CN110425536A - A kind of angle-style porous media combustor - Google Patents
A kind of angle-style porous media combustor Download PDFInfo
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- CN110425536A CN110425536A CN201910720848.4A CN201910720848A CN110425536A CN 110425536 A CN110425536 A CN 110425536A CN 201910720848 A CN201910720848 A CN 201910720848A CN 110425536 A CN110425536 A CN 110425536A
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- 238000002485 combustion reaction Methods 0.000 claims abstract description 68
- 239000007789 gas Substances 0.000 claims abstract description 51
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000003546 flue gas Substances 0.000 claims abstract description 21
- 239000000463 material Substances 0.000 claims abstract description 7
- 239000000919 ceramic Substances 0.000 claims description 28
- 239000006260 foam Substances 0.000 claims description 27
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 24
- 239000011148 porous material Substances 0.000 claims description 19
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 15
- 239000011449 brick Substances 0.000 claims description 13
- 239000011810 insulating material Substances 0.000 claims 1
- 230000005855 radiation Effects 0.000 abstract description 10
- 230000006378 damage Effects 0.000 abstract description 3
- 230000035939 shock Effects 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000005496 tempering Methods 0.000 description 4
- 238000009826 distribution Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012774 insulation material Substances 0.000 description 2
- 238000004088 simulation Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
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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
- F23D14/12—Radiant burners
- F23D14/14—Radiant burners using screens or perforated plates
-
- 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
- F23D14/66—Preheating the combustion air or gas
-
- 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
- F23D14/74—Preventing flame lift-off
-
- 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
- F23D14/82—Preventing flashback or blowback
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gas Burners (AREA)
Abstract
一种角型多孔介质燃烧器,包括燃气进口、燃烧前室、燃烧器外壳、保护区、预热区、缓冲区、燃烧区和烟气出口,预热区、缓冲区、燃烧区统称为多孔介质区域,均采用多孔介质材料填充;将预热区和燃烧区分别向内渐缩和向外渐扩一定的角度α,同时在预热区和燃烧区设置一个缓冲区,减小气流速度,防止火焰发生倾斜现象。能够明显拓宽火焰稳定速度极限范围,不仅有效地防止了火焰回火和脱火,也提高了出口辐射效率,同时也减小了多孔介质热震性损坏的发生。An angular porous media burner, including a gas inlet, a combustion front chamber, a burner casing, a protection zone, a preheating zone, a buffer zone, a combustion zone, and a flue gas outlet. The preheating zone, buffer zone, and combustion zone are collectively referred to as porous The medium area is filled with porous media materials; the preheating zone and the combustion zone are respectively tapered inward and outward by a certain angle α, and a buffer zone is set in the preheating zone and the combustion zone to reduce the airflow velocity. Prevent the flame from tilting. It can obviously widen the limit range of flame stability speed, not only effectively prevent flame backfire and defire, but also improve outlet radiation efficiency, and reduce the occurrence of thermal shock damage of porous media at the same time.
Description
技术领域technical field
本发明属于燃烧器技术领域,尤其涉及一种角型多孔介质燃烧器。The invention belongs to the technical field of burners, in particular to an angular porous media burner.
背景技术Background technique
近年来,随着中国经济的迅猛发展,能源和环境问题越来越成为人们关注的重点。我国目前面临着化石燃料的不断减少,环境污染的不断加剧的困境,因此要建立可持续发展的经济模式,改善能源结构,改进能源消费方式,提高能源有效利用率,必须充分利用工业生产及能源生产中的各种低热值燃气,实现常规能源的高效清洁利用。低热值气体的可燃成分稀薄,使用常规燃烧技术难以有效利用,如何实现该种气体的有效燃烧、减缓直接排放造成的环境问题,一直是燃烧界的难题。In recent years, with the rapid development of China's economy, energy and environmental issues have increasingly become the focus of attention. Our country is currently facing the dilemma of the continuous reduction of fossil fuels and the increasing environmental pollution. Therefore, in order to establish a sustainable economic model, improve the energy structure, improve the energy consumption mode, and improve the effective utilization of energy, we must make full use of industrial production and energy. Various low calorific value gases in production realize efficient and clean utilization of conventional energy. The combustible components of low-calorific-value gas are thin, and it is difficult to effectively use conventional combustion technology. How to realize the effective combustion of this kind of gas and reduce the environmental problems caused by direct emissions has always been a difficult problem in the combustion industry.
