CN104727976A - Combustion heating system for Stirling engine - Google Patents
Combustion heating system for Stirling engine Download PDFInfo
- Publication number
- CN104727976A CN104727976A CN201510101420.3A CN201510101420A CN104727976A CN 104727976 A CN104727976 A CN 104727976A CN 201510101420 A CN201510101420 A CN 201510101420A CN 104727976 A CN104727976 A CN 104727976A
- Authority
- CN
- China
- Prior art keywords
- combustion
- stirling engine
- heating system
- porous medium
- layer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 76
- 238000010438 heat treatment Methods 0.000 title claims abstract description 48
- 239000002184 metal Substances 0.000 claims abstract description 22
- 229910052751 metal Inorganic materials 0.000 claims abstract description 22
- 238000009413 insulation Methods 0.000 claims abstract description 16
- 230000003197 catalytic effect Effects 0.000 claims abstract description 12
- 239000000919 ceramic Substances 0.000 claims abstract description 11
- 239000010410 layer Substances 0.000 claims description 46
- 239000000463 material Substances 0.000 claims description 15
- 238000011144 upstream manufacturing Methods 0.000 claims description 9
- 238000005485 electric heating Methods 0.000 claims description 7
- 239000011229 interlayer Substances 0.000 claims description 7
- 238000002347 injection Methods 0.000 claims description 4
- 239000007924 injection Substances 0.000 claims description 4
- 229910000746 Structural steel Inorganic materials 0.000 claims description 3
- 229910052593 corundum Inorganic materials 0.000 claims description 3
- 239000010431 corundum Substances 0.000 claims description 3
- 239000012774 insulation material Substances 0.000 claims description 3
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 claims description 3
- 239000003381 stabilizer Substances 0.000 claims description 3
- 239000007769 metal material Substances 0.000 claims description 2
- 238000012546 transfer Methods 0.000 abstract description 12
- 230000008901 benefit Effects 0.000 abstract description 6
- 238000005338 heat storage Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 27
- 239000003546 flue gas Substances 0.000 description 9
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 238000013461 design Methods 0.000 description 6
- 238000009422 external insulation Methods 0.000 description 4
- 230000005855 radiation Effects 0.000 description 4
- 150000003254 radicals Chemical class 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000010892 electric spark Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 230000000739 chaotic effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000001902 propagating effect Effects 0.000 description 2
- 238000007348 radical reaction Methods 0.000 description 2
- 230000036632 reaction speed Effects 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 230000001629 suppression Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02G—HOT GAS OR COMBUSTION-PRODUCT POSITIVE-DISPLACEMENT ENGINE PLANTS; USE OF WASTE HEAT OF COMBUSTION ENGINES; NOT OTHERWISE PROVIDED FOR
- F02G1/00—Hot gas positive-displacement engine plants
- F02G1/04—Hot gas positive-displacement engine plants of closed-cycle type
- F02G1/043—Hot gas positive-displacement engine plants of closed-cycle type the engine being operated by expansion and contraction of a mass of working gas which is heated and cooled in one of a plurality of constantly communicating expansible chambers, e.g. Stirling cycle type engines
- F02G1/053—Component parts or details
- F02G1/055—Heaters or coolers
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gas Burners (AREA)
Abstract
本发明涉及一种斯特林发动机的燃烧加热系统,由上下设置的直形渐变叠式多孔介质燃烧器及填充式多孔介质加热器构成,直形渐变叠式多孔介质燃烧器包括壳体,以及设置在壳体内从上到下依次设置的燃气进口、预混室、轴向隔热层、点火器引线保护管、点火器、渐变型陶瓷多孔介质层、催化层,填充式多孔介质加热器由外部保温层,设置在保温层内的金属网圆筒,及在金属网圆筒内呈中心对称布置的加热管,加热管的间隙内填充金属丝。本发明具有燃烧稳定、燃烧效率高、传热性能好、蓄热性能好、工作稳定、负荷调节范围广、易调节、污染排放少等优点,对提高燃气型斯特林发动机工作效率作用显著。
The invention relates to a combustion heating system of a Stirling engine, which is composed of a straight gradient stacked porous medium burner and a filled porous medium heater arranged up and down. The straight gradient stacked porous medium burner includes a shell, and The gas inlet, premixing chamber, axial heat insulation layer, igniter lead protection tube, igniter, gradient ceramic porous medium layer, catalytic layer, and the filled porous medium heater are arranged in the shell from top to bottom. The outer insulation layer, the metal mesh cylinder arranged in the insulation layer, and the heating pipes arranged symmetrically in the center of the metal mesh cylinder, and the gaps of the heating pipes are filled with metal wires. The invention has the advantages of stable combustion, high combustion efficiency, good heat transfer performance, good heat storage performance, stable operation, wide load adjustment range, easy adjustment, less pollution discharge, etc., and has a significant effect on improving the working efficiency of the gas type Stirling engine.
Description
技术领域technical field
本发明属于燃烧及换热装置,尤其是涉及一种斯特林发动机的燃烧加热系统。The invention belongs to a combustion and heat exchange device, in particular to a combustion heating system of a Stirling engine.
背景技术Background technique
斯特林发动机是一种封闭式外燃机,具有燃料来源广,热效率高,排气污染少,运转特性好,噪音低等优点,并且在分布式能源领域、清洁燃气发电领域、太阳能发电领域有着重要的应用,越来越受到人们的关注。The Stirling engine is a closed external combustion engine, which has the advantages of wide fuel sources, high thermal efficiency, less exhaust pollution, good operating characteristics, low noise, etc., and is widely used in the fields of distributed energy, clean gas power generation and solar power generation It has important applications and has attracted more and more attention.
