of the low-concentration pulsating gas supply pipe 90 is not aligned with any one of the gas burner 10. A better velocity field, as can be seen from the local vector velocity cloud diagram of the CFD analysis of the gas burner in Fig. It is entrained to the root of the flame and transfers heat with the new gas. During the initial ignition period, the effect of the recirculation zone will be more obvious. The high-temperature flue gas will flow back to the root of the burner from the beginning, and its flow rate will increase. The recirculated flue gas is mixed with the medium in the main flow to carry out efficient momentum transmission, which promotes the exchange and mixing of old and new gas in the recirculation area, thereby further making the temperature distribution inside the combustion chamber more uniform; The unburned gas at the root of the combustion chamber will be reburned at the root together with the new gas, which plays an important role in the complete combustion of the gas.
以上所述仅是本发明的优选实施方式,应当指出:对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the present invention, some improvements and modifications can also be made, and these improvements and modifications are also possible. It should be regarded as the protection scope of the present invention.
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