近年来,为了解决上述问题,不得不持续寻找更为高效、低排放的燃烧技术。在诸多强化燃烧和控制排放的新技术中,多孔介质燃烧器作为一种新型的节能环保燃烧器,以其独特的优势越来越受到人们的关注。多孔介质本身具有热能积累和反馈效应。由于多孔介质较大的比表面积,气体和固体之间可进行充分的热交换;同时,由于固体本身的比热容远大于气体的比热容,可燃气体燃烧时释放的热量经对流换热存储在固体内,其中的一部分再以热福射的形式反馈到上游,用来预热未燃的可燃气体。多孔介质中的预混燃烧有如下优点:提高燃料的燃烧效率,降低污染物排放,而且能够显著拓宽燃烧贫燃极限,同时无需传统的换热设备来进行燃烧余热的回收和传递,在减小设备体积、实现燃烧设备小型化方面具有强大的优势,为气体、液体、固体等燃料,特别低热值气体燃料高效清洁燃烧提供一条新途径。In recent years, in order to solve the above problems, it is necessary to continuously search for more efficient and low-emission combustion technologies. Among many new technologies for enhancing combustion and controlling emissions, the porous media burner, as a new type of energy-saving and environment-friendly burner, has attracted more and more attention due to its unique advantages. Porous media itself has thermal energy accumulation and feedback effects. Due to the large specific surface area of the porous medium, sufficient heat exchange can be carried out between the gas and the solid; at the same time, because the specific heat capacity of the solid itself is much greater than that of the gas, the heat released by the combustible gas is stored in the solid through convective heat exchange. A part of it is fed back upstream in the form of thermal radiation to preheat the unburned combustible gas. Premixed combustion in porous media has the following advantages: it improves fuel combustion efficiency, reduces pollutant emissions, and can significantly expand the lean burn limit of combustion. It has strong advantages in terms of equipment volume and miniaturization of combustion equipment, and provides a new way for efficient and clean combustion of gas, liquid, solid and other fuels, especially low calorific value gas fuels.
传统的多孔介质燃烧器基本上都是轴向等宽的圆柱体或者是长方体燃烧器。在实践探究中出现了燃烧器的回火和脱火现象,甚至造成了爆炸等安全问题。除此之外,还造成火焰面附近温度梯度陡,温度分布不均,局部温度过高,燃烧不完全,同时内部压力过大破坏了燃烧器结构,缩短了燃烧器的使用寿命等一系列问题。Traditional porous media burners are basically cylindrical or cuboid burners with the same axial width. In the practical exploration, the phenomenon of tempering and defiring of the burner appeared, and even caused safety problems such as explosion. In addition, the temperature gradient near the flame surface is steep, the temperature distribution is uneven, the local temperature is too high, the combustion is incomplete, and the internal pressure is too high, which destroys the structure of the burner and shortens the service life of the burner. .
因此,亟需一种能够有效解决燃烧器回火和脱火的不稳定现象,保证功率调节范围大,燃烧更加充分,燃烧效率更高的多孔介质燃烧器。Therefore, there is an urgent need for a porous media burner that can effectively solve the unstable phenomenon of burner backfire and defire, ensure a large power adjustment range, more complete combustion, and higher combustion efficiency.