外燃系统是斯特林发动机的重要组成部分,其主要功能是通过合理、高效地组织燃烧与换热,将燃料的化学能转化为热能并通过热交换器传递给加热器,再由加热器将热能通过热交换传递给机内工质,从而使得机内工质在发动机内膨胀做功,将热能转换成机械能。由此可见,一台发动机效率的高低,不仅取决于发动机本身的循环效率,而且与其外燃系统的燃烧转换效率的高低也有着很大的关系。为此,要设计出高效、可靠的斯特林发动机,外燃系统的设计至关重要。The external combustion system is an important part of the Stirling engine. Its main function is to convert the chemical energy of the fuel into thermal energy through a reasonable and efficient organization of combustion and heat exchange, and transfer it to the heater through the heat exchanger, and then the heater The heat energy is transferred to the working medium in the machine through heat exchange, so that the working medium in the machine expands and does work in the engine, and converts heat energy into mechanical energy. It can be seen that the efficiency of an engine not only depends on the cycle efficiency of the engine itself, but also has a great relationship with the combustion conversion efficiency of its external combustion system. Therefore, to design an efficient and reliable Stirling engine, the design of the external combustion system is very important.
斯特林的加热器内部的工质都处于加压状态,其密度较大;流速也比较高,所以内部换热是充分的。外部燃烧产物的密度小,流速低,以至于受有很大的温差才能传递必要的传热量,因此提高加热器管外的传热效果将会大大改善加热器的工作性能。同时,在很多加热器部分经常会发生受热不均匀现象即出现“热点”。为了防止加热管被烧毁,“热点”温度必须等于或低于金属所能承受的最高工作温度(冶金限)。事实上加热器部分的平均温度比冶金限要低得多(可低到100℃),这么低的平均温度使发动机的功率和效率同时下降。The working fluid inside the Stirling heater is in a pressurized state, and its density is relatively high; the flow rate is also relatively high, so the internal heat exchange is sufficient. The density of the external combustion products is small and the flow rate is low, so that the necessary heat transfer can only be transferred by a large temperature difference. Therefore, improving the heat transfer effect outside the heater tube will greatly improve the working performance of the heater. At the same time, uneven heating often occurs in many heater parts, that is, "hot spots". In order to prevent the heating tube from being burned, the "hot spot" temperature must be equal to or lower than the maximum operating temperature (metallurgical limit) that the metal can withstand. In fact, the average temperature of the heater part is much lower than the metallurgical limit (can be as low as 100 ℃), and such a low average temperature will reduce the power and efficiency of the engine at the same time.
综上所述,为改进斯特林机的工作性能,对其燃烧室与加热器进行优化设计是必要的。因此,本发明通过采用多孔燃烧换热技术,设计了一种用于燃气型斯特林发动机的燃烧加热系统。充分利用多孔介质良好的蓄热能力、激烈的扰动、较强的导热及辐射能力,使得燃烧室内温度更加均匀,到达加热器表面平均温度高,从而提高发动机的功率和效率。该系统可应用于燃气型斯特林发动机,尤其是工作在分布式能源站内的主要以稳定工况运作的燃气型斯特林发动机。In summary, in order to improve the working performance of the Stirling machine, it is necessary to optimize the design of its combustion chamber and heater. Therefore, the present invention designs a combustion heating system for a gas-type Stirling engine by adopting porous combustion heat exchange technology. Make full use of the good heat storage capacity, intense disturbance, strong heat conduction and radiation capacity of porous media, so that the temperature in the combustion chamber is more uniform, and the average temperature reaching the heater surface is high, thereby improving the power and efficiency of the engine. The system can be applied to a gas-type Stirling engine, especially a gas-type Stirling engine working in a distributed energy station and mainly operating in a stable working condition.
现有技术中也公开了相关的斯特林装置,例如,中国矿业大学张保生、龚小茂、周凡等发明了一种储热式煤层气斯特林装置,专利号:201120056598.8。此实用新型利用多孔介质燃烧器产生的高温烟气通过盘绕在储热器中的盘管实现热量的高效率传递。实现了不稳定煤层气尤其低浓度煤层气发电,有效降低了煤层气气源不稳定尤其是浓度波动大对整个装置的冲击,同时具有热效率高、污染小、噪音低、移动方便、维修简便等优点。但其多孔介质燃烧器结构过于简单,容易产生燃烧不稳定现象,同时热头设计简单,也使传热性能有所限制。Related Stirling devices are also disclosed in the prior art. For example, Zhang Baosheng, Gong Xiaomao and Zhou Fan of China University of Mining and Technology invented a thermal storage coalbed methane Stirling device, patent number: 201120056598.8. This utility model utilizes the high-temperature flue gas produced by the porous medium burner to achieve high-efficiency transfer of heat through the coil pipe coiled in the heat storage. Realize the power generation of unstable coalbed methane, especially low-concentration coalbed methane, effectively reduce the impact of unstable coalbed methane gas sources, especially large concentration fluctuations, on the entire device, and at the same time have high thermal efficiency, low pollution, low noise, convenient movement, and easy maintenance, etc. advantage. However, the structure of the porous media burner is too simple, which is prone to combustion instability. At the same time, the design of the heat head is simple, which also limits the heat transfer performance.