发明内容Contents of the invention
针对现有技术存在的不足,本发明提供一种角型多孔介质燃烧器,能够有效解决燃烧器回火和脱火的不稳定问题,具有功率调节范围大,燃烧更加充分,燃烧效率更高的优点。Aiming at the deficiencies in the prior art, the present invention provides an angular porous media burner, which can effectively solve the unstable problems of burner tempering and defiring, and has the advantages of large power adjustment range, more complete combustion and higher combustion efficiency. advantage.
一种角型多孔介质燃烧器,其特征在于:包括燃气进口(1)、燃烧前室(2)、燃烧器外壳(3)、保护区(4)、预热区(5)、缓冲区(6)、燃烧区(7)和烟气出口(8),缓冲区(6)设置在预热区(5)和燃烧区(7)之间,预热区(5)、缓冲区(6)、燃烧区(7)统称为多孔介质区域,均采用多孔介质材料填充,预热区5和燃烧器区7分别向外渐缩和渐扩一定的角度α,角度范围为0°<α<40°。An angular porous media burner, characterized in that it includes a gas inlet (1), a combustion front chamber (2), a burner casing (3), a protection zone (4), a preheating zone (5), a buffer zone ( 6), the combustion zone (7) and the flue gas outlet (8), the buffer zone (6) is set between the preheating zone (5) and the combustion zone (7), the preheating zone (5), the buffer zone (6) , The combustion zone (7) is collectively referred to as the porous medium zone, all of which are filled with porous medium materials. The preheating zone 5 and the burner zone 7 taper and expand outwards at a certain angle α respectively, and the angle range is 0°<α<40 °.
所述燃烧器主体形状为两个漏斗关于中心对称。The shape of the burner body is two funnels symmetrical about the center.
所述预热区(5)、缓冲区(6)和燃烧区(7)分别装填小孔多孔介质、中孔多孔介质和大孔多孔介质。The preheating zone (5), the buffer zone (6) and the combustion zone (7) are respectively filled with small-pore porous media, medium-pore porous media and large-pore porous media.
所述多孔介质材料选用氧化铝泡沫陶瓷或者氧化锆泡沫陶瓷,其中小孔多孔介质采用孔密度为50PPI~60PPI,孔隙率为80%以上的氧化铝泡沫陶瓷或者氧化锆泡沫陶瓷;中孔多孔介质采用孔密度为30PPI~40PPI,孔隙率为80%以上的氧化铝泡沫陶瓷或者氧化锆泡沫陶瓷;大孔多孔介质采用孔密度为10PPI~20PPI,孔隙率为80%以上的氧化铝泡沫陶瓷或者氧化锆泡沫陶瓷。The porous medium material is selected from alumina foam ceramics or zirconia foam ceramics, wherein the small-pore porous medium adopts alumina foam ceramics or zirconia foam ceramics with a pore density of 50PPI-60PPI and a porosity of more than 80%; Alumina foam ceramics or zirconia foam ceramics with a pore density of 30PPI-40PPI and a porosity of more than 80% are used; for macroporous porous media, alumina foam ceramics or zirconia ceramics with a pore density of 10PPI-20PPI and a porosity of more than 80% are used. Zirconium foam ceramics.
所述保护区(4)为挡板砖,挡板砖的板厚为10~40mm,孔隙率为80%~90%,挡板砖上开设有多个通孔,通孔的平均孔径为2~4mm。The protected area (4) is a baffle brick, the thickness of the baffle brick is 10-40mm, the porosity is 80%-90%, and a plurality of through holes are provided on the baffle brick, and the average aperture of the through hole is 2mm. ~4mm.
所述挡板砖的通孔沿燃烧器外壳的轴向平行设置。The through holes of the baffle bricks are arranged parallel to the axial direction of the burner shell.
所述燃烧器外壳3采用保温材料。The burner shell 3 is made of thermal insulation material.
当燃气从下方进入燃烧器时,所述燃气进口(1)、燃烧前室(2)设置在燃烧器外壳(3)的底部,所述烟气出口(8)设置在燃烧器外壳(3)的上部;当燃气从上方进入燃烧器时,所述燃气进口(1)、燃烧前室(2)设置在燃烧器外壳(3)的上部,所述烟气出口(8)设置在燃烧器外壳(3)的底部;当燃气从左方进入燃烧器时,所述燃气进口(1)、燃烧前室(2)设置在燃烧器外壳(3)的左侧,所述烟气出口(8)设置在燃烧器外壳(3)的右侧;当燃气从右方进入燃烧器时,所述燃气进口(1)、燃烧前室(2)设置在燃烧器外壳(3)的右侧,所述烟气出口(8)设置在燃烧器外壳(3)的左侧。When the gas enters the burner from below, the gas inlet (1) and the combustion front chamber (2) are arranged at the bottom of the burner casing (3), and the flue gas outlet (8) is arranged at the burner casing (3) when the gas enters the burner from above, the gas inlet (1) and the combustion front chamber (2) are arranged on the upper part of the burner casing (3), and the flue gas outlet (8) is arranged on the burner casing (3) bottom; when the gas enters the burner from the left, the gas inlet (1) and the combustion front chamber (2) are arranged on the left side of the burner housing (3), and the flue gas outlet (8) It is arranged on the right side of the burner casing (3); when the gas enters the burner from the right, the gas inlet (1) and the combustion front chamber (2) are arranged on the right side of the burner casing (3), and the The flue gas outlet (8) is arranged on the left side of the burner casing (3).
本发明的有益效果是:本发明提供一种角型多孔介质燃烧器,当超低热值燃气进入燃烧器燃烧,由于燃烧器预热区采用了向内渐缩的结构,使来流气体的速度逐渐增大,让燃气不易停留在预热区或回流至燃气进口处;由于燃烧器燃烧区采用了向外渐扩的结构,使来流气体的速度逐渐减小,让火焰易驻定在燃烧区或不易移动到出口处甚至脱离燃烧器,同时由于燃烧区采用了向外渐扩的结构,扩大了出口截面积,而多孔介质燃烧器作为一个辐射加热装置,这样会强化出口的对外辐射换热,使出口辐射效率高达30%左右;在预热区和燃烧区间设置缓冲区,能够使来流气体的速度得到一个缓冲效果,这样防止局部速度过大,造成火焰面的倾斜或分布不均。The beneficial effects of the present invention are: the present invention provides an angular porous media burner. When the ultra-low calorific value gas enters the burner for combustion, since the preheating zone of the burner adopts an inwardly tapered structure, the velocity of the incoming gas Gradually increases, so that the gas is not easy to stay in the preheating area or return to the gas inlet; because the burner combustion area adopts a structure that expands outwards, the velocity of the incoming gas gradually decreases, making it easier for the flame to stay in the combustion zone. It may not be easy to move to the outlet or even break away from the burner. At the same time, because the combustion zone adopts a structure that expands outwards, the cross-sectional area of the outlet is enlarged, and the porous media burner is used as a radiation heating device, which will strengthen the external radiation exchange of the outlet. Heat, so that the outlet radiation efficiency is as high as about 30%; setting a buffer zone in the preheating zone and the combustion zone can make the velocity of the incoming gas get a buffer effect, so as to prevent the local velocity from being too large, resulting in the inclination or uneven distribution of the flame surface .
与现有技术相比,本发明的能够明显拓宽火焰稳定速度极限范围,不仅有效地防止了火焰回火和脱火,也提高了出口辐射效率,同时也减小了多孔介质热震性损坏的发生。Compared with the prior art, the present invention can obviously widen the limit range of the flame stability speed, not only effectively prevent the flame from tempering and defiring, but also improve the outlet radiation efficiency, and reduce the thermal shock damage of the porous medium at the same time. occur.