浙江大学的岑可法、程乐鸣等设计了一种渐变型多孔介质燃烧器实用新型,专利号:01226080.0。具有燃烧器壳体及其保温层,在燃烧器壳体及其保温层内壁设有二次空气配气圈,燃烧器壳体及其保温层一端设有散热圈、预混室、燃气进口和空气进口,在散热器中心设有混合燃气均匀分配器,在二次空气配气圈内设有渐变空隙率非均匀多孔介质。该渐变型多孔介质燃烧器燃烧稳定,燃烧效率高,NOx排放低,污染物排放低的优点,体积小、结构紧凑、负荷调节范围广,具有明显经济效率。但由于该发明主要用于研究实验,为了不改变燃烧器内部多孔介质层结构,故选择在燃烧室出口使用电火花引燃,这样的设计不利于在斯特林机上应用,并使得燃烧器的点火时间大大增加。Cen Kefa and Cheng Leming from Zhejiang University designed a utility model for a gradual change porous media burner, patent number: 01226080.0. It has a burner shell and its insulation layer, a secondary air distribution ring is provided on the inner wall of the burner shell and its insulation layer, and a heat dissipation ring, a premixing chamber, a gas inlet and The air inlet is equipped with a mixed gas uniform distributor in the center of the radiator, and a non-uniform porous medium with a gradient void ratio is installed in the secondary air distribution ring. The gradually changing porous media burner has the advantages of stable combustion, high combustion efficiency, low NOx emission, and low pollutant emission, small volume, compact structure, wide load adjustment range, and obvious economic efficiency. But because this invention is mainly used for research experiments, in order not to change the structure of the porous medium layer inside the burner, it is selected to use electric spark ignition at the outlet of the combustion chamber. This design is not conducive to the application on the Stirling machine, and makes the burner The ignition time is greatly increased.
发明内容Contents of the invention
本发明的目的就是为了克服上述现有技术存在的缺陷而提供一种可供斯特林发动机使用,燃烧效率高、传热性能好、污染排放低的燃烧加热系统。The object of the present invention is to provide a combustion heating system with high combustion efficiency, good heat transfer performance and low pollution emission, which can be used by a Stirling engine in order to overcome the above-mentioned defects in the prior art.
本发明的目的可以通过以下技术方案来实现:The purpose of the present invention can be achieved through the following technical solutions:
一种斯特林发动机的燃烧加热系统,由上下设置的直形渐变叠式多孔介质燃烧器及填充式多孔介质加热器构成,A combustion heating system of a Stirling engine, which is composed of a straight gradient stacked porous medium burner and a filled porous medium heater arranged up and down,
所述的直形渐变叠式多孔介质燃烧器包括壳体,以及设置在壳体内从上到下依次设置的燃气进口、预混室、轴向隔热层、点火器引线保护管、点火器、渐变型陶瓷多孔介质层、催化层,The straight gradient stacked porous media burner includes a casing, and a gas inlet, a premixing chamber, an axial heat insulation layer, an igniter lead wire protection tube, an igniter, Gradient ceramic porous medium layer, catalytic layer,
所述的填充式多孔介质加热器由外部保温层,设置在保温层内的金属网圆筒,及在金属网圆筒内呈中心对称布置的加热管,加热管的间隙内填充金属丝。The filled porous medium heater consists of an external insulation layer, a metal mesh cylinder arranged in the insulation layer, and heating tubes arranged symmetrically in the center of the metal mesh cylinder, and metal wires are filled in the gaps of the heating tubes.
所述的预混室内填充细丝状多孔介质材料,一方面可以形成紊流流动气流使燃气与预热风空气进行很好的混合,另一方面,防止由于回火或者预热风温度过高等原因,导致预混气温度超过燃气燃点,造成预混室爆炸。当由于某些因素造成预混室局部空间温度过高而引起突然着火时,其周围温度较低的多孔介质材料可以迅速吸收燃烧热量,使燃烧热损失大于燃烧产生的反应热;同时分析链式反应机理可知,由于与混乱的多孔介质材料接触,火焰中的部分活性基团(自由基)失去活性而销毁,使链式自由基反应中止,产生间隙消焰,保障预混室不会发生爆炸危险。The pre-mixing chamber is filled with filamentous porous medium material, on the one hand, it can form a turbulent flow to make the gas and the preheating air mix well, on the other hand, it can prevent the gas from being tempered or the temperature of the preheating air is too high, etc. The reason is that the temperature of the premixed gas exceeds the ignition point of the gas, causing the premixed chamber to explode. When the temperature of the local space in the premixing chamber is too high due to some factors to cause a sudden fire, the porous media material with a lower temperature around it can quickly absorb the heat of combustion, so that the loss of combustion heat is greater than the reaction heat generated by combustion; at the same time, the analysis of the chain The reaction mechanism shows that due to the contact with the chaotic porous media material, some active groups (free radicals) in the flame lose their activity and are destroyed, so that the chain free radical reaction is terminated, resulting in gap flame suppression, and the premix chamber will not explode. Danger.
所述的壳体为内壳及外壳组成的双层结构,所述的内壳为耐高温的刚玉材料,所述的外壳包括内层保温材料与外层结构钢材料,内壳及外壳之间留有空气预热夹层。The shell is a double-layer structure composed of an inner shell and an outer shell. The inner shell is made of high temperature resistant corundum material. The outer shell includes an inner layer of thermal insulation material and an outer layer of structural steel material. Between the inner shell and the outer shell Leave air to preheat the interlayer.