附图说明Description of drawings
图1为本发明一种角型多孔介质燃烧器轴向剖视图;Fig. 1 is an axial sectional view of an angular porous media burner of the present invention;
图2为本发明中多孔介质区域示意图;Fig. 2 is a schematic diagram of the porous medium region in the present invention;
图3为本发明一种角型多孔介质燃烧器的俯视图;Fig. 3 is a top view of an angular porous media burner of the present invention;
其中,in,
1燃气进口,2燃烧前室,3燃烧器外壳,4保护区,5预热区,6缓冲区,7燃烧区,8烟气出口。1 gas inlet, 2 combustion front chamber, 3 burner shell, 4 protection zone, 5 preheating zone, 6 buffer zone, 7 combustion zone, 8 flue gas outlet.
具体实施方式Detailed ways
为了更好的解释本发明,以便于理解,下面结合附图,通过具体实施方式,对本发明的技术方案和效果作详细描述。In order to better explain the present invention and facilitate understanding, the technical solutions and effects of the present invention will be described in detail below through specific implementation manners in conjunction with the accompanying drawings.
如图1-3所示,一种角型多孔介质燃烧器内部依次由燃气进口1、燃烧前室2、保护区4、预热区5、缓冲区6、燃烧区7和烟气出口8构成,四周由燃烧器外壳3封闭而成,燃烧器外壳3采用保温材料,预热区5、缓冲区6、燃烧区7统称为多孔介质区域,所述多介质区域中预热区5和燃烧区7均为漏斗状,分别设置在缓冲区6两端,预热区5和燃烧区7关于缓冲区6中心对称。所述保护区4为挡板砖,挡板砖的板厚为10~40mm,孔隙率为80%~90%,挡板砖上开设有多个通孔,通孔的平均孔径为2~4mm,将挡板砖的通孔沿燃烧器外壳3的轴向平行设置,本实施例中挡板砖的厚度为10mm、孔隙率为80%、通孔的平均孔径为2mm。As shown in Figure 1-3, the interior of an angular porous media burner is composed of gas inlet 1, combustion front chamber 2, protection zone 4, preheating zone 5, buffer zone 6, combustion zone 7 and flue gas outlet 8 , surrounded by the burner shell 3 closed, the burner shell 3 using insulation materials, the preheating zone 5, the buffer zone 6, the combustion zone 7 are collectively referred to as the porous medium zone, the preheating zone 5 and the combustion zone in the multi-media zone 7 are all funnel-shaped, respectively set at both ends of the buffer zone 6, the preheating zone 5 and the combustion zone 7 are symmetrical about the center of the buffer zone 6. The protection area 4 is a baffle brick, the thickness of the baffle brick is 10-40mm, the porosity is 80%-90%, and a plurality of through holes are opened on the baffle brick, and the average diameter of the through hole is 2-4mm , the through holes of the baffle bricks are arranged parallel to the axial direction of the burner housing 3, the thickness of the baffle bricks in this embodiment is 10mm, the porosity is 80%, and the average aperture of the through holes is 2mm.
如图2所示,多孔介质区域由预热区5、缓冲区6、燃烧区7组成,预热区5和燃烧区7分别向内和向外渐扩一定的角度α,其范围是0°<α<40°,在本实施例中将该角度设置为α=10°。多孔介质区域均采用多孔介质材料填充,多孔介质材料选用氧化铝泡沫陶瓷或者氧化锆泡沫陶瓷,其中预热区5装填小孔多孔介质,采用孔密度为50PPI~60PPI、孔隙率为80%以上的氧化铝泡沫陶瓷或者氧化锆泡沫陶瓷;缓冲区6装填中孔多孔介质,采用孔密度为30PPI~40PPI、孔隙率为80%以上的氧化铝泡沫陶瓷或者氧化锆泡沫陶瓷;燃烧区7装填大孔多孔介质,采用孔密度为10PPI~20PPI、孔隙率为80%以上的氧化铝泡沫陶瓷或者氧化锆泡沫陶瓷;本实施例中预热区5装填的是孔密度为60PPI、孔隙率为83.5%的氧化铝泡沫陶瓷,缓冲区6装填的是孔密度为40PPI、孔隙率为85%的氧化铝泡沫陶瓷,燃烧区7装填的是孔密度为10PPI、孔隙率为87%的氧化铝泡沫陶瓷。As shown in Figure 2, the porous medium area is composed of a preheating zone 5, a buffer zone 6, and a combustion zone 7. The preheating zone 5 and the combustion zone 7 gradually expand inward and outward at a certain angle α, and the range is 0° <α<40°, the angle is set to α=10° in this embodiment. The porous media area is filled with porous media materials, and the porous media materials are alumina foam ceramics or zirconia foam ceramics, and the preheating zone 5 is filled with small-pore porous media, with a pore density of 50PPI-60PPI and a porosity of more than 80%. Alumina foam ceramics or zirconia foam ceramics; the buffer zone 6 is filled with mesoporous porous media, and alumina foam ceramics or zirconia foam ceramics with a pore density of 30PPI-40PPI and a porosity of more than 80% are used; the combustion zone 7 is filled with large pores The porous medium adopts alumina foam ceramics or zirconia foam ceramics with a pore density of 10PPI to 20PPI and a porosity of 80% or more; in this embodiment, the preheating zone 5 is filled with a pore density of 60PPI and a porosity of 83.5%. Alumina foam ceramics, the buffer zone 6 is filled with alumina foam ceramics with a pore density of 40PPI and a porosity of 85%, and the combustion zone 7 is filled with alumina foam ceramics with a pore density of 10PPI and a porosity of 87%.
本发明所提供的一种角型多孔介质燃烧器可以有四种使用形式,当燃气从下方进入燃烧器时,所述燃气进口1、燃烧前室2设置在燃烧器外壳3的底部,所述烟气出口8设置在燃烧器外壳3的上部,即燃气下进上出;当燃气从上方进入燃烧器时,所述燃气进口1、燃烧前室2设置在燃烧器外壳3的上部,所述烟气出口8设置在燃烧器外壳3的底部,即上进下出;当燃气从左方进入燃烧器时,所述燃气进口1、燃烧前室2设置在燃烧器外壳3的左侧,所述烟气出口8设置在燃烧器外壳3的右侧,即左进右出;当燃气从右方进入燃烧器时,所述燃气进口1、燃烧前室2设置在燃烧器外壳3的右侧,所述烟气出口8设置在燃烧器外壳3的左侧,即右进左出;如图1所示,本实施例中采用的是燃气下进上出的方式。An angular porous media burner provided by the present invention can have four usage forms. When the gas enters the burner from below, the gas inlet 1 and the combustion front chamber 2 are arranged at the bottom of the burner shell 3. The flue gas outlet 8 is arranged on the upper part of the burner casing 3, that is, the gas enters from the bottom and goes out from the top; The flue gas outlet 8 is set at the bottom of the burner shell 3, that is, it goes in and out from the top; when the gas enters the burner from the left, the gas inlet 1 and the pre-combustion chamber 2 are set on the left side of the burner shell 3. The flue gas outlet 8 is set on the right side of the burner shell 3, that is, it enters from the left and goes out from the right; when the gas enters the burner from the right, the gas inlet 1 and the combustion front chamber 2 are set on the right side of the burner shell 3, The flue gas outlet 8 is arranged on the left side of the burner casing 3, that is, it enters from the right and exits from the left;
一种角型多孔介质燃烧器燃气燃烧过程如下:The gas combustion process of an angular porous media burner is as follows:
如图1所示,首先,燃气从燃气进口1进入燃烧前室2,然后经过多孔介质上游至预热区5,燃气被预热之后在多孔介质中游缓冲区6中点火开始燃烧,随着燃气的不断供给,燃烧的火焰逐渐驻定在燃烧区7,最后燃烧所形成的高温烟气由烟气出口8排出燃烧器外。As shown in Figure 1, first, the gas enters the pre-combustion chamber 2 from the gas inlet 1, and then goes upstream to the preheating zone 5 through the porous medium. Continuous supply, the burning flame gradually settles in the combustion zone 7, and finally the high-temperature flue gas formed by combustion is discharged out of the burner through the flue gas outlet 8.