所述的壳体下方设有空气进口,新鲜空气从空气进口被外接鼓风机吹入空气预热夹层,形成预热风,同时也可对内壳进行冷却,避免其温度过高。An air inlet is arranged below the housing, and fresh air is blown into the air preheating interlayer by an external blower from the air inlet to form preheating air, and at the same time, the inner housing can be cooled to prevent its temperature from being too high.
所述的轴向隔热层的中央为混合气体喷气孔,四周设有预热风通道。The center of the axial heat insulation layer is a mixed gas injection hole, and preheating air passages are arranged around it.
所述的点火器为圆锥形电加热型点火器,在点火器附近留有一定自由空间,做成微型钝体稳燃器,并置于燃烧主区域上游。相对于电火花型点火器,电加热型点火器点火可靠。圆锥形状的钝体稳燃器,可以在钝体尾部形成回流区,达到稳定火焰的目的。位于燃烧主区域上游可以很好地预热燃烧区域的多孔介质,提高点火速度。当燃烧稳定后,相对于多孔介质传热性较差的自由空间有效地阻隔热量及火焰向上游传播,保护点火器不被烧坏并可以防止回火的发生。The igniter is a conical electric heating igniter, and there is a certain free space near the igniter, which is made into a miniature blunt stable burner and placed upstream of the main combustion area. Compared with the electric spark type igniter, the electric heating type igniter ignites reliably. The conical blunt body stabilizer can form a recirculation zone at the tail of the blunt body to achieve the purpose of stabilizing the flame. Located upstream of the main combustion zone can well preheat the porous media in the combustion zone and increase the ignition rate. When the combustion is stable, the free space with poorer heat transfer than the porous medium can effectively block the heat and flame from propagating upstream, protect the igniter from being burned out and prevent the occurrence of backfire.
所述的渐变型陶瓷多孔介质层为自上而下孔径逐渐增大的多层泡沫陶瓷组成的介质层。The gradient ceramic porous medium layer is a medium layer composed of multilayer foamed ceramics whose pore diameter gradually increases from top to bottom.
所述的催化层为多孔介质催化层,一方面该位置处于燃烧区域下游,可以催化燃烧过程产生的NOx、CO、HO发生反应转化为无害的CO2、H2O、N2;另一方面,该位置接近燃烧区域,温度相对较高,可以使反应速度保持在很高的水平,使催化过程更加完全。The catalytic layer is a porous media catalytic layer. On the one hand, the position is located downstream of the combustion area, and can catalyze the reaction of NOx , CO, and HO generated during the combustion process into harmless CO 2 , H 2 O, and N 2 ; On the one hand, the location is close to the combustion area, and the temperature is relatively high, which can keep the reaction speed at a high level and make the catalytic process more complete.
所述的金属网圆筒中心位置设置气流旋流器,在旋流器四周中心对称布置46根倒U形加热管,使用气流旋流器将烟气气流分割为八股不同方向的等流量切向气流,可以使各个方向的气流更加均匀,并且使气流切向的通过换热管区域,增加气流冲刷换热管的时间,提高传热效率。The center position of the metal mesh cylinder is provided with an air cyclone, and 46 inverted U-shaped heating pipes are arranged symmetrically around the center of the cyclone, and the air cyclone is used to divide the flue gas flow into eight equal-flow tangential streams in different directions. The air flow can make the air flow in all directions more uniform, and make the air flow tangentially pass through the heat exchange tube area, increase the time for the air flow to scour the heat exchange tube, and improve the heat transfer efficiency.
金属网圆筒与外部保温层之间留有一定厚度自由空间,使网筒四周各个位置气压大致相同,从而保证筒内各个方向充分换热的气流分布均匀。There is a certain thickness of free space between the metal mesh cylinder and the external insulation layer, so that the air pressure at all positions around the mesh cylinder is roughly the same, so as to ensure that the airflow in all directions in the cylinder is fully distributed and evenly distributed.
与现有技术相比,本发明具有以下优点:Compared with the prior art, the present invention has the following advantages:
1.使用电加热型点火器(形状为圆锥形)在燃烧室上游处引燃预混气体并稳燃火焰大大缩减了多孔介质燃烧器的启动时间,同时此时排出的烟气也可以预热斯特林机加热器,从而尽量减少多孔介质燃烧器启动阶段的热量浪费。并且掏空中心位置的多孔介质有效地阻隔稳定燃烧后热量及火焰向上游传播,保护了点火器不被烧坏并可以防止回火的发生。1. Using an electric heating type igniter (conical in shape) to ignite the premixed gas at the upstream of the combustion chamber and stably burn the flame greatly reduces the start-up time of the porous media burner, and at the same time the exhausted flue gas can also be preheated Stirling machine heaters, thereby minimizing heat waste during the start-up phase of the porous media burner. And the hollowed-out porous medium at the center effectively blocks the heat and flame from spreading upstream after stable combustion, protecting the igniter from being burned out and preventing the occurrence of backfire.
2.降低燃烧室的热不均匀性,减少局部高温范围并有效降低其温度,从而减少NOx等污染气体的排放。2. Reduce the thermal inhomogeneity of the combustion chamber, reduce the local high temperature range and effectively reduce its temperature, thereby reducing the emission of NOx and other polluting gases.
3.提高整个燃烧区域的平均温度,改善燃烧状况,燃烧区域末端的催化层进一步催化可燃气体燃尽。使燃烧更完全,减少了不完全燃烧所造成的CO等污染物的排放;并减少了过量空气系数从而减少废气热的排放,提高机器效率。3. Increase the average temperature of the entire combustion area, improve the combustion conditions, and the catalytic layer at the end of the combustion area further catalyzes the burnout of combustible gases. Make the combustion more complete, reduce the emission of pollutants such as CO caused by incomplete combustion; and reduce the excess air coefficient to reduce the emission of exhaust heat and improve machine efficiency.
4.通过合理的布置气流流向,及多孔介质温度均匀的特性,均匀加热管附近温度分布,改善加热管的热应力状况,降低加热管对金属材料的高温性能要求,可使用更为廉价的材料制作加工,降低斯特林机的制造成本有利于斯特林机商品化推广。4. By rationally arranging the flow direction of the airflow and the uniform temperature of the porous medium, the temperature distribution near the heating tube can be uniform, the thermal stress of the heating tube can be improved, the high temperature performance requirements of the heating tube for metal materials can be reduced, and cheaper materials can be used Production and processing, reducing the manufacturing cost of the Stirling machine is conducive to the commercialization of the Stirling machine.
5.利用多孔介质良好的辐射、对流、导热增大加热器与外部烟气的换热效果,优化加热器换热性能,提高发动机燃烧室及加热器单位体积功率及效率。5. Utilize the good radiation, convection, and heat conduction of porous media to increase the heat exchange effect between the heater and external flue gas, optimize the heat exchange performance of the heater, and improve the power and efficiency per unit volume of the engine combustion chamber and heater.
6.增强斯特林发动机加热器的蓄热性能,使加热器温度更容易保持稳定,优化了发动机各种运行性能(如转速更容易保持稳定,适应相对苛刻的负载变化与燃气不稳定,优化启动性能等)提高了斯特林机的实用性。6. Enhance the heat storage performance of the Stirling engine heater, make it easier to maintain a stable heater temperature, and optimize various operating performances of the engine (such as easier to maintain a stable speed, adapt to relatively harsh load changes and gas instability, optimize Starting performance, etc.) improve the practicality of the Stirling machine.
附图说明Description of drawings
图1为本发明的结构示意图;Fig. 1 is a structural representation of the present invention;
图2为本发明应用在斯特林发动机上的结构示意图;Fig. 2 is the structural representation that the present invention is applied on the Stirling engine;
图3为气流旋流器的结构示意图。Fig. 3 is a schematic diagram of the structure of the air cyclone.
图中,1-燃气进口,2-点火器引线保护管,3-预混室,4-预热风通道,5-混合气体喷气孔,6-点火器,7-渐变型陶瓷多孔介质层、8-空气预热夹层,9-外壳,10-内壳,11-空气进口,12-催化层,13-金属丝,14-加热管,15-气流旋流器,16-烟气出口,17-热头加热管口,18-斯特林发动机,19-燃烧加热系统。In the figure, 1-gas inlet, 2-igniter lead protection tube, 3-premix chamber, 4-preheating air channel, 5-mixed gas injection hole, 6-igniter, 7-gradient ceramic porous medium layer, 8-air preheating interlayer, 9-outer shell, 10-inner shell, 11-air inlet, 12-catalytic layer, 13-metal wire, 14-heating pipe, 15-air cyclone, 16-flue gas outlet, 17 - Thermal head heating nozzle, 18 - Stirling engine, 19 - Combustion heating system.
具体实施方式Detailed ways
下面结合附图和具体实施例对本发明进行详细说明。The present invention will be described in detail below in conjunction with the accompanying drawings and specific embodiments.
实施例Example
一种斯特林发动机的燃烧加热系统19,其结构如图1所示,由上下设置的直形渐变叠式多孔介质燃烧器及填充式多孔介质加热器构成。A combustion heating system 19 of a Stirling engine, the structure of which is shown in Figure 1, is composed of a straight gradient stacked porous medium burner and a filled porous medium heater arranged up and down.
直形渐变叠式多孔介质燃烧器包括壳体,以及设置在壳体内从上到下依次设置的燃气进口1、预混室3、轴向隔热层、点火器引线保护管2、点火器6、渐变型陶瓷多孔介质层7、催化层12。填充式多孔介质加热器由外部保温层,设置在保温层内的金属网圆筒,及在金属网圆筒内呈中心对称布置的加热管14,加热管14的间隙内填充金属丝13。The straight-shaped gradient stacked porous media burner includes a shell, and a gas inlet 1, a premixing chamber 3, an axial heat insulation layer, an igniter lead wire protection tube 2, and an igniter 6 are arranged sequentially in the shell from top to bottom. , Gradient ceramic porous medium layer 7, catalytic layer 12. The filled porous medium heater consists of an external insulation layer, a metal mesh cylinder arranged in the insulation layer, and heating tubes 14 arranged symmetrically in the center of the metal mesh cylinder, and metal wires 13 are filled in the gaps of the heating tubes 14 .
具体来说,在预混室3内填充细丝状多孔介质材料,一方面可以形成紊流流动气流使燃气与预热风空气进行很好的混合,另一方面,防止由于回火,或者预热风温度过高,导致预混气温度超过燃气燃点,造成预混室爆炸。当由于某些因素造成预混室局部空间温度过高而引起突然着火时,其周围温度较低的多孔介质材料可以迅速吸收燃烧热量,使燃烧热损失大于燃烧产生的反应热;同时分析链式反应机理可知,由于与混乱的多孔介质材料接触,火焰中的部分活性基团(自由基)失去活性而销毁,使链式自由基反应中止,产生间隙消焰,保障预混室不会发生爆炸危险。Specifically, filling the pre-mixing chamber 3 with a filamentous porous medium material can form a turbulent flow on the one hand to mix the gas and preheated air well; The temperature of the hot air is too high, causing the temperature of the premixed gas to exceed the ignition point of the gas, causing the premixed chamber to explode. When the temperature of the local space in the premixing chamber is too high due to some factors to cause a sudden fire, the porous media material with a lower temperature around it can quickly absorb the heat of combustion, so that the loss of combustion heat is greater than the reaction heat generated by combustion; at the same time, the analysis of the chain The reaction mechanism shows that due to the contact with the chaotic porous media material, some active groups (free radicals) in the flame lose their activity and are destroyed, so that the chain free radical reaction is terminated, resulting in gap flame suppression, and the premix chamber will not explode. Danger.
壳体为内壳10及外壳9组成的双层结构,内壳10为耐高温的刚玉材料,外壳9包括内层保温材料与外层结构钢材料,内壳10及外壳9之间留有空气预热夹层8。在壳体下方设有空气进口11,新鲜空气从空气进口11被外接鼓风机吹入空气预热夹层8,形成预热风,同时也可对内壳10进行冷却,避免其温度过高。The shell is a double-layer structure consisting of an inner shell 10 and an outer shell 9. The inner shell 10 is made of high-temperature-resistant corundum material, and the outer shell 9 includes an inner layer of thermal insulation material and an outer layer of structural steel material. Air is left between the inner shell 10 and the outer shell 9. Preheat sandwich 8. An air inlet 11 is arranged below the shell, and fresh air is blown into the air preheating interlayer 8 by an external blower from the air inlet 11 to form preheating air, and meanwhile, the inner shell 10 can also be cooled to prevent its temperature from being too high.
轴向隔热层的中央为混合气体喷气孔5,四周设有预热风通道4。点火器6为圆锥形电加热型点火器,在点火器6的附近留有一定自由空间,做成微型钝体稳燃器,并置于燃烧主区域上游。相对于电火花型点火器,电加热型点火器点火可靠。圆锥形状的钝体稳燃器,可以在钝体尾部形成回流区,达到稳定火焰的目的。位于燃烧主区域上游可以很好地预热燃烧区域的多孔介质,提高点火速度。当燃烧稳定后,相对于多孔介质传热性较差的自由空间有效地阻隔热量及火焰向上游传播,保护点火器不被烧坏并可以防止回火的发生。The center of the axial heat insulation layer is a mixed gas injection hole 5, and a preheating air passage 4 is arranged around it. The igniter 6 is a conical electric heating type igniter, leaving a certain free space near the igniter 6, making a miniature blunt body stable burner, and placing it upstream of the main combustion area. Compared with the electric spark type igniter, the electric heating type igniter ignites reliably. The conical blunt body stabilizer can form a recirculation zone at the tail of the blunt body to achieve the purpose of stabilizing the flame. Located upstream of the main combustion zone can well preheat the porous media in the combustion zone and increase the ignition rate. When the combustion is stable, the free space with poorer heat transfer than the porous medium can effectively block the heat and flame from propagating upstream, protect the igniter from being burned out and prevent the occurrence of backfire.
渐变型陶瓷多孔介质层7为自上而下孔径逐渐增大的多层泡沫陶瓷组成的介质层。催化层12为多孔介质催化层,一方面该位置处于燃烧区域下游,可以催化燃烧过程产生的NOx、CO、HO发生反应转化为无害的CO2、H2O、N2;另一方面,该位置接近燃烧区域,温度相对较高,可以使反应速度保持在很高的水平,使催化过程更加完全。Gradient ceramic porous medium layer 7 is a medium layer composed of multilayer foamed ceramics whose pore diameter gradually increases from top to bottom. The catalytic layer 12 is a porous media catalytic layer. On the one hand, this position is located downstream of the combustion area, and can catalyze the reaction of NOx , CO, and HO generated during the combustion process into harmless CO 2 , H 2 O, and N 2 ; , the position is close to the combustion area, and the temperature is relatively high, which can keep the reaction speed at a high level and make the catalytic process more complete.
在金属网圆筒中心位置设置气流旋流器15,其结构如图3所示。在旋流器四周中心对称布置46根倒U形加热管14,使用气流旋流器15将烟气气流分割为八股不同方向的等流量径向气流,可以使各个方向的气流更加均匀,并且使气流径向的通过换热管区域,增加气流冲刷换热管的时间,提高传热效率。金属网圆筒与外部保温层之间留有空间,旋流器翅片及加热管间隙填充金属丝13制成的多孔介质导热材料,从而保证筒内各个方向充分换热的气流分布均匀。外部保温层下方设置有烟气出口18,加热管14的底部设置热头加热管口17用以连接回热器。An airflow swirler 15 is arranged at the center of the metal mesh cylinder, the structure of which is shown in FIG. 3 . 46 inverted U-shaped heating pipes 14 are symmetrically arranged in the center around the cyclone, and the airflow swirler 15 is used to divide the flue gas flow into eight equal-flow radial airflows in different directions, which can make the airflow in all directions more uniform and make the The air flow passes through the heat exchange tube area in a radial direction, increasing the time for the air flow to scour the heat exchange tube and improving heat transfer efficiency. There is a space between the metal mesh cylinder and the external insulation layer, and the gap between the fins of the cyclone and the heating tube is filled with a porous medium heat-conducting material made of metal wire 13, so as to ensure that the airflow fully exchanging heat in all directions in the cylinder is evenly distributed. A flue gas outlet 18 is arranged under the outer insulation layer, and a heating nozzle 17 of a heating head is arranged at the bottom of the heating pipe 14 to connect to the regenerator.
本燃烧加热系统19可以应用在斯特林发动机18上,空气经鼓风机以较高流速由空气进口11进入燃烧器的内壳10与外壳9之间的空气预热夹层8进行预热,同时冷却内壳10,随后穿过预热风通道进入燃烧器上部的预热室3与经燃气进口1进入预混室的燃气进行混合,再通过混合气体均匀分配器进入燃烧室部分,经电加热型的点火器6加热引燃后进入渐变型陶瓷多孔介质层7进行燃烧。最后通过催化层12完全燃烧后进入加热器部分,经过气流旋流器15调整流向后进入换热区,利用金属丝多孔介质良好的导热、对流、辐射特性与加热管换热后由烟气出口16排出。This combustion heating system 19 can be applied on the Stirling engine 18, and the air enters the air preheating interlayer 8 between the inner shell 10 and the outer shell 9 of the burner through the blower at a relatively high flow rate through the air inlet 11 for preheating and cooling The inner casing 10, then enters the preheating chamber 3 on the upper part of the burner through the preheating air passage, mixes with the gas entering the premixing chamber through the gas inlet 1, and then enters the combustion chamber part through the mixed gas uniform distributor, and is heated by electric heating. After being heated and ignited, the igniter 6 enters the gradient ceramic porous medium layer 7 for combustion. Finally, it enters the heater part after being completely burned through the catalytic layer 12, and then enters the heat exchange area after being adjusted by the airflow swirler 15. It uses the good heat conduction, convection, and radiation characteristics of the metal wire porous medium to exchange heat with the heating tube and then exits the flue gas. 16 discharge.
斯特林发动机18的热头与加热管吸收高温烟气的热量后,通过气缸内活塞的相对运动产生容积变化,推动介质在封闭的腔体内做往复循环,在较低的温度和压力下对工质进行压缩,在较高的温度和压力下工质受热膨胀,从而在斯特林循环中获得循环功,与动力传动系统的配合向外部输出机械能。After the hot head and the heating tube of the Stirling engine 18 absorb the heat of the high-temperature flue gas, the relative movement of the piston in the cylinder produces a volume change, pushing the medium to reciprocate in the closed cavity, and the gas is heated at a lower temperature and pressure. The working medium is compressed, and the working medium is heated and expanded under higher temperature and pressure, so as to obtain cycle work in the Stirling cycle, and cooperate with the power transmission system to output mechanical energy to the outside.
作为一种新的燃烧加热系统,经过理论分析与实践检验,认为本系统是切实可行的,主要有以下几个方面作为理论和应用依据:As a new combustion heating system, after theoretical analysis and practice test, it is considered that this system is feasible, and there are mainly the following aspects as the theoretical and application basis:
本发明所述的斯特林发动机的燃烧加热系统,与其他斯特林机燃烧加热系统的主要区别在于其燃烧器与加热器采用了不同于以往通过自由空间进行燃烧及加热工质,而是通过使用几个简单的部件,巧妙的布置气流流向,充分利用多孔介质良好的蓄热能力、激烈的扰动、较强的导热及辐射能力;实现预热新鲜冷空气,预热风与燃气的安全充分混合,混合气体的充分清洁燃烧,及换热器换热能力的改良,全面优化斯特林机燃烧器及加热器的性能。The main difference between the combustion heating system of the Stirling engine of the present invention and other Stirling engine combustion heating systems is that its burner and heater adopt different combustion and heating working fluid through free space in the past, but By using a few simple components and cleverly arranging the air flow direction, making full use of the good heat storage capacity, intense disturbance, strong heat conduction and radiation capacity of porous media; realizing the safety of preheating fresh cold air, preheating air and gas Fully mixed, fully clean combustion of the mixed gas, and the improvement of the heat exchange capacity of the heat exchanger, fully optimize the performance of the Stirling machine burner and heater.
本发明专利所述的燃烧加热系统具有燃烧稳定、燃烧效率高、传热性能好、蓄热性能好、工作稳定、负荷调节范围广易调节、污染排放少等优点,具有明显的实用价值与应用价值。The combustion heating system described in the patent of the present invention has the advantages of stable combustion, high combustion efficiency, good heat transfer performance, good heat storage performance, stable work, wide load adjustment range, easy adjustment, and less pollution discharge, etc., and has obvious practical value and application value.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510101420.3A CN104727976B (en) | 2015-03-09 | 2015-03-09 | A kind of combustion heating system of Stirling engine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510101420.3A CN104727976B (en) | 2015-03-09 | 2015-03-09 | A kind of combustion heating system of Stirling engine |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104727976A true CN104727976A (en) | 2015-06-24 |
CN104727976B CN104727976B (en) | 2016-07-06 |
Family
ID=53452264
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510101420.3A Expired - Fee Related CN104727976B (en) | 2015-03-09 | 2015-03-09 | A kind of combustion heating system of Stirling engine |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104727976B (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106765082A (en) * | 2016-11-16 | 2017-05-31 | 许华雄 | A kind of water temperature adjustment porous media pulse isovolumic burner |
CN108199059A (en) * | 2017-12-27 | 2018-06-22 | 中国科学院上海高等研究院 | Compound combustion reactor, fuel cell system and its multiplexing combustion method |
CN110440617A (en) * | 2018-05-02 | 2019-11-12 | 中国科学院理化技术研究所 | A kind of heat-pipe heat exchanger |
CN112628735A (en) * | 2020-12-31 | 2021-04-09 | 松山湖材料实验室 | Burner and submerged combustion apparatus |
CN113864782A (en) * | 2021-10-28 | 2021-12-31 | 广东万和新电气股份有限公司 | Porous medium burners and gas hot water equipment |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3717993A (en) * | 1970-11-02 | 1973-02-27 | Gen Motors Corp | Preheater assembly for stirling engine |
JPS60243416A (en) * | 1984-05-17 | 1985-12-03 | Matsushita Electric Ind Co Ltd | Stirling engine |
JPS6146449A (en) * | 1984-08-11 | 1986-03-06 | Toshiba Corp | Stirling engine |
CN101158469A (en) * | 2007-11-06 | 2008-04-09 | 东北大学 | A segmented porous ceramic medium gas fuel burner |
CN202055933U (en) * | 2011-04-06 | 2011-11-30 | 中国科学院工程热物理研究所 | Stirling engine heating head for strengthening heat convection by utilizing rotational flow |
CN103277799A (en) * | 2013-05-21 | 2013-09-04 | 大连亿莱森玛机电有限公司 | External heated combustor system |
-
2015
- 2015-03-09 CN CN201510101420.3A patent/CN104727976B/en not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3717993A (en) * | 1970-11-02 | 1973-02-27 | Gen Motors Corp | Preheater assembly for stirling engine |
JPS60243416A (en) * | 1984-05-17 | 1985-12-03 | Matsushita Electric Ind Co Ltd | Stirling engine |
JPS6146449A (en) * | 1984-08-11 | 1986-03-06 | Toshiba Corp | Stirling engine |
CN101158469A (en) * | 2007-11-06 | 2008-04-09 | 东北大学 | A segmented porous ceramic medium gas fuel burner |
CN202055933U (en) * | 2011-04-06 | 2011-11-30 | 中国科学院工程热物理研究所 | Stirling engine heating head for strengthening heat convection by utilizing rotational flow |
CN103277799A (en) * | 2013-05-21 | 2013-09-04 | 大连亿莱森玛机电有限公司 | External heated combustor system |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106765082A (en) * | 2016-11-16 | 2017-05-31 | 许华雄 | A kind of water temperature adjustment porous media pulse isovolumic burner |
CN106765082B (en) * | 2016-11-16 | 2019-01-15 | 许华雄 | A kind of water temperature adjustment porous media pulse isovolumic burner |
CN108199059A (en) * | 2017-12-27 | 2018-06-22 | 中国科学院上海高等研究院 | Compound combustion reactor, fuel cell system and its multiplexing combustion method |
CN108199059B (en) * | 2017-12-27 | 2020-11-06 | 中国科学院上海高等研究院 | Composite combustion reactor, fuel cell system and multiplexing combustion method thereof |
CN110440617A (en) * | 2018-05-02 | 2019-11-12 | 中国科学院理化技术研究所 | A kind of heat-pipe heat exchanger |
CN112628735A (en) * | 2020-12-31 | 2021-04-09 | 松山湖材料实验室 | Burner and submerged combustion apparatus |
CN113864782A (en) * | 2021-10-28 | 2021-12-31 | 广东万和新电气股份有限公司 | Porous medium burners and gas hot water equipment |
Also Published As
Publication number | Publication date |
---|---|
CN104727976B (en) | 2016-07-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR102232434B1 (en) | Catalytic flameless combustion device and combustion method with minimized pollutant emission | |
CN104727976B (en) | A kind of combustion heating system of Stirling engine | |
CN101655239B (en) | Ceramic high-efficiency air self-preheating type combustor | |
CN104501162A (en) | Porous medium burner with packed bed structure | |
CN107893993A (en) | A kind of Self inhaling porous media heating furnace | |
CN204438099U (en) | Heat storage type porous medium burner assembly | |
CN2597893Y (en) | Solar-Gas Hybrid Heat Receiver | |
CN204534588U (en) | A kind of water-cooled gas burner | |
CN106402869A (en) | Porous medium burner with cylinders stacked in order | |
CN107504487B (en) | Continuous dispersion type combustion device and method for forming continuous dispersion type combustion | |
CN112179138B (en) | A Porous Medium Combustion Heating Furnace with High Efficiency and Low NOX Emission | |
CN110822426B (en) | Variation micro-channel cooling type surface flame low NOx gas device | |
CN211782735U (en) | a tube furnace | |
CN109340741B (en) | Pipeline flue gas heating device | |
CN207648854U (en) | A kind of soft homogeneous catalysis burner | |
CN212841553U (en) | Spiral coil pipe cooling type low NOx pulverized coal burner | |
WO2022096021A1 (en) | Burner and applications thereof | |
CN104633657A (en) | Porous media burner with taper type bluff bodies | |
CN101430090B (en) | Rotational flow dispersion burner | |
CN114623443A (en) | A segmented porous medium burner and its working method | |
CN102937292A (en) | Flame-immersion porous medium burner reversing periodically | |
CN206973561U (en) | Continuous disperse formula burner | |
CN109945192B (en) | High-calorific-value fuel concentric jet air single-heat-storage burner | |
CN101706102A (en) | Counter flow heat exchange catalytic burner without ignition device | |
CN105841146A (en) | Nearly zero pollutant discharge flameless catalytic combustion condensing boiler |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160706 |
|
CF01 | Termination of patent right due to non-payment of annual fee |