在本实例中,由于角型多孔介质燃烧器预热区5采用了向内渐缩的结构,使来流气体的速度逐渐增大,让燃气不易停留在预热区5或回流至燃气进口1处,遏制了回火现象的产生;由于角型多孔介质燃烧器燃烧区7采用了向外渐扩的结构,使来流气体的速度逐渐减小,让火焰易驻定在燃烧区7或不易移动到烟气出口8处甚至脱离燃烧器,抑制了脱火现象的产生,同时由于燃烧区7采用了向外渐扩的结构,扩大了烟气出口8的截面积,而多孔介质燃烧器作为一个辐射加热装置,这样会强化出口的对外辐射换热,在本实施例中,定义出口辐射效率是出口辐射热量与燃烧释放热量之比,通过fluent16.0仿真模拟,在当量比φ=4.0-6.0、入口流速v=0.4-0.6m/s时,出口辐射效率高达30%。预热区5和燃烧区7间置缓冲区6是为了让来流气体的速度得到一个缓冲效果,这样防止局部速度过大,造成火焰面的倾斜或分布不均,使燃烧器结构减少热震性的破坏。In this example, since the preheating zone 5 of the angular porous media burner adopts an inwardly tapering structure, the velocity of the incoming gas gradually increases, making it difficult for the gas to stay in the preheating zone 5 or return to the gas inlet 1 The occurrence of tempering phenomenon is curbed; since the combustion zone 7 of the angular porous media burner adopts a structure that gradually expands outwards, the velocity of the incoming gas gradually decreases, making it easy for the flame to settle in the combustion zone 7 or not easily Move to the flue gas outlet 8 or even break away from the burner, which suppresses the occurrence of fire-off phenomenon. At the same time, because the combustion zone 7 adopts a structure that expands outwards, the cross-sectional area of the flue gas outlet 8 is enlarged, and the porous media burner acts as a A radiation heating device, which will strengthen the external radiation heat transfer of the outlet. In this embodiment, the outlet radiation efficiency is defined as the ratio of the outlet radiated heat to the heat released by combustion. Through fluent16.0 simulation simulation, the equivalent ratio φ = 4.0- 6.0. When the inlet velocity v=0.4-0.6m/s, the outlet radiation efficiency is as high as 30%. The buffer zone 6 between the preheating zone 5 and the combustion zone 7 is to allow the velocity of the incoming gas to obtain a buffer effect, so as to prevent the local velocity from being too large, resulting in the inclination or uneven distribution of the flame surface, and reducing the thermal shock of the burner structure sexual destruction.
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CN112128751A (en) * | 2020-08-19 | 2020-12-25 | 江苏大学 | A porous medium burner with foam ceramic |
CN112628735A (en) * | 2020-12-31 | 2021-04-09 | 松山湖材料实验室 | Burner and submerged combustion apparatus |
CN114623443A (en) * | 2022-04-11 | 2022-06-14 | 西安交通大学 | A segmented porous medium burner and its working method |
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CN115289470B (en) * | 2021-04-19 | 2024-11-12 | 广东万和新电气股份有限公司 | Segmented porous medium burner and gas water heater |
CN115143456B (en) * | 2022-06-06 | 2024-04-19 | 武汉科技大学 | A multi-layer porous medium burner and its preparation method |
CN115894015B (en) * | 2022-11-29 | 2023-08-15 | 武汉理工大学 | High-strength porous ceramic combustion medium and manufacturing method thereof |